Dresden Station Units 2 and 3 Hydraulic Calculations.F-80 is the most hydraulically remote fire hose...

Volume 10

AMENDMENT 13

DRESDEN 2 & 3

HYDRAULIC CALCULATIONS

TABLE OF CONTENTS

Tab Numbers Book 2

System Numbers Suppression System Descriptions

DR01 DR02 DR03 DR04 DR05

DR06 DR07 DROS DR09 DRIO

DRI I DRI2 DRI3 DR14 & 15 DR16

DR17 DR18 & 19 DR20 to 25 DR26 DR27



4

5

6

I

III-i

Unit 2 Condensate Pumps Unit 3 Condensate Pumps

Unit 2 Component Cooling Service Water Pumps

Unit 2 HPCI Pump Unit 3 HPCI Pump

Unit 2 Trackway Unit 3 Trackway Units 2 and 3 EHC Oil Reservoir Unit 2 Instrument Air Compressor Unit 2 Bus Duct Penetration

Unit 3 Bus Duct Penetration Units 2 and 3 Turbine Mezzanine (C-D and 40-48)

Units 2 and 3 Turbine Mezzanine (D-H and 43-45)

Units 2 and 3 Turbine Lube Oil Reservoir

Unit 2 Hydrogen Seal Oil Unit

Unit 3 Hydrogen Seal Oil Unit

Unit 2 Turbine Mezzanine Cable Concentration Units 2 and 3 Cable Tunnel Unit 2 ACAD Air Compressor Unit 3 ACAD Air Compressor

Units 2 and 3 Fire Pump and Fuel Day Tank

Unit I Fire Pump and Fuel Day Tank

Unit 3 Turbine Condenser Pit (Hotwell)

Unit 2 Turbine Condenser Pit (Hotwell)

Unit 2 High Pressure Heater Bay

Unit 3 High Pressure Heater Bay Unit 2 Low Pressure Heater Bay Unit 3 Low Pressure Heater Bay Unit 2 Oil Storage Area

Units 2 and 3 Auxiliary Heating Boiler

AMENDMENT 13 DRESDEN 2 & 3

HYDRAULIC CALCULATIONS

TABLE OF CONTENTS

Tab Numbers System Numbers Suppression System Descriptions Book 2

7 DR38 Unit 2 Main Transformer DR39 Unit 2 Auxiliary Transforner 21 DR40 Unit 2 Auxiliary Transfonner 22, PLC 8/1-2/84, Grinnell

5-3-89 DR41 Unit 3 Main Transfomler (refer to Calculations DRE 96

0145 and DRE 97-0290 for Unit 3 Main Power Transformer hydraulic requirenients)

DR42 Unit 3 Auxiliary Transformer 31

8 DR43 Unit 3 Auxiliary Transformer 32 APPROI Unit 3 Reactor Building Ladder Penetration APPR02 Unit 3 Reactor Building Hatchway APPR03 Unit 2 Reactor Building Hatchway and Stairwell APPR04 Unit 2 Reactor Building Ladder Penetration

9 APPR05 Units 2 and 3 Turbine Building Corridor APPR07B Unit 3 CRD and CCSW Pump Rooms APPRO8 Crib House Lower Level Deluge (Diesel Generator

Cooling Water Pump) APPR09 Crib House Lower Level Ceiling APPRIOA Crib House Upper Level-East Half, Crib House Upper

Level-West Half

10 AREA LL Units 2 and 3 Crib House Cable Tray Deluge System

11 Units 2 and 3 Makeup Dernineralizer System Demineralizer Resin Storage Room

12 Hydraulic Analysis of Fire Suppression System Demands

13 APPR10 Hydraulic Analysis of the Dresden Station Unit 2/3 Crib House Fire Suppression System APPR10

III-]]

Volume 11

AMENDMENT 13

DRESDEN 2 & 3

FIRE PROTECTION PROGRAM DOCUMENTATION PACKAGE

Volume Index

Volume 11 - Hydraulic Calculations (Continued)

IV C-Factor Verilication Data (C=80)

V Supplement One - Hydraulic Verification Study

VI Supplement Two - Hydraulic Verification Study

VII Supplement Three - Hydraulic Verification Study

VIII Supplement Four -- Hydraulic Verification Study

IX Unit 2/3 Turbine Building Hose Station Hydraulic Analysis

Mia 1)A77.-rA'j 0 KT/z / t,

CALCULATION TITLE PAGE Page No. 1.0

Dresden Station CALCULATION NO: DREOO-0008 DESCRIPTION CODE (C018): FOO

[ ]U1 [ U2 []U3 [X] Unit 0 DISCIPLINE CODE (C011): M SYSTEM CODE: 41 ELEVATION CODE (C016): 561'-6"

Title: Unit 213 Turbine Building Hose Station Hydraulic Analysis

[ ] Safety Related [X] Augmented Quality ] Non-Safety Related

REFERENCE NUMBERS: (C011 Panel)

Type Number Type Number

COMPONENT EPN: (c014 Panel) DOCUMENT NUMBERS: (CO12 Panel) (Calc. References)

EPN Component Type DocType SubType Document Number DWGC M-23, Sht 2

DWGC M-375, Sht 2

- -. = ,- - J I |•Il•SI%

REMARKS: This calculation was performed under the Comt--approvea 4 1 a Quality Assurance Program. QA documentation and data files are retained with

NTSC.REV. REVISING

No. ORGANIZATION

IX-1

CornEd CALCULATION REVISION PAGE

CALCULATION NO. DREOO-0008 PAGE NO.: 2.0 I REVISION SUMMARIES

I

Supplemental Review Required? [ ] Yes (NEP-12-05 documentation attached) [ 3 No

s..... vI.,_,s (CornEd USE ONLY)

ou t:lv"Ibul

DO ANY ASSUMPTIONS IN THE CALCULATION REQUIRE LATER VERIFICATION? []YES [X] NO

Tracked by: (NTS#, AT#, EWCS#)

IX-2

REV: 0 REVISION SUMMARY:

The hydraulic demand for the Unit 2 Turbine Deck hose stations F-75 and F-80, and for Unit 3

Turbine Deck hose station F-126, is calculated herein.

Electronic Calculation Data Files: (Program Name, Version, File name extlsize/datefhour/min)

Prepared by: I '/ Pdnt/Sign/Initial Date

Reviewed by: "• -. / /-/74' Print/Sign/Initi I Date

Type of Review [X] Detailed [ ] Alternate [ Test [ ] By Repetitive Calc

Review

upplemental Review Required? Yes (NEP-12-05 documentation attached) No Supervisor (ComEd USE ONLY)

DO ANY ASSUMPTIONS IN THE CALCULATION REQUIRE LATER VERIFICATION? []YES [X] NO

Tracked by: (NTS#, AT#, EWCS#) N/A

REV: R•EVISION SUMMARY:

Electronic Calculation Data Files: (Program Name, Version, File name extlsize/date/hour/:min)

Prepared by: Print/Sign/Initial Date

Reviewed by: Print/Sign/Initial Date

Type of Review []Detailed []Alternate []Test []By Repetitive Calc

Review

Calculation Table of Contents Page

CALCULATION NO. DREOO-0008 REV. NO. 0 PAGE NO. 3.0

SECTION: PAGE NO. SUB-PAGE NO.

"TITLE PAGE 1.0

REVISION SUMMARY 2.0

TABLE OF CONTENTS 3.0

PURPOSE/OBJECTIVE 4.0

METHODOLOGY AND ACCEPTANCE CRITERIA 4.0

ASSUMPTIONS 5.0

DESIGN INPUT 5.0

REFERENCES 5.0

CALCULATIONS 6.0

SUMMARY AND CONCLUSIONS 7.0

ATTACHMENTS:

A: NFPA 14 Deviation Close Out Matrix, NTSC Al to A2

Report No. 93-124, Rev. 0. B: SPRINK-1000 output data, Fire Hose Station B1 to B27

F-80 C: SPRINK-1000 output data, Fire Hose Station C1 to C27

F-75 D: SPRINK-1000 output data, Fire Hose Station D1 to D27

Ff-126

IX-3

I

COMED COMPANY CALCULATION PAGE

CALCULATION NO. DREOO-0008 PAGE NO. 4.0

PURPOSE I OBJECTIVE

NFPA 14-1974, Paragraph 219, requires standpipes to be at least 2 inches in diameter. However, some

Turbine Building standpipes are 1-1/2 inches in diameter as documented in Deviation No. 14-02, listed in

the Dresden Unit 2/3 NFPA 14 Deviation Close Out Matrix (Ref. 1). The purpose of this report is to

provide a technical justification for this deviation.

METHODOLOGY AND ACCEPTANCE CRITERIA

The SPRINK-1000 computer program (Ref. 4) was used to verify that the fire water system is capable of

supplying a minimum flow rate of 100 gpm at 65 psi at the outlet of the most hydraulically remote 1-1/2"

hose station. The design criteria that was used satisfies the requirements of NFPA 14, Standard for the

Installation of Standpipe and Hose Systems (Design Input 1, Paragraph 541).

FIRE HOSE STATION SELECTION- -� .L.. � .- �4+b� � lr�cp �t 2 tinn�

In order to determine if the fire water system can adequately meet me uemanu Uv ...

whose piping is less than 2 inches, three hose stations were selected for hydraulic analysis based on their

physical location in the plant. Two of these hose stations are located in the Unit 2 Turbine Building, and

one is located in the Unit 3 Turbine Building. All three are located at the 561 '-0" elevation. Piping

layout drawings (Ref. 3), P&IDs (Ref. 2), and engineering judgment were used to determine the most

hydraulically remote hose stations.

The latest revision of the station drawings was used as design input for this report. Pending changes to

the drawings were reviewed and verified not to affect the hydraulic calculations.

Only the Turbine Building was studied because it was the only building identified in the NFPA 14

Deviation Close Out Matrix (Ref. 1) to contain fire hose stations that did not satisfy the NFPA 14 (Design

Input 1, Paragraph 219) requirement for minimum 2" piping.

Hose stations F-75 and F-80 on the Unit 2 Turbine Deck (El. 561 '-6") and F-126 on the Unit 3 Turbine

Deck (El. 561 '-6") were selected.

STATION MODEL APPLICATION

An existing hydraulic calculation (Design Input 2) that uses the SPRINK-1000 computer program (Ref. 4)

was used in this analysis to model the fire water system. The referenced calculation models the

underground and above-ground fire protection loop piping.

REVISION NO. 0

IX-4


CALCULATION NO. DREOO-0008 PAGE N. 5.0

FIRE HOSE STATION HYDRAULIC SUPPLY CALCULATION

"rL. ....... tl,, Of the fire hose station to the fire water system was located on the P&IDs (Ref. 2) and the

pipin the n

FAIl

The An i No.

AS5

Non

DE

RE

ag layout drawings (Ket 3). Piping data w as a,. . . .. .... ... Lode point nearest to the hose station connection to the fire water system.

LURE SCENARIO

Unit I Diesel Fire Pump (U1 DFP) out of service is the only failure scenario analyzed in this report.

noperable U I DFP was determined to be the worst-case scenario based on the results of Calculation

DRE97-0256, Rev. 2 (Design Input 2).

3UMPTIONS

Le.

SIGN INPUT

1. NFPA 14, Standard for the Installation of Standpipe and Hose Systems, 1974 Edition.

2. Dresden Calculation DRE97-0256, Rev. 2, "Dresden Station Fire Protection System Design Basis

Hydraulic Calculations," dated 8/21/98.

"FERENCES

1. Table A, NFPA 14 Deviation Close Out Matrix, NTSC Report No. 93-124, Rev. 0, dated 5/16/94.

2. Dresden Station P&IDs:

M-23, Sht. 2, Rev. P M-375, Sht. 2, Rev. L

F•-253, Rev. 1 F-254, Rev. B

F-434, Sht. 1, Rev. R

F-434, Sht. 2, Rev. D

REVISION NO. 01

IX-5

S.. .. ,-.,.x .n__:__ .1^÷ .... . elA, tn• the station fire water system hydraulic model at

1 -1 - 1- 1 - 1 -


CALCULATION NO. DREOO-0008 PAGE

I NO. 6.0

3. Dresden Station Piping Layout Drawings:

M-103, Rev. H M-108, Rev. U M-121, Rev. S M-427, Rev. H M-43 1, Rev. L

4. SPRINK-1000, A Microcomputer Program for the Hydraulic Analysis of Fire Sprinkler Systems,

Version 11.00. Municipal Hydraulics Ltd.

5. NFPA Fire Protection Handbook, Eighteenth Edition.

CALCULATIONS

The SPRINK-1000, Version 11.00, computer program (Ref. 4) was used to calculate the fire water system

supply for the two most hydraulically remote hose stations in the Unit 2 Turbine Building, and one in the

Unit 3 Turbine Building.

The accuracy of the computer program was validated against a controlled output file in accordance with

the NTSC Quality Assurance Program.

The K-Factor for the hose stations used in the calculation is as follows:

K = QI/ 1i- Derived from Ref. 5, Page 6-171

Design Criteria per NFPA 14 Design Input 1, Paragraph 541

Q 100 gpm P 65 psi

K= 100/,r65= 12.4

The SPRINK-1000 output files containing the available pressure and flow rate for hose stations F-75, F

80 and F-126 are included in Attachments B, C and D.

[REVISION NO. 0I

IX-6


CALCULATION NO. DREOO-0008 PAGE NO. 7.0 of 7.0

SUMMARY AND CONCLUSIONS

F-80 is the most hydraulically remote fire hose station based on the hydraulic calculations. The results of

the calculation show that the fire water system is capable of supplying 119 gpm at 92 psi to hose station

F-80. As a result, the Dresden Station fire water system is capable of supplying the demand of the fire

hose stations in the Turbine Building.

REV/ISION NO. 0

IX-7

CALCULATION NO. DREOO-0008 Revision No. 0

ATTACHMENT A

NFPA 14 DEVIATION CLOSE OUT MATRIX

IX-8

322I

NFPA #14 DEVIATION CLOSE OUT MATRIX

TABLEA

Deviation justification

Rec ndd Action

The addition of hose reel numbers to P&Ios and F-Drawings have been updated DD

the F-drawings would simplify the (Ref.2, pg 1.1-12, item 4.1).

gathering of needed information (Ref.1,

pg 8,•pare 2)

In the Turbine Building some standpipe A hydraulic analysis was performed on Locate hydraulic

sizes are less than 2 inches (Ref.1, pg three hose stations to verify adequacy calcs and reference

8, pars 5). of 1-1/2" supply pipe. The analysis them in the

indicates the required amount of water adjacent

Several plant areas shown in Table 3.1

can be delivered (Ref.1, pg 8, pare 5). NTSC could not find the analysis

referenced in the above justification.

In specified areas, due to the minimal

amount of combustibles and other fire

justifione.on.

None.

S.. .. cannot be reached W• E • ovi ed the...

a 30' hose stream (Ref.1, pg 9, 10, protection features provided, tne existing configuration Is adequate (Ref.1, pg 9, 10, 11).

Recommendation made for additional hose Procedure 4114-06

to select hose stations with less than does not require

100 ft hose (Ref.1, pg 17, Item 4.3). 100' of hose to be verified(except for

ones that are justified in Table 3.1). Revise Procedure. Add justified hoses to this deviation.

14-04 342 As identified in Table 3.1 standpipes Table 3.1 does not reference any stand 0DDt

not provided with 1-1/2" outlets at pipes without 1 1/2 inch outlets.

each floor (Ref.1, pg 11, pare 3).

- oved hose is at The additional hose length is required None.

som e hose stations (Ref.1, pg 11, pare to provide adequate coverage for the

7). Two 150 ft hard rubber hoses are control room (NTSC)o

provided to protect the Control Room.

14-06 43 Labels Indicating use and operating The fire hoses are for use by the fire None.

Instructions ape not provided on hose brigade only. Signs have been provided

racks (Ref.1, pg 11, pars 8). on each hose station identifying that only the fire brigade can use the

*hoses. All fire brigade member have been adequately trained to handle

hoses. As a result, operating instructions on the hose stations are

unnecessary (NTSC).

Note: References are located on the last page of this matrix.

>

Deviation

14-01

14-02

I /�-O3

I

NFPA #14 DEVIATION

CLOSE OUT MATRIX TABLE A

Deviation I Code Deviation Justification RecActon No.I secti(on.I1-1

14-07 44; OSHA Sub- Pressure reducing devices are not CECo policy is not to use pressure None. part L provided for standpipes exceeding 100 reducing devices ... (Ref.2, pg 1.1-12,

psi (Ref.1, pg 12, pare 3). Item 4.4) Fire hoses are for the use of the fire brigade only. ALL brigade members have been adequately trained to handle hoses subject to high pressure.

(NTSC)

14-08 6 The main 2/3 discharge valve is not of A NTSC walkdown found that an indicator DD an indicating type as required (Ref.1, has been installed on the valve. pg 15, para 2).

14-09 67 Water flow switches are not provided on A primary function of a flow switch Is None. alt standpipes (Ref.1, pg 1S, pare 5). to provide notification of unauthorized

use. Since access to a nuclear power plant is controlled, unauthorized operation is not normally a concern. in addition, operation of a hose station should activate the fire purp running alarm (NTSC).

References: 1. An Evaluation of Standard for the Installation of Standpipe and Hose Systems (NFPA# 14) at the Dresden Nuctear Power Station,

Units 2 and 3 for CommonweaLth Edison Company, 5/30/85, Rev.1

2. Sargent and Lundy Letter dated 8/7/87 from J.W. Zesuteck to R.J. Whalen, Project 7927-05 >

•= 3 S

Page AZ- o"/2p

I

o


ATTACHMENT B

SPRINK-1000 OUTPUT DATA HOSE STATION F-80

IX-1I

KevisIon U Attachment B

DESIGN PROGRAM FOR SPRINKLER SYSTEMS P 7c

by

MUNICIPAL HYDRAULICS LTD, LADYSMITH, B.C. CANADA

COPYRIGHT (C) 1995 MUNICIPAL HYDRAULICS LTD

VERSION 11.00

COMPANY Nexus Technical Services Corporation

DESIGNER : BY: BRIAN FOX CHECKED:,•A& L/"j/7

CLIENT : ComEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis

PROJECT : Ul DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP

JOB NO. U2TB Hose Station F-80

FIX

C-62

p 01 01 02 3.5 11.938

P 02 02 03 16.1 11.938 1GV ITT 3SE CV

P 03 03 04 21.2 7.981 2SE

C-132

P 04 04 05 60.0 11.2 HE SE 3ZSE(7)

P 05 05 06 13.5 11.2 TT GV

C-66

P 06 06 07 156.6 7.85

P 07 07 08 161.0 7.85

P 14 08 13 86.0 7.981 ITT

C-55

P 15 13 14 54.6 7.981

P 750 700 701 72.8 7.981 4HE

P 16 14 15 14.1 11.2 GV

P 17 15 700 44.5 11.2 GV

P 751 701 16 29.3 11.2

C-86

P 18 16 35 9.1 11.2

P 19 35 702 82.7 11.2 HE

P 752 702 17 41.9 7.85

P 20 17 726 119.6 7.85 HE

P 21 725 19 97.9 7.85

P 725 18 725 6.8 11.2 GV

P 726 18 726 4.5 11.2 GV

P 727 18 727 2.1 11.2 GV

C-59

P 762 723 919 12.5 8.385 GV

P 922 919 19 29.2 7.85

C-66

P 22 20 723 82.2 8.385 TT SE ZSE(S)

P 23 20 21 133.3 8.385 TT 3HE GV

P 30 27 703 4.0 7.981 1GV

P 753 703 21 26.0 7.85 TT

C-86

P 29 21 26 147.0 7.981 ITT

P 28 26 25 146.0.7.981 2SE

C-62

P 27 25 601 81.9 7.981 6SE IGV

P 601 601 24 10.8 7.981 ISE

P 754 602 704 58.7 7.981 4SE IHE ITT 1GV

P 602 602 24 123.0 7.981 5SE 2HE GV

P 755 704 705 221.92 7.981 7SE 2HE ITT

C-86

P 756 705 727 141.27 7.981 2HE ITT IX-12

C-62

P 300 24 200 136.5 7.981 5SE IGV ITT

P 26 200 923 7.5 7.981 ISE ITT 1GV

P 757 704 706 197.01 4.026 8SE 4HE GV

P 758 706 923 178.37 4.026 12SE 4HE GV

P 925 923 23 21.25 7.981 3SE ITT 1GV

C-132

P 25 22 724 75.0 11.2 TT 4HE

C-62

P 719 719 23 5.86 7.981 2HE

C-86

P 763 724 719 26.0 7.85

C-132

P 24 05 22 149.9 11.2 GV TT

C-35

P 50 45 48 255.0 9.564 5SE 2GV IHE

*.NE***************

/. NOTE

THE FOLLOWING PIPES HAD A*

/ CALCULATED C FACTOR OF 27.4. DUE*

/ TO LIMITATIONS OF THE SPRINK

/ PROGRAM, A C OF 35 WAS USED*

/* (THE MINIMUM) AND PIPE LENGTHS*

/* ADJUSTED TO REFLECT EQUIVALENT*

/* FRICTION LOSS.*

P ACTUAL LENGTHS ARE AS FOLLOWS:*

/*PIPE 41 - 10.8"

/-PIPE 42 - 9.8*

/-PIPE 45 - 22.3*

/-PIPE 46 - 10.0

/-PIPE 49 = 2.0'

**************************** *****,,

p 41 40 41 17.0 10.02

P 42 41 42 15.4 10.02 1HE 1GV ICV ISE

P 45 42 45 35.1 10.02 ITT

P 46 37 38 15.1 7.981 IGV SE 2HE

P 49 45 37 3.5 7.981 ITT

C-132

P 47 38 39 230.0 11.2 3SE 2HE 4ZSE(7) 3ZSE(3)

P 48 39 22 59.3 11.2

C-62

P 55 48 67 115.92 10.02 7SE

P 70 67 69 3.25 10.02

P 69 69 80 2.17 10.02

P 68 80 64 5.33 10.02 1GV

P 67 64 63 86.75 7.981 9SE 2TT 1GV 2HE

P 66 63 62 36.93 6.065 4SE IGV ITT

P 65 62 61 70.08 6.065 3SE 2HE

P 64 61 60 130.25 6.065 3SE 4HE ITT

P 63 60 59 30.83 6.065

P 62 59 58 6.75 6.065

P 302 58 201 80.0 6.065 1GV 4HE

P 303 201 202 482.5 10.02 2TT

P 305 57 201 89.0 6.065 ISE IGV 2HE

P 60 56 57 1.0 7.981

P 59 55 56 15.08 7.981 4HE

P 58 54 55 107.58 7.981 2HE

P 57 53 54 15.5 7.981

P 56 70 53 118.25 7.981 7SE 1HE IGV IX-13

Revision 0 Attachment B

P 54 51 70 11.67 10.02

P 53 50 51 2.33 10.02

P 52 49 50 1.0 10.02

P 51 48 49 6.0 10.02 ITT

P 8 8 9 30.0 7.981 bGV

P 9 9 10 110.0 4.026 2SE 1HE 2TT 1GV

P 10 10 12 215.42 4.026 15SE 7HE 2GV ITT

P 11 10 11 77.5 4.026 5SE 2HE 1GV

P 12 11 12 80.25 4.026 8SE 4HE 1GV

P 13 12 15 34.75 4.026 4SE 1GV ITT

P 83 70 68 2.33 10.02 1GV

P 82 68 71 89.83 7.981 3SE

P 81 71 72 54.75 7.981 4SE 1HE

P 80 72 73 15.58 7.981

p 79 73 74 103.58 7.981

P 78 74 75 1.75 7.981

p 77 75 76 14.50 7.981

P 76 76 77 21.50 6.065 2SE

P 75 77 78 175.67 6.065 4SE 2HE 1GV

P 74 78 79 65.83 6.065 2HE

p 73 79 98 122.0 6.065 2SE 2HE

P 72 98 81 32.25 6.065 3SE 2TT 1HE

P 71 81 63 84.83 6.065 IGV

P 110 64 102 0.5 10.02

P 84 102 82 10.5 10.02

P 99 82 86 1.0 10.02 ITT

p 100 86 85 48.5 6.065 2SE 3HE 1GV

P 102 97 84 14.33 7.981 2HE ITT

P i03 84 66 1.50 7.981

P 104 66 47 27.75 7.981 4SE 2GV SR

P 105 47 28 115.0 7.981 ISE 1GV ITT

C-56

P 31 28 721 125.0 7.981

P 761 721 720 17.0 8.385 2HE

P 760 720 27 75.5 7.981 ISE

C-62

P 90 82 88 1.00 10.02 ITT

P 93 88 87 66.0 6.065 4SE 3HE 1GV ITT

P 95 96 83 14.17 7.981 2HE ITt

P 96 83 65 1.50 7.981

P 97 65 46 31.25 7.981 5SE 2GV 1SR

P 98 46 29 112.0 7.981 1SE 1GV ITT

C-56

P 932 29 929 2.5 7.981

P 32 929 928 184.0 8.425 2SE 5HE 2GV

P 931 928 28 98.2 7.981

P 33 30 29 20.0 7.981

C-41

P 40 37 36 160.0 7.981 1GV ITT 4SE 3HE

C-61

P 39 36 52 160.0 7.981

P 38 52 34 10.00 7 .981

P 37 34 33 280.0 7.981 5SE 1HE

C-55

P 36

C-71

33 32 300.0 7.981

P 35 32 31 285.0 7.981

C-61

P 34 31 30 285.0 7.981

/ ...... *...*...........A......... IX-14

Revision 0 Attachment B

F¾Ct 9P3

NOTE/-

/* THE FOLLOWING PIPES WERE

/* ADDED TO ATTACH SYSTEMS

/ TO THE BASE MODEL

C-120

P 611

p 612

P 621

P 834

R 834

p 803

R 800

P 804

601 611 4.5 6.065 2SE ITT

611 612 1.0 6.065

602 621 3.6 6.065 3SE ITT

54 834 28.6 6.065 2SE 2HE 2TT 1GV

536.3

834 800 30.9 6.065 3SE IHE

518.3

800 801 121.75 5.047 7SE 4HE

R

P

R

P

I

GV

*801 509.0

822 801 804 5.5 3.068 ITT

1 804 509.0

805 56 805 25.75 7.981 1HE ITT

805 529.3

P 815 805 819 6.0 7.981 ISE

R 819 536.0

P 816 819 820 6.58 6.065 IHE ITT 1GV

R 820 526.5

P 819 819 822 16.75 6.065 iSE iHE 1GV

R 822 526.5

p 809 77 808 1.0 2.469 ITT tGV

R 808 554.5

P 106 51 812 1.0 7.981 ITT tGV ISE

R 812 538.8

P 806 49 849 84.1 4.026 3SE 2HE ITT 1

P 808 849 815 18.0 4.026 4SE IKE 1GV

P 807 849 814 2.5 4.026 ISE ITT 1GV

R 849 541.8

R 814 541.8

R 815 544.5

P 810 60 809 28.08 4.026 2SE ITT

R 809 549.5

P 842 809 810 23.33 3.068 ISE 1GV

R 810 549.5

P 811 79 811 51.5 3.068 4SE ITT 2GV

R 811 546.0

P 833 98 833 25.58 6.065 ISE ITT 1GV

R 833 554.5

P 836 833 828 75.92 6.065 9SE 2TT

R 828 552.92

P 837 828 829 100 6.065 8SE 2HE ITT

R 829 488.0

P 832 61 832 9.9 6.065 ISE 1GV ITT

R 832 554.5

P 835 73 835 24.5 6.065 ITT 2SE 2HE

R 835 536.3

P 812 55 813 62.7 7.981 4SE 4HE ITT

R 813 525.5

P 813 813 817 1.0 2.469 1TT iGV

R 817 525.5

P 814 813 818 1.5 7.981 1GV

R 818 522.8

P 841 75 823 32.0 7.981 ITT 2SE IHE

R 823 523.3

P 820 76 824 32.0 7.981 2SE 1TT iHEIX-15

1GV

Attachment B

a a - KCVIUIOfl U

0-824 523.3

P 821 824 825 23.25 6.065 ISE iHE IGV

R 825 523.3

P 826 824 826 6.3 6.065 ITT IHE lGV

R 826 523.3

p 850 93 850 12.5 6.065 1GV 2SE ITT

R 850 521.0

P 87 92 93 152.1 4.026 2SE 6HE

P 86 91 92 16.0 6.065 2HE IGV ITT

P 85 82 91 1.0 10.020 ITT

R 91 526.2

R 92 527.0

R 93 527.0

P 851 89 851 12.9 4.026 3SE ITT IGV IHE

R 851 521.5

P 91 88 89 166.9 4.026 yGV 8HE

R 89 527.0

P 800 928 802 33.83 6.065 ITT lGV 2SE

R 802 519.5

P 802 802 803 115.08 4.026 2HE iTT 4SE lGV

R 803 527.7

P 840 838 845 117.8 4.026 5HE 2SE ITT IGV

R 845 591.0

C-62

P 839 96 838 62.4 6.065 1HE 1GV ITT

P 94 838 87 206.1 6.065 6SE 2HE ITT

P 860 97 860 51.5 6.065 1GV IHE

P 101 860 85 168.5 6.065 7SE 3HE

C-120

R 838 505.5

P 861 860 861 119.75 4.026 3HE 3SE TT GV

R 860 505.5

R 861 593.3

P 827 102 855 4.39 6.065 ITT IGV iHE ISE

P 831 42 837 11.0 10.02 2HE

P 824 835 836 63.5 6.065 iGV 5SE 3HE 4TT ICV

R 836 527.08

P 823 836 827 121.5 5.047 4HE 8SE

R 827 509.8

R 837 510.9

R 855 527.9

C-62

P 828 200 839 2.3 6.065 ITT

P 829 839 831 3.0 6.065

P 304 831 202 2.7 6.065

C-120

R 839 527.5

R 831 527.5 ****************** ** ******* *

END

/ ******.****.*******************

C-120

P 500 97 400 26.17 6.065 1HE

P 501 400 401 132.67 6.065 2SE 4HE ITT iGV

P 502 401 402 52.17 4.026 3SE ITT 2GV

P 503 96 403 7.75 6.065 1HE

P 504 403 404 132.33 6.065 ITT 2SE 3HE 1GV

P 505 404 405 47.0 4.026 ITT 3SE 2GV

/* ...... * .... **n.......... * pipes

/* The following nodes and pipes *

Attachment B

IX-16

Revision 0

/* refer to hose stations. To Attachment

/* switch between hose stations, * • •1

/'change the S to an R and remove *

/ the flow and K-factor on the hose *

/ stations that you do not want

/ to flow. /***********************************

/ HOSE STATION F-75

P 600 57 600 13.5 1.610 TT 2SE GV

R 600 566.5

/HOSE STATION F-80

P 651 61 651 49.1 1.610 TT 2SE GV

S 651 566.5 100 12.4 / . *************** **.********

END

R 02 509.5

R 03 516.0

R 04 510.8

R 05 510.8

R 06 510.8

R 07 510.3

R 08 509.6

R 09 509.6

R 10 515.5

R 11 554.2

R 12 515.5

R 13 509.8

R 14 509.3

R 15 509.1

R 16 510.9

R 17 510.1

R 18 509.3

R 19 509.4

R 20 511.4

R 21 510.6

R 22 511.5

R 23 511.5

R 24 525.0

R 25 511.0

R 26 511.5

R 27 510.5

R 28 512.0

R 29 512.0

R 30 511.2

R 31 512.2

R 32 513.0

R 33 512.0

R 34 511.7

R 35 510.1

R 36 512.5

R 37 510.9

R 38 511.0

R 39 511.1

R 41 510.9

R 42 510.9

R 45 510.9

R 46 513.0

R 47 513.0

R 48 529.5 IX-17

AMENDMENT 13 Caic. No. DREOO-OOOS Revision 0

Attachment B R 49 535.5

R 50 536.5

R 51 538.8

R 52 511.7

R 53 556.0

R 54 556.0

R 55 556.0

R 56 556.0

R 57 556.0

R 58 554.5

R 59 554.5

R 60 554.5

R 61 554.4

R 62 562.5

R 63 569.6

R 64 526.0

R 65 520.5

R 66 520.5

R 67 526.0

R 68 552.7

R 69 526.0

R 70 550.5

R 71 558.5

R 72 555.5

R 73 555.5

R 74 555.5

R 75 555.5

R 76 555.5

R 77 555.5

R 78 554.5

R 79 554.5

R 80 526.0

R 81 569.7

R 82 526.0

R 83 519.0

R 84 519.0

R 85 517.5

R 86 526.0

R 87 517.5

R 88 526.3

R 96 505.5

R 97 505.5

R 98 551.2

R 102 526.0

R 200 535.5

R 201 556.0

R 202 535.5

R 400 505.5

R 401 601.0

R 402 593.3

R 403 505.5

R 404 601.0

R 405 593.3

R 601 525.0

R 602 528.3

R 611 532.5

R 612 532.5

R 621 527.3

R 720 512.0

R 721 512.0 IX-18

AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0 Attachment B

R 723 510.5

R 724 511.5 - g

R 700 509.1

R 701 510.4

R 702 510.6

R 703 512.0

R 704 528.5

R 705 511.3

R 706 524.7

R 719 511.5

R 725 509.3

R 726 509.3

R 727 509.3

R 919 510.5

R 923 541.0

R 928 512.0

R 929 512.0 /*****************************************************

NOTE

/ TO DEACTIVATE PUMP UNIT 1:*

I. CHANGE:*

/* 1 01 500.0 0.0 150 2000 150 2500 140 3750 91 3751 10*

/* TO:

