+ All Categories
Home > Documents > €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler...

€¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler...

Date post: 08-May-2018
Category:
Upload: lynhu
View: 219 times
Download: 2 times
Share this document with a friend
99
File: document.xls NREL Protected Information 05/14/2022 00:19:15 Ethanol Production Process Engineering Analysis Dilute Acid Prehydrolysis with Saccharification and Co-Fermentation All Values in 2002 $ Annual Ethanol Production Cost #REF! Per Gallon Net Operating Cost #REF! Per Gallon Fuel Ethanol Production (MM Gal. / Year) #REF! Ethanol at 68°F Fuel Ethanol Yield (Gal / Dry US Ton Feedstock) #REF! Feedstock Cost $/Dry US Ton $40 Ethanol Yield (Gal / Bushel Corn) 2.84 Operating Costs ($/gal ethanol) Shelled Corn 0.49 Variables that can be Changed Biomass Feedstock #REF! Cost Year for Analysis 2002 CSL #REF! Life of Equipment 10 Cellulase #REF! Days of Operation per Year 330 Other Raw Materials #REF! % Denaturant in Final Fuel Et 5% Waste Disposal #REF! Feedstock Cost $/Dry US Ton $40 Electricity #REF! Feedstock Cost $/ Bushel $2.80 Fixed Costs #REF! DDGS Price $/ton $115.00 Denaturant #REF! DDG Co-product 0.00 Starch Utilities 0.00 Capital Depreciation #REF! Total Product Cost per Gallo #REF! Capital Costs Feed Handling #REF! Pretreatment #REF! Operating Costs ($/yr) Neutralization/Conditio #REF! Shelled Corn $24,700,000 Saccharification & Ferm #REF! Feedstock #REF! Distillation and Solids #REF! CSL #REF! Wastewater Treatment #REF! Cellulase #REF! Storage #REF! Other Raw Matl. Costs #REF! Boiler/Turbogenerator #REF! Denaturant #REF! Utilities #REF! Waste Disposal #REF! Total Stover Capital Investme #REF! Electricity #REF! Fixed Costs #REF! DDG Co-product $0 Total Starch Capital Investme $9,600,000 Starch Utilities $0 Capital Depreciation #REF! Total Annual Production Cost #REF! Total Combined Capital Invest #REF!