/* R 01 500.0 /************************************ .******t*****

R 01 500.0 /***t********************** ****** *****************

NOTE

/* TO DEACTIVATE PUMP UNIT 2/3:*

/- CHANGE:*

/* I 40 500.0 0.0 150 2250 150 3000 131 3600 120 4900 110 4901 10*

/* TO:*

/* R 40 500.0

I 40 500.0 0.0 150 2250 150 3000 131 3600 120 4900 110 4901 10

LENGTH DIAMETER FLOW HEAD ELEVATION PRESSURE

UNITS BEING USED: FEET INCHES US GPM FEET FEET PSI

HAZEN-WILLIAMS FORMULA USED

FITTINGS SPECIFIED AS NFPA

ITERATION STOPS WHEN GREATEST FLOW CHANGE IS .05000 IN ANY PIPE

MULTIPLICATIVE FACTOR OF EACH CONSUMPTION IS 1.00000

DEFAULT ROUGHNESS COEFFICIENT - C-120.0

THERE ARE 1 SPRINKLERS AND 0 BOOSTER PUMPS

THERE ARE 181 PIPES AND 169 REFERENCE POINTS

THE NUMBER OF INPUT POINTS IN SYSTEM IS I

NODE NO. OF PUMPS PUMP INPUT PUMP PARAMETERS

NO. IN PARALLEL ELEVATION FRACTION OR X-Y COORDINATES

40 1 500.00 1.00 .0 2250.0 3000.0 3600.0 4900.0 4901.0

150.0 150.0 131.0 120.0 110.0 10.0

IX-19

AMENDMNT 13 Caic. No. DREOO-OOOS AMENDMNT 13 Revision 0

Attachmncn B

Initial estimate of demand on the system is

NET UNBALANCED DEMAND ON THE SYSTEM - .00000

LOOP PIPES

1 651 65 66 67 68 69 70 55 50 45

2 65 64 63 62 302 305 60 59 58 57

66

54 83 82 81 80 79 78 77 76 75

52 53

68 110 84 90 93 94 839 95 96 97

50 55 70 69

303 305 60 59 58 57 56 54 53 52

26 828 829 304

99 90 93 94 839 95 96 97 98 932

932 33 34 35 36 37 38 39 40 46

28 29 753 30 760 761 31 931 32

754 757 758 26 300 602

25 24 5 6 7 14 15 16 17 750

758 925 719 763

725 727 756 755 754 602 601 27 28 29

14 8 9 10 13 16 15

10 11 12

BANDWIDTH 5 5

Iteration # 0 Max change in flow is


Iteration 6 2 Max change in flow is




NUMBER OF ITERATIONS= 6

42 41

56 54 53 52 51 55 70 69 68 67

74 73 72 71 67 68 69 70 55 51

98 33 34 35 36 37 38 39 40 49

51 50 49 46 47 48 25 763 719 925

32 931 105 104 103 102 860 101 100

47 48 25 763 719 925 26 300 601 27

751 18 19 752 20 726 727 756 755 757

23 22 762 922 21

74.714 in loop # 2

33.536 in loop # 3

15.510 in loop # 3

4.344 in loop # 3

.456 in loop # 3

.005 in loop # 3

IX-20

100.00

f 1c ( 7 C Re0-0

3

4

5

6

7

8

9

10

11

12


SUMMARY REPORT

COMPANY Nexus Technical Services Corporation PAGE 90 :e

DESIGNER BY: BRIAN FOX CHECKED: LDATE 2000 JAN 6

CLIENT ComEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis

PROJECT UI DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP


MINIMUM FLOW OF ALL OPERATING SPRINKLER HEADS IS 118.89

AVERAGE FLOW FROM ALL OPERATING SPRINKLER HEADS IS 118.89

TOTAL FLOW FROM ALL OPERATING SPRINKLER HEADS IS 118.89

TOTAL DEMAND ON THE WHOLE SYSTEM IS 118.89

SPECIFIED AVAILABLE PRESSURE AT INPUT NODE IS 346.40 FEET

OR 150.00 P.S.I.

IX-21

AMENDMENT 13Calc. No. DREOO-OOOS Revision 0 Attachment B

HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS

I PAGE 0JAN 1 JDATE 2000 JAN6COMPANY Nexus Technical Services Corporation

DESIGNER BY: BRIAN FOX CHECKED:


PROJECT 1U1 DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP

JOB No. IU2TB nose -~' a .

I I PIPE DIAMETERI PIPE/FTG TOTAL 1HEAD LOSSIHEAD LOSS I STATIC TOTAL ROUGH) WATER I VELOC.I

IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH I PER FT. OVER PIPE 1HEAD LOSSIHEAD LOSS NESS IVELOCITYi PRESS.!

INO. I NODES (US GPM) I (IN) (IN) I # (FT) (FT) I (PSI) (PSI) (PSI) I (PSI) ICOEFFI (FT/SEC)i (PSI) 0•00,II.00

I I_ I __ _ _ _ __ _ _ _ _

1 1

2

3

4

6 71 81

9O

10I

11

12

13

14

15

1 2

2 3

3 4

4 5

5 6

6 7

7 8

8 9

9 10

10 12

10 11

11 12

12 15

8 13

13 14

0.00

0.00

0.00

0.00

13.47

13.47

13.47

1.54

1.54

0.71

0.83

0.83

1.54

11.93

11.93

4.114 62 1

12 12

12

12

8

12

12

12

12

12

.p 11.94 C:

11.94 C

1'

1 13

7.98 C

2

11.20 C

1

II

3

11.20 C

7.85

7.85I

7.98

4 .03

4.03

40

4.03

4.03

4.03

7.98

7.98

____________I I__________ I _____I_______

IX-22

SAM

SAM GV

TT

SE

CV

SAM

SE

SAM

HE

SE

3ZSE

CSAM

TT

IGV

CSAM

CSAM

CSAM

1GV

CSAM

2SE

1HE

2TT

IGV

CSAM

5SE

7HE

2GV

ITT

CSAM

5SE

2HE

1GV

CSAM

8SE

4HE

1GV

CSAM

4SE

1GV

lTT

CSAM lITT

CSAM

3.5 16.1

1.7

17.2

23.3

18.7

21.2

10.0

60.0

11 .1I

23.0

21.0

13.5

51.2

5.1

156.6

161.0

30.0

1.1

110.0

5.9

1.2

11.8

0.6

215.4

44 .2

8.2

1.2

5.9

77.5

14 .7

2.4

0.6

80.3

23.6

4.7

0.6

34.8

11.8

0.6

5.9

86.0

11.0

54.6

8

4

4

4

4

4

4

4

4

4

4

4

4

4

4

4

4

4

8

3.5 0.000 0.000

77.0 0.000 0.000

31.2 0.000 0.000

115.1 0.000 0.000

69.8 10.516E-6 10.00003601

156.6 10.000010 1 0.00165 1

161.0 10.000010 0.00169 1

31.1 10.197E-6 10.0000061 1

129.4 10.00000551 0.000715 1

II

274.9 10.00000131 0.000360 1

II

I I

95.2 10.00000171 0.000168

109.1 10.00000171 0.000192

53.0 10.00000551 0.0002931

97.0 10.00000771 0.000750 1

54.6 10.000010 0.000592 1

4.114 2.815

-2.252

0.000

0.000 10.

-0.217 1

-0.303 1

0.000 l0

2.555 1

0.000

16.758

-16.758

-2.771

0.0866

-0.217

2.815

-2.252

0.000 I

0000360

-0.215

-0.301

.0000061

2.556

0.000360

16.758

-16.758

-2.771

0.0873

-0.216

62

62

.32

132

66

66

62

62

62

62

62

62

66

55

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.0439 10.13E-41

0.0893 10.53E-41

0.0893 10.53E-41

0.00990 0.66E-61

0.0389 10.10E-41

I I

0.01-79 10.21E-51

I I I I I I I I

0.0210 10.29E-51

I I I I I I

0.0389 10.10E-41

0.0765 10.39E-41

I I 0.0765 10.39E-41


PAGE B 12.HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS

I I I PIPE DIAMETERI PIPE/FTG TOTAL

IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH

INO. I NODES (US GPM) I (IN) (IN) I # (FT) (FT)

IHEAD LOSSIHEAD LOSS

PER FT. JOVER PIPE

I (PSI) (PSI)

STATIC TOTAL

HEAD LOSSIHEAD LOSS

I (PSI) I (PSI)

IROUGHJ WATER I VELOC.I

INESS IVELOCITYI PRESS.L

ICOEFFI (FT/SEC)I (PSI) I

I I I I __________ ______ I ______ _______ I ______ I _______ ( ____ I ______ I _____ I - H ______________________________

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

38

14 15

15 700

16 35

35 702

17 726

725 19

723 20

20 21

22 5

22 724

923 200

601 25

25 26

26 21

703 27

721 28

929 928

30 29

31 30

32 31

33 32

34 33

52 34

11.93

13.47

13.47

13.47

13.47

8.61

8.61

8.61

13.47

40.36

39.32

3.04

3.04

3.04

11.66

11.66

2.08

14.29

14.29

14.29

14.29

14.29

14.29

12

12

12

8

8

8

8

8

8

8

12

12

12

12

8

8

8

8

8

8

8

8

8

8

8

8

8

______ I _____ I _______ I ________ I ____ I _____ I ______ I _____ I ______ I ___ I ____ I ____ I

IX-23

U2TB Hose St

11.20 CSAM

1GV

11.20 CSAM

1GV

11.20 CSAM

11.20 CSAM

1HE

7.85 CSAM

1HE

7.85 CSAM

8.39 CSAM

ITT

ISE

I1ZSE 8.39 CSAM

ITT 3HE

IGV

11.20 CSAM

1GV

ITT

11.20 CSAM

ITT

4HE

7.98 CSAM

ISE

ITT

1GV

7.98 CSAM

6SE

I1GV 7.98 CSAM

2SE

7.98 CSAM

ITT

7.98 CSAM

1GV

7.98 CSAM

8.43 CSAM

2SE

5HE

2GV

7.98 CSAM

7.98 CSAM

7.98 CSAM

7.98 CSAM

7.98 CSAM

5SE

IHE 7.98 CSAM

14.1

1.0

44.5

1.0

9.1

82.7

5.0

119.6

4.2

97.9

82.2

13.9

7.2

5.0

133.3

13.9

10.7

1.6

149.9

5.1

51.2

75.0

51.2

44.3 3

7.5

5.0

9.8

1.1I

81.9

30.1

1.1I

146.0

18.4

147.0

17.9

4.0

1.3

125.0

184.0

10.8

13.5

2.4

20.0

285.0

285.0

300.0

280.0

24.3

2.4

10.0

15.1 10.000002010.0000315

45.5 10.00000261 0.000119

9.1 10.000001110.0000104

87.7 10.000001110.0001000

123.8 10.00000641 0.000797

1 1 97.9 10.00000281 0.000275

108.3 10.00000331 0.000361

159.6 10.00000331 0.000531

206.2 10.516E-6 0.000106

II II

170.5 10.00000391 0.000670

23.4 0.000079 1 0.00185

113.1 10.693E-6 10.0000784

1 I I I

164.4 10.378E-6 10.0000622

164.9 10.378E-6 10.0000623

1 1 5.3 I0.000007410.0000390

125.0 0.000010 1 0.00126

210.7 10.316E-6 10.0000667

1 1

1 I

20.0 10.000014 0.000293

285.0 10.000012 0.00357

285.0 10.00000941 0.00269

300.0 10.000015 0.00455

306.8 0.000012 0.00384

10.0 10.000012 0.000125

I I

-0.0866

0.000

-0.346

0.217

-0.346

0.0433

0.390

-0.346

-0.303

0.000

-2.382

-6.062

0.217

-0.390

-0.650

0.000

0.000

0.346

-0.433

-0.346

0.433

0.130

0.000

-0.0866

0.000119

-0.346

0.217

-0.346

0.0436

0.390

-0.346

-0.303

0.000670

-2.38060

-6.062

0.217

-0.390

-0.649

0.00126

0.0000667

0.347

-0.429

-0.344

0.438

0.134

0.000125

55

55

86

86

86

86

66

66

132

132

62

62

86

86

66

56

56

56

61

71

55

61

61

0.0388 10.10E-41

1 I 0.0439 I0.13E-41

0.0439 0.1E-41

0.0439 10.13E-41

1 1 0.0893 10.53E-41

0.0571 10.21E-41

0.0500 10.16E-41

I I I I

0.0500 10.16E-41

I I

I

0.0439 10.13E-41

II

0.131 10.000111

0.252 10.000421

1 1

0.0195 10.25E-51

II 0.0195 10.25E-51

1 1

0.0195 I0.25E-51

1 1 0.0748 I0.37E-41

I i 0.0748 10.37E-41

0.0119 10.96E-61

1o.0917 10.56E-41 0.0917 10.56E-41

0.0917 10.56E-41

0.0917 10.56E-41

0.0917 I0.56E-41

I I I I

0.0917 10.56E-41


PAGE a(.3HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS

I I IPIPEI PIPE

INO. NODES (I

PIPE DIAMETERI

FLOW NOM ACTUALI

US GPM)l (IN) (IN) I

PI PE/FTG

CODE LENGTH

# (FT)

TOTAL LENGTH

(FT)


PER FT. lOVER PIPE

I (PSI) I (PSI)

STATIC TOTAL IROUGHI WATER VELOC.I STATIC I TOTAL


I (PSI) I (PSI)

I ________ I ____________________ I __________________ I __________________________ I ______________________________ I ________________ I __________________ I ____________________ I __________________ ____________________ 0.00200 I 0.346 I -0.344 I

39

40

41

42

45

46

47

48

49

50

51

52

53

54

55

56

57

58

59

60

62

63

36 52

37 36

40 41

41 42

42 45

37 38

38 39

39 22

45 37

45 48

48 49

49 50

50 51

51 70

48 67

70 53

53 54

54 55

55 56

56 57

58 59

59 60

14.29

14.29

118.89

118.89

118.89

53.83

53.83

53.83

68.12

50.77

22.24

22.24

22.24

22.24

28.52

9.47

9.47

9.47

9.47

9.47

51.64

51.64

7.98 CSAM

7.98 CSAM

8 I1GV

8 ITT

8 4SE

8 3HE

10.02 CSAM

10.02 CSAM

10 IHE

10 1GV

10 ICV 10 ISE

10.02 CSAM

10 ITT

7.98 CSAM

8 1GV

8 ISE

8 2HE

11.20 CSAM

12 3SE

12 2HE

12 4ZSE

12 3ZSE

11.20 CSAM

7.98 CSAM

8 ITT

9.56 CSAM

10 5SE

10 2GV

10 IHE

10.02 CSAM

10 ITT

10.02 CSAM

10.02 CSAM

10.02 CSAM

10.02 CSAM

10 7SE

7.98 CSAM

8 7SE

8 IHE

8 IGV

7.98 CSAM

7.98 CSAM

8 2HE

7.98 CSAM

8 4HE

7.98 CSAM

6.07 CSAM

6.07 CSAM

160.0160.0

160.0

0.5

4.5

9.3

3.5

17.0

15.4

1.1

0.5

5.6

2.2

35.1

5.1

15.1

0.4

1.7

1.7

230.0

69.1

22.2

28.0

9.0

59.3

3.5

3.4

255.0

9.0

0.8

0.9

6.0

14 .7

1.0

2.3

11.7

115.9

45.3

118 .3

35.1

2.5

1.1

15.5

107.6

5.0

15.1

10.0

1.0

6.8

30.8

160.0 0.000012

177.9 10.000026

17.0 10.000584

24.9 10.000584

40.2 10.000584

19.0 10.000408

358.2 10.00000671

1 I

1 1

59.3 10.00000671

6.9 10.000631 1

265.7 10.000152

20.7 10.00000901

1 11.0 2.3

10.00000901

10.00000901

11.7 l0.00000901

161.3 10.000014 I

1 I 157.0 10.00000561

1 I 1 I

15.5 10.00000561

112.6 10.00000561

I 1 25.1 10.00000561

I 1 1.0 10.00000561

6.8 10.000499 1

30.8 10.000499 1

IROUGHI WATER I NESS IVELOCITYI

ICOEFFI(FT/SEC)l

VELOC. PRESS.

(PS I)

I 1 ___ _ _ _

I0.00200 0.00465

0.00993

0.0145

0.0235

0.00774

0.00240

0.000398

0.00434

0.0403

0.000188

0.0000090

0.0000212

0.000106

0.00232

0.000890

0.0000878

0.000638

0.000142

0.0000056

0.00337

0.0154

______ I _____ I _______ I ________ I ____ I _____ I ______ I _____ I ______ I ___ I ____ ____ I

DX-24

U2TB Hose St

-0.346 -0.344 0.693 0.697

4.720 4.730

0.000 0.0145

0.000 0.0235

0.0433 0.0510

0.0433 0.0457

0.173 0.174

0.000 0.00434

8.054 8.095

2.598 2.598

0.433 0.433

0.996 0.996

5.066 5.066

-1.516 -1.513

2.382 2.383

0.000 10.0000878

0.000 1 0.000638

0.000 1 0.000142

0.000 10.0000056

0.000 1 0.00337

0.000 I 0.0154

61

41

35

35

35

35

132

132

35

35

62

62

62

62

62

62

62

62

62

62

62

62

0.0917 10.56E-41 0.0917 10.56E-41

0.484 10.0015

0.484 10.0015

0.484 0.0015

0.345 10.000801

I 1

1 1 I 1

i

0.175 10.000201

0.437 10.0012 1

1 1

0.227 10.000341

1 1 1 I

1 1

0.0905 0.550-4

1 1

0.0905 10.55E-41

0.0905 10.55E-41

0.0905 10.55E-41

0.116 10.90E-41

0.0607 10.24E-41

I I II II

0.0607 10.24E-41

0.0607 10.24E-41

1 1

0.0607 10.24E-41

0.0607 10.24E-41

0.573 10.0022 1

0.573 0.0022 1

AMENDMENT 13 Calc- No. DREOO-OOOS Rev ision 0 Attachment B


PIPE DIAMETERI

PIPE FLOW I NOM ACTUALI

NODES (US GPM) (IN) (IN) I

PIPE/FTG

CODE LENGTH

# (FT)

TOTAL IHEAD LOSSIHEAD LOSS I STATIC I TOTAL IROUGHI WATER

LENGTH I PER FT. OVER PIPE HEAD LOSSIHEAD LOSS INESS IVELOCITYI

(FT) I (PSI) I (PSI) I (PSI) I (PSI) ICOEFFI(FT/SEC)l

____________ __________ _______________I _________________ _________ __________ ______ I ______ I ___ I _____ I ____ I

86.6 0.000814

63.1 0.000814

0.0797

0.0704

0.0514

I 130.3 1 159.7 10.000499

__________________ I ________________ I _______________________ I ___________________________ I ______________ I ________________ I __________________ I _________________ I __________________ l...................I ______________ I ____________ I

IX-25

U2TB Hose St PAGE ,i4-,

VELOC.

PRESS.

(PSI)

64

65

66

67

68

69

70

71

72

73

74

75

76

77

78

79

80

81

82

83

84

60 61

62 61

63 62

64 63

80 64

69 80

67 69

81 63

98 81

79 98

78 79

77 78

76 77

75 76

74 75

73 74

72 73

71 72

68 71

70 68

82 102

51.64

67.25

67.25

54.47

28.52

28.52

28.52

12.77

12.77

12.77

12.77

12.77

12.77

12.77

12.77

12.77

12.77

12.77

12.77

12.77

25.95

6.07

6

6

6

6.07

6

6

6.07

6

6

6

7.98

8

8

8

8

10.02

10

10.02

10.02

6.07

6

6.07

6

6

6

6.07

6

6

6.07

6

6.07

6

6

6

6.07

6

7.98

7.98

7.98

7.98

7.98

8

8

7.98

8

10.02

10

10.02

I-

CSAM

3SE

4HE

ITT

CSAM

3SE

2HE

CSAM

4SE

yGV

ITT

CSAM

9SE

2TT

1GV

2HE

CSAM

1GV

CSAM

CSAM

CSAM

1GV

CSAM

3SE

2TT

1HE

CSAM

2SE

2HE

CSAM

2HE

CSAM

4SE

2HE

IGV

CSAM

2SE

CSAM

CSAM

CSAM

CSAM

CSAM

4SE

IHE

CSAM

3SE

CSAM

IGV

CSAM

12.4

8.2

8.8

70.1

12 .4

4.1

36.9

16.5

0.9

8.8

86.8

45.2

19.5

1.1

5.0

5.3

1.5

2.2

3.3

84.8

0.9

32 . 3

12.4

17.7

2.1

122.0

8.2

4.1

65.8

4.1

175.7

16.5

4.1

0.9

21.5

8.2

14.5

1.8

103.6

15.6

54.8

20.1

2.5

89.8

15.1

2.3

1.5

10.5

157.6 10.000145 0.0228

6.8 10.000014 10.0000981

1 1 2.2 10.000014 0.0000313

3.3 0.00014 10.0000469

85.7 10.0000371 0.00322

I I 64.3 10.0000371 0.00242

134.4 10.0000371 0.00505

70.0 10.000037 1 0.00263

1 1 197.2 10.000037 0.00740

29.7 10.000037 0.00112

14.5 10.00000981 0.000143

1.8 10.000009810.0000173

103.6 10.00000981 0.00102

15.6 10.00000981 0.000154

77.3 10.00000981 0.000763

1 I

104.9 10.00000981 0.00103

3.8 I0.000003210.0000124

I 1 10.5 10.000012 1 0.000127

I 1

-0.0433 0.0364

-3.507 -3.437

-3.074 -3.023

18.880 18.903

0.000 10.0000981 1

I I 0.000 10.0000313

0.000 0.0000469

-0.0433 1 -0.0401

8.011 8.013

-1.429 -1.424

0.000 0.00263

-0.433 -0.426

0.000 0.00112

0.000 0.000143

0.000 10.0000173 1

0.000 0.00102

0.000 0.000154

-1.299 -1.298

2.512 2.513

0.953 0.953

0.000 0.000127

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

0.573 10.0022 1

1 1

I 1

0.747 10.0037 1

1 1

0.747 10.0037 1

1 I I 1

0.349 10.000821

1 1 1 1 1 1

0.116 0.90E-4

0.116 10.90E-41

0.116 I0.9E-41

0.142 10.000131

I 1

0.142 10.000131

0.142 10.000131

1 1 1 1

0.142 10.000131 1 1

0.142 10.000131 1 1

0.0142 0.45E-41

1 1 1 1

0.142 10.000131

1 1

0.0819 10.45E-41

0.0819 10.45E-41

0.0819 10.45E-41

0.0819 10.45E-41

0.0819 10.45E-41

I I 1 1

0.0819 10.45E-41

1 1 0.0520 10.18E-41

1 1 0.106 10.75E-41

I I

AMENDMENT 13 r.Calc. No. DREOO-OOOS F Revision 0 ,i Attachment B


I I I IPIPEI PIPE

NO. NODES

I - 1 -1.....I ________________

85

86

87

90

91

93

94

95

96 97

98

99

1100

101

I102

1103

2I

31

82 91

91 92

92 93

88 82

88 89

87 88

838 87

83 96

65 83

46 65

29 46

86 82

85 86

860 85

84 97

66 84

PIPE DIAMETERI

FLOW I NOM ACTUALI

US GPM) (IN) (IN)

PIPE/FTG

CODE LENGTH

# (FT)

"TOTAL HEAD LOSSIHEAD LOSS

LENGTH PER FT. lOVER PIPE

(FT) I (PSI) I (PSI)

STATIC I TOTAL HEAD LOSSIHEAD LOSS

I (PSI) I (PSI)

IROUGHI WATER I VELOC.IROUGHI WATER I INESS IVELOCITYI

ICOEFFI (FT/SEC) IPRESS.

(PSI)

_____ ________ I _________ I _____ I _____ I ______ I _____ ______ I ___ _____ I ____

0.0866 I 0.0866 I 120 0.000 0.0000.00

0.00

0.00

12.22

0.00

12.22

12.22

12.22

12.22

12.22

12.22

13.73

13.73

13.73

13.73

13.73

10.02 CSAM

10 ITT 6.07 CSAM

6 2HE

6 I1GV

6 ITT

4.03 CSAM

4 2SE

4 6HE

10.02 CSAM

10 ITT

4.03 CSAM

4 IGV

4 8HE

6.07 CSAM

6 4SE

6 3HE

6 I1GV 6 ITT

6.07 CSAM

6 6SE

6 2HE

6 ITT

7.98 CSAM

8 2HE

8 ITT

7.98 CSAM

7.98 CSAM

8 5SE

8 2GV

8 I1SR

7.98 CSAM

8 ISE

8 IGV

8 ITT

10.02 CSAM

10 ITT

6.07 CSAM

6 2SE

6 3HE

6 1GV

6.07 CSAM

6 7SE

6 3HE

7.98 CSAM

B 2HE

8 ITT

7.98 CSAM

1.0

50.0

16.0

14.0

3.0

30.0

152.1

20.0

24.0

1.0

14.7

166.9

2.0

32.0

66.0

16.5

6.2

0.9

8.8

206.1

24 .7

4.1

8.8

14.2

5.0

9.8

1.5

31.3

25.1

2.2

19.5

112.0

5.0

9.8

1.0

14.7

48.5

8.2

6.2

0.9

168.5

28.9

6.2

14.3

5.0

9.8

1.5

51.0 0.000 0.000

63.0 0.000 0.000

196.1 0.000 0.000

15.7 10.0000030 0.0000471

1 1 200.9 0.000 0.000

98.4 0.000034 0.00340

243.8 0.000034 0.00843

28.9 10.00000901 0.000263

1 1 1 1

1.5 10.000009010.0000136

78.1 10.00000901 0.000709

1 1

I I

127.9 10.00000901 0.00116

15.7 10.000003710.0000585

63.8 10.000042 0.00274

I I

1 1

203.5 10.000042 0.00874

29.1 0.000011 0.000328

1.5 10-000011 10.0000169

II

0.0866

0.346

0.000

-0.130

0.303

3.811

5.196

5.846

-0.650

3.248

0 .433

0.000 0.

3.681

5.196

-5.846

-0.650

0.0866

0.346

0.000

-0.130

0.303

3.814

5.205

-5.846

-0.650

3.248

0.434

0000585

3.683

5.205

-5.845

-0.650

120

120

120

62

120

62

62

62

62

62

62

62

62

62

62

62

__ _ _I_ _ _ I_ _ _ _ I_ _ _ __I _I__ -I- _ _1_ 11 1 _ __ 1 _ _ 1_ I1 __1_ I I _ _ _ I _

IX-26

U2TB Hose StP A G E J3 1 -5

0.000 0.000

0.000 0.000

0.000 0.000

0.0497 10.16E-4

0.000 0.000

0.136 10.00012

0.136 10.00012

0.0784 10.41E-4

0.0784 10.41E-4

0.0784 10.41E-4

0.0784 10.41E-4

0.0559 I0.21E-4

0.153 0.00015

0.153 0.00015

0.0881 0.52E-4

0.0881 10.52E-4


PAGE 6 lbHYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS

PIPE DIAMETERI

FLOW NOM ACTUALI

(US GPM)I (IN) (IN) I

PI PE/FTG

CODE LENGTH

# (FT)

TOTAL

LENGTH

(FT)

HEAD LOSSIHEAD LOSS

PER FT. OVER PIPE

I (PSI) I (PSI)

I STATIC I TOTAL ROUGH I WATER I VELOC.ISTATIC ITOTAL HEAD LOSSIHEAD LOSS

I (PSI) (PSI)


ICOEFFI (FT/SEC)l

I I I _____ ________ I _________ I _____ _____ I ______ I _____ I ______ I ___ I _____ ____ 3.248 3 248 62 I 0.0881 I0.52E-4I

Ii

I'

I]

I:

I:

04

105

06

110

300

302

303

304

305

500

501

502

503

504

505

47 66

28 47

51 812

102 64

24 200

201 58

202 201

831 202

57 201

97 400

400 401

401 402

96 403

403 404

404 405

13.73

13.73

0.00

25.95

2.85

51.64

42 .17

42.17

9.47

0.00

0.00

0.00

0.00

0.00

0.00

8

8

8

8

8

8

8

8

8

8

8

8

6

6

10

6

6

6

6

6 6

6

4

4

4

6

6

6

6

6

4

4

4

7.98 CSAM

4SE

2GV

ISR

7.98 CSAM

ISE

1GV

ITT

7.98 CSAM

ITT

1GV

ISE

10.02 CSAM

7.98 CSAM

5SE

IGV

ITT

6.07 CSAM

1GV

4HE

10.02 CSAM

2TT

6.07 CSAM

6.07 CSAM

ISE

IGV

2HE

6.07 CSAM

IHE

6.07 CSAM

2SE

4HE

ITT

IGV

4.03 CSAM

3SE

ITT

2GV

6.07 CSAM

IHE

6.07 CSAM

ITT

2SE

3HE

1GV

4.03 CSAM

ITT

3SE

2GV

_____ I _____ I _______ I ________ I ____ I _____ ______ I _____ I _____ I ___ I ____ ____ I

U2TB Hose St

I I IPIPEI

I NO.

PIPE

NODES

VELOC. PRESS.

(PSI)

27.8

20.1

2.2

19.5

115.0

5.0

1.1

9.8

1.0

33 .1i

3.8

17.0

0.5

136.5

25.1

1.1

9.8

80.0

0.9

8.2

482.5

29.4

2.7

89.0

4.1

0.9

4.1

26.2

7.0

132.7

28.0

28 .0

30.0

3.0

52.2

30.0

20.0

4.0

7.8

7.0

132.3

30.0

28.0

21.0

3.0

47.0

20.0

30.0

4.0

69.6 10.

130.9 10.

55.0

0.5 10.

172.5 10.

89.1 10.

511.9 0.

2.7 10.

98.1 I0.

33.2 1

221.7

106.2

14.8

214.3

101.0

000011 0.000785

000011 0.00148

0.000 0.000

000012 10.0000060

612E-6 0.000105

000499 0.0445

000029 0.0152

000343 0.000926

000021 0.00212

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

11I

IX-27

3 .248

0.433

0.000

0.000

4.547

-0.650

8.877

3.464

0.000

0.000

41.354

-3.334

0.000

41.354

-3.334

3 .248

0 .435

0.000

0.0000060

4.547

-0.605

8.892

3.465

0.03212

0.000

41.354

-3.334

0.000

41.354

-3.334

62

62

120

62

62

62

62

62

62

120

120

120

120

120

120

0.0881 10.52E-41

0.000 0.000

0.106 10.75E-41

0.0183 10.22E-51

II

I 0.573 0.0022 1

I 1

0.172 10.000191

0.468 10.0014 1

0.105 I0.74E-41

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

AMENDMENT 13Calc. No. DREOO-000S Revision 0 Attachment B

PAGE 131 -7HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS

I I IPIPEI PIPE I•JA Nc•DF.

PIPE DIAMETERI

FLOW NOM ACTUALI

(US GPM)j (IN) (IN) I

PIPE/FTG

CODE LENGTH

# (FT)

TOTAL

LENGTH

(FT)

HEAD LOSSIHEAD LOSS I STATIC I TOTAL IROUGHI WATER I VELOC.1

PER FT. IOVER PIPE HEAD LOSS IHEAD LOSS NESS IVELOCITYi PRESS.

(PSI) I (PSI) (PSI) I (PSI) ICOEFFI(FT/SEC) (PSI)

.I -

600

1601

1602

1611

1612

1621

1651

719

725

1726

727

1750

751

75

175

175

57 600

24 601

602 24

601 611

611 612

602 621

61 651

719 23

18 725

726 18

18 727

700 701

701 16

702 17

21 703

4 704 602

5 705 704

6 727 705

0.00

1

1

3.04

5.89

0.00

0.00

0.00

118.89

40.36

8.61

13.47

4 .86

13.47

13.47

13 .47

11 .66

5.89

4.86

4.86

______ I _____ I _______ I ________ I ____ I _____ I ______ I _____ I ______ I ___ I _____ I ____ I

IX-28

U2TB Hose St

1.61 CSAM

1/2 ITT

1/2 2SE

1/2 1GV

7.98 CSAM

8 ISE

7.98 CSAM

8 5SE

8 2HE

8 IGV

6.07 CSAM

6 2SE

6 ITT

6.07 CSAM

6.07 CSAM

6 3SE

6 ITT

1.61 CSAM

1/2 ITT

1/2 2SE

1/2 IGV

7.98 CSANM

8 I2HE 11.20 CSAM

12 1GV

11.20 CSAM

12 IGV

11.20 CSAM

12 1GV

7.98 CSAM

8 I4HE

11.20 CSAM

7.85 CSAM

7.85 CSAM

8 ITT

7.98 CSAM

8 4SE

8 iHE

8 ITT

8 1GV

7.98 CSAM

8 7SE

8 2HE

8 1 TT

7.98 CSAM

8 2HE

8 ITT

13.5

8.0

8.0

1.0

10.8

5.0

123.0

25.1

5.0

1.1

4.5

28.0

30.0

1.0

3.6

42.0

30.0

49.1

8.0

8.0

1.0

5.9

5.0

6.8

2.3

4.5

2.3

2.1

2.3

72.8

8.0

29.3

41.9

26.0

10.1

58.7

20.1

2.5

9.8

1.1 1

221.9

35.1

5.0

9.8

141.3

9.2

17.9

30.5 0.000 0.000

15.8 0.693E-6 10.0000110

154.2 10.00000231 0.000363

1 I

62.5 0.000 0.000

1.0 0.000 0.000

75.6 0.000 0.000

66.1 0.439 1 29.048

10.9 10.000083 0.000903

1 I 9.1 10.498E-6 10.0000045

6.8 10.000001110-0000077

1 i 4.4 0.172E-6 10.00000076

1 I 80.8 10.000013 1 0.00110

1 i 29.3 10.000002610.0000764

41.9 10.00000641 0.000270

36.1 10.00000801 0.000290

1 1 92.1 10.00000231 0.000217

271.8 10.00000161 0.000448

1 1 1 1 1 1

168.3 I0.898E-6 0.000151

II II

I I

4.547 4.547

0.000 10.0000110 1

-1.429 -1.429

3.248 3.248

0.000 0.000

-0.433 -0.433

5.240 34.287

0.000 0.000903

0.000 10.0000045 1

0.000 10.0000077 1

0.000 10.000000761

0.563 0.564 1

0.217 0.217

-0.217 -0.216

0.606 0.607

-0.0866 -0.0864

7.448 7.448

0.866 0.866

120

62

62

120

120

120

120

62

86

86

86

55

55

86

66

62

62

86

0.000 0.000

0.0195 10.25E-51

1 1 0.0378 10.96E-51

II

0.000 I0.000

0.000 0.000

0.000 I0.000

18.736 2.362

0.259 10.000451

0.0280 10.52E-51

0.0439 10.13E-41

I i 0.0158 I0.16E-51

0.0864 10.50E-41

0.0439 10.13E-41

0.0893 10.53E-41

0.0773 10.40E-41

0.0378 10.96E-51

II

0.0312 10.65E-51

0.0312 10.65E-51

I

Calc. No. DREOO-OOOS AMENDMENT 13 Revision 0

Attachment B

PAGE 0 isHYDRAULIC CALCULATIONS - PIPE CHARACTERISTICS

I I PIPE DIAMETERI PIPE/FTG TOTAL

IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH

INO. I NODES (US GPM)I (IN) (IN) I # (FT) (FT)


I PER FT. JOVER PIPE

I (PSI) I (PSI)

STATIC TOTAL HEAD LOSSIHEAD LOSS

I (PSI) I (PSI)

IROUGHI WATER I VELOC.1

NESS IVELOCITYI PRESS.!

ICOEFFI(FT/SEC)I (PSI) i

I I I ____________ _____________ I _______ i __________ I _________ I

I I I I ___________ I ______ _______ I ________ I _______ I ________ ____ ______ _____ I 62 I �.0260 !0.45E.5

1757 1

1 I I I 1 1 1758 1

1 1 1 1

1760

1761

762 1

1 1 1763

1800

1802

1803

1804

1805

1806

807

1808

1809

706 704

923 706

27 720

720 721

919 723

724 719

928 802

802 803

834 800

800 801

56 805

49 849

849 814

849 815

77 808

1.03

1.03

L1.66

11.66

8.61

40.36

0.00

0.00

0.00

0.00

0.00

0.00

0.00

0.00

0.00

4.03 CSAM

4 8SE

4 4HE

4 IGV

4.03 CSAM

4 12SE

4 4HE

4 1GV

7.98 CSAM

8 ISE

8.39 CSAM

8 2HE

8.39 CSAM

8 1GV

7.85 CSAM

6.07 CSAM

6 ITT

6 1GV

6 2SE

4 .03 CSAM

4 2HE

4 ITT

4 4SE

4 IGV

6.07 CSAM

6 3SE

6 IHE

5.05 CSAM

5 7SE

5 4HE

7.98 CSAM

8 1HE

8 ITT

4.03 CSAM

4 3SE

4 2HE

4 1TT

4 IGV

4.03 CSAM

4 ISE

4 ITT

4 1GV

4.03 CSAM

4 4SE

4 IHE

4 IGV

2.47 CSAM

2 1/2 I iTT

2 1/2 I1GV

197.0

23.6

4.7

0.6

178.4

35.3

4.7

0.6

75.5

4.2

17.0

5.3

12.5

1.3

26.0

33.8

30.0

3.0

28.0

115.1

8.0

20.0

40.0

2.0

30.9

42.0

7.0

121.8

84.0

20.0

25.8

8.5

33.1

84.1

30.0

8.0

20.0

2.0

2.5

10.0

20.0

2.0

18.0

40.0

4.0

2.0

1.0

12.0

1.0

I ______ I _____ I ________ I _________ I _____ _____ I ______ I _____ I ______ I ___ I _____ I ____ I

LX-29

U2TB Hose St

225.9 10.00000261 0.0005921

219.0 10.00000261 0.000574 1

79.7 10.000010 0.000801

22.3 10.00000791 0.000176

13.8 i0.000004110.0000565 1

26.0 10.000049 0.00128

94.8 0.000 0.000

185.1 0.000 1 0.000

79.9 0.000 0.000

225.8 0.000 0.000

67.4 0.000 0.000

144.1 0.000 0.000

34.5 0.000 1 0.000

64.0 0.000 1 0.000

14.0 0.000 0.000

1.645 1.646

-7.058 -7.058

0.650 0.650

0.000 0.000176

0.000 10.0000565

0.000 0.00128

3.248 3.248

3.551 3.551

-7.794 -7.794

-4.027 -4.027

-11.562 -11.562

2.728 2.728

0.000 0.00(

1.169 1.16

-0.433 -0.43

62

62

56

56

59

86

120

120

120

; 120

120

120

0 120

9 120

3 120

0.0260 !0.45E-5

0.0260 ;0.45E-5:

0.0748 10.37E-41

0.0677 10.30E-4:

0.0500 10.16E-4;

1 I

0.268 10.000481

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 I0.000 I

0.000 0.000

0.000 1 0.000

0.000 0.000

0.000 0.000

0.000 0.000


U2T8 Hose St HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS

I I PIPE DIANETERI PIPE/FTG I TOTAL HEAD LOSSIHEAD LOSS I STATIC I TOTAL IROUGHI WATER I

IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH I PER FT. lOVER PIPE HEAD LOSSIHEAD LOSS NESS IVELOCITYI

NO. I NODES (US GPM) I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI) I (PSI) I (PSI) ICOEFFI (FT/SEC)

I I I I I

VELOC.

PRESS.

(PSI)

I I I 1 ~ 1 - 1 1 -______________ I ________I_________ __________I_________

1810

1811I

1812

1813

1814 1

1815 1

1816

819

1820

1821

1822

1823

1824

1826

1_

I- - - - 20 I 0.000 I 0.000 I

I ______________I ____________ __________________I ____________________ I____________ ____________ I______________ _____________ I__________________________I

IX-30

60 809

79 811

55 813

813 817

813 818

805 819

819 820

819 822

76 824

824 825

801 804

836 827

835 836

I . 824 826 I

0.00

4 4

0.00

3

3

3

0.00

8 18

18

0.00

2 1/2

2 1/2

0.00

8

0.00

0.00

6

6

6

0.00

6

6 16

0.00

8

8

8

0.00

6

6 16

0.00

3

0.00

5

5

0.00

6

6

6

6

6

0.00

6

6 6

I

4.03 CS

2S

I11 3.07 CS

4I 14

2(

7.98 C

4•

41

2.47 C

I

-7.98 C Ii

7.98 C

1

6.07 C

79

6.07 I

7.98

6.07

3.07

5.05

6.07

6.07

20 1o.o00o 0,0001AM

SE

T

SAM

SE

TT

GV

SAM

SE

HE

TT

SAM

TT

GV

SAM

GV

ZSAM

2SE

SAM

iHE

ITT

IGV

CSAM

OSE

IHE

1GV

CSAM

2SE

1TT

IHE

CSAM

ISE

CHE

1GV

CSAM

4TT

CSAM

4HE

8SE

CSAM

1GV

5SE

3HE

4TT

lC`V

CSAM

ITT

1HE

IGV

28.1

20.0

20.0

51.5

28.0

15.0

2.0

62.7

68.2

34.1

33 .1i

1.0

12.0

1.0

1.5

3.8

6.0

17.0

6.6

7.0

30.0

3.0

16.8

14.0

7.0

3.0

32.0

34.1

33.1

8.5

23.3

14.0

7.0

3.0

5.5

15.0

121.5

20.0

96.0

63.5

3.0

70.0

21.0

120.0

32.0

6.3

30.0

7.0

3.0

68.1

96.5

198.1

14.0

5.3

23.0

46.6

40.8

107.7

47.3 3

20.5

237.5

309.5

46.3

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

-2.165

-3.681

-13.207

0.000

-1.169

2.901

-4.114

-4.114

-13.943

0.000

0.000

-7.483

-3.992

0.000

-2 .165 1:

-3.681

-13.207

0.000

-1.169

2.901

-4.114

-4.114

-13.943

0.000

0.000

-7.483

-3.992

0.000

20

20

20

.20

120 J

120

120

120

120

120

120

120

120

0.000 0

0.000 0

0.000 0

0.000 0

0.000 I

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

.000

.000

'.000I

.000I

3.000I

0.000

0 .ooo

O.ooo

0.000

0.000

0.000

0.000

0.000

0.00

AMENDMENT 13Calc No. L)KLUU-UUU3 Revision 0 Attachment B


I I PIPE DIAMETERI

IPIPEI PIPE I FLOW NOM ACTUALI COI

NO. I NODES I (US GPM)I (IN) (IN) I#

1I 1 ...-....-... _____________ ____________ __________________I_____________________ ___________ ___________

1827 1

1828 I

829 1

1831

1832 I

I 1

I I

833 1

1 1 1 I

1834

1835

1836

1837

1839

1840

1841

102 855

200 839

839 831

42 837

61 832

98 833

54 834

73 835

833 828

828 829

96 838

838 845

75 823

I

PIPE/FTG

DE LENGTH

(FT)

TOTAL HEAD LOSSJHEAD LOSS I STATIC TOTAL

LENGTH PER FT. lOVER PIPE HEAD LOSSIHEAD LOSS

(FT) I (PSI) I (PSI) (PSI) I (PSI)

IROUGHI WATER I VELOC.INESSGH WATELOITY PRESS.

ICOEFFI (FT/SEC) I (PSI) I

0 000 I0.00

42.17

42.17

0.00

0.00

0.00

0.00

0.00

0.00

0.00

12.22

0.00

0.00

0.823 0.823 I 120 I 0.000 I 0.000 I

6.07 CSAM

6 ITT

6 I1GV

6 1HE

6 ISE

6.07 CSAM

6 ITT

6.07 CSAM

10.02 CSAM

10 2HE

6.07 CSAM

6 ISE

6 IGV

6 1TT

6.07 CSAM

6 ISE

6 ITT

6 I1GV

6.07 CSAM

6 2SE

6 2HE

6 2TT

6 IGV

6.07 CSAM

6 ITT

6 2SE

6 2HE

6 IGV

6.07 CSAM

6 9SE

6 2TT

6.07 CSAM

6 8SE

6 2HE

6 ITT

6.07 CSAM

6 IHE

6 I1GV

6 ITT

4.03 CSAM

4 SHE

4 2SE

4 ITT

4 I1GV

7.98 CSAM

8 ITT

8 2SE

8 IHE

4.4

30.0

3.0

7.0

14.0

2.3

8.8

3.0

11.0

22.0

9.9

14.0

3.0

30.0

25.6

14.0

30.0

3.0

28.6

28.0

14.0o

60.0

3.0

24.5

30.0

28.0

14.0

3.0

75.9

126.0

60.0

100.0

112.0

14.0

30.0

62.4

2.1

0.9

8.8

117.8

20.0

20.0

20.0

2.0

32.0

33.1

34.1

8.5

58.4 0.000

11.1 0.000343

3.0 0.000343

33.0 I 0.000

56.9 0.000

72.6 0.000

133.6 0.000

99.5 0.000

261.9 0.000

256.0 0.000

74.2 10.000034

179.8 0.000

107.7 0.000

______ I _____ I ________ I _________ I _____ I _____ I ______ I _____ I ______ I ___ I ____ I ____ I

IX-31

U2TB Hose St

0.000

0.00382

0.00103

0.000

0.000

0.000

0.000

0 .000

0.000

0.000

0.00257

0.000

0.000

0.823

-3.464

0.000

0.000

0.0433

1.429

-8.531

-8 .314

-0.684

-28.112

0.000

37.024

-13.943

0.823 120

-3.460 62

0.00103 62

0.000 120

0.0433 120

1.429 120

-8.531 120

-8.314 120

-0.684 120

-28.112 120

0.00257 62

37.024 120

-13.943 120

I--

PAGE i:3,26

0.000 0.000

0.468 0.0014

0.460 0.0014

0.000 0.000

0.000 0.000

0.000 0.0(00

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.136 10.000121

1 1 1 1

. 0

0.000 0.000

0.000 I0.000


PAGE E3z-HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS

I I PIPE DIAMETER! PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS

IPIPEi PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH PER FT. OVER PIPE

INO. I NODES (US GPM) (IN) (IN) # (FT) (FT) I (PSI) (PSI)

STATIC I TOTAL

HEAD LOSSIHEAD LOSS

I (PSI) I (PSI)

IROUGHI WATER I VELOC.I INESS IVELOCITYI PRESS.I

ICOEFFI(FT/SEC)i (PSI)

I I I t

I I I I _____________ I _______ I _______ I ________ I _______ ________ I ____ _______ I ______________________________

______________________________________________ o 000 I 0 000 120 0.000 0.000 I1842 1

I 1

1850 1

1 1 1 I

1851

1860

1861

1922

1925

1931

1932

809 810

93 850

89 851

97 860

860 861

19 919

23 923

928 28

29 929

0.00

0.00

0.00

13.73

0.00

8.61

40.36

2.08

2.08

3.07 CSAM

ISE

1GV

6.07 CSAM

1GV

2SE

ITT

4.03 CSAM

3SE

ITT

1GV

IHE 6.07 CSAM

IGV

IHE

4.03 CSAM

3HE

3SE

1TT

1GV

7.85 CSAM

7.98 CSAM

3SE

ITT

1GV

7.98 CSAM

7.98 CSAM

23.323. 3

7.0

1.0

12.5

3.0

28.0

30.0

12.9

30.0

20.0

2.0

4.0

51.5

0.9

2.1

119.8

12.0

30.0

20.0

2.0

29.2

21.2

15.1

9.8

1.1

98.2

2.5

31.3 0.000

73.5 0.000

68.9 0.000

54.4 10.000042

183.8 0.000

29.2 10.0000056

47.2 10.000083

1 1

98.2 I0.412E-6

2.5 I0.412E-6

0.0000.000

0.000

0.000

0.00234

0.000

0.000165

0.00392

10.0000404

,0.0000010

I I

1 - 1 1.......I- 1 -1_________ ____________I_________________ ____________________1 __ 1_ I1 _ _ _ _ _ I1 -_ _ _ _I_ _1 - 1_ _ _ __ _ I_

IX-32

U2TB Hose St

0.000 0.000

-2.598 -2.598

-2.382 -2.382

0.000 0.00234

38.020 38.020

0.476 0.476

12.774 12.778

0.000 10.0000404

0.000 I0.0000010

120

120

120

62

120

59

62

56

56

0.000 0.000

0.000 0.000

0.000 0.000

0.153 10.000151

1 1

0.000 0.000

0.0571 10.21E-41 0.259 10.000451

I I

I I 1 I

0.0133 0.11E-51

0.0133 10-11E-51

Caic. No. DREOO-OOOS AMENDMENT 13 Revision 0

Attachment B

HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS

COMPANY Nexus Technical Services Corporation IPAGE Z

DESIGNER BY BRIAN FOX CHECKED: IDATE 2000 JAN 6


PROJECT I Ul DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP

I JOB NO. IU2TB Hose Station F-B0

SPRINKLER/NOZZLE{N) POINTS REFERENCE POINTS INPUT POINTS POINT REQUIRED

ELEVATION DISCHARGE K-FACTORs

I NO. IDISCHG. GPM P.S.I. NO. IDISCHG. GPM I P.S.I. NO. IDEMAND GPM I P.S.I. (FT) I (US GPM)

1 149.937 500.000

2 145.823 509.500

3 143.009 516.000

4 145.260 510.800

5 145.260 510.800

6 145.260 510.800

7 145.475 510.300

8 145.777 509.600

9 145.777 509.600

i 0 143.221 515.500

I11 126.463 554.200

12 143.221 515.500

13 145.689 509.800

14 145.905 509.300

15 145.992 509.100

16 145.211 510.900

17 145.557 510.100

18 145.903 509.300

19 145.859 509.400

20 144.993 511.400

211 145.338 510.600 1 1

221 144.957 511.500 1

23 1 144.955 511.500

241 139.103 525.000

251 145.165 511.000

26 144.949 511.500

27 145.381 510.500

28 144.730 512.000

29 144.730 512.000

30 145.076 511.200

31 144.647 512.200

32 144.303 513.000

33 144.741 512.000

34 144.875 511.700

35 145.558 510.100

361 144.530 512.500

371 145.228 510.900

38 145.177 511.000

39 145.131 511.100

40 118.89 150.000 500.000

41 145.270 510.900

42 145.256 510.900

45 145.232 510.900

46 144.295 513.000

IX-33

AMENDMENT 13Caic. No. DRPUE-UUO0 Revision 0 Attachment B

U2TB Hose StHYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS

SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS I INPUT POINTS POINT REQUIRED I ELEVATION DISCHARGE K-FACTORI

NO. IDISCHG. GPM P.S. . NO. IDISCHG. GPM P.S.I. NO. IDErAND GPM I P.S.I. I (FT) (US GPM) I

47 144.295

48 137.138

49 134.539

50 134.106

51 133.110

52 144.875

53 125.661

54 125.661

55 125.660

56 125.660

57 125.660

58 126.263

59 126.260

60 126.245

61 126.208

62 122.771

63 119.748

64 138.651

65 141.047

66 141.047

67 138.651

68 127.091

69 138.651

70 128.044

I71 124.578

72 125.877

73 125.877

74 125.876

I 75 125.876

76 125.875

77 125.874

78 126.300

79 126.297

80 138.651

81 119.708

82 138.651

83 141.697

84 141.696

85 142.334

86 138.651

87 142.335

88 138.521

89 138.218

91 138.564

92 138.218

93 138.218

96 147.542

97 147.542

98 127.721

513.000

I I

______________ ______________I............ _____________ I______________I.........l______________ _____________ _____________II_______I___

IX-34

PAGE 0 2-

513.000 529.500

535.500

536.500

538.800

511.700

556.000

556.000

556.000

556.000

556.000

554.500

554.500

554.500

554.400

562.500

569.600

526.000

520.500

520.500

526.000

552.700

526.000

550.500

558.500

555.500

555.500

555.500

555.500

555.500

555.500

554.500

554.500

526.000

569.700

526.000

519.000

519.000

517.500

526.000

517.500

526.300

527.000

526.200

527.000

527.000

505.500

505.500

551.200

AMENDMENT 13Calc. No. DKLUU-0UUW Revision 0 Attachment B

U2TB Hose StPAGE BZ4-


SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS I INPUT POINTS POINT REQUIRED

ELEVATION DISCHARGE

INO. DISCHG- GPM P.S.I. NO. IDISCHG. GPM P.S.I. NO. IDEMAND GPM I P.S.I. I (FT) I (US GPM)

IK- FACTOR I

I I I I

102 138.651

200 134.556

201 125.658

202 134.550

400 147.542

401 106.188

402 109.522

403 147.542

404 106.188

405 109.523

600 121.114

601 139.103

602 137.674

611 135.855

612 135.855

1 621 138.107

651 1 118.89 91.921

700 145.992

701 145.428

702 145.341

7031 144.732 1 I

704 1 137.588 1

7051 145.037

7061 139.234

719 1 144.955

1 -7201 144.731

1 721 144.731

723 145.383

724 144.957

725 145.903

726 145.903

7271 1 145.903

800 141.986

801 146.013

802 141.482

803 137.931

804 146.013

8051 137.222

1 8081 126.307

1 809 128.410

810 128.410

811 129.978

812 133.110

813 138.868

I I814 131.811

I 815 130.642

I 817 138.868

I 818 140.037

I 819 134.321

-I26.000

526.000 535.500

556.000

535.500

505.500

601.000

593.300

505.500

601.000

593.300

566.500

525.000

528.300

532.500

532.500

527.300

566.500

509.100

510.400

510.600

512.000

528.500

511.300

524 .700

511.500

512.000

512.000

510.500

511.500

509.300

509.300

509.300

518.300

509.000

519.500

527.700

509.000

529.300

554.500

549.500

549.500

546.000

538.800

525.500

541.800

544.500

525.500

522.800

536.000

100.00 12.400

_____________________ ____________________ I ________ _____________________I ____________________ I................I _____________________I ____________________ I _____________________I _________________ I______________ I

IX-35

I


U2T8 Hose St HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS PAGE F

SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS INPUT POINTS POINT REQUIRED

ELEVATION DISCHARGE K-FACTC=.

I NO. DISCHG. GPM I P.S.I. NO. IDISCHG. GPM I P.S.I. I NO. DEMAND GPM I P.S.I. I (FT) (US GPM)

820 138.435 526.500

822 138.435 526.500

823 139.819 523.300

824 139.819 523.300

825 139.819 523.300

826 139.819 523.300

827 145.666 509.800

828 126.976 552.920

829 155.088 488.000

831 138.016 527.500

832 126.165 554.500

833 126.292 554.500

834 134.192 536.300

835 134.191 536.300

836 138.183 527.080

I 837 145.256 510.900

838 147.540 505.500

839 138.017 527.500

845 110.516 591.000

849 131.811 541.800

850 140.816 521.000

851 140.599 521.500

855 137.828 527.900

860 1 147.539 505.500

861 1 109.520 593.300

919 1 145.383 510.500

923 132.176 541.000

928 144.730 512.000

929 144.730 512.000

IX-36


WARNING: THE FOLLOWING PIPE(S) HAVE FLOW(S) SMALLER THAN 0.1 GPM

2 3 4 85 86 87 91 106 500

501 502 503 504 505 600 611 612 621 800

802 803 804 805 806 807 808 809 810 811

812 813 814 815 816 819 820 821 822 823

824 826 827 831 832 833 834 835 836 837

840 841 842 850 851 861

MAXIMUM UNBALANCED HEAD LOSS= .00001 IN LOOP # I

IX-37

AMENDMENT 13

15X-

Calc. No. DREO0-000S Revision 0 Attachment B

[,•ý b2-7 -F P-/-7

'P

1131R

IE

is

Is

IU

761 R

IE

X is operating point for

Co-ordinates are

FLOW = 118.89

PRESSURE - 150.00

SPECIFIED pressure

0 1635 3268 4901

Pump Curve Input Point No.

FLOW

40

IX-38

391

AMENDMENT 13


ATTACHMENT C

SPRINK-1000 OUTPUT FIRE HOSE STATION

DATA F-75

IX-39

AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0

Attachment C

DESIGN PROGRAM FOR SPRINKLER SYSTEMS C cl

by



VERSION 11.00

COMPANY : Nexus Technical Services Corporation

DESIGNER BY: BRIAN FOX CHECKED:,f_;-L . -I&'' CLIENT : CornEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis

PROJECT Ul DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP

JOB NO. : U2TB Hose Station F-75

FIX

C-62

P 01 01 02 3.5 11.938

P 02 02 03 16.1 11.938 1GV ITT 3SE CV

P 03 03 04 21.2 7.981 2SE

C-132

P 04 04 05 60.0 11.2 HE SE 3ZSE(7)

P 05 05 06 13.5 11.2 TT GV

C-66

P 06 06 07 156.6 7.85

P 07 07 08 161.0 7.85

P 14 08 13 86.0 7.981 ITT

C=55

P 15 13 14 54.6 7.981

P 750 700 701 72.8 7.981 4HE

P 16 14 15 14.1 11.2 GV

P 17 15 700 44.5 11.2 GV

P 751 701 16 29.3 11.2

C-86

P 18 16 35 9.1 11.2

P 19 35 702 82.7 11.2 HE

P 752 702 17 41.9 7.85

P 20 17 726 119.6 7.85 HE

P 21 725 19 97.9 7.85

P 725 18 725 6.8 11.2 GV

P 726 18 726 4.5 11.2 GV

P 727 18 727 2.1 11.2 GV

C-59

P 762 723 919 12.5 8.385 GV

P 922 919 19 29.2 7.85

C-66

P 22 20 723 82.2 8.385 TT SE ZSE(5)

P 23 20 21 133.3 8.385 TT 3HE GV

P 30 27 703 4.0 7.981 1GV

P 753 703 21 26.0 7.85 TT

C-86

P 29 21 26 147.0 7.981 ITT

P 28 26 25 146.0 7.981 2SE

C-62

P 27 25 601 81.9 7.981 6SE 1GV

P 601 601 24 10.8 7.981 ISE

P 754 602 704 58.7 7.981 4SE iHE lTT lGV

P 602 602 24 123.0 7.981 5SE 2HE GV

P 755 704 705 221.92 7.981 7SE 2HE ITT

C-86 [X-40

AMENDMENT 13 Cakc No. DREOO-OOOS Revision 0

P 756 705 727 141.27 7.981 2HE ITT

C=62

P 300 24 200 136-5 7.981 5SE 1GV ITT

P 26 200 923 7.5 7.981 ISE ITT 1GV

p 757 704 706 197.01 4.026 8SE 4HE GV

P 758 706 923 178.37 4.026 12SE 4HE GV

P 925 923 23 21.25 7.981 3SE ITT IGV

C=132

P 25 22 724 75.0 11.2 TT 4HE

C-62

P 719 719 23 5.86 7.981 2HE

C-86

P 763 724 719 26.0 7.85

C-132

P 24 05 22 149.9 11.2 GV TT

C-35

P 50 45 48 255.0 9.564 5SE 2GV IHE

***********************************

NOTE *

/* THE FOLLOWING PIPES HAD A*

/* CALCULATED C FACTOR OF 27.4. DUE*

/- TO LIMITATIONS OF THE SPRINK*

/* PROGRAM, A C OF 35 WAS USED*


/* ADJUSTED TO REFLECT EQUIVALENT*

/ FRICTION LOSS.*

/- ACTUAL LENGTHS ARE AS FOLLOWS:*

/-PIPE 41 - 10.8*

/-PIPE 42 - 9.8*

/-PIPE 45 = 22.3*

/-PIPE 46 = 10.0"

/-PIPE 49 = 2.0*

P/....... **..****

P 41 40 41 17.0 10.02

P 42 41 42 15.4 10.02 IHE 1GV 1CV ISE

P 45 42 45 35.1 10.02 ITT

P 46 37 38 15.1 7.981 IGV SE 2HE

P 49 45 37 3.5 7.981 ITT

C-132

P 47 38 39 230.0 11.2 3SE 2HE 4ZSE(7) 3ZSE(3)

P 48 39 22 59.3 11.2

C-62

P 55 48 67 115.92 10.02 7SE

P 70 67 69 3.25 10.02

P 69 69 80 2.17 10.02

P 68 80 64 5.33 10.02 1GV

P 67 64 63 86.75 7.981 9SE 2TT 1GV 2HE

P 66 63 62 36.93 6.065 4SE IGV ITT

P 65 62 61 70.08 6.065 3SE 2HE

P 64 61 60 130.25 6.065 3SE 4HE ITT

P 63 60 59 30.83 6. 065

P 62 59 58 6.75 6.065

P 302 58 201 80.0 6.065 1GV 4HE

P 303 201 202 482.5 10.02 2TT

P 305 57 201 89.0 6.065 ISE 1GV 2HE

P 60 56 57 1.0 7.981

P 59 55 56 15.08 7.981 4HE

P 58 54 55 107.58 7.981 2HE

P 57 53 54 15.5 7.981

Attachment C

p." 'c-- c_.z.

IX-41


P 56 70 53 118.25 7.981 7SE IHE 1GV Attachment C

P 54 51 70 11.67 10.02

P 53 50 51 2.33 10.02

P 52 49 50 1.0 10.02

P 51 48 49 6.0 10.02 ITT

P 8 8 9 30.0 7.981 IGV

p 9 9 10 110.0 4.026 2SE IHE 2TT IGV

P 10 10 12 215.42 4.026 15SE 7HE 2GV ITT

P 11 10 11 77.5 4.026 5SE 2HE 1GV

P 12 11 12 80.25 4.026 8SE 4HE 1GV

P 13 12 15 34.75 4.026 4SE 1GV ITT

P 83 70 68 2.33 10.02 1GV

P 82 68 71 89.83 7.981 3SE

P 81 71 72 54.75 7.981 4SE IHE

P 80 72 73 15.58 7.981

P 79 73 74 103.58 7.981

P 78 74 75 1.75 7.981

P 77 75 76 14.50 7.981

P 76 76 77 21.50 6.065 2SE

P 75 77 78 175.67 6.065 4SE 2HE 1GV

P 74 78 79 65.83 6.065 2HE

P 73 79 98 122.0 6.065 2SE 2HE

P 72 98 81 32.25 6.065 3SE 2TT IHE

P 71 81 63 84.83 6.065 IGV

P 110 64 102 0.5 10.02

P 84 102 82 10.5 10.02

P 99 82 86 1.0 10.02 ITT

P 100 86 85 48.5 6.065 2SE 3HE IGV

P 102 97 84 14.33 7.981 2HE ITT

P 103 84 66 1.50 7.981

P 104 66 47 27.75 7.981 4SE 2GV SR

P 105 47 28 115.0 7.981 ISE 1GV ITT

C-56

P 31 28 721 125.0 7.981

P 761 721 720 17.0 8.385 2HE

P 760 720 27 75.5 7.981 ISE

C-62

P 90 82 88 1.00 10.02 ITT

P 93 88 87 66.0 6.065 4SE 3HE 1GV ITT

P 95 96 83 14.17 7.981 2HE ITT

P 96 83 65 1.50 7.981

P 97 65 46 31.25 7.981 5SE 2GV 1SR

P 98 46 29 112.0 7.981 ISE IGV ITT

C-56

P 932 29 929 2.5 7.981

P 32 929 928 184.0 8.425 2SE 5HE 2GV

P 931 928 28 98.2 7.981

P 33 30 29 20.0 7.981

C-41

P 40 37 36 160.0 7.981 1GV ITT 4SE 3HE

C-61

P 39 36 52 160.0 7.981

P 38 52 34 10.00 7.981

P 37 34 33 280.0 7.981 5SE iHE

C-55

P 36 33 32 300.0 7.981

C-71

P 35 32 31 285.0 7.981

C-61

P 34 31 30 285.0 7.981 IX-42

AMENDMENT 13

........................

NOTE*

/ THE FOLLOWING PIPES WERE

/ ADDED TO ATTACH SYSTEMS *

/ TO THE BASE MODEL * */********************************

C=120

P 611

P 612

P 621

P 834

R 834

P 803

R 800

P 804

R 801

P 822

R 804

P 805

R 805

P 815

R 819

P 816

R 820

P 819

R 822

P 809

R 808

P 106

R 812

P 806

P 808

P 807

R 849

R 814

R 815

P 810

R 809

P 842

R 810

P 81)

R 811

P 83:

R 83:

P 83'

R 821

P 83

R 82'

P 83

Calc. No. DREO0-0008 Revision 0 Attachment C

601 611 4.5 6.065 2SE ITT

611 612 1.0 6.065

602 621 3.6 6.065 3SE ITT

54 834 28.6 6.065 2SE 2HE 2TT IGV

536.3

834 800 30.9 6.065 3SE 1HE

518.3

800 801 121.75 5.047 7SE 4HE

509.0

801 804 5.5 3.068 ITT

509.0

56 805 25.75 7.981 1HE ITT

529.3

805 819 6.0 7.981 ISE

536.0

819 820 6.58 6.065 iHE ITT IGV

526.5

819 822 16.75 6.065 ISE 1HE 1GV

526.5

77 808 1.0 2.469 ITT IGV

554.5

51 812 1.0 7.981 ITT 1GV ISE

538.8

49 849 84.1 4.026 3SE 2HE ITT 1GV

849 815 18.0 4.026 4SE IHE IGV

849 814 2.5 4.026 lEE ITT 1GV

541.8

541.8

544.5

60 809 28.08 4.026 2SE ITT

549.5

809 810 23.33 3.068 ISE 1GV

549.5

79 811 51.5 3.068 4SE ITT 2GV

546.0

3 98 833 25.58 6.065 ISE ITT IGV

3 554.5

6 833 828 75.92 6.065 9SE 2TT

8 552.92

7 828 829 100 6.065 8SE 2HE ITT

9 488.0

2 61 832 9.9 6.065 ISE 1GV ITT

R 832 554.5

P 835 73 835

R 835 536.3

P 812 55 813

R 813 525.5

P 813 813 811

R 817 525.5

P 814 813 811

R 818 522.8

P 841 75 823

R 823 523.3

24.5 6.065 ITT 2SE 2HE 1GV

62.7 7.981 4SE 4HE ITT

7 1.0 2.469 ITT

8 1.5 7.981 IGV

32.0 7.981 ITT

IGV

2SE IHE

IX-43

AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0 Attachment C

P 820 76 824 32.0 7.981 2SE ITT IHE

R 824 523.3

P 821 824 825 23.25 6.065 ISE 1HE 1GV

R 825 523.3

P 826 824 826 6.3 6.065 ITT 1HE 1GV

R 826 523.3

P 850 93 850 12.5 6.065 1GV 2SE iTT

R 850 521.0

P 87 92 93 152.1 4.026 2SE 6HE

P 86 91 92 16.0 6.065 2HE 1GV ITT

P 85 82 91 1.0 10.020 ITT

* 91 526.2

* 92 527.0

R 93 527.0

P 851 89 851 12.9 4.026 3SE ITT 1GV 1HE

R 851 521.5

P 91 88 89 166.9 4.026 GV 81HE

R 89 527.0

P 800 928 802 33.83 6.065 ITT IGV 2SE

R 802 519.5

P 802 802 803 115.08 4.026 2HE ITT 4SE IGV

R 803 527.7

P 840 838 845 117.8 4.026 5HE 2SE ITT iGV

R 845 591.0

C-62

P 839 96 838 62.4 6.065 1HE 1GV ITT

P 94 838 87 206.1 6.065 6SE 2HE ITT

P 860 97 860 51.5 6.065 iGV 1HE

P i01 860 85 168.5 6.065 7SE 3HE

C-120

R 838 505.5

P 861 860 861 119.75 4.026 3HE 3SE TT GV

R 860 505.5

R 861 593.3

P 827 102 855 4.39 6.065 ITT iGV 1HE ISE

P 831 42 837 11.0 10.02 2HE

P 824 835 836 63.5 6.065 iGV 5SE 3HE 4TT iCV

R 836 527.08

P 823 836 827 121.5 5.047 4HE 8SE

R 827 509.8

R 837 510.9

R 855 527.9

C-62

P 828 200 839 2.3 6.065 iTT

P 829 839 831 3.0 6.065

P 304 831 202 2.7 6.065

C-120

R 839 527.5

R 831 527.5 / **********.*.************

END *

*/.........**fl.**.***** * A.....

C-120

P 500 97 400 26.17 6.065 IHE

P 501 400 401 132.67 6.065 2SE 4HE ITT 1GV

P 502 401 402 52.17 4.026 3SE iTT 2GV

P 503 96 403 7.75 6.065 IHE

P 504 403 404 132.33 6.065 ITT 2SE 3HE iGV

P 505 404 405 47.0 4.026 ITT 3SE 2GV

/-....... .**.......* . * ........ * ....*

Attc C

IX-44


/* The following nodes and pipes Attachment C

/ r refer to hose stations. o To

/" switch between hose stations, Cf.

/ change the S to an R and remove *

/, the flow and K-factor on the hose *

/* stations that you do not want *

/* to flow. *

/ HOSE STATION F-75

P 600 57 600 13.5 1.610 TT 2SE GV

S 600 566.5 100 12.4

/HOSE STATION F-80

P 651 61 651 49.1 1.610 TT 2SE GV

R 651 566.5 * A************* * *********

END *

R 02 509.5

R 03 516.0

R 04 510.8

R 05 510.8

R 06 510.8

R 07 510.3

R 08 509.6

R 09 509.6

R 10 515.5

R 11 554.2

R 12 515.5

R 13 509.8

R 14 509.3

R 15 509.1

R 16 510.9

R 17 510.1

R 18 509.3

R 19 509.4

R 20 511.4

R 21 510.6

R 22 511.5

R 23 511.5

R 24 525.0

R 25 511.0

R 26 511.5

R 27 510.5

R 28 512.0

R 29 512.0

R 30 511.2

R 31 512.2

R 32 513.0

R 33 512.0

R 34 511.7

R 35 510.1

R 36 512.5

R 37 510.9

R 38 511.0

R 39 511.1

R 41 510.9

R 42 510.9

R 45 510.9

R 46 513.0

R 47 513.0 IX-45

AMENDMENT 13

R 48 529.5

R 49 535.5

R 50 536.5

R 51 538.8

R 52 511.7

R 53 556.0

R 54 556.0

R 55 556.0

R 56 556.0

R 57 556.0

R 58 554.5

R 59 554.5

R 60 554.5

R 61 554.4

R 62 562.5

R 63 569.6

R 64 526.0

R 65 520.5

R 66 520.5

R 67 526.0

R 68 552.7

R 69 526.0

R 70 550.5

R 71 558.5

R 72 555.5

R 73 555.5

R 74 555.5

R 75 555.5

R 76 555.5

R 77 555.5

R 78 554.5

R 79 554.5

R 80 526.0

R 81 569.7

R 82 526.0

R 83 519.0

R 84 519.0

R 85 517.5

R 86 526.0

R 87 517.5

R 88 526.3

R 96 505.5

R 97 505.5

R 98 551.2

R 102 526.0

R 200 535.5

R 201 556.0

R 202 535.5

R 400 505.5

R 401 601.0

R 402 593.3

R 403 505.5

R 404 601.0

R 405 593.3

R 601 525.0

R 602 528.3

R 611 532.5

R 612 532.5

R 621 527.3

R 720 512.0

Calc. No. DREOO-OOOS Revision 0 Attachment C

phq-C-Il

IX-46

R 721 512.0

R 723 510.5

R 724 511.5

R 700 509.1

R 701 510.4

R 702 510.6

R 703 512.0

R 704 528.5

R 705 511.3

R 706 524.7

R 719 511.5

R 725 509.3

R 726 509.3

R 727 509.3

R 919 510.5

R 923 541.0

R 928 512.0

R 929 512.0

NOTE

/ TO DEACTIVATE PUMP UNIT 1:*

/* CHANGE:*

/* I 01 500.0 0.0 150 2000 150 2500 140 3750 91 3751 10'

/* TO:*

/* R 01 500.0

/t*t **************************** ****

R 01 500.0

.......... .....* .....................***............*****

/* NOTE *

/. TO DEACTIVATE PUMP UNIT 2/3:*

/* CHANGE:*

/* I 40 500.0 0.0 150 2250 150 3000 131 3600 120 4900 110 4901 10*

/ TO:*

/ R 40 500.0

I 40 500.0 0.0 150 2250 150 3000 131 3600 120 4900 110 4901 10





ITERATION STOPS WHEN GREATEST FLOW CHANGE IS .05000 IN ANY PIPE


DEFAULT ROUGHNESS COEFFICIENT - C=120.0



THE NUMBER OF INPUT POINTS IN SYSTEM IS 1



40 1 500.00 1.00 .0 2250.0 3000.0 3600.0 4900.0 4901.0

150.0 150.0 131.0 120.0 110.0 10.0

IX-47

-aic. NO. UJKLUU-VUUU)

AMENDMNT 13 Revision 0 AMENMEN 13 Attachment C

Attachme Co

AMENDMENT 13Caic. No. DKLUO-UUU• Revision 0 Attachment C

Initial estimate of demand on the system is 100.00

NET UNBALANCED DEMAND ON THE SYSTEM = .00000

LOOP PIPES

1 600 60 59 58 57 56 54 53 52 51

2 65 64 63 62 302 305 60 59 58 57

66

3 54 83 82 81 80 79 78 77 76 75

52 53

68 110 84 90 93 94 839 95 96 97

50 55 70 69

5 303 305 60 59 58 57 56 54 53 52

26 828 829 304

6 99 90 93 94 839 95 96 97 98 932

7 932 33 34 35 36 37 38 39 40 46

28 29 753 30 760 761 31 931 32

8 754 757 758 26 300 602

9 25 24 5 6 7 14 15 16 17 750

758 925 719 763

10 725 727 756 755 754 602 601 27 28 29

11 14 8 9 10 13 16 15

12 10 11 12

50 45 42 41

56 54 53 52 51 55 70 69 68 67

74 73 72 71 67 68 69 70 55 51

98 33 34 35 36 37 38 39 40 49

51 50 49 46 47 48 25 763 719 925

32 931 105 104 103 102 860 101 100

47 48 25 763 719 925 26 300 601 27

751 18 19 752 20 726 727 756 755 757

23 22 762 922 21

BANDWIDTH - 5







NUMBER OF ITERATIONS= 6

80.582 in loop # 27.711 in loop #

6.840 in loop #

2.551 in loop #

.600 in loop #

.040 in loop #

5 5

3

3

3

3

IX-48

AMENDMENT 13Caic. No. DREOO-000S Revision 0 Attachment C

SUMMARY REPORT

IPAGE •/o

COMPANY I Nexus Technical Services Corporation IDATE 2000 JAN

DESIGNER BY: BRIAN FOX CHECKED: " -iDL

200JA



JOB NO. I U2TB Hose Station F-75

__ _ _I

MINIMUM FLOW OF ALL OPERATING SPRINKLER HEADS IS

AVERAGE FLOW FROM ALL OPERATING SPRINKLER HEADS IS

TOTAL FLOW FROM ALL OPERATING SPRINKLER HEADS IS

TOTAL DEMAND ON THE WHOLE SYSTEM IS

127.53

127.53

127.53

127.53

SPECIFIED AVAILABLE PRESSURE AT INPUT NODE IS 346.40 FEET OR 150.00 P.S.I.

IX-49

AMENDMENT 13Caic. No. DREOO-000O Revision 0 Attachment C



DESIGNER BY: BRIAN FOX CHECKED: -- e

CLIENT ComEd. Dresden Nuclear Power Station - Hose Station Hydraulic Analysis

PROJECT UI DFP Out. 10% Degraded C-Factors. 10% Deg. U2/3 DFP

- Hose.I Staon mi F-75

DPATE c20 I) J

[DATE 2000 JAN 6 ;

JOBNV. I u

I I PIPE DIAMETERI PIPE/FTG I TOTAL IHEAD LOSSIHEAD LOSS I STATIC I TOTAL !ROUGHI WATER VELOC.1

IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. OVER PIPE HEAD LOSSIHEAD LOSS NESS IVELOCITY! PRESS.I

INO. I NODES (US GPM) (IN) (IN) # (FT) I (FT) I (PSI) I (PSI) (PSI) i (PSI) ICOEFF[ (FT/SEC)l (PSI)

_ _ _ _ _ _ _ ___ _ I_ _ _ _ I _ _ _ _ _ _ _ _ I___ __ _ _ _ ___I._ _

____________________ I __________________ 11.94 I CSAN

11

21

3

4

6

7

8

91

10

11I

12

13

14

i15

1 2

2 3

3 4

4 I

5 6

6 7 7 8

8 9

9 10

10 12

10 11I

11 12

12 15

8 13

13 14

1

1

I ....-.... _____-____________ _______ I ________ I ____ I _____ I ______ I _____ I ______ I ___ I _____ I ____

IX-50

3.5 I0.00

0.00

0.00

0.00

14.47

14 .47

14.47

1.66

1.66

0.76

0.90

0.90

1.66

12.81

12.81

11.94 C 11.94 C

2 1

.2 I1

2 3

.2 1

7.98 C

8 2

11.20 C

12 I

12 I

12 3

11.20 I

12

12

7.85

7.85

7.98

8

4.03

4

4

4

4

4.03

4 l

4

4

4

4.03

4

4

4

4.03

4

4

4 4.03

4

4

4 7.98

8 7 I 7.98I

SAM

SAM GV

TT

SE

CV

SAM

SE

:SAM

HE

SE

3ZSE

'SAM

ITT

LGV

CSAM

CSAM

CSAM

IGV

CSAM

2SE

1HE

2TT

IGV

CSAM

5SE

7HE

2GV

1TT

CSAM

5SE

2HE

IGV

CSAM

8SE

4HE

1GV

CSAM

4SE

IGV

iTT

CSAM

1TT

CSAM

3.5 16.1

1.7

17.2

23.3 I 18.7

21.2

10.0

60.0

11.1

23 .0

21.0

13.5

51.2

5.1

156.6

161.0

30.0

1.1

110.0

5.9

1.2

11.8

0.6

215.4

44 .2

8.2

1.2

5.9

77.5

14.7

2.4

0.6

80.3

23.6

4.7

0.6

34.8

11.8

0.6

5.9

86.0

11.0

54.6

3.5 0.000 1 0.000 77.0 0.000 1 0.000

31.2 0.000 1 0.000

115.1 0.000 1 0.000

69.8 10.589E-6 0.0000411

156.6 10.0000121 0.00188

161.0 0.000012 1 0.00193

31.1 10.225E-6 10.0000070

129.4 10.00000631 0.000816

274.9 10.00000151 0.000411 1

95.2 10.00000201 0.000192 1

109.1 10.00000201 0.000220 1

53.0 10.00000631 0.000334 1

97.0 10.00000881 0.000857 1

54.6 10.000012 I 0.000676 I

4.114 4.114 2.815 2.815

-2.252 -2.252

0.000 0.000

0.000 10.0000411

-0.217 1 -0.215

-0.303 1 -0.301

0.000 10.0000070

2.555 1 2.556

0.000 1 0.000411

16.758 16.758

-16.758 -16.758

-2.771 -2.771

0.0866 0.0875

-0.217 -0.216

62

62

62

132

132

66

66

62

62

62

62

62

62

66

55

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.0471 10.15E-41

0.0959 I0.61E-4'

0.0959 0.61E-4

0.0106 10.76E-6

0.0418 10.11E-4

0.0192 I0.24E-5

0.0226 10.34E-5

0.0226 10.34E-5

0.0418 10.11E-4

0.0822 10.45E-4

I 10.0822 10.45E-4

AMENDMENT 13t-aIC. No. UKtUU-UUUV Revision 0 Attachment C

HYDRAULIC CALCULATIONS " - PIPE CHARACTERISTICS

I I IPIPE DIAMETERI PIPE/FTG TOTAL IHEAD LOSSIHEAD LOSS I STATIC I TOTAL IROUGHI WATER I VELOC.I

IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH I PER FT. JOVER PIPE HEAD LOSSIHEAD LOSS NESS IVELOCITYL PRESS.I

INO. NODES (US GPM)l (IN) (IN) I# (FT) (FT) I (PSI) (PSI) (PSI) I (PSI) ICOEFFI (FT/SEC) I (PSI)

0 .086 I5' 0.47I.IE1

112 I CS 14.-11

16

17

18

19

20

21

22

23

24

25

26

27

21

2

3

3

3

3

3

3:

3.

91

0

1

2

.3

14

15

16

37

38

14 15

15 700

16 35

35 702

17 726

725 19

723 20

20 21

22 5

22 724

923 200

601 25

25 26

26 21

703 27

721 28

929 928

30 29

31 30

32 31 I 33 32 1

34 33 I

52 34

12.81

14.47

14.4-7 '

14.47

14.47

14 .47I

8.93

8.93

8.93

14 .47

44.25

43.24

0.82

0.82

0.82

9.75

9.75

3.33

15.03

15.03

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2

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8

1

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] I.I 11.20 CS$

IG'

11.20 CSI

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11.20 CS,

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7.85 CS

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7.85 CS

8.39 CS

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8 I 1 8.39 CS

8 i

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2 1

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8 1

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8 E

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184 .0

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20.0

285.0

285.0

300.0

280.0

24.3

2.4

10.0

125.0 10.00000721

210.7 10.757E-6

20.0 10.000016

285.0 10.000013

285.0 10.000010

300.0 0.000016

306.8 10.000013

I 1 10.0 0o.o0oo13I

0.000903

0.000160

0.000322

0.00391

0.00295

0.00499

0.00421

0.000137

_I0.0866 1 5!

I -

IX-51

I

PAGE c- i 2,

15.1 10.000002310.0000359 1

I I 1

45.5 10.00000291 0.000136

I I

9.1 i0.000001310.0000118

87.7 0o.0000013I 0.0001141

I 123.8 10.00000731 0.000910

I 97.9 10.00000301 0.000294

108.3 10.00000351 0.000386

1 1

159.6 10.00000351 0.000568 I

206.2 10.589E-6 I 0.000121

170.5 10.00000461 0.000795

1 1

23.4 10.0000941 0.00221

113.1 I0.614E-7 0.0000069

1 1

1 I

164.4 1O.335E-7 10.0000055

1 1 164.9 IO.335E-7 100005

1 1 5.3 10.000005310.0000

2 80

0.0B66

0.000

-0.346

0.217

-0.346

0.0433

0.390

-0.346

-0.303

0.000

-2.382

-6.062

0.217

-0.390

-0.650

0.000

0.000

0.346

-0.433

-0.346

0.433

0.130

0.000

____________________ I __________________ I ____________________ � ________________ I ______________

0.000136 5

-0.346 8

0.217 8

-0.346 8

0.0436 8

0.390 6

-0.346

-0.303 I:

0.000795

-2.379

-6.062

0 0.217

-0.390

-0.650

0.000903

0.000160

0.347

-0.429

-0.343

0.438

0.134

0.000137

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5 0.0

6 0.

6 0.

6 0.

16 0. 56 0.

66 0.

32 0.

32

62

62 10.

86 10.

86 10.

66 1 0

56 1

56 1

56

61

71

55

61

61

417 10.11E-41

3471 .15E-4

0471 10.15E-41

0471 10.15E-41

Ii 0959 10.61E-41

0592 10.23E-41

0519 10.18E-41

II

0519 10.18E-41

0471 10.15E-41

0.144 10.000141

0.277 0.00051

00528 0.18E-6'

00528 IO.18E-61

00528 I0.18E-6;

1 I

0.0626 10.26E-41

0.0626 10.26E-41

0.0191 10.24E-5 1

0.0964 10.62E-4'

0.0964 I0.62E-4!

0.0964 10.62E-41

0.0964 0.62E-4!

0.0964 10.62E-4'

0.0964 10.62E-41

AMENDMENT 13taic. tNO. UKrLUU-UUU Revision 0 Attachment C

HYDRAULIC CALCULATIONS -. PIPE CHARACTERISTICS

I I I PIPE DIAMETERI PIPE/FTG TOTAL IHEAD LOSSIHEAD LOSS I STATIC TOTAL IROUGHI WATER I VELOC.I

IPIPEI PIPE I FLOW NOM ACTUALI CODE LENGTH I LENGTH I PER FT. lOVER PIPE HEAD LOSSIHEAD LOSS NESS IVELOCITYI PRESS.I

lNO. I NODES I (US GPM) (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI) I (PSI) I (PSI) ICOEFFI(FT/SEC)i (PSI) I ,1__________ I I

[ _ _ _ _I _ _

_______________________ ____________________ I _____________________________ 7.98 I CS.h�M 160.0

39

40

41

42

45

46

47

48

4.

5(

5

5

5

5

5

5

-0.346 I

I_ II

U2TB Hose St

9

0

II

2

3

4

s5

56

57

58

59

60

62

63

_-I.

AM 160.0

IX-52

36 52

37 36

40 41

41 42

42 45

37 38

38 39

39 22

45 37

45 48

48 49

49 50

50 51

51 70

67 48

70 53

53 54 54 55

55 56 I

56 57

59 58

60 59

15.03

15.03

127.53

127.53

127.53

58.72

58.72

58.72

73.74

53.78

66.19

66.19

66.19

66.19

12.41

69.01

69.01

69.01

69.01

69.01

9.55

9.55

7.98 CS.

7.98 CS

8 IG 8 IT

8 4S

8 I3H 10.02 CS

10.02 CS

10 IH

10 1i

10 1I

10 is

10.02 Cc

10 1

7.98 C,

8 i

8 1

8 21

11.20 C

12 3

12 2

12 4

12 3

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7.98 C

8 I

9.56 C

10 I 10

10

10.02

10

10.02

10.02

10.02

10.02

10

7.98

8

8

8

7.98

7.98

8 79

7.98

8

7.98

6.07

6.07

PAGE ý 1.3

AM V

T

E

AM

A•M CE

V

SE

TT

SAM GV

SE

HE SAM

$ E

H E ZSE

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CSAM

7SE

CSAM

7SE

1HE

IGV

CSAM

CSAM

2HE

CSAM

4HE

CSAM

CSAM

CSAM

160.0 0.5

4.5

9.3

3.5

17.0

15.4

1.1

0.5

5.6

2.2

35.1

5.1

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0.4

1.7

1.7

230.0

69.1

22.2

28.0

9.0

59.3

3.5

3.4

255.0

9.0

0.8

0.9

6.0

14.7

1.0

2.3

11.7

115.9

45.3

118.3

35.1

2.5

1.1

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107.6

5.0

15.1

10.0

1.0

6.8

30.8

II

160.0 10.000013 0.00220 177.9 10.000028 0.00510

17.0 10.000665 1 0.0113

24.9 10.000665 1 0.0166

II I I

40.2 10.000665 1 0.0268 1

19.0 10.000479 1 0.00909 1

1 1 I I

358.2 10.00000781 0.00282

I 1 1 1

59.3 10.00000781 0.000467

6.9 10.000731 0.00503

265.7 0.000169 0.0448

20.7 10.0000681 0.00142

1 I 1.0 10.000068 10.0000685

2.3 10.000068 0.000160

11.7 10.000068 0.000800

161.3 10.00000301 0.000498

1 1 157.0 10.000224 0.0352

15.5 10.000224 0.00347

112.6 10.000224 1 0.0252

25.1 10.000224 0.00563

1 1 1.0 10.000224 0.000224

6.8 10.000021 0.000148

30.8 0.000021 0.000676

-0.346 0.693

4.720

0.000

0.000

0.0433

0.0433

0.173

0.000

8.054

2.598

0.433

0.996

5.066

1.516

2.382

0.000

0.000

0.000

0.000

0.000

0.000

-0.344 61 10.0964 10 0.698 41 1 0.0964 0

4.731 1 35 0.519 Ic

0.0166 1 35 1 0.519 1

0.0268 1 35 1 0.519

0.0524 1 35 0.377

0.0461 132 0.191 1

0.174 132 0.191

0.00503 35 0.473

8.099 35 0.240

II

2.600 1 62 1 0.269

0.433 62 0.269

0.996 62 0.269

5.067 62 0.269

1.516 62 0.0505

2.417 62 0.443

0.00347 62 0.443

0.0252 62 0.443

0.00563 62 0.443

0.000224 62 0.443

0.000148 62 0.106

0.000676 62 0.106

.62E-41 ).62E-41

0.0018

0.0018

0.0018

0.000951

0.000241

0.000241

0.0015

10.000381

I 1 I

10.000481

10.000481

10.000481

0.00048 I 10.17E-4i

S0 1

10.0013

10.0013 10.0013 10.0013I I

10.0013

10.75E-4

10.75E-4

I

AMENDMENT 13Calc. No. DREOO-000U Revision 0 Attachment C

PAGE :14,HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS

I I I PIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS

IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. lOVER PIPE

INO. NODES I (US GPM)l (IN) (IN) I # (FT) (FT) I (PSI) I (PSI)

I 1 1 __ 1_1 I _ _ _ __ _ __ _ _ _ __ _ _I__ _ _ _ _ _ _

64

65

66 6

67

68

69

70

71

72

73

74

75

76

77

78

79

80

81

82

83

84

61 60

62 61

63 62

64 63

64 80

80 69

69 67

63 81

81 98

98 79

79 78

78 77

77 76

76 75

75 74

74 73

73 72

72 71

71 68

68 70

82 102

130.3 I9.55

9.55

9.55

12.37

12.41

12.41

12.41

2.82

2.82

2.82

2 .82

2.82

2.82

2.82

2.82

2.82

2.82

2.82

2.82

2.82

24 .78

6.07 CSAM

6 3SE

6 4HE

6 ITT

6.07 CSAM

6 3SE

6 2HE

6.07 CSAM

6 4SE

6 I1GV

6 ITT

7.98 CSAM

8 9SE

8 2TT

8 I1GV

8 2HE

10.02 CSAI

10 1GV

10.02 CSM

10.02 CSAf

6.07 CSAJ

6 1GV

6.07 CSAJ

6 3SE

6 2TT

6 iHE

6.07 CSA.

6 2SE

6 2HE

6.07 CSA

6 2HE

6.07 CSA

6 4SE

6 2HE

6 I1GV

6.07 CS•

6 2SE

7.98 CS•

7.98 CS•

7.98 CS•

7.98 CS

7.98 CS

8 4S

8 1HE

7.98 CSJ

8 3Si

10.02 CS;

10 IG

10.02 CS

STATIC TOTAL IROUGHI WATER I VELOC.ISTATIC TOTAL

HEAD LOSSIHEAD LOSS

(PSI) (PSI)INESS IVELOCITYI PRISS.

ICOE-FFI (FT/SEC) I (PSI) I

I ______ I ______ ___ I _____ I ____ I 0.0433 0 0468 62 I 0.106 I0.75E.41

4

M

am

M

M

E

AM

AM

v

AM

130.3 12 .4

8.2

8.8

70.1

12.4

4.1

36.9

16.5

0.9

8.8

86.8

45.2

19.5

1.1

5.0

5.3

1.5

2.2

3.3

84.8

0.9

32.3 3

12.4

17.7

2.1

122.0

8.2

4.1

65.8

4.1

175.7

16.5

4.1

0.9

21.5

8.2

14 .5

1.8

103.6

15.6

54.8

20.1

2.5

89.8

15.1

2.3

1.5

10.5

______ I _____ I _______ I _________ I _____ I _____ I ______ _____ I ______ I ___ I ____ I ____ I

IX-53

U2TB Hose St

159.7 10.000021 1 0.00350

86.6 10.000021 0.00190

63.1 10.000021 0.00138

157.6 10.00000921 0.00146

6.8 10.000003010.0000210

2.2 10.000003010.0000067

3.3 10.000003010-0000100

85.7 10.00000221 0.000196

64.3 10.0000022! 0.000147

134.4 10.00000221 0.0003071

70.0 10.00000221 0.0001601

197.2 10.00000221 0.000450 1

29.7 10.000002210.0000679 1

14.5 10.6O0E-6 10.00000871

1.8 10.600E-6 I0.00000 1 0

103.6 10.600E-6 10.0000621

15.6 10.600E-6 10.0000093

77.3 0.600E-6 10.0000464

104.9 10.600E-6 10.00006291

3.8 10.198E-6 10.000000751

10.5 10.000011 0.000117 1

0.0433 0.0468

-3.507 -3.506

-3.074 -3.073

18.880 18.881

0.000 10.0000210

0.000 10.0000067

0.000 10.0000100

0.0433 0.0435

-8.011 -8.011

1.429 1.429

0.000 0.000160

0.433 0.433

0.000 10.0000679

0.000 10.0000087

0.000 10.0000010

0.000 10.0000621

0.000 10.0000093

1.299 1 1.299

-2.512 -2.511

-0.953 -0.953

0.000 0.000117

I

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

I~O Io I•a

0.106 10.75E-41 1 I

1 1

0.106 10.75E-41

0.0793 0.42E-41

II II

0.0505 10.17E-41

0.0505 I0.17E-41

0.0505 10.17E-41

0.0313 10.65E-51

0.0313 10.65E-51 II

0.0313 10.65E-51

II I

0.0313 10.65E-51

0.0313 10.65E-51

II

0.0181 10.225E-51

10.0181 10.22E-51 0.0181 10.22E-51

0.0181 10.22E-51

1 0.0181 10.22E-5I

II I

0.0181 10.225-5I

0.0115 10.88E-61

II I 0.101 0.68E-41

II I

AMENDMENT 13Calc. No. DREOO-OOOS Revision 0 Attachment C

PAGE <zi.-HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS

I I

IPIPEi PIPE

PIPE DIAMETERI

FLOW NOM ACTUALI

(US GPM)l (IN) (IN) I

PIPE/FTG

CODE LENGTH

# (FT)

TOTAL

LENGTH

(FT)

HEAD LOSSIHEAD LOSS

PER FT. lOVER PIPE

I (PSI) I (PSI)

STATIC I TOTAL

HEAD LOSS HEAD LOSS

I (PSI) I (PSI)

IROUGHI WATER VELOC.IROUGHI WATER I NESS IVELOCITYI

ICOEFFI(FT/SEC)

- I NODES ____ _____I___I __ ___ __ ______ I ___ I _____ I ____ I

85

86

87

90

91

93

94

95

96

97

98

99

1100

101

102

1103

82 91

91 92

92 93

88 82

88 89

87 88

838 87

83 96

65 83

46 65

29 46

86 82

85 86

860 85

84 97

66 84

____ ________ I _________ I _____ I _____ I ______ I _____ I ______ I ___ I _____ I ____ I

IX-54

U2TB Hose St

VELOC. PRESS.

(PSI)

1--

0.00

0.00

0.00

11.70

0.00

11.70

11.70

11.70

11.70

11.70

11.70

13.08

13.08

13.08

13.08

13.08

10.02 C

10 1

6.07 C

6 2

6 1

6 I 4.03 C

4 2

4 E 10.02 C

10 1

4.03 C

4

4

6.07

6

6

6

6

6.07

6

6

6

7.98

8

8

7.98

7.98

8

8

B

7.98

8

8

8

10.02

10

6.07

6

6

6

6.07

6

6

7.98

8

8

7.98

"SAM "TT SAM

HE

GV

TT

:SAM

SE

HE

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CSAM

IGV

HE

CSAM

4SE

3HE

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ITT

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6SE

2HE

ITT

CSAM

2HE

ITT

CSAM

CSAM

5SE

2GV

ISR

CSAM

ISE

IGV

ITT

CSAM

ITT

CSAM

2SE

3HE

IGV

CSAM

7SE

3HE

CSAM

2HE

ITT

CSAM

1.0

50.0

16.0

14.0

3.0

30.0

152.1

20.0

24.0

1.0

14.7

166.9

2.0

32.0

66.0

16.5

6.2

0.9

8.8

206.1

24.7

4.1

8.8

14.2

5.0

9.8

1.5

31.3

25.1

2.2

19.5

112.0

5.0

1.1

9.8

1.0

14.7

48.5

8.2

6.2

0.9

168.5

28.9

6.2

14.3

5.0

9.8

1.5

51.0 0.000 0.000

63.0 0.000 0.000

196.1 0.000 0.000

15.7 10.000002710.0000435

1 1 200.9 1 0.000 1 0.000

98.4 10.000031 0.00314

243.8 10.000031 0.00778

28.9 10.00000831 0.000243

1 1

1.5 10.000008310.0000126

78.1 10.00000831 0.000655

1 1 1 1

127.9 10.00000831 0.00107

15.7 10.000003410.0000535

1 1 63.8 0.000039 1 0.00250

1 1 1 1 1 1

203.5 10.000039 0.00799

1 1 1 1

29.1 10.000010 0.000300

1.5 10.000010 10.0000155

0.0866 0.0866

0.346 0.346

0.000 0.000

-0.130 -0.130

0.303 0.303

3.811 3.814

5.196 5.204

-5.846 -5.846

-0.650 -0.650

3.248 3.248

0.433 0.434

0.000 10.0000535

3.681 3.683

5.196 5.204

-5.846 -5.846

-0.650 -0.650

120

120

120

62

120

62

62

62

62

62

62

62

62

62

62

62

0.000 0.000

0.000 0.000

0.000 0.000

0.0476 I0.15E-41

0.000 0.000

0.130 10 000111

0.130 10.000111

0.0750 0.37E-41

0.0750 10.37E-41

0.0750 I0.37E-41

0.0750 10.37E-4!

II

0.0532 I0.19E-41

1 1 0.145 10.000141

II II

0.145 0.000141

0.0839 10.47E-41

3 1I II

0.0839 I0.47E-41

I I I i

AMENDMENT 13Calc. No. DRE00-000S Revision 0 Attachment C

PAGE n /4HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS


PIPEJ PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH PER FT. lOVER PIPE

NO. I NODES (US GPM)I (IN) (IN) I # (FT) (FT) I (PSI) I (PSI)

__ I ______ I ______ I ________ I _________ I _____ SAN

1104

105

1106

1110

300 I 1 1 1 1

302

I 303

1304

1305

I500

1501

1502

1503

1504

1505

STATIC I TOTAL

HEAD LOSSIHEAD LOSS

I (PSI) I (PSI)

ROUGH) WATER VELOC.)

INESS IVELOCITYI PRESS.I

ICOEFFI(FT/SEC)I (PSI) I

I ______ I ______ I ___ I _____ I ____ I 3.248 I 3.248 62 I 0.0839 I0.47E 41

47 66 I

28 47

51 812

102 64 2

24 200

58 201

202 201

831 202

201 57

97 400

400 401

401 402

96 403

403 404

404 405

8

8

8

3.08

3.08

0.00

4.78

5.73

9.55

48.96

48.96

58.52

0.00

0.00

0.00

0.00

0.00

0.00

8

8

8

8

8

8

8

8

8

6

6

10

6

6

6

6

6

6

6

6

4

4

4

6

6

6

6

6

4

4

4

I I ______ I _____ I ________ I _________ I _____ I _____ I ______ I _____ ______ ___ I _____ I ____ I

IX-55

U2TB Hose St

7.98 C

4

2

1

7.98 C

100

Ii

7.98 (

6.07

10.02

6.07

6.07

6.07

6.07

4.03

6.07

6.07

4.03

SAM SE

GV

SR

SSAM

SE

GV

TT

SAM

.TT

.GV

SSE

CSAM

CSAM

5SE

LGV

ITT

CSAM

IGV

4HE

CSAM

2TT

CSAM

CSAM

ISE

1GV

2HE

CSAM

IHE

CSAM

2SE

4HE

ITT

IGV

CSAM

3SE

ITT

2GV

CSAM

IHE

CSAM

ITT

2SE

3HE

1GV

CSAM

ITT

3SE

2GV

27.8 8

20.1

2.2

19.5

115.0

5.0

1.i1

9.8

1.0

33.1

3.8

17.0 0

0.5

136.5

25.1

1.1

9.8

80.0

0.9

8.2

482.5

29.4

2.7

89.0

4.1

0.9

4.1

26.2

7.0

132.7

28.0

28.0

30.0

3.0

52.2

30.0

20.0

4.0

7.8

7.0

132.3

30.0

28.0

21.0

3.0

47.0

20.0

30.0

4.0

69.6 10.00

130.9 0.00

55.0 0

0.5 10.00

172.5 10.00

89.1 I0.00

511.9 10.0

2 .7 0.0

98.1 10.0

33.2 1

221.7

106.2

14.8

214.3

101.0

0010 0.000717

0010 0.00135

.000 0.000

00011 10.0000055

0000221 0.000385 1

00021 0.00195

00039 0.0201

00452 0.00122

00629 0.0617

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

3 .248 3 .248

0.433 0.434

0.000 0.000

0.000 10.0000055

4.547 1 4.547

0.650 1 0.651

8.877 8.897

3 .464 3.465

0.000 0.0617

0.000 0.000

41.354 41.354

-3.334 -3.334

0.000 0.00(

41.354 41.35'

-3.334 -3.33.

I

I-1-

0

4

4

62

62

120

62

62

62

62

62

62

120

120

120

120

120

120

0.0839 0.47E-41

0.0839 10.47E-41

0.000 0.000

0.101 10.68E-41

0.0367 10.90E-51

I I

0.106 10.75E-41 II II

0.199 0.000261

0.544 0.0019

0.650 10.0028

0 0

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

AMENDMENT 13Calc. No. UKLUU-UUUW Revision 0 Attachment C

PAGE c i 7HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS


JPIPEI PIPE FLOW I NOM ACTUALI CODE LENGTH I LENGTH PER FT. lOVER PIPE

NO. I NODES I (US GPM) I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)

1I _ _I_ _- 1I _ __ __ _ _

1600 1

1 1 1 1 1 1

601

602

1611

612

621 1

1651

1719

1725

1726

1727

1750

1751

1752

1753

1754

1755

1756

r

STATIC TOTAL HEAD LOSSIHEAD LOSS

I (PSI) i (PSI)

IROUGHI WATER I VELOC. IIROUGHI WATER I NESS IVELOCITYI

ICOEFFI(FT/SEC)l

VELOC. PRESS.

(PSI)

II I I i

- I ______________ I ________________ I __________________ I ________________ I __________________ I _________ 4.547 19.810 120 2

157 600

24 601

602 24

601 611

611 612

602 621

61 651

719 23

18 725

726 18

18 727

700 701

701 16

702 17

21 703

704 602

705 704

727 705

27.53

1

0.82

6.55

0.00

0.00

0.00

0.00

1

44.25

8.93

14.47

5.54

14.47

14.47

14.47

9.75

6.55

5.54

5.54

1 1 _ _ I__ _ _ I _ __ __ _ _ I~...

1.61 CSAM

1/2 ITT

1/2 2SE

1/2 1GV

7.98 CSAM

8 ISE

7.98 CSAM

8 5SE

8 2HE

8 1GV

6.07 CSAM

6 2SE

6 ITT

6.07 CSAM

6.07 CSAM

6 3SE

6 ITT

1.61 CSAM

1/2 ITT

1/2 2SE

1/2 IGV

7.98 CSAM

8 2HE

11.20 CSAM

12 1GV

11.20 CSAM

12 1GV

11.20 CSAM

12 IGV

7.98 CSAM

84HE

11.20 CSAM

7.85 CSAM

7.85 CSAM

ITT

7.98 CSAM

8 4SE

8 IHE

8 ITT

8 1GV

7.98 CSAM

8 7SE

8 2HE

8 iTT

7.98 CSAM

8 2HE

8 ITT

IX-56

U2TB Hose St

13.5

8.0

8.0

1.0

10.8

5.0

123.0

25.1

5.0

1.1

4.5

28.0

30.0

1.0

3.6

42.0o

30.0

49.1

8.0

8.0

1.0

5.9

5.0

6.8

2.3

4.5

2.3

2.1

2.3

72.8

8.0

29.3

41.9

26.0

10.1

58.7

20.1

2.5

9.8

1.1

221.9

35.1

5.0

9.8

141.3

9.2

17.9

30.5 0.500 15.263

15.8 10.614E-7 10.000000971

154.2 10.00000281 0.000442 1

62,5 1 0.000 0.000

1.0 0.000 0.000

75.6 0.000 0.000

66.1 0.000 1 0.000

10.9 10.000098 0.00107

9.1 10.532E-6 10-0000048

6.8 10.000001310.0000088

4.4 0.220E-6 0000000971

80.8 10.000015 0.00125

29.3 10.000002910.0000873

41.9 10.00000731 0.000308

36.1 10.00000571 0.000209

92.1 10.00000281 0.000264

271.8 10.00000211 0.000571

168.3 10.00000111 0.000193

4.547 19.810

0.000 10.000000971

-1.429 -1.429

3.248 3.248

0.000 0.000

-0.433 -0.433

5.240 5.240

0.000 0.00107

0.000 10.0000048

0.000 10.0000088

0.000 10.00000097

0.563 1 0.564

0.217 I 0.217

-0.217 -0.216

0.606 0.606

-0.0866 -0.0863

7.448 7.449

0.866 0.866

120 2

62 0.

62 10

120

120

120

120

62

86

86

86

55

55

86

66

62

62

86

____________________ I ________________ I __________________ I ____________________ I __________________ I ____________________ 1...................I ________________ I ______________ I

0.097 2.718

00528 10.18E-61

.0420 J0.11E-41

0.000 0.000

0.000 0.000 0.000 0.000

0.000 0.000

0.284 0.00054'

0.0291 10.56E-51

0.0471 10.15E-4,

0.0180 10.21E-51

0.0928 10.58E-4

0.0471 I0.15E-4'

0.0959 10.61E-4i

0.0647 I0.28E-4

0.0420 10.11E-41

0.0355 0.85E-5

0.0355 10.85E-51


PAGE C./ /HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS

IIPIPE DIAMETERI PIPE/FTG TOTAL JHEAD LOSSIHEAD LOSS

PIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH I PER FT. JOVER PIPE

NO. I NODES (US GPM) (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)

STATIC TOTAL IROUGHI WATER VELOC.IISTATIC ITOTAL HEAD LOSSIHEAD LOSS

I (PSI) I (PSI)NESS IVELOCITYI PRESS.I

lCOEFFI (FT/SEC) I (PSI) I

! - 1 -__________ 1 -- 1__________ _______________I________________

175

175

17

76 18

16

76

18

18

18

17

18

18

7 706 704

8 923 706

0 27 720

1 720 721

62 919 723

63 724 719

00 928 802

02 802 803

03 834 800

04 800 801

05 56 805

806 49 849

807 849 814

808 849 815

809 77 808

1.01

1.01

9.75

9.75

8.93

44.25

0.00

0.00

0.00

0.00

0.00

0.00

0.00

0.00

0.00

4.03 CSAM

4 8SE

4 4HE

4 1GV

4.03 CSAM

4 12SE

4 4HE

4 IGV

7.98 CSAM

8 iSE

8.39 CSAM

8 2HE

8.39 CSAM

8 IGV

7.85 CSAM

6.07 CSAM

6 ITT

6 1GV

6 2SE

4 .03 CSAM

4 2HE

4 ITT

4 4SE

4 IGV 6.07 CSAtM

6 3SE

6 iHE

5.05 CSAM

5 7SE

5 4HE

7.98 CSAM

8 IHE

8 I1TT 4 .03 CSAM

4 3SE

4 2HE

4 ITT

4 1GV

4.03 CSAM

4 ISE

4 ITT

4 1GV

4.03 CSAM

4 4SE

4 IHE

4 1GV

2.47 CSAM

2 1/2 ITT

2 1/2 IGV

197.0

23.6

4.7

0.6

178.4

35.3

4.7

0.6

75.5

4.2

17.0

5.3

12 .5

1.3

26.0

33.8

30.0

3.0

28.0

115.1

a.0

20.0

40.0

2.0

30.9

42.0

7.0

121.8

84.0

20.0

25.8

8.5

33.1

84.1

30.0

8.0

20.0

2.0

2.5

10.0

20.0

2.0

18.0

40.0

4.0

2.0

1.0

12.0

1.0

_______________________ I __________________________ I _____________ I ____________________ I __________________ I 1.645 I 1 64� I 62 0.0254 l0.43E-5I

225.9 10.00000251 0.000566

1 1

219.0 10.00000251 0.000549

1 1

79.7 10.00000721 0.000576

1 1 22.3 10.00000561 0.000127

13.8 10.000004310.0000604

26.0 10.0000581 0.00151

94.8 0.000 0.000

185.1 0.000 0.000

79.9 0.000 0.000

225.8 0.000 0.00C

67.4 0.000 0.00(

144.1 0.000 0.00(

34.5 0.000 0.00*

64.0 0.000 0.00

14.0 0.000 0.00

31 0

0

0

0

0

0I

I1- 1I____________ _____________________ I _____________________________ I __________________________________ I __________________ ____________________ _______________________ I ____________________ I _______________________ I ____________ __________________ I _______________ I

IX-57

U2TB Hose St

1.645

-7.058

0.650

0.000

0.000 I0

0.000

3.248

3.551

-7.794

-4.027

-11.562

2.728

0.000

1.169

-0.433

-1-1-1.646

-7.058

0.650

0.000127

0.0000604

0.00151

3.248

3.551

-7.794

-4.027

-11.562

2.728

0.000

1.169

-0.433

62 10.0254 10-43E-51

II

I 1I

I I 62 1 0.0254 I0.43E-S1

I 1 I

I I I 5610.0626 I0.26E-41

5610.0567 0O.21E-4I

59 1 0.0519 10.18E-41

I 1 1 86 1 0.293 10.000571

120 1 0.000 1 0.000

120 0.000 0.000

120 0.000 10.000

120 0.000 0.000

120 0.000 0.000

120 0.000 10.000

120 0.000 0.000

120 0.000 0.000

120 0.000 0.000

AMENDMENT 13Calc. No. DKREU-IUU) Revision 0 Attachment C


I I I IPIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS

IPIPEL PIPE I FLOW I NOM ACTUALI CODE LENGTH I LENGTH PER FT. lOVER PIPE

NO. I NODES (US GPM)I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)

STATIC TOTAL IROUGHI WATER I VELOC.

jHEAD LOSSIHEAD LOSS

I(PSI) I(PSI)

I I I I I ______________________________ I ________________ __________________ I ____________________ I __________________

28.1 I 0.000 I 0.000 I -2.165

1810 I

1811I

1812

1813

1814 I

1 1 1815 1

1 1 816 1

1819

1820

1821

822

823

824

1826

1

4.03 I ,AM60 809

79 811

55 813

813 817

813 818

805 819

819 820

819 822

76 824

824 825

801 804

836 827

835 836

824 826

68.1 I0.00

4

4

0.00

3

3

3

0.00

8

8 8

0.00

2 1/2

2 1/2

0.00

18

0.00

8

0.00

6

6

0.00

6

6

6

0.00

18

B 8

18

0.00

6

6

6

0.00

13 0.00

5

5

0.00

6

6

6

6

6

0.00

6

6

6

IROUGHI WATER I VELOC. NESS IVELOCITYI PRESS.

ICOEFFI(FT/SEC)l (PSI)

1 1_ - 1__ _ _ _

4.03 C• 2.

3.07 C

4•

2

7.98 C

4

4

1

2.47- C

7.98 C

1 7.98 IC

I] 6.07 C

6.07

7.98

6.07

3.07

5.05

6.07

6.07

SAM

SE

TT

SAM

SE

TT

GV

SAM

SE

HE

TT

:SAM

[GV

:SAM

IGV

=SAM

[SE

CSAM

[HE

ITT

1GV

CSAM

ISE

IHE

1GV

CSAM

2SE

ITT

1HE

CSAM

ISE

1HE

1GV

CSAM

ITT

CSAM

4HE

8SE

CSAM

IGV

SSE

3HE

4TT

ICv

CSAM

ITT

IHE

1GV

.1 ____________________ I __________________ I _________________________ I ______________________________ I ________________ I __________________ I ____________________ I __________________ I ____________________ I __________ I ________________ I ______________

IX-58

U2TB Hose St

28.1

20.0 20.0

51.5

28.0

15.0

2.0

62.7

68.2

34 .1

33.1

1.0

12.0

1.0

1.5

3.8

6.0

17.0

6.6

7.0

30.0

3.0

16.8

14.0

7.0

3.0

32 .0

34.1

33.1

8.5

23.3

14.0

7.0

3.0

5.5

15.0

121.5

20.0

96.0

63.5

3.0

70.0

21.0

120.0

32.0

6.3

30.0

7.0

3.0

PACE C- /gy

68.1

96.5

198.1 i

14.0

5.3

23.0

46.6 6

40.8

107.7

47.3 3

20.5

237.5

309.5

46.3

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

-2.165

-3.681

13.207

0.000

-1.169

2.901

-4.114

-4.114

-13.943

0.000

0.000

-7.483

-3.992

0.000

-2.165 I1:

-3.681 i1

-13.207 1

0.000 1

-1.169 I1

2.901 1

-4.114 I

-4.114

-13.943

0.000

0.000

-7.483

-3.992

0.000

20

20

20

20

.20

.20

120

120

120

120

120

120

120

20 10.000 10.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

AMENDMENT 13Revision 0 Attachment C

HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS PAGE CZ0

I I I PIPE DIAMETERI PIPE/FTG TOTAL IHEAl) LOSSIHEAD LOSS

IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH I PER FT. OVER PIPE

INO. I NODES (US GPM) (IN) (IN) # (FT) (FT) I (PSI) I (PSI)

STATIC I TOTAL

;HEAD LOSSIHEAD LOSS

I (PSI) I (PSI)

IROUGHI WATER I VELOC.I

NESS IVELOCITYI PRESS.I

ICOEFFI(FT/SEC)l (PSI) I

I I I I I I_I I I ___________ I ______ I _______ I ________ ____ 0.823 I IC I

. _I. --

182

182

182

83

183

183

183

8

18

1I

iI

71

8

9

2

33

34

35

.36

837

839

840

841

102 855

200 839 1 4

839 831 4

42 837

61 832

98 833

54 834

73 835

833 828

828 829

96 838

838 845 J

75 823

I__ 4.40.00

8.96

8.96

0.00

0.00

0.00

0.00

0.00

0.00

0.00

11.70

0.00

0.00

I6.07 CS

6 IT

6 1G

6 i1

6 is

6.07 CS

6 11

6.07 CS

10.02 CS

10 21

6.07 C

6 1,

6 I

6 i1' 6.07 C

6 I1

6 1

6 1,

6.07 C

6 2

6 2

6 2

6 1

6.07 C

6 1

6

6

6

6.07

6

6

6.07

6

6

6

6.07

6

6

6

4.03

4

4

4

4

7.98

8

8

8

AM

T

'V

;E

IE

AM

I.T

SAM

SAM

HE

SAM

SE

GV

TT

SAM

SE

TT

GV

:SAM

SE

HE

2TT

LGV

:SAM

2TT

2SE

2HE

lGV

CSAM

9SE

2TT

CSAM

8SE

2HE

ITT

CSAM

1HE

IGV

ITT

CSAM

SHE

2SE

ITT

lGV

CSAM

ITT

2SE

1HE

I _______________________ I ___________________________ I _______________ I ________________ I __________________ I ________________ I __________________ l.....................I ______________ I ____________

IX-59

U2TB Hose St

30.0

3.0

7.0

14.0

2.3

8.8

3.0

11.0

22.0

9.9

14.0

3.0

30.0

25.6

14.0

30.0

3.0

28.6

28.0

14.0

60.0

3.0

24.5

30.0

28.0

14.0

3.0

75.9

126.0

60.0

100.0

112.0

14.0

30.0

62.4

2.1

0.9

8.8

117.8

20.0

20.0

20.0

2.0

32.0

33.1

34.1

8.5

1-1-1-

58.4 0.000oo II

II

11.1 10.000452

3.0 10.000452

33.0 1 0.000

56.9 0.000

72.6 1 0.000

133.6 0.000

99.5 0.000

261.9 0.000

256.0 0.000

74.2 10.000031

179.8 0.000

107.7 0.000

0.000

0.00503

0.00136

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.00237

0.000

0.000

0.823

-3.464

0.000

0.000

0.0433

1.429

-8.531

-8.314

-0.684

-28.112

0.000

37.024

-13.943

0.823 12

-3.459

0.00136

0.000

0.0433

1.429 1

-8.531 1

-8.314 1

-0.684

-28.112

0.00237

37.024

-13.943

20

62

62

20

20

20

120

120

120

120

62

120

120

0.000 0.000

0.544 10.0019

0.544 10.0019

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 O.00C

0.000 0.00(

0.130 10.000

0.000 0.00

0.000 0.00

0

0

0

o0

AMENDMENT 13


I I I PIPE DIAMETERI PIPE/FTG I TOTAL IHEAD LOSSIHEAD LOSS I STATIC TOTAL

IPIPEI PIPE I FLOW I NOM ACTUALI CODE LENGTH I LENGTH I PER FT. OVER PIPE HEAD LOSSIHEAD LOSS

NO. I NODES I (US GPM)I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI) (PSI) (PSI)

CaIc. No. DREOO-00O0 Revision 0 Attachment C

PAGE : I

IROUGHI WATER I INESS IVELOCITYI

ICOEFFI (FT/SEC)l

VELOC.I

PRESS.

(PSI)

1842 I 809 810 0.00

850 1 93 850 0.00

I I I I 1851 89 851 I 0.o00

I I

I I 1860 I 97 860 I 13.08

861 860 861 0.00

I I I I

II

1922 19 919 8.93

1925 23 923 44.25

1931 928 28 3.33

932 29 929 3.33

1 ____________ I ___________I____________

3.07 I CSAM3.07 CSAM

ISE

1GV

6.07 CSAM

1GV

2SE

ITT

4.03 CSAM

3SE

ITT

1GV

IHE

6.07 CSAM

1GV

1HE

4.03 CSAM

3HE

3SE

ITT

IGV

7.85 CSAM

7.98 CSAM

3SE

ITT

IGV

7.98 CSA!

7.98 CSAM

23.3 I23 .3

7.0

1.0

12 .5

3.0

28.0

30.0

12.9

30.0

20.0

2.0

4.0

51.5

0.9

2.1

119.8

12.0

30.0

20.0

2.0

29.2

21 .2

15.1

9.8

1.1

98.2

2.5

31.3 I 0.000 I 0.000I

12 II 0.000 I 0.000 II

I _____ I ______ I ___ I _____ I ____ I______________________ I ____________________ I _____________________________ I __________________________________ I __________________ I ____________________ I

IX-60

U2TB Hose St

I

31.3 0.000 0.000

73.5 0.000 0.000

68.9 0.000 0.000

54.4 10.0000391 0.00214

183.8 0.000 0.000

29.2 10.00000601 0.000176

47.2 0.000098 1 0.00464

1 1

1 1

98.2 0.98SE-6 10.0000968

2.5 10.985E-6 0.0000024

0.000 0.000

-2.598 -2.598

-2.382 -2.382

0.000 0.00214

38.020 38.020

0.476 0.477

12.774 12.779

0.000 10.0000968

0.000 10.0000024

120

120

120

62

120

59

62

56

56

0.000 0.000

0.000 0.000

0.000 0.000

0.145 10.000141

1 1 1 1

0.000 0.000

0.0592 10.23E-41 0.284 10.000541

I I

I I

0.0213 10.30E-51

0.0213 I0.30E-51



COMPANY Nexus Technical Services Corporation IPAGE 200J

DESIGNER BY: BRIAN FOX CHECKED: J

A.-." G DATE 2000 JAN 6




SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS I INPUT POINTS POINT REQUIRED 1

1 ELEVATION DISCHARGE I K-FACTORI

NO. JDISCHG. GPM P.S.I. NO. IDISCHG. GPM I P.S.I. I NO. jDEMAND GPM P.S.I. (FT) (US GPM)

i1 149.928 500.000

2 145.814 509.500

3 142.999 516.000

4 145.25i 510.800

5 145.251 510.800

6 1 1 145.251 510.800

7 145.466 510.300

8 145.767 509.600

9 145.767 509.600

1 I 10 143.211

515.500

I1 126.453 554.200

12 143.211 515.500

13 145.679 509.800 I

14 145.895 509.300

I 15 1 145.982 509.100

16 145.201 510.900

17 145.547 510.100

le 145.892 509.300

9I 145.849 509.400

20 144.982 511.400

21 145.328 510.600

22 144.948 511.500 I

23 144.945 511.500

24 139.093 525.000

25 145.155 511.000

26 144.938 511.500

27 145.371 510.500

28 144.720 512.000

29 144.720 512.000

30 145.067 511.200 I

31 144.638 512.200 I

32 144.294 513.000 I

33 144.732 512.000

34 144.867 511.700

35 145.547 1 1 1 510.100 1

361 1 144.522 1 1 1 512.500 1

37 145.220 510.900

38 145.168 511.000 1 I

39 145.122 511.100 1

1 401 127.53 1 150.000 1 500.000 I

41 145.2691 1 1 1510.9001

42 145.252 510.900 1

45 145.225 510.9001

46 144.286 513.000 1

IX-61

AMENDMENT 13Calc. No. DREOO-0008 Revision 0 Attachment C


SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS INPUT POINTS POINT REQUIRED ELEVATION DISCHARGE K-FACTOR'

NO. IDISCHG. GPM P.S.I. NO. IDISCHG. GPM P.S.I. NO. IDEMAND GPM I PSI. - (FT) I (US GPM)

47 144.286 513.000 1

48 137.126 529.500 1

49 134.527 535.500

50 134.094 536.500

51 133.098 538.800

52 144.867 511.700

53 125.614 556.000

54 125.610 556.000

55 125.585 556.000

56 125.579 556.000

57 125.579 556.000

58 126.292 554.500

59 126.292 554.500 1

60 126.293 554.500

61 126.340 554.400

62 122.834 562.500

63 119.761 569.600

64 138.642 526.000 1

65 141.038 520.500 1

66 141.037 520.500 1

67 138.642 526.000

68 127.078 552.700

69 138.642 526.000

I70 128.030 550.500

71 124.566 558.500

72 125.865 555.500

73 125.865 555.500

74 125.865 555.500

75 125.865 555.500

76 125.865 555.500

77 125.866 555.500

78 126.299 554.500

79 126.299 554.5000

80 138.642 526.000

81 119.718 569.700 1

82 138.643 526.000

83 141.687 519.000

84 141.687 519.000

85 142.326 517.500

86 138.643 526.000

87 142.326 517.500

88 138.513 526.300

89 138.210 527.000

91 138.556 526.200

92 138.210 527.000

93 138.210 527.000

96 147.533 505.500

97 147.532 505.500

98 127.728 551.200

IX-62

U2TB Hose StPAGE CZ3

Cabc. No. DREOO-OOOS AMENDMENT 13 Rcvision 0

Attachment C

HYDRAULIC CALCULATIONS .. NODE CHARACTERISTICS


ELEVATION DISCHARGE

df IrnTCHG. GPM P.S.I. NO. IDISCHG- GPM I P.S.I. NO. IDEMAND GPM I P.S.I. I (FT) I (US GPM)

526.00_ _ _ _ _ _ _ _ _ _ _ _ __.__ _ _ _ _ __I_ _ _ _ _ _ _ _I.. . . . . . . . ._

_ _ _ _ _ 1 ..........I _ _ _ _ _ _ _ _ _ _ _ _ _ _ _

102 138.642 I

200 134.545 1

201 125.641 1

202 134.538

400 147.532

401 106.178

4021 109.513

4031 147.533

404 106.179 1

405 109.513 1

600 127.53 1 105.769

601 139.093

602 137.664

611 135.845

612 135.845

621 138.097 1

651 121.100 1

700 145.982 1

701 145.418 1

7021 145.331 1

703 144.722

704 137.578

705 145.026

706 139.224

7191 144.946

720 144.721

721 144.721

723 145.372

724 144.947

725 145.892

1 1 1 726 145.892

1 I 1 727 145.892 1 I

1 1 800 1 141.935

1 1 801 1 145.962

1 1 802 141.472

1 803 137.922

804 145.962

805 137.141

808 126.299 1 1

809 128.458

810 128.458

811 129.980

812 133.098

813 138.792

814 131.799

815 130.630

817 138.792

818 139.961

819 134.240 I

________________________ I ________________________ l...................I ________________________ I ________________________

K-.FACTOR

526.000 535.500

556.000

535.500

505.500

601.000

593.300

505.500

601.000

593.300

566.500

525.000

528.300

532.500

532.500

527.300

566.500

509.100

510.400

510.600

512.000

528.500

511.300

524.700

511.500

512.000

512.000

510.500

511.500

509.300

509.300

509.300

518.300

509.000

519.500

527.700

509.000

529.300

554.500

549.500

549.500

546.000

538.800

525.500

541.800

544.500

525.500

522.800

536.000

_ _ _- _I -_ _

IX-63

U2TB Hose St

PA GE. No <R0-000

I I

I I

I I

I I

I I

100.00 I

I I

I I

I I

I I

I I

I I

I I

I P

I I

I I

I I

I I

I I

I I

I I

I I

I I

I I

I I

I I

I I

I I

I I

I I

I I

I I

I I

I I

I I

I I

i00.00 12.400

AMENDMENT 13Calc. No. DRE0O-OOS Revision 0 Attachment C

PAGE CZ5HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS

I SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS INPUT POINTS POINT

ELEVATION

I NO.' IDST•CHC_ GPM P.S.I. NO. DEMAND GPM I P.S.I. I (FT)

IREQUIREDI DISCHARGE K-FACTOR

I (US GPM) I

IX-64

U2TB Hose St

NO. IDISCHG. GPM1- .I. .... ........ ....

820 138.353 526.500 1

822 138.353 526.500

823 139.809 523.300

824 139.809 523.300

825 139.809 523.300

826 139.809 523.300

827 145.655 509.800

828 126.984 552.920

829 155.096 488.000

831 138.003 527.500

832 126.297 554.500

833 126.299 554.500

834 134.141 536.300

835 134.179 536.300

836 138.172 527.080

837 145.252 510.900

838 147.531 505.500

839 138.005 527.500

845 110.507 591.000

1 849 131.799 541.800

1 850 140.808 521.000

851 140.591 521.500 1

855 137.820 527.900 1

I 860 147.530 505.500 1 I

I 861 109.511 593.300 1

919 145.372 510.500

923 132.166 541.000

928 144.720 512.000

929 144.720 512.000

Calc. No. DREOO-OOOS AMENDMENT 13 Re% ision 0

Attachment C

WARNING: THE FOLLOWING PIPE(S) HAVE FLOW(S) SMALLER THAN 0.1 GPM - c__•

1 2 3 4 85 86 87 91 106 500

501 502 503 504 505 611 612 621 651 800

802 803 804 805 806 807 808 809 810 811

812 813 814 815 816 819 820 821 822 823

824 826 827 831 832 833 834 835 836 837

840 841 842 850 851 861

MAXIMUM UNBALANCED HEAD LOSS= .00006 IN LOOP 8 1

IX-65

AMENDMENT 13Calc. No. DREOO-0008 Revision 0 Attachment C

lP-NC C27 o -C._-

IE

Is

Is I U

391 X is operating point for SPECIFIED pressure

I Co-ordinates are

I FLOW - 127.53

PRESSURE 150.00

1 1635 3268 4901

Pump Curve Input Point No.

FLOW 40

IX-66

AMENDMENT 13

CALCULATION NO. DREOO-0008

Revision No. 0

ATTACHMENT D

SPRINK-1000 OUTPUT DATA FIRE HOSE STATION F-126

IX-67

Cakc. No. DREOO-OOOS AMENDMENT 13 Revision 0

Attachment D

DESIGN PROGRAM FOR SPRINKLER SYSTEMS

by



VERSION 11.00


DESIGNER BY: CARL BALINGIT CHECKED:,J4 7"• ILLT CLIENT ComEd. Dresden Nuclear Power Station - Hose Station Hydraulic Analysis



FIX

C-62

P 01 01 02 3.5 11.938

P 02 02 03 16.1 11.938 1GV ITT 3SE CV

P 03 03 04 21.2 7.981 2SE

C-132

P 04 04 05 60.0 11.2 HE SE 3ZSE(7)

P 05 05 06 13.5 11.2 TT GV

C-66

P 06 06 07 156.6 7.85

P 07 07 08 161.0 7.85

P 14 08 13 86.0 7.981 ITT

C-55

P 15 13 14 54.6 7.981

P 750 700 701 72.8 7.981 4HE

P 16 14 15 14.1 11.2 GV

P 17 15 700 44.5 11.2 GV

P 751 701 16 29.3 11.2

C-86

P 18 16 35 9.1 11.2

P 19 35 702 82.7 11.2 HE

P 752 702 17 41.9 7.85

P 20 17 726 119.6 7.85 HE

P 21 725 19 97.9 7.85

P 725 18 725 6.8 11.2 GV

P 726 18 726 4.5 11.2 GV

P 727 18 727 2.1 11.2 GV

C-59

P 762 723 919 12.5 8.385 GV

P 922 919 19 29.2 7.85

C-66

P 22 20 723 82.2 8.385 TT SE ZSE(5)

P 23 20 21 133.3 8.385 TT 3HE GV

P 30 27 703 4.0 7.981 1GV

P 753 703 21 26.0 7.85 TT

C-86

P 29 21 26 147.0 7.981 ITT

P 28 26 25 146.0 7.981 2SE

C-62

P 27 25 601 81.9 7.981 6SE IGV

P 601 601 24 10.8 7.981 ISE

P 754 602 704 58.7 7.981 4SE iHE ITT 1GV

P 602 602 24 123.0 7.981 5SE 2HE GV

P 755 704 705 221.92 7.981 7SE 2HE ITT

IX-68

AMENDMNT 13Caic. No. DREOO.OOOS AMENDMNT 13Revision 0

Attachmnent D

P 756 705 727 141.27 7.981 2HE ITT

C-62

P 300 24 200 136.5 7.981 5SE 1GV ITT

P 26 200 923 7.5 7.981 ISE ITT IGV

P 757 704 706 197.01 4.026 8SE 4HE GV

P 758 706 923 178.37 4.026 12SE 4HE GV

P 925 923 23 21.25 7.981 3SE ITT iGV

C=132

P 25 22 724 75.0 11.2 TT 4HE

C-62

P 719 719 23 5.86 7.981 2HE

C-86

P 763 724 719 26.0 7.85

C-132

P 24 05 22 149.9 11.2 GV TT

C-35

P 50 45 48 255.0 9.564 5SE 2GV IHE

NOTE *

/* THE FOLLOWING PIPES HAD A

/* CALCULATED C FACTOR OF 27.4. DUE*

/- TO LIMITATIONS OF THE SPRINK*

/* PROGRAM, A C OF 35 WAS USED*


/- ADJUSTED TO REFLECT EQUIVALENT

/* FRICTION LOSS.*

/* ACTUAL LENGTHS ARE AS FOLLOWS:

/-PIPE 41 - 10.8*

/-PIPE 42 = 9.8*

/-PIPE 45 = 22.3*

/*PIPE 46 = 10.0.

/*PIPE 49 - 2.0*

/.

P 41 40 41 17.0 10.02

P 42 41 42 15.4 10.02 1HE IG1CV ICy iSE

P 45 42 45 35.1 10.02 ITT

P 46 37 38 15.1 7.981 iGV SE 2HE

P 49 45 37 3.5 7.981 ITT

C-132

P 47 38 39 230.0 11.2 3SE 2HE 4ZSE(7) 3ZSE(3)

P 48 39 22 59.3 11.2

C-62

P 55 48 67 115.92 10.02 7SE

P 70 67 69 3.25 10.02

P 69 69 80 2.17 10.02

P 68 80 64 5.33 10.02 1GV

P 67 64 63 86.75 7.981 9SE 2TT IGV 2HE

P 66 63 62 36.93 6.065 4SE IGV ITT

P 65 62 61 70.08 6.065 3SE 2HE

P 64 61 60 130.25 6.065 3SE 4HE ITT

P 63 60 59 30.83 6.065

P 62 59 58 6.75 6.065

P 302 58 201 80.0 6.065 IGV 4HE

P 303 201 202 482.5 10.02 2TT

P 305 57 201 89.0 6.065 iSE IGV 2HE

P 60 56 57 1.0 7.981

P 59 55 56 15.08 7.981 4HE

P 58 54 55 107.58 7.981 2HE

P 57 53 54 15.5 7.981

F.(:C, t)z-

IX-69


P 56 70 53 118.25 7-981 7SE 1HE 1GV

Attachment D

P 54 51 70 11.67 10.02

P 53 50 51 2.33 10.02

P 52 49 50 1.0 10.02

P 51 48 49 6.0 10.02 ITT

P 8 8 9 30.0 7.981 IGV

p 9 9 10 110.0 4.026 2SE IHE 2TT 1GV

P 10 10 12 215.42 4.026 15SE 7HE 2GV ITT

p 11 10 11 77.5 4.026 5SE 2HE 1GV

P 12 11 12 80.25 4.026 8SE 4HE 1GV

P 13 12 15 34.75 4.026 4SE 1GV ITT

P 83 70 68 2.33 10.02 1GV

P 82 68 71 89.83 7.981 3SE

P 81 71 72 54.75 7.981 4SE IHE

P 80 72 73 15.58 7.981

P 79 73 74 103.58 7.981

p 78 74 75 1.75 7.981

P 77 75 76 14.50 7.981

P 76 76 77 21.50 6.065 2SE

P 75 77 78 175.67 6.065 4SE 2HE IGV

P 74 78 79 65.83 6.065 2HE

P 73 79 98 122.0 6.065 2SE 2HE

P 72 98 81 32.25 6.065 3SE 2TT IHE

P 71 81 63 84.83 6.065 IGV

P 110 64 102 0.5 10.02

P 84 102 82 10.5 10.02

P 99 82 86 1.0 10.02 ITT

P 100 86 85 48.5 6.065 2SE 3HE 1GV

P 102 97 84 14.33 7.981 2HE 1TT

P 103 84 66 1.50 7.981

P 104 66 47 27.75 7.981 4SE 2GV SR

P 105 47 28 115.0 7.981 ISE 1GV ITT

C-56

P 31 28 721 125.0 7.981

P 761 721 720 17.0 8.385 2HE

P 760 720 27 75.5 7.981 ISE

C-62

P 90 82 88 1.00 10.02 ITT

P 93 88 87 66.0 6.065 4SE 3HE 1GV ITT

P 95 96 83 14.17 7.981 2HE ITT

P 96 83 65 1.50 7.981

P 97 65 46 31.25 7.981 5SE 2GV 1SR

P 98 46 29 112.0 7.981 ISE 1GV ITT

C-56

P 932 29 929 2.5 7.981

P 32 929 928 184.0 8.425 2SE 5HE 2GV

P 931 928 28 98.2 7.981

P 33 30 29 20.0 7.981

C=41

P 40 37 36 160.0 7.981 IGV 1TT 4SE 3HE

C-61

P 39 36 52 160.0 7.981

P 38 52 34 10.00 7.981

P 37 34 33 280.0 7.981 5SE IHE

C-55

P 36 33 32 300.0 7.981

C.71

P 35 32 31 285.0 7.981

C-61

p 34 31 30 285.0 7.981 IX-70

............. **.. ****.

NOTE

/* THE FOLLOWING PIPES WERE *

/ ADDED TO ATTACH SYSTEMS *

/ TO THE BASE MODEL

/ . ** * ** *

C.120

P 611

P 612

P 621

P 834

R

P

AMENDMENT 13 Calc. No. DREOO-OOOS Rev.ision 0 Attachment D

&tc 14-

601 611 4.5 6.065 2SE iTT

611 612 1.0 6.065

602 621 3.6 6.065 3SE ITT

54 834 28.6 6.065 2SE 2HE 2TT IGV

834 536.3

803 834 800 30.9 6.065 3SE IHE

R 800

P 804

R 801

P 822

R 804

P 805

R 805

P 815

R 819

P 816

R 820

P 819

R 822

P 809

R 808

P 106

R 812

P 806

P 808

P 807

R 84

R 81

518.1518.3

800 801

509.0

801 804

121.75 5.047 7SE 4HE

5.5 3.068 ITT

509.0

56 805 25.75 7.981 1HE ITT

529.3

805 819 6.0 7.981 ISE

536.0

819 820 6.58 6.065 IHE ITT iGV

526.5

819 822 16.75 6.065 ISE 1HE 1GV

526.5

77 808 1.0 2.469 ITT .GV

554.5

51 812 1.0 7.981 ITT IGV ISE

538.8

49 849 84.1 4.026 3SE 2HE ITT 1GV

849 815 18.0 4.026 4SE IHE 1GV

7 849 814 2.5 4.026 ISE ITT yGV

9 541.8

4 541.8

R 815 544.5

P 810 60 809 28.08 4.026 2SE ITT

R 809 549-5

P 842 809 810 23.33 3.068 ISE IGV

R 810 549.5

P 811 79 811 51.5 3.068 4SE ITT 2GV

R 811 546.0

P 833 98 552 11.17 6.065

P 552 552 833 11.0 6.065 ISE iTT 1GV

R 833 554.5

P 836 833 828 75.92 6.065 9SE 2TT

R 828 552.92

P 837 828 829 100 6.065 8SE 2HE ITT

R 829 488.0

P 832 61 832 9.9 6.065 ISE iGV ITT

R 832 554.5

P 835 73 835 24.5--6.065 ITT 2SE 2HE 1GV

R 835 536.3

P 812 55 813 62.7 7.981 4SE 4HE ITT

R 813 525.5

P 813 813 817 1.0 2.469 ITT iGV

R 817 525.5

P 814 813 818 1.5 7.981 yGV

R 818 522.8

P 841 75 823 32.0 7.981 ITT 2SE IKEIX-71

i


Attachment D

R 823 523.3

P 820 76 824 32.0 7.981 2SE ITT IHE

R 824 523.3

P 821 824 825 23.25 6.065 ISE iHE 1GV

R 825 523.3

P 826 824 826 6.3 6.065 ITT IHE 1GV

R 826 523.3

P 850 93 850 12-5 6.065 1GV 2SE iTT

R 850 521.0

P 87 92 93 152.1 4.026 2SE 6HE

P 86 91 92 16.0 6.065 2HE IGV ITT

P 85 82 91 1.0 10.020 ITT

R 91 526.2

R 92 527.0

R 93 527.0

P 851 89 851 12.9 4.026 3SE ITT 1GV iHE

R 851 521.5

P 91 88 89 166.9 4.026 IGV 8HE

R 89 527.0

P 800 928 802 33.83 6.065 iTT iGV 2SE

R 802 519.5

P 802 802 803 115.08 4.026 2HE ITT 4SE

R 803 527.7

P 840 838 845 117.8 4.026 5HE 2SE ITT 1

R 845 591.0

C-62

P 839 96 838 62.4 6.065 IHE 1GV iTT

P 94 838 87 206.1 6.065 6SE 2HE iTT

P 860 97 860 51.5 6.065 iGV IRE

P 101 860 85 168.5 6.065 7SE 3HE

C-120

R 838 505.5

P 861 860 861 119.75 4.026 3HE 3SE TT

R 860 505.5

R 861 593.3

P 827 102 855 4.39 6.065 ITT iGV IHE 1

P 831 42 837 11.0 10.02 2HE

P 824 835 836 63.5 6.065 IGV 5SE 3HE 4

R 836 527.08

P 823 836 827 121.5 5.047 4HE 8SE

R 827 509.8

R 837 510.9

R 855 527.9

C-62

P 828

P 829

P 304

1GV

GV

GV

SE

TT icV

200 839 2.3 6.065 ITT

839 831 3.0 6.065

831 202 2.7 6.065

C=120

R 839 527.5

R 831 527.5 */***************** ***********

END

.*** **.**********

C=120

p 500

P 501

P 502

P 503

P 504

P 505

97 400 26.17 6.065 iHE

400 401 132.67 6.065 2SE 4HE ITT IGV

401 402 52.17 4.026 3SE ITT 2GV

96 403 7.75 6.065 iHE

403 404 132.33 6.065 ITT 2SE 3HE IGV

404 405 47.0 4.026 ITT 3SE 2GV

PýNý tlS

IX-72

Calc. No. DREuU-000U

AMENDMENT 13 Revision 0 Attachment D

/ .... .. .. .. . * .. . . . . . * .

/. The following nodes and pipes

/ refer to hose stations. To *

/ switch between hose stations,

/ change the S to an R and remove

* the flow and K-factor on the hose *

/* stations that you do not want *

/ to flow.

/ HOSE STATION F-75

p 600 57 600 13.5 1.610 ITT 2SE 1GV

R 600 566.5

/HOSE STATION F-80

P 651 61 651 49.1 1.610 ITT 2SE 1GV

R 651 566.5

/ HOSE STATION F-126

P 550 552 550 21.33 6.065 ITT

P 551 550 551 28.75 1.610 2SE lGV

S 551 566.5 100 12.4

/************ ***************t*******

/, END

/.............. **** *

R 02 509.5

R 03 516.0

R 04 510.8

R 05 510.8

R 06 510.8

R 07 510.3

R 08 509.6

R 09 509.6

R 10 515.5

R 11 554.2

R 12 515.5

R 13 509.8

R 14 509.3

R 15 509.1

R 16 510.9

R 17 510.1

R 18 509.3

R 19 509.4

R 20 511.4

R 21 510.6

R 22 511.5

R 23 511.5

R 24 525.0

R 25 511.0

R 26 511.5

R 27 510.5

R 28 512.0

R 29 512.0

R 30 511.2

R 31 512.2

R 32 513.0

R 33 512.0

R 34 511.7

R 35 510.1

R 36 512.5

R 37 510.9

R 38 511.0

R 39 511.1 IX-73

AMENDMENT 13Calc. No. DREOO-OOOS Revision 0 Attachment D

S41 510.9

S42 510.9

S45 510.9

R 46 513.0

. 47 513.0

R 48 529.5

R 49 535.5

R 50 536.5

R 51 538.8

R 52 511.7

R 53 556.0

R 54 556.0

R 55 556.0

R 56 556.0

R 57 556.0

R 58 554.5

R 59 554.5

R 60 554.5

R 61 554.4

R 62 562.5

R 63 569.6

R 64 526.0

R 65 520.5

R 66 520.5

R 67 526.0

R 68 552.7

R 69 526.0

R 70 550.5

R 71 558.5

R 72 555.5

R 73 555.5

R 74 555.5

R 75 555.5

R 76 555.5

R 77 555.5

R 78 554.5

R 79 554.5

R 80 526.0

R 81 569.7

R 82 526.0

R 83 519.0

R 84 519.0

R 85 517.5

R 86 526.0

R 87 517.5

R 88 526.3

R 96 505.5

R 97 505.5

R 98 551.2

R 102 526.0

R 200 535.5

R 201 556.0

R 202 535.5

R 400 505.5

R 401 601.0

R 402 593.3

R 403 505.5

R 404 601.0

R 405 593.3

R 601 525.0

-PýC- P7

IX-74


Attachment D

R 602 528.3

R 611 532.5 P' 7 .pb

R 612 532.5

R 621 527.3

R 120 512.0

R 721 512.0

R 723 510.5

R 724 511.5

R 700 509.1

R 701 510.4

R 702 510.6

R 703 512.0

R 704 528.5

R 705 511.3

R 706 524.7

R 719 511.5

R 725 509.3

R 726 509.3

R 727 509.3

R 919 510.5

R 923 541.0

R 928 512.0

R 929 512.0

R 552 554.5

R 550 554.5

/* NOTE

/* TO DEACTIVATE PUMP UNIT 1:*

/ CHANGE:*

/1 1 01 500.0 0.0 150 2000 150 2500 140 3750 91 3751 10"

/ TO:*

/ R 01 500.0

/***************** *** ******************

R 01 500.0 ********************************************************

NOTE

/ TO DEACTIVATE PUMP UNIT 2/3:*

/* CHANGE:'

1' 1 40 500.0 0.0 150 2250 150 3000 131 3600 120 4900 110 4901 10'

/* TO:'

/* R 40 500.0 *****************************************

I 40 500.0 0.0 150 2250 150 3000 131 3600 120 4900 110 4901 10





ITERATION STOPS W•IEN GREATEST FLOW CHANGE IS .05000 IN ANY PIPE


DEFAULT ROUGHNESS COEFFICIENT - C-120.0



IX-75

AMENDMENT 13Calc. No. DREOO-OOOS Revision 0 Attachment D

THE NUMBER OF INPUT POINTS IN SYSTEM IS I



40 1 500.00 1.00 .0 2250.0 3000.0 3600.0 4900.0 4901.0

150.0 150.0 131.0 120.0 110.0 10.0

Initial estimate of demand on the system is 100.00

NET UNBALANCED DEMAND ON THE SYSTEM - .00000

LOOP PIPES

1 551 550 833 72 71 67 68 69

2 73 72 71 67 68 69 70 55

75 74

3 67 66 65 64 63 62 302 305

68

4 50 55 70 69 68 110 84 90

70 55 50

51 52 53

60 59 58

93 94 839

38 39 40 49

303 305 60 59 58 57 56 54 53 52 51

26 828 829 304

99 90 93 94 839 95 96 97 98 932 32

932 33 34 35 36 37 38 39 40 46 47

28 29 753 30 760 761 31 931 32

754 757 758 26 300 602

25 24 5 6 7 14 15 16 17 750 751

758 925 719 763

725 727 756 755 754 602 601 27 28 29 23

14 8 9 10 13 16 15

10 11 12

BANDWIDTH - 5







NUMBER OF ITERATIONS- 6

45 42 41 54 83 82 81

57 56 54 53

95 96 97 98

50 49 46 47

931 105 104 103

48 25 763 719

80 79 78 77 76

52 51 55 70 69

33 34 35 36 37

48 25 763 719 925

102 860 101 100

925 26 300 601 27

18 19 752 20 726 727 756 755 757

22 762 922 21

82.890 in loop 9 2

33.376 in loop # 2

17.310 in loop 9 5

2.817 in loop # 10

.221 in loop # 8

.008 in loop # 11

IX-76

F^ýC- fxq

5

6

7

8

9

10

11

12

AMENDMENT 13 Caic. No. DREOO-OOOS Revision 0 Attachment D

SUMMARY REPORT

PAGE tDj I COMPANY Nexus Technical Services Corporation

DATE 00 .

DESIGNER BY: CARL BALINGIT CHECKED: DATE 2000 JAN 13


PROJECT lUI DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP


I ______I

MINIMUM FLOW OF ALL OPERATING SPRINKLER HEADS IS 125.54

AVERAGE FLOW FROM ALL OPERATING SPRINKLER HEADS IS 125.54

TOTAL FLOW FROM ALL OPERATING SPRINKLER HEADS IS 125.54

TOTAL DEMAND ON THE WHOLE SYSTEM IS 125.54

SPECIFIED AVAILABLE PRESSURE AT INPUT NODE IS 346.40 FEET

OR 150.00 P.S.I.

IX-77

AMENDMENT 13 Calc. No. DREOO-000S Revision 0 Attachment D

HYDRAULIC CALCULATIONS - PIPE CHARACTERISTICS

I PAGE 2 N13 ]DATE 2000 JAN 13I COMPANY Nexus Technical Services Corporation

DESIGNER BY: CARL BALINGIT CHECKED:



JOB NO. I mU3T ose I

I PIPE DIETER PIPE/TG TOTA AD LOSSIHEAD LOSS I STATIC TOTAL IROUGHI WATER I VELOC.

IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. OVER PIPE 1HEAD LOSSIHEAD LOSS INESS IVELOCITYI PRESS.[

NO. I NODES (US GPM)I (IN) (IN) I # (FT) I (FT) (PSI) I (PSI) I (PSI) I (PSI) ICOEFFI (FT/SEC)l (PSI)

1 1 2 0.00 11.94 CSAM 3.5 3.5

2 2 3 0.00 11.94 CSAM 16.1 77.0

12 1GV 1.7

12 ITT 17.2

12 3SE 23.3

12 ICV 18.7

3 3 4 0.00 7.98 CSAM 21.2 31.2

8 2SE 10.0

4 4 5 0.00 11.20 CSAM 60.0 115.1

12 lHE 11.1

12 ISE 23.0

12 3ZSE 21.0

5 5 6 13.65 11.20 CSAM 13.5 69.8

12 ITT 51.2

12 1GV 5.1

6 6 7 13.65 7.85 CSAM 156.6 156.6

7 7 8 13.65 7 7.85 CSAM 161.0 161.0

8 8 9 1.56 7.98 CSAN 30.0 31.1

8 I1GV 1.1

9 9 10 1.56 4.03 CSAM 110.0 129.4

4 2SE 5.9

4 1HE 1.2

4 2TT 11.8

4 I1GV 0.6

10 I 10 12 0.72 4.03 CSAM 215.4 274.9

I 1 4 115SE 44.2 1

1 1 4 7HE 8.2

1 1 4 2GV 1.2

1 4 ITT 5.9

11 10 11 0.85 4.03 CSAM 77.5 95.2

4 5SE 14.7

4 2HE 2.4

4 1GV 0.6

12 11 12 0.85 4.03 CSAM 80.3 109.1

4 8SE 23.6

4 4HE 4.7

4 I1GV 0.6

13 12 15 1.56 4.03 CSAM 34.8 53.0

4 4SE 11.8

[4 1GV 0.6

I 4 I1TT 5.9

141 8 13 12.09 7.98 CSAN 86.0 97.0

I 8 ITT 11.0

15 I 13 14 12.09 7.98 CSAM 54.6 54.6

0.000 0.000 0.000 0.000

0.000 0.000

0.000 0.000

0.529E-6 10.0000369

0.000010 I 0.00169

-0000Z10 1 0.00173

,0.202E-6 10.0000062

;0.00000561 0.000733

10.00000131 0.000369

10.00000181 0.000172

l0.00000181 0.00019•

10.0000056I 0.00030

1 1

10.00000791 0.00076

S0 1 l0.000011 10.00060

7

0

9

7

4.11 .14 64.114 4.114 2.815 2.815

-2.252 -2.252

0.000 0.000

0.000 10.0000369

-0.217 -0.215

-0.303 -0.301

0.000 10.0000062

2.555 1 2.556

0.000 1 0.00036S

16.758 16.753

-16.758 -16.751

-2.771 -2.77

0.0866 0.087

-0.217 -0.21

Ii

8

4

6

62

62

62

32

32

66

66

62

62

62

62

62

62

66

55

0.0 .0

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.0445 10.13E-4

0.0905 10.55E-4

0.0905 10.55E-4

0.0100 10.67E.6

0.0394 10.10E-4

0.0181 10.22E-5

0.0213 10.30E-5:

0.0213 I0.30E-5

0.0394 10.10E-4'

0.0775 10.40E-41

0.0775 10.40E-41

I I I I

______________ I _____________ I __________________ I _____________________ I ___________ I ____________ ______________ I ____________ I ______________

IX-78

AMENDMENT 13Calc. No. DREOO-OOOS Revision 0

Attachment D


I I I PIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSS IHEAD LOSS

IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH PER FT. lOVER PIPE

INO. I NODES (US GPM) I (IN) (IN) I # (FT) (FT) (PSI) I (PSI)

I STATIC TOTAL

HEAD LOSSIHEAD LOSS

I (PSI) I (PSI)

IROUGHI WATER I VELOC.IIROUGHI WATER I VELOC. INESS IVELOCITYI PRESS.1

ICOEFFI(FT/SEC) (PSI) I

I I ___________ I __________ 15.1 10.00000211

16

17

18i

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

38

14 15 I

15 700 1

16 35 I 35 702

17 726

725 19

723 20

20 21

22 5

22 724

923 200

601 25

25 26

26 21

703 27

721 28

929 928

30 29

31 30

32 31

33 32

34 33

52 34

2.09

3.65

.3.65

.3.65

L3.65

9.69

9.69

9.69

13.65

39.68

38.55

6.52

6.52

6.52

16.21

16.21

0.44

15.19

15.19

15.19

15.19

15.19

15.19

15.1 0.0000021

45.5 10.00000261

1 1 9.1 I0.00000111

87.7 10.0000011l

1 1 123.8 10.00000661

1 1 97.9 10.00000341

3.0000323 I0.0000323

0.000122

0.0000106

0.000103

0.000817

0.000342

•..

I 006 I 0086 I 55 II

11.20 C

12 1'

11.20 C

12 1

11.20 C

11.20 C

12 1

7.85 C

8 1

7.85 C

8.39 C

8 1

8 1

8 1

8.39 I 8

8

8

11.20

12

12

11.20

12

12

7.98

8

8

8

7.98

8

8

7.98

8

7.98

8

7.98

8

7.98

8.43 3

8

8

8

7.98

7.98

7.98

7.98

7.98

8

8

7.98

I ______ I _____ I _______ I ________ I ____ I _____ I ______ I _____ I ______ I ___ I _____ I ____ I

IX-79

U3TB Hose St

SAM

GV

SAM

GV

SAM

SAM

HE

SAM

HHE

SAM

SAM

TT

SE

.ZSE

:SAM

ITT

3HE

LGV

CSAM

1GV

ITT

CSAM

ITT

4HE

CSAM

ISE

ITT

1GV

CSAM

6SE

1GV

CSAM

2SE

CSAM

ITT

CSAM

1GV

CSAM

CSAM

2SE

5HE

2GV

CSAM

CSAM

CSAM

CSAM

CSAM

5SE

1HE

CSAM

14.1

1.0

44.5

1.0

9.1

82.7

5.0

119.6

4.2

97.9

82.2

13.9

7.2

5.0

133.3

13.9

10.7

1.6

149.9

5.1

51.2

75.0

51.2

44 .3

7.5

5.0

9.8

1.1

81.9

30.1

1.1

146.0

18.4

147.0

17.9

4.0

1.3

125.0

184.0

10.8

13.5

2.4

20.0

285.0O

285.0

300.0

280.0

24.3

2.4

10.0

108.3 10.00000411 0.0004481

159.6 10.00000411 0.000660 1

206.2 10.529E-6 0.000109

170.5 10.00000381 0.000650

23.4 10.000076 1 0.00178

113.1 10.00000281 0.000321

164.4 I0.00000151 0.000255

1 1 164.9 10.00000151 0.000256

5.3 10.000013 10.0000717

125.0 10.000018 0.00231

210.7 I0.176E-7 10.0000037

1 1 1 1 1 1

20.0 0.000016 0.000328

285.0 0.000014 0.00399

285.0 10.000010 0.00302

300.0 10.000017 0.00509

306.8 10.000014 0.00430

10.0 10.000014 0.000140

PAGE p i"Z-,

-0.0866

0.000 0

-0.346

0.217

-0.346

0.0433

0.390

-0.346

-0.303

0.000

-2.382

-6.062

0.217

-0.390

-0.650

0.000

0.000

0.346

-0.433

-0.346

0.433

0.130

0.000

-0.0866

.000122

-0.346

0.217

-0.346

0.0436

0.390

-0.346

-0.303

0.000650

-2.380

-6.062

0.217

-0.389

-0.649

0.00231

0.0000037

0.347

-0.429

-0.343

0.438

0.134

0.000140

55

55

86

86

86

86 66

66

132

132

62

62

86

86

66

56

56

56

61

71

55

61

61

0.0394 10.10E-41 1 I

0.0445 10.13E-41

1 I 0.0445 10.13E-41

0.0445 10.13E-41

1 1 0.0905 10.55E-41

1 I 0.0642 10.27E-41

0.0563 10.21E-41

0.0563 10.21E-41

0.0445 10.13E-41

1 1 1 1

0.129 10.00011

0.247 10.000411

1 I

0.0418 10.IXE-41

II

0.0418 10.11E-41

0.0418 1 .11E-4

0.0418 10.1E-4

0.104 0.72E-41

1 I 0.104 10.72E-41

0.00251 10.42E-71

III

III 1 0.0974 10.63E-41

0.0974 10.63E-41

0.0974 10.63E-41

0.0974 10.63E-41

1 0.0974 10.63E-41

I 0 I

10.0974 10.63E-41

AMENDMENT 13Calc. No. DKLUU-Utluu Revision 0 Attachment D

HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS PAGE C13

I I PIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS

IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. JOVER PIPE

NO. I NODES (US GPM) (IN) (IN) I # (FT) (FT) I (PSI) I (PSI)

_______________ - ____________ _______________ I _________________ _________ I __________ -0346 I -0.344 160 0 10.000014 I 0.00224 I

39

40

41

42

45

46

47

48

49

50

51

52

53 54

55

56

57 58

59

60

62

63

I STATIC I TOTAL VELOC. I IROUGHI WATER IISTATIC I TOTAL HEAD LOSSIHEAD LOSS

I (PSI) I (PSI)


ICOEFFI (FT/SEC)I

VELOC. PRESS.

(PSI)

36 52

37 36

40 41

41 42

42 45

37 38

38 39

39 22

45 37

45 48

48 49

49 50

50 51

51 70

48 67

53 70

54 53

55 54

56 55

57 56

58 59

59 60

61 0.0974 I0. I4

15.19

15.19

125.54

125.54

125.54

53.33

53.33

53.33

68.52

57.02

28.58

28.58

28.58

28.58

28.44

16.46

16.46

16.46

16.46

16.46

20.66

20.66

8 8

8

8

10

10

10

10

10

8

8

8

12

12

12

12

8

10

10

10

10

10

8

8

8

8

8

____________________ I __________________ I __________________________ I ______________________________ I ________________ I __________________ I ____________________ I __________________

IX-80

U3TB Hose St

7.98 CSAM

7.98 CSAM

1GV

ITT

4SE

3HE

10.02 CSAM

10.02 CSAM

IHE

I1GV

ICV

ISE

10.02 CSAM

ITT

7.98 CSAM

1GV

ISE

2HE

11.20 CSAM

3SE

2HE

4ZSE

3ZSE

11.20 CSAM

7.98 CSAM

ITT

9.56 CSAM

5SE

2GV

IHE

10.02 CSAM

ITT

10.02 CSAM

10.02 CSAM

10.02 CSA1M

10.02 CSAM

7SE

7.98 CSAM

7SE

1HE

1GV

7.98 CSAM

7.98 CSAM

2HE

7.98 CSAM

4HE

7.98 CSAM

6.07 CSAM

6.07 CSAM

I

160.0

160.0

0.5

4.5

9.3

3.5

17.0

15.4

1.1

0.5

5.6

2.2

35.1

5.1

15.1

0.4 J

1.7

1.7

230.0

69.1

22.2

28.0

9.0

59.3

3.5

3.4

255.0

9.0

0.8

0.9

6.0

14.7

1.0

2.3

11.7

115.9

45.3

118.3

35.1

2.5

1.1

15.5

107.6

5.0

15.1

10.0

1.0

6.8

30.8

160.0 10.000014 1 0.00224 1

177.9 10.000029 0.00520

17.0 10.000646 1 0.0110

24.9 10.000646 1 0.0161

40.2 10.000646 1 0.0260

19.0 10.000401 0.00761

358.2 10.00000651 0.00236

1 1 1 1

I 1 59.3 10.00000651 0.000391

6.9 0.000638 0.00439

265.7 10.000188 0.0500

20.7 10.000014 0.000300 1

1.0 10.000014 I0.0000145 1

2.3 10.000014 10.00003371

11.7 10.000014 0.000169

161.3 0.000014 0.00231

157.0 10.000015 0.00248

15.5 10.000015 0.000244

112.6 10.000015 0.00178

25.1 10.000015 0.000396

1.0 10.000015 10.0000158

6.8 10.000091 0.000618

30.8 10.000091 0.00282

-0.346 -0.344 0.693 0.698

4.720 4.731

0.000 0.0161

0.000 0.0260

0.0433 0.0509

0.0433 0.0457

0.173 0.174

0.000 0.00439

8.054 8.104

2.598 2.598

0.433 0.433

0.996 0.996

5.066 5.067

-1.516 -1.513

-2.382 -2.379

0.000 0.000244

0.000 0.00178

0.000 0.000396

0.000 10.0000158

0.000 0.000618

0.000 0.00282

I61

41

35

35

35

35

132

132

35

35

62

62

62

62

62

62

62

62

62

62

62

62

0.0974 10.63E-41

0.0974 10.63E-41

0.511 0.0017

0.511 0.0017

0.511 10.0017

0.342 0.000781

1 1

0.174 I0.000201 1 1

1 1

0.174 10.000201

0.439 10.0013 1

0.255 0.000431

I 1 1 1

0.116 10.91E-4

0.116 0.91E-4

0.116 10.91E-41

0.116 10.91E-41

0.116 10.90E-41

II 0.106 I0.79E-41

0.116 10.91E-41 0.116 10.90E-41

0.106 10.75E-41 0.106 10.75E-41 0.106 10.75E-41

0.106 10.75E-41

I I 0.106 10.'75E-41

0.229 10.000351

0.229 10.000351

1 I


I I PIPE DIAMETERI PIPE/FTG TOTAL IHEAD LOSSIHEAD LOSS

IPIPEI PIPE I FLOW NOM ACTUALI CODE LENGTH LENGTH PER FT. lOVER PIPE

NO. NODES I (US GPM)I (IN) (IN) # (FT) (FT) (PSI) I (PSI)

______-___________-_________I_-________________I __________________________________ I I ____________________ 0.0146 0.0433 I 0.0287

I

159.7 10.000091 I64

65

66

67

68

69

70

71

72

73

74

75

76

77

78 79

80

81

82

83

84

I

STATIC TOTAL IROUGHI WATER VELOC.

ISTATIC I TOTAL HEAD LOSSIHEAD LOSS

I (PSI) (PSI)

IROUGHI WATER I VELOC. NESS IVELOCITYI PRESS.

ICOEFFI(FT/SEC)I (PSI)

I I I I

60 61

61 62

62 63

64 63

80 64

69 80

67 69

63 81

81 98

79 98

78 79

77 78

76 77

75 76

74 75

73 74

72 73

71 72

68 71

70 68

82 102

(2 0.29 0000I

20.66

20.66

20.66

59.84

28.44

28.44

28.44

80.50

80.50

45.04

45.04

45.04

45.04

45.04

45.04

45.04

45.04

45.04

45.04

45.04

31.40

6.07 CSAM

6 3SE

6 4HE

6 ITT

6.07 CSAM

6 3SE

6 2HE

6.07 CSAM

6 4SE

6 1GV

6 ITT

7.98 CSAM

8 9SE

8 2TT

8 1GV

8 2HE

10.02 CSAM

10 1GV

10.02 CSAM

10.02 CSAM

6.07 CSAM

6 I1GV 6.07 CSAM

6 3SE

6 2TT

6 IHE

6.07 CSAt

6 2SE

6 2HE

6.07 CSAI

6 I2HE 6.07 CSAJ

6 4SE

6 2HE

6 I1GV 6.07 CSA

6 2SE

7.98 CSA

7.98 CSA

7.98 CSA

7.98 CSA

7.98 CS•

8 4SE

8 1HE

7.98 CS•

8 3SE

10.02 CS7

10 IG\

10.02 CS)

M

M

M

14

'M

'M

LM

UM

AM

1 - - 1 1 -____________I __________I _______________I__________________I _________I___________I____________

IX-81

U3TB Hose St

rkIviJ-...L ,1�Aifl.A�a A ± Revision U Attachment D

PAGE L/4-

130.3 12.4

8.2

8.8

70.1

12.4

4.1

36.9

16.5

0.9

8.8

86.8

45.2

19.5

1.1i

5.0

5.3

1.5

2.2

3 .3

84.8

0.9

32.3

12 .4

17.7

2.1

122 .0

8.2

4.1

65.8

4.1

175.7

16.5

4.1

0.9

21.5

8.2

14.5

1.8

103.6

15.6

54.8

20.1

2.5

89.8

15.1

2.3

1.5

10.5

159.7 10000091

86.6 10.000091

63.1 10.000091

157.6 10.000172

6.8 10.000014

2.2 10.000014

3.3 10.000014

85.7 1 0.00114

64.3 0.00114

134.4 10.000387

70.0 10.000387

197.2 0.000387

29.7 10.000387

14.5 10.000102

1.8 0.000102

103.6 10.000102

15.6 10.000102

77.3 0.000102

104.9 10.000102

3.8 10.000033

10.5 10.000017

0.0146

0.00792

0.00578

0.0271

0.0000975

0.0000311

0.0000466

0.0973

0.0731

0.0520

0.0271

0.0764

0.0115

0.00148

0.000171

0.0105

0.00151

0.0078

0.010

0.00012

0.00018

5 8 8 5 8 7 7 8 1

71

81

_____ I ______ I ___ I _____ I ____

0.0433 -0.0287

3.507 3.515

3.074 3.080

18.880 18.907

0.000 10.0000975

0.000 10.0000311

0.000 0.0000466

0.0433 0.141

-8.011 -7.938

-1.429 -1.377

0.000 0.0271

-0.433 -0.357

0.000 0.0115

0.000 0.00148

0.000 0.000178

0.000 0.0105

0.000 0.00158

-1.299 -1.291

2.512 2.52

0.953 0.95:

0.000 0.00018

3

5I

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

62

0.229 10.00035

0.229 10.00035'

0.229 10.00035

0.384 10.00099'

0.116 10.90E-4t

0.116 10.90E-4,

0.116 10.90E-4

0.894 10.0053

0.894 10.0053

0.500 10.0016

0.500 10.0016

0.500 0.0016

0.500 10.0016 i

0.289 0.000561

0.289 10.000561

0.289 0.00056:

0.289 10.000561

0.289 10.000561

0.289 0.00056!

0.183 10.000221

0.128 10-00011


I I IPIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS

IPIPEI PIPE I FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. OVER PIPE

INO. I NODES I (US GPM)j (IN) (IN) # (FT) (FT) (PSI) (PSI)

1 - 1- 1 -_____________ 50I 0.0 I - 0.000

85

86

87

90

91

93

94

95

96

97

98

99

1100

101

1102

1103

I-

IAN 1.0

82 91 1

91 92

92 93

88 82

88 89

87 88 I

838 87 ]

83 96

65 83

46 65

29 46

86 82

85 86

860 85

84 97

66 84

0.00

0.00

0.00

4.76

0.00

4.76

4 .76

14.76

14 .76

14 .76

14.76

16.65

16.65

16.65

16.65

16.65

10.02 C

10 1'

6.07 C

6 2

6 i1

6 I

4.03 C

4 2

4 6

10.02 C

10 1

4.03 C

4 I

4 8

6.07 C

6 4

6

6

6

6.07

6

6

6

7.98

8

8

7.98

7.98

8

8

8

7.98

8

8

8

10.02

10

6.07

6

6

6

6.07

6

6

7.98

8

8 7.98

STATIC TOTAL IROUGHI WATER VELOC.ISTATIC ITOTAL


I (PSI) (PSI)

S AM TT

SAX

HE

GV

TT

SAM

SE

HE

SAM

TT SAM

GV

IHE

7SAM

SSE

IHE

LGV

ITT

CSAM

6SE

2HE

ITT

CSA•M

2HE

ITT

CSAM

CSAlM

5SE

2GV

ISR

CSAM

ISE

IGV

ITT

CSAM

ITT

CSAM

2SE

3HE

1GV

CSAM

7SE

3HE

CSAM

2HE

ITT

CSAM

IROUGHI WATER IVELOC.j NESS IVELOCITYI PRESS.

ICOEFFI(FT/SEC)l (PSI) I

1.0 50.0

16.0

14.0

3.0

30.0

152.1

20.0

24.0

1.0

14.7

166.9

2.0

32.0

66.0

16.5

6.2

0.9

8.8

206.1

24 .7

4.1

8.8

14.2

5.0

9.8

1.5

31.3

25.1

2.2

19.5

112.0

5.0

1.1

9.8

1.0

14.7

48.5

8.2

6.2

0.9

168.5

28.9

6.2

14.3

5.0

9.8

1.5

0

___ -________ 1 _____1____ I- ________________ - 1_______________ - 1______

_________ -___________I__________I___________ _____ ________ ______

IX-82

U3TB Hose St

J-1AY.kJ.�,I � A Kevision U Attachment D

PAGE b 15

51.0 0.000

63.0 0.000

196.1 0.000

15.7 10.00000421

1 1 200.9 0.000 1

98.4 10.000049 1

243.8 10.000049

28.9 10.000012

1.5 10.000012

78.1 10.000012

127.9 0.000012

15.7 10.0000053

63.8 10.000061

203.5 0.000061

29.1 10.000016

1.5 10.000016

0

0.000

0.000

0.000

.0000669

0.000

0.00483

0.0120

0.000373

0.0000193

0.00101

0.00165

0.0000836

0.00391

0.0125

0.000469

10.0000242

0.0866 0.0866

0.346 0.346

0.000 0.000

-0.130 -0.130

0.303 0.303

3.811 3.815

5.196 5.208

-5.846 -5.845

-0.650 -0.650

3.248 3.249

0.433 0.435

0.000 10.0000836

3.681 3.685

5.196 5.209

-5.846 -5.845

-0.650 -0.650

120

120

120

62

120

62

62

62

62

62

62

62

62

62

62

62

_1

0.000 0.000

0.000 0.000

0.000 0.000

0.0600 l0.24E-4i

0.000 0.000

0.164 0.00018

0.164 10.00018

0.0946 10.60E-4

0.0946 10.60E-4

0.0946 10.60E-4

0.0946 0.60E-4

0.0677 10.30E-4

0.185 10.00023

0.185 10.0002:

0.107 10.76E-'

0.107 10.76E--

HYDRAULIC CALCULATIONS .- PIPE CHARACTERISTICS

I I I PIPE DIAMETERI PIPE/FTG TOTAL IHEAD LOSSIHEAD LOSS

IPIPEI PIPE FLOW I NOM ACTUALI CODE LENGTH I LENGTH I PER FT. lOVER PIPE

NO. I NODES (US GPM)I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)

I STATIC TOTAL IROUGHI WATER VELOC. I IHEAD LOSSIHEAD LOSS NESS IVELOCITYI PRESS.I

I (PSI) I (PSI) ICOEFFI(FT/SEC)i (PSI) I

I I I I I II I I I - 1_____________ 1 ________________I_________I_____ 1____ _________

1104

105

1106

1110

1300 1

1 1

1302

1303

1304 1

1305 1

1500

1501

1502

1503

1504

1505

1

-I69.6 10.00

3.248 I 3.249 I I 0

47 66

28 47

51 812

102 64

200 24

201 58

202 201

831 202

201 57

97 400

400 401

401 402

96 403

403 404

404 405

16.65

16.65

0.00

31 .40

1.43

20.66

37. 12

37.12

16.46

0.00

0.00

0.00

0.00

0.00

0.00

7.98 CSAM

8 4SE

8 2GV

8 I1SR

7.98 CSAM

8 ISE

8 I1GV

8 ITT

7.98 CSAM

8 ITT

8 IGV

8 ISE

10.02 CSAM

7.98 CSAM

8 5SE

8 IGV

8 ITT

6.07 CSAM

6 1GV

6 4HE

10.02 CSAf

10 2TT

6.07 CSAM

6.07 CSA"

6 ISE

6 1GV

6 2HE

6.07 CSAI

6 IRE

6.07 CSAJ

6 2SE

6 4HE

6 IiTT

6 IGV

4.03 CSA

4 3SE

4 1TT

4 2GV

6.07 CSA

6 1HE

6.07 CS•

6 ITT

6 2SE

6 3 HEf1 M

6 I1G\

4.03 CS)

4 1Tr

4 3S1

4 2G•

.1 ______________________ I _____________________ I _____________________________ I __________________________________ I __________________ I _____________________ I _______________________ I _____________________ I _______________________ I ___________

IX-83

U3TB Hose St

ZJVlI ¥ xL.,1 .L-I - IJ.. A - NuI,1UIb V Attachment D

PAGE L)I

4

M

M

M km

EM

v

27.8

20.1

2.2

19.5

115.0

5.0

1.1i

9.8

1.0

33.1

3.8

17.0

0.5

136.5

25.1

1.1

9.8

80.0

0.9

8.2

482.5

29.4

2.7

89.0

4.1 I 0.9

4.1

26.2

7.0

132.7

28.0

28.0

30.0

3.0

52 .2

30.0

20.0

4.0

7.8

7.0

132.3

30.0

28.0

21.0

3.0

47.0o

20.0

30.0

4.0

130.9 10.00

55.0 1

0.5 10.0¢

172.5 10.17

89.1 10.0

511.9 10.0

2.7 10.0

98.1 10.0

33.2

221.7

106.2

14.8

214.3

101.0

0016 0.00112

0016 0.00211

0.000 0.000

00017 10.0000086

71E-6 10.0000295 1

00091 0.00815

00023 0.0120

00271 0.000731

00060 I0.00589

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

_________ 1__

3.248

0.433

0.000

0.000 10

-4.547 1

-0.650 1

8.877 1

3.464

0.000

0.000

41.354

-3.334

0.000

41.354

-3.334

3 .249 1 6

0.435

0.000

.0000086

-4.547

-0.641

8.889

3.465

0.00589

0.000

41.354

-3.334

0.000

41.354

-3.334

52 0

62 0

20 0

62 0

62 10.0

62 1 0

62 1

62 1

62 1

120

120

120

120

120

120

.107 10.76E-41

.107 I0.76E-41

II II

.000 0.000

.128 10.000111

0917 I0.56E-61

.229 10.000351

1 1

0.151 10.000151

0.412 10.0011

0.183 10.00022

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

HYDRAULIC CALCULATIONS -" PIPE CHARACTERISTICS

I I PIPE DIAMETERI PIPE/FTG TOTAL IHEAD LOSSIHEAD LOSS STATIC I TOTAL IROUGHI WATER I VELOC.

IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH PER FT. lOVER PIPE HEAD LOSSIHEAD LOSS NESS IVELOCITYI PRESS.

NO. I NODES (US GPM)I (IN) (IN) N (FT) (FT) I (PSI) I (PSI) I (PSI) I (PSI) ICOEFFI(FT/SEC)I (PSI)

I_ _ _ _ 1 _ 1 _ 1 _ 1

1 ___________ I ___________ I_______________

1550

1551

552

600

160

160

61

61

160

16

1

7

1

16

552 550

550 551

552 833

57 600

1 24 601

2 602 24

1I 601 611

.2 1 611 612

21 602 621

51 1 61 651

19 719 23

25 18 725

26 726 18

27 18 727

750 700 701

751 701 16

752 702 17

753 21 703

754 704 602

I 125.54

6

125.54

1 1/2

1 1/2

0.00

6

6

6

0.00

1 1/2

1 1/2

1 1/2

6.52

18

5.09

8

8

18

0.00

6

6

0.00

0.00

6

6

0.00

i 1/:

I1 1if

39.68

8

9.69

12

13.65

12

3.97

12

13.65

8

13.65

13.65

16.21

8

5.09

8

8 8

18

6.07 CSAM ITT

1.61 CSAM

2SE

1GV

6.07 CSAM

ISE

ITT

IGV

1.61 CSAM

1TT

2SE

1GV

7.98 CSAM

ISE

7.98 CSAM

SSE

2HE

1GV

6.07 CSAM

2SE

ITT

6.07 CSAM

6.07 CSAM

3SE

ITT

1.61 CSAM

2 ITT

2 2SE

2 1GV

7.98 CSAM

2HE

11.20 CSAM

I1GV

11.20 CSA4

1GV

11.20 CSAM

1GV

7.98 CSAM

4HE

11.20 CSAM

7.85 CSAM

7.85 CSAM

ITT

7.98 CSAM

4SE

1HE

I1TT

IGV

1 _ __ __ _. _______ I _____ I _____ I ______ I _____ I ______ I ___ I

IX-84

U3TB Hose St

A1VL•lNLIlVILlN" " I.) I\CV Iblul U Attachment D

21.3

30.0

28.8

8.0

1.0

11.0

14.0

30.0

3.0

13.5

8.0

8.0

1.0

10.8

5.0

123.0

25.1

5.0

1.1

4.5

28.0

30.0

1.0

3.6

42.0

30.0

49.1

8.0

8.0

1.0

5.9

5.0

6.8

2.3

4.5

2.3

2.1

2.3

72.8

8.0

29.3

41.9

26.0

10.1

58.7

20.1

2.5

9.8

1.1

51.3 0.000761 0.0391

37.8 0.486 18.350

58.0 0.000 0.000

30.5 0.000 0.000

15.8 10.000002810.0000449 1

154.2 10.00000181 0.000277 1

62.5 0.000 0.000

1.0 0.000 0.000

75.6 0.000 0.000

66.1 0.000 0.000

10.9 0.000080 1 0.000875

I 1 9.1 10.619E-6 10.0000056

6.8 10.000001110.0000079

1 1 4.4 10.118E-6 10.00000052

I I 80.8 10.0000131 0.00113

29.3 10.000002610.0000783

41.9 10.00000661 0.000276

36.1 I0.000014 0.000534

I 1 92.1 l0.00000181 0.000166

II

PAGE L>0

0.000 0.0391 12

5.196 23.546 12

0.000 0.000 12

4.547 4.547 12

0.000 10.0000449 1

1 1 -1.429 -1.429

3.248 3.248 1

0.000 0.000 1

-0.433 -0.433 1

5.240 5.240

0.000 0.000875

0.000 10.0000056.

II

0.000 10.000007 9

0.000 10.000000521

1 1 0.563 1 0.564 1

0.217 0.217

-0.217 -0.216

0.606 0.607

-0.0866 -0.0864

0

0

.0

20

62

62

20

.20

120

120

62

86

86

86

55

55

86

66

62

1.394 10.0131

19.785 2.634

0.000 0.000

0.000 0.000

0.0418 10.11E

0.0327 10.71E

0.000 0.000

0.000 0.00C

0.000 .0QOC

0.000 0.00(

0.254 10.000

II

0.0315 I0.67E

0.0445 10.13E

0.0129 10.11E

0.0876 10.51E II

0.0445 10.13E

0.0905 1o.55E

0.107 10.771

0.0327 10.711 II

II

II

-I-



IPIPEI PIPE I FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. lOVER PIPE

NO. I NODES I (US GPM)j (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)

STATIC TOTAL IROUCHI WATER VELOC.

STATIC ITOTAL HEAD LOSS HEAD LOSS

(PSI) (PSI)NESS IVELOCITYI PRESS.

ICOEFFI (FT/SEC) I (PSI)

I I I I I __ __

271.8_ I0.000 1I 0.000

175

175

175

175

1

Is

5 705 704 1

6 1 727 705 1

-7 706 704 1

8 923 706 1

60 1 27 720 1

1 1 61 1 720 721 1

62 919 723

63 724 719

00 928 802

02 1 802 803

803 834 800

804 1 800 801

805 56 805

806 49 849

807 1 849 814

7.9 - CsM 22.

I -

3.97

3.97

1.13

1.13

16.21

16.21

9.69

39-68

0.00

0.00

0.00

0.00

0.00

0.00

0.00

221.97.98 CS 8 7S

8 2H

8 1'

7.98 CS

8 21

8 11

4.03 C€

4 8

4 4

4 1

4.03 C

4 12

4 4

4 i1

7.98 C

8 1

8.39 C

8 2

8.39 C

8 1

7.85 C

6.07 C

6 1

6 1

6 2

4.03

4

4

4

4

6.07

6

6

5.05

5

5 7.98

8

8

4.03

4

4

4

4

4.03

4

4 4

•AM

LE

•E

rT

SAM

HE

TT

SAM

SE

HE

GV

SAM

SE

HE

GV

"SAM SE

:SAM

HE

SAM

LGV

SAM

SAM

ITT

IGV

2SE

CSAM

2HE

ITT

4SE

1GV

CSAM

3SE

IHE

CSAM

7SE

4HE

CSAM

IHE

ITT

CSAM

3SE

2HE

1TT

IGV

CSAM

ISE

ITT

1GV

I~~~~~~~~~~~ II___ __ ___ _____I___I___I__

IX-85

U3TB Hose St

t-1Yil-liNL)1V11-,4 I 1.) Attachment D

35.1 5.0

9.8

141.3

9.2

17.9

197.0

23.6

4.7

0.6

178.4

35.3

4.7

0.6

75.5

4.2

17.0

5.3

12.5

1.3

26.0

33.8

30.0

3.0

28.0

115.1

8.0

20.0

40.0

2.0

30.9

42.0

7.0

121.8

84.0

20.0

25.8

8.5

33.1

84.1

30.0

8.0

20.0

2.0

2.5

10.0

20.0

2.0

PAGE : L->iE

I 271.8 100000011 0.000307

168.3 I0.617E-6 0.000104

225.9 10.00000301 0.000696

1 I

219.0 J0.00000301 0.000675

1 1 1 1

79.7 10.000018 I 0.00147

1 1 22.3 10.000014 1 0.000324

13.8 10.000005010.0000702

26.0 0.000047 I 0.00124

94.8 0.000 1 0.000

185.1 0.000 0.OOC

79.9 0.000 0.004

225.8 0.000 0.00

67.4 0.000 0.00

144.1 0.000 0.00

34.5 0.000 0.OC

__________________________ I _____________ I ____________________ I -

0

0

0

0

0

7.448 7.448

0.866 0.866

1.645 1.646

-7.058 -7.058

0.650 0.651

0.000 0.000324

0.000 10.0000702 I

0.000 0.00124

3.248 3.248

3.551 3.551

-7.794 -7.794

-4.027 -4.027

-11.562 -11.562

2.728 2.728

0.000 0.000

62

86

62

62

56

56

59

86

120

120

120

120

120

120

120

0.0254 I0.43E-5

0.0254 10.43E-5

0.0284 I0.54E-!

0.0284 J0.54E-!

0.104 10.72E-

0.0942 10.59E

0.0563 10.21E

1 0.263 10.0004

0.000 0.000

0.000 0.00c

0.000 0.00(

0.000 0.00(

0.000 0.00,

0.000 0.00

0.000 0.00


.tAAVILINLJIVI-•L,14 1 A J

PAGE rlej

I I PIPE DIAMETERI PIPE/FTG TOTAL IHEAD LOSSIHEAD LOSS I STATIC TOTAL IROUGHI WATER I VELOC.I

IPIPEI PIPE I FLOW NOM ACTUAL[ CODE LENGTH LENGTH I PER FT. lOVER PIPE JHEAD LOSSIHEAD LOSS NESS IVELOCITY1 PRESS.

. ... ,-, f I I (PSI) I (PSI) ICOEFFI (FT/SEC)i (PSI)

- I NODES I (US GPM)I (IN) (IN) I#I,".,.

__________________ I __________________________ I _______________________________ I ________________ I __________________

I _____________________ I _______________________ l................1 __________________ I _______________ I 1.169 I 1.169 I 0.000 I 0.000 I

1808

1809

1810 I

1811 1

1812

1813 1

814

1815I

1816

1819

1820

1821

822

1823

849 815

77 808

60 809

79 811

55 813

813 817

813 818

805 819

819 820

819 822

76 824

824 825

801 804

836 827

____ -_________ 1 -__________ 1______________ I___________________I__________ __________

IX-86

U3TB Hose St

Attachment D

AM 18.0 I0.00

4 4

4

0.00

2 1/2

2 1/2

0.00

4

4

0.00

3

3

3

0.00

8

8

8

0.00

2 1/2

2 1/2

0.00

8

0.00

8

0.00

6

6

6

0.00

6

6

6

0.00

8

8

18

0.00

6

6

6

0.00

3

0.00

5

5

000 I

4.03 CS

4S

I C

2.47 CS

11

1(

4.03 C,

2)

3.07 C:

4

1

2 7.98 C

4

4 1

2.47 C

7.98 C

7.98

6.07

6.07

7.98

6.07

3.07

5.05

jAM

LE

rE

lv

lAM

SAM

ST

GV

SAM

SE

TT

SAM

SE

TT

GV

SAM

SE

HE

ITT

SAM

"ITT 1GV

CSAM

1GV

CSAM

ISE

CSAIM

IHE

ITT

IGV

CSAM

ISE

IHE

1GV

CSAM

2SE

ITT

1HE

CSAM

ISE

1HE

1GV

CSAM

ITT

CSAM 4HE

8SE

18.0

40.0

4 .0 2.0

1.0

12.0

1.0

28.1

20.0

20.0

51.5

28.0

15.0

2.0

62.7

68.2

34.1

33.1

1.0

12.0

1.0

1.5

3.8

6.0 .

17.0

6.6 6

7.0

30.0

3.0

16.8

14.0

7.0

3.0

32.0

34 .1

33.1

8.5

23.3

14.0

7.0

3.0

5.5

15.0

121.5

20.0

96.0

64.0

14.0

68.1I

96.5

198.1

14.0

5.3 I

23.0

46.6

40.8

107.7

47.3

20.5

237.5

_______ 1_____ _____ 1_____ ____________ ............ I1_________ _1 _____

(FT I... . . . ýP j

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

0.000

1.169

-0.433

-2.165

-3.681

-13.207

0.000

-1.169

2.901

-4.114

-4.114

-13.943

0.000

0.000

-7.483

1.169 12

-0.433 i1:

-2.165 I:

-3.681 1

-13.207 1

0.000 I

-1.169

2.901

-4.114

-4.114

-13.943

0.000

0.000

-7.483

20

20

20

20

20

120

120

120

120

120

120

120

120

120

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.OOc

0.000 0.000

0,000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000


I IPIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS

IPIPEI PIPE FLOW I NOM ACTUALI CODE LENGTH I LENGTH PER FT. lOVER PIPE

INO. I NODES I (US GPM)I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)

STATIC TOTAL IROUGHI WATER I HEAD LOSSIHEAD LOSS INESS IVELOCITYI

I (PSI) I (PSI) ICOEFFI (FT/SEC)

VELOC.

VELOC. PRESS.

(PSI)

I I I I ______________ I ________ _________ I __________ _________ I _________ I _____ _______ I ______ 0.000 I -3.992 -3.992 1: 20 I 0.000 I 0.000

1824 1

I 1

1 1

826 1

1 1 1 1

1827

1 1

1828 1

1 1 1829 1

1831

832

833

1834

1835

1836

1837

1839

83

8

1

309.5 I 0.000 II - , -

8

8

1

35 836

24 826

02 855

00 839 3

839 831 3

42 837

61 832

98 552

54 834

73 835

833 828

828 829

96 838

I -

____ I _______ I _________ I ____ I _____ I ______ I _____ I ______ I ___ I ____ I ____

IX-87

U3TB Hose St

ZILII!¥1J •Nlj-lvl~ul 1 x A •'

PAGE C)ZO

0.00

0.00

0.00

7.12

7.12

0.00

0.00

25.54

0.00

0.00

0.00

0.00

14.76

6

6

6

6

6

6

6

6

6

6

6

6

6

10

6

6

6

6

6

6

6

6

6

6

6

6

6

6

6

6

6

6

6

].

I

6.07 CSAM

I1GV 5SE

3HE

4TT

1CV

6.07 CSAM

ITT

1HE

1GV

6.07 CSAM

ITT

1GV

1HE

ISE

6.07 CSAM

ITT

6.07 CSAM

10.02 CSAM

2HE

6.07 CSAM

ISE

IGV

ITT

6.07 CSAM

6.07 CSAM

2SE

2HE

2TT

1GV

6.07 CSAM

ITT

2SE

2HE

1GV

6.07 CSAM

9SE

2TT

6.07 CSAM

8SE

2HE

ITT

6.07 CSAM

1HE

1GV

ITT

63.5 3.0

70.0

21.0

120.0

32.0

6.3

30.0

7.0

3.0

4.4

30.0

3.0

7.0

14.0

2.3

8.8

3.0

11.0

22.0

9.9

14.0

3.0

30.0

11.2

28.6

28.0

14.0

60.0

3.0

24 .5

30.0

28.0

14.0

3.0

75.9

126.0

60.0

100.0

112.0

14.0

30.0

62.4

2.1

0.9

8.8

1-1-1

KeVlsion u Attachment D

309.5 0.000

46.3 0.000

58.4 0.000

11.1 10.000271

3.0 10.000271

33.0 0.000

56.9 0.000

11.2 10.000761

133.6 0.000

99.5 0.000

261.9 0.000

256.0 0.000

74.2 10.000049

0.000

0.000

0.000

0.00301

0.000812

0.000

0.000

0.00850

0.000

0.000

0.000

0.000

0.00364

-3.992

0.000

0.823

-3.464

0.000

0.000

0.0433

1 .429

-8.531

-8.314

-0.684

-28.112

0.000

-3 .992 1:

0.000 1

0.823 1

-3.461

0.000812

0.000 1

0.0433

1.437

-8.531

-8.314

-0.684

-28.112

0.00364

20

20

20

62

62

.20

120

120

120

120

120

120

62

0.000 0.000

0.000 0.000

0.000 0.000

0.412 10.0011

0.412 10.0011

0.000 0.000

0.000 0.000

1.394 10.0131

0.000 0.000

0.000 0.000

0.000 0.000

0.000 0.000

0.164 0.000181


I I IPIPE DIAMETERI PIPE/FTG I TOTAL IHEAD LOSSIHEAD LOSS

JPIPEI PIPE I FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. OVER PIPE

INO. I NODES I (US GPM)I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)

STATIC TOTAL IROUGHI WATER I VELOC.IISTATIC I TOTAL IROUGH1 WATER I VELOC.1 HEAD LOSSIHEAD LOSS INESS IVELOCITYI PRESS.l

(PSI) I (PSI) ICOEFFI(FT/SEC)I (PSI) I

12 .0 0.00I _ _ _ _ _ _I_ _ _ __ _ _I_ _ _ _ 704 3.2

1 - 1 -****.... ____________I _________ 179.8 I 0.000 0.000 I1840 1

I 1

1841 1

842

850

1851

1860

861

1922

925

931

1932

I-

838 845

75 823

809 810

93 850

89 851

97 860

860 861

19 919

23 923

928 28

29 929

I 0.00

0.00

0.00

0.00

0.00

16.65

0.00

9.69

39.68

0.44

0.44

____________________ I __________________ I ___________________________ I ______________________________ I ________________ I __________________ I ____________________ I __________________ I ____________________ I�..................-I ________________ I ______________ I

IX-88

U3TB Hose St

1ýllvjkl-li 141-11VIA-11 1 - - -

PAGE Dzi

4

4

4

4

8

8

8

3

3

6

6

6

4

4

4

4

6

6

4

4

4

4

8

8

8

4.03 CSAM 5HE

2SE

ITT

IGV

7.98 CSAM

ITT

2SE

IHE

3.07 CSAM

ISE

1GV

6.07 CSAM

1GV

2SE

ITT

4.03 CSAM

3SE

ITT

IGV

IHE

6.07 CSAM

1GV

IHE

4 .03 CSAM

3HE

3SE

ITT

1GV

7.85 CSAM

7.98 CSAM

3SE

ITT

XGV

7.98 CSAM

7.98 CSAM

117.8 1

20.0

20.0

20.0

2.0

32.0

33.1

34.1i

8.5

23.3

7.0

1.0

12.5

3.0

28.0

30.0

12.9

30.0

20.0

2.0

4.0

51.5

0.9

2.1

119.8

12.0

30.0

20.0

2.0

29.2

21.2

15.1

9.8

1. I 98.2

2.5

Kevslon U Attachment D

179.8 0.000 0.000

107.7 0.000 0.000

31.3 0.000 0.000

73.5 0.000 1 0.000

68.9 0.000 1 0.000

54.4 0.000061 0.00334

183.8 0.000 0.000

29.2 10.00000701 0.000205

47.2 10.000080 0.00379

I 1

98.2 10.229E.7 10.0000022

2.5 10.229E-7 10.572E-7

37.024 37.024

-13.943 -13.943

0.000 0.000

-2.598 -2.598

-2.382 -2.382

0.000 0.00334

38.020 38.020

0.476 0.477

12.774 12.778

0.000 10.0000022

0.000 10.572E-7

120 0.000

120 0.000

120 0.000

120 0.000

120 0.000

62 1 0.18!

120 0.00(

59 0.064:

62 0.25

1 56 10.0028

56 10.0028

I I- II I

0.000

0.000

0.000

0.000

0.000

S10.000231

1 0.000

2 10.27E-41

4 0.000431 II

II

0 10.52E-71

0 10.52E-71

"II-VI1LINJ IVI..IN 1 I - Revision 0 Attachment D

HYDRAULIC CALCULATIONS - NODE CHARACTERISTICS

COMPANY Nexus Technical Services Corporation IPAGE 20 A

I DESIGNER BY: CARL BALINGIT CHECKED: ODATE 2000 JAN 13

I CLIENT ComEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis



SPRINKLER/NOZZLE(N) POINTS I REFERENCE POINTS INPUT POINTS POINT I REQUIRED I

ELEVATION IDISCHARGE I K-FACTOR.

I I.. .. . . NO. JDEMAND GPM I P.S.I. I (FT) I {US GPM) II

IX-89

NO. IDISCHG. GPM P.S.I. NO. JDISCHG. GPM I....

1 500.000 I 1 149.932 5

I 2 145.818 5 16.00 0

I 3 143.004 516.000 1 1

I I 4I ~ I I510.800I S4 145.255

5 145.255 I 510.800

6 145.255 1 1 510.800

7 145.470 1 510.300

8 145.772 1 509.600

9 145.772 51509.600 1

I10 143.216 515.500 1I 126.458 554.200 1

12 143.216 515.500

131 145.684 509.800

14 1 145.900 509.300

15 1 145.987 509.100

16 1 145.206 510.900

17 1 145.552 510.100

18 1 145.898 509.300

19 1 145.854 509.400

201 144.987 511.400

21 145.333 510.600

22 144.952 511.500

23 144.950 511.5000

24 139.098 525.000

25 I 145.160 1 1 511.000

26 144.943 1 1 511.500

27 145.376 510.500

28 144.722 1 512.000

29 144.722 1 512.000 1 I

1 30 145.069 I 511.200

31 144.640 512.200

32 144.296 513.000

331 144.734 512.000

34 1 144.869 511.700 1

35 145.552 510.100

36 144.525 1 512.500

37 145.223 1 510.900

38 145.172 1 511.000

I 39 145.126 1 511.100 3 1 401 125.54 1 150.000 1 500.000

I 510.900

I 41 145.269 510.900

I I I 42 145.253 510.900

I 45 145.227 510.900

I 46 144.287 513.000

I _____ I______________ ______________ ______I______________ I______________ ............ ______________I______________ ______________I ___________ __________

Attachment D

U3TB Hose St HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS PAGE DC-3


ELEVATION IDISCHARGE K-FACTORI

NO. IDISCHG. GPM P.S.I. NO. IDISCHG. GPM P.S.I. I NO. DEMAND GPM I P.S.I. (FT) I (US GPM)

47 144.287 513.000

48 137.123 529.500

49 134.524 535.500

50 134.091 536.500

51 133.095 538.800

52 144.869 511.700

53 125.650 556.000

54 125.650 556.000

55 125.652 556.000

56 125.652 556.000

57 125.652 556.000

58 126.299 554.500

59 126.299 554.500

60 126.296 554.500

61 126.325 554.400

62 122.809 562.500

63 119.729 569.600

1 64 138.636 526.000

65 141.039 1 520.500

66 141.038 520.500

67 138.636 526.000

68 127.076 552.700

691 138.636 5526.000

701 128.029 550.500

71 124.554 558.500 721 125.845 555.500 72 125.843 555,500 74 125.833 555.500

75 125.833 555.500

76 125.831 555.500

77 125.820 555.500

78 126.176 554.500

79 126.149 554.500

80 138.636 526.000

81 119.588 569.700

82 138.636 526.000

83 141.688 519.000

84 141.687 519.000

85 142.321 517.500

86 138.636 526.000

87 142.322 517.500

88 138.506 526.300

89 138.203 527.000

91 138.549 526.200

92 138.203 527.000

93 138.203 527.000

96 147.534 505.500

97 147.533 505.500

98 127.526 551.200

IX-90

I-luvil-I 14A-111- I - - -

U3TB Hose St HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS

SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS INPUT POINTS POINT REQUIRED

ELEVATION DISCHARGE

NO. IDISCHG. GPM I P.S.I. NO. IDISCHG. GPM P.S.I. NO. DEMAND GPM P.S.1. I (FT) (US GPM)

- 526.000

102 138.636

200 134.551

201 125.658

202 134.547

400 147.533

401 106.179

402 109.513

403 147.534

404 106.180

405 109.514

550 126.050

551 1 125.54 102.503

1 552 126.089

600 121.105

601 139.098

602 137.670

611 135.850

612 135.850

621 138.103

651 121.085

700 145.987

I701 145.423

702 145.336

703 144.726

I704 137.583

705 145.031

706 139.229

I719 144.951

720 144.725

721 144.724

723 145.377

724 144.952

725 145.898

726 145.898

727 145.898

800 141.975

801 146.002

802 141.474

803 137.923

804 146.002

805 137.214

808 126.253

809 128.461

810 128.461

811 129.830

812 133.095

813 138.859

814 131.796

815 130.627

K-FACTOR

I __________ I ________________________ I ________________________ I __________ I ________________________ I ________________________ I....................I ________________________ ________________________ ____________________ I _________________

IX-91

Attachment D

PAGE oz4- ,

526.000 535.500

556.000

535.500

505.500

601.000

593.300

505.500

601.000

593.300

554.500

566.500

554.500

566.500

525.000

528.300

532.500

532.500

527.300

566.500

509.100

510.400

510.600

512.000

528.500

511.300

524.700

511.500

512.000

512.000

510.500

511.500

509.300

509.300

509.300

518.300

509.000

519.500

527.700

509.000

529.300

554.500

549.500

549.500

546.000

538.800

525.500

541.800

544.500

100.00 12.400

Attachment D

U3TB Hose St HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS PAGE ,. 2 g.

SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS I INPUT POINTS POINT REQUIRED I I ELEVATION DISCHARGE I K-FACTORI

NO. IDISCHG GPM P.S.I. NO. IDISCHG. GPM P.S.I. NO. DEMAND GPM I P.S.I. (FT) I (US GPM) I

817 138.859 525.500

818 140.028 522.800

819 134.313 536.000

820 138.426 526.500

822 138.426 526.500

823 139.776 523.300

824 139.775 523.300

825 139.775 523.300

826 139.775 523.300

827 145.633 509.800 1

8281 126.773 552.920

829 I 154.885 I 488.000

831 138.012 527.500

832 126.281 554.500

833 126.089 554.500

834 134.180 536.300

835 134.157 536.300

836 138.150 527.080

837 145.253 510.900

838 147.530 505.500

839 138.013 527.500

845 110.506 591.000

849 131.796 541.800

850 140.801 521.000

851 140.585 521.500

855 137.813 527.900

860 147.530 505.500

861 109.510 593.300

919 145.377 510.500

923 132.172 541.000

928 144.722 512.000

929 144.722 512.000

IX-92

Attachmernt D

" WARNING: THE FOLLOWING PIPE(S) HAVE FLOW(S) SMALLER THAN 0.1 GPM

1 2 3 4 85 86 87 91 106 500

501 502 503 504 505 552 600 611 612 621

651 800 802 803 804 805 806 807 808 809

8i0 811 812 813 814 815 816 819 820 821

822 823 824 826 827 831 832 834 835 836

837 840 841 842 850 851 861

MAXIMUM UNBAILANCED HEAD LOSS- .00005 IN LOOP # 1

IX-93

A-MfNIJMLItN 1 1.

15X*

Revision 0 Attachment D

R-ýC- DZI --F UVz1

IP

1131R

IE Is

is

It! 761 R

IE

391 X is operating point for SPECIFIED pressure

Co-ordinates are

FLOW - 125.54

PRESSURE = 150.00

0 1635 3268 4901

FLOW

Pump Curve Input Point No. 40

IX-94

Volume 12

AMENDMENT 13

DRESDEN 2&3


Volume Index

VOLUME 12 - REFERENCES

I. Fire Protection Program Audit and Open Item Closure

1. S&L closure of PLC Evaluation Report Open Items.

2. PLC Fire Protection Program Evaluation.

3. Fire Protection Modification Review.

11. Previous Commitment Review and Open Item Closure

1. Proposed Fire Protection Licensing Amendment (Open Item Closure).

2. Review of Fire Protection Requirements (12/2/85).

3. PLC Review of Previous Fire Protection Commitments.

4. NRC Fire Protection Commitment Matrix Status.

5. September 29, 1994, Review of Modifications Committed to Under 1978

SER.

6. March 15, 1993, Fire Protection Engineering Evaluation.

Ili. PLC Review of Procedures in Support of Technical Specifications

IV. Fire Protection Procedures

I. List of Fire Protection Procedures.

2. Fire Protection Program.

V. Pre-Fire Plans

VI. Suppression Effects Analysis

I

AMENDMENT 13

DRESDEN 2&3


Volume Index

VOLUME 12 - REFERENCES (Continued)

VII. Fire Protection Reevaluation Project Plan

1. Fire Protection Evaluation Report.

2. Appendix R Fire Protection File Index

VIII. Fire Protection Evaluation Plan

IX. Audit/Inspection Reports, Responses and Closure

I. Fire Protection Closure Documentation and NFPA Review.

2. PLC Fire Detection and Alarm Survey.

3. PLC Fire Suppression System Survey.

4. PLC Fire Suppression Hydraulic Analysis.

5. PLC Technical Specification Evaluation.

6. PLC Supplemental Guidance Review.

7. PLC Suppression Effects Analysis.

8. Appendix R Fire Protection-Recommendation Summary, Rev. 15.

9. Annual Fire Protection - Audit (April 10-14 1989) Report.

10. August 18, 1989, Letter from PLC to CECo responding to finding of

Annual Fire Protection Audit.

11. Fire Protection for Quality Records.

12. Dresden Fire Protection Assessment January 9-11, 1989.

13. Offsite Quality Assurance Audit 12-87-Il. Open Item #03.

14. Dresden Station Site Quality Verification Audit 12-94-01.

2

AMENDMENT 13

DRESDEN 2&3


Volume Index

VOLUME 12 - REFERENCES (Continued)

15. 1994 Trienmial Fire Protection Audit 12-94-01B.

16. Dresden Station Site Quality Verification Audit #12-95-10.

17. Site Quality Verification Audit # 12-96-13.

18. Triennial Fire Protection Program Audit 12-97-13.

19. Quality & Safety Assessment Audit CornEd 98-01.

20. Nuclear Oversight Audit 12-98-04.

3

AMENDMENT 13

DRESDEN 2&3


Previous Commitment Review and Open Item Closure

Tab Title

1. Proposed Fire Protection Licensing Amendment (Open Item Closure)

2. Review of Fire Protection Requirements (12/2/85)

3. PLC Review of Previous Fire Protection Commitments

4. NRC Fire Protection Commitment Matrix Status

5. September 29, 1994, Review of Modifications Committed to Under 1978 SER

6. March 15, 1993, Fire Protection Engineering Evaluation

11-i

Volume 13

AMENDMENT 13

DRESDEN 2&3


Fire Protection Supporting Calculations

Tab Title

1. Radiological Consequences of Fire in the Off-Gas System (NSLD Calc.

No. 2-78-D2&3)

2. Primary System (RPV) Makeup by Control Rod Drivc Mechanism Flow

(NSLD Calc. 3C2-0584-001 and 3C3-0382-001)

3. Timelines for Spuriously Open Electronic Relief Valves (Preliminary)

4. Isolation Condenser Inboard Valves Transfer Starters (EPED Calc. No.

6779-31-19-1)

5. Torus Water Temperature (Quad Cities NSLD Caic. No. 3C3-0779-001)

6. Control Rod Drive Pump Crosstie (MAD Calc. No. 81-568)

7. Spurious Valvc Operations Analysis (September 2, 1987)

8. System Supporting Documents

9. IE Information Notice 85-09 Analysis (Dresden 85-09 Analysis) Revision

0

10. Technical Basis of Dresden Station Fire Damper Surveillance Program,

August 1985

11. Evaluation for the Effects of the December Unit 3 Poly-urethane Fire

12. Safe Shutdown Appendix R Analysis for Dresden Nuclear Power Station

Units 2 & 3

13. Using the Service Water System as Backup for the Fire Water System

14. Electrical Cable Review Calculations (S&L Calc. Nos. 7927-05-19-1,

7923-06-19-2, 6972-62-19-1)

X.0-i

AMENDMENT 13 DRESDEN 2&3


Electrical Cable Review Calculations

(S&L Calc. Nos. 7927-05-19-1, 7923-06-19-2, 6972-62-19- 1)

Paoe Title

X.14-1 Calc. For Consideration of Fire Induced "Hot Shorts," between Medium

and Low Voltage Cables (S&L Caic. No. 7927-05-19-1).

X.14-10 Appendix R "Hot shorts," between Medium and LV Cables in Common

Enclosures (S&L Calc. No. 7923-06-19-2).

X.14-50 Cable Ampacity Derating for Cable Trays Wrapped in 3M Fire Wrap

(S&L Calc. No. 6972-62-19-1).

X. 14-i

AMENDMENT 13

DRESDEN 2&3


Appendix R Station Modification Meetings

Title Pan

Station Modification Meeting, January 27, 1984 XI.1-1

Station Modification Meeting, February 29, 1984 XI. 1-7

Station Modification Meeting, April 23, 1987 XI. 1-13

Station Modification Meeting, August 20, 1987 XI.1-19

Station Modification Meeting. September18, 1987 XI.1-26

Station Modification Meeting, October 23, 1987 XI.1-33

XI.1-i

I

AMENDMENT 13

DRESDEN 2&3


General Appendix R Meeting Notes

Title Page

April 6 and 7, 1987, Fire Protection Exemption Items Walkdown XI.2-1

August 3 and 12. 1987, Meetings to Prepare for Upcoming Appendix R Audit XI.2-9

April 6 and 7, 1987, Review of Draft SER (Meeting Notes) XI.2-36

August 17, 1988 Conference Call with NRC on Automatic

Depressurization System I OCFR50 Appendix R Concerns XI.2-43

February 2, 1989, Teleconference with NRC on Out-of-Service

Equipment XI.2-46

October 13, 1987, Meeting Notes XI.2-49

XI.2-i

AMENDMENT 13

DRESDEN 2 & 3


Letters and Memos

Title PA9e

February 11, 1985 Fusing of Control Power Transformers XI.3-1

December 15, 1987 Carbon Dioxide Monitoring for Fire Detection XI.3-3

December 29, 1988 Update of Dresden FHA and Appendix R Safe XI.3-21

Shutdown Analysis

September 7, 1989 Dresden Radwaste Upgrade Project XI.3-30

February 23, 1987 S&L letter from B. M. Barth to .1. J. McDonald (CECo), XI.3-33

discussing Fire Zone Designations on the Turbine Building Ground Floor

June 12, 1986 telecon between C. E. Ruth (S&L) and C. Ksobiech (CECo), XI.3-35

Extension of Preaction Suppression System Snubber Recorder Shack

May 5. 1997 NDIT No. S040-DH-0445 Standby Gas Treatment System XI.3-36

and the Appendix R Analysis

XI.3-i

COMED NUCLEAR DESIGN INFORMATION TRANSMITTAL

Z SAFETY-RELATED Originating Organization NDIT No. S040-DH-0445 SNON-SAFETY RELATED LI ComEd SREGULATORY RELATED Z Other (specify) S&L

Station Dresden Unit(s) 2&3 Page 1 of 2

Design Change Authority No.:

System Designation: 7500 - C om__

__________________________________________To J. Steiner - CornEd

Subject Standby Gas Treatment System and esindix R AwIvsi

C. M. Launi Division Mana er 5 Preparer Position P a Date

B. J. Andrews Project EnQineer . Reviewer Position Si nature Date

C. M_ Launi Division Manager Approver Position K __App 1 wver's Signature Date Status of Information: Approved for Use

Method and Schedule of Verification for Unverified NDITs:

Description of Information:

During the Dresden Independent Safety Inspection (ISI), a question arose about the HPCI turbine gland seal leak value (Question 3260-002). A gland seal leak value of 216 Ibm/hr was used in the room thermal response zalculation. This number is 10% of the leakage that would occur from a locked rotor condition resulting from a water slug damage in the turbine which is 2160 Ibm/hr (0.6 lbm/s)(UFSAR Section 6.3.3.1.3.2.1.5). Noncondensables are removed from the HPCI gland seal condenser by the gland seal exhauster (gland seal leak off blower) via the (cont'd on page 2)

XI.3-36

Purpose of Issuance:

This information is being issued to close out NTS Items 237-201-96-56101-01, 237-201-96-56101-02, 237-201-9656101-03 and 237-20196-56101-04. Since the SGTS does not need to be incorporated into the Appendix R safe shutdown analysis, the actions required by these NTS items are no longer required.

Source of Information:

UFSAR Section 6.3.3.1.3.2.1.5; Fire Protection Reports, Volume 2; Drawings M-49, Rev. QG; M-51, Rev. BF; M-269 shý 1, Rev. C; sh. 2, Rev. A; M-374, Rev. BP; M-529, sh. 1,Rev. D, sh. 2, Rev. A; Response to ISI Question 3260-002.

Distribution: E. Connell - CornEd, J. Dawn - CornEd, T. Behringer D. Bianchini - 23

File No.: CHRON No.: Project No.: 10128-040

AAVrJV'qNIVIc_•I,4i i-1

"PAIVA ,IAN "; V 11-1 N I I -

COMED NDIT. S040-DH-0445

NUCLEAR DESIGN INFORMATION TRANSMITTAL Page 2 of 2

Description of Information (Continued):

standby gas treatment system. During the ISI, it was assumed that failure of the gland seal exhauster could result in

failure of the gland seals resulting in the a leakage rate equal tothat of the locked rotor condition. For the 1 OCFR50

Appendix R scennrin faiiures to equipment oocur only as a result of damage from the fire. Single failures are not

required to be postulated. A fire that damaged the gland seal exhauster or cables that power and control the

exhauster would also prevent operation of the HPCI system and an alternate means of shutting down the reactor is

provided (isolation condenser/CRD pump per Fire Protection Reports, Volume 2). For the safe shutdown paths that

ust. trie HPCI system for reactor water makeup (C and D) for a fire in Fire Areas RB2-l and RB3-1, the gland seal

exhauster would be operable. However, during the ISI, it was thought that the Standby Gas Treatment System

(SGTS) is needed to accommodate the exhaust from the gland seal blower. The SGTS is not currently included in the

Appendix R analysis.

The assumption that the SGTS was needed to accommodate the exhaust from the exhauster was based on the failure

of the reactor building ventilation system due to loss of offsite power and no flow path through the reactor ventilation

system to the reactor building. However, review of P&IDs M-49 and M-269 sheets 1, 2 for Unit 2 and M-49 and M-529

sheets 1,2 for Unit 3 indicates that a path exists to the reactor building from the gland seal exhauster. This path is via

lines 2(3) 2320-3", 2(3)-7501-6" and 2(3)-7504-18" into the reactor building ventilation ducts.

Based on the existence of a pathway to the reactor building to accommodate the discharge flow from the gland seal

exhauster, the SGTS does not need to be included in the 10CFR50 Appendix R safe shutdown analysis.

Since a design basis accident is not postulated to occur with a fire, fuel damage is not postulated. Therefore, any

release to the reactor building will contain the normal operation source terms. The radiological consequences of this

release are bounded by the design basis accident (LOCA) since the number of curies released to the environment for

the DBA would be several orders of magnitude greater.

XI.3-37

AMENDMENT 13

DRESDEN 2&3


Microfiche Indcx

Microfiche Pocket Title

A This has been intentionally deleted.

B.C Technical Basis of Dresden Station Fire Damper

Surveillance Program, dated August 1985. (This

document contains "Licensing Classification of Fire

Dampers," Rev. I - See Pocket G, below.)

D,E Evaluation for the Effects of the Dresden Unit 3

Polyurethane Fire.

F Resolution of Consequences of the Dresden Unit 3

Polyurethane Fire, June 4, 1988.

G Licensing Classification of Fire Dampers, Rev. 2.

XII.0-i

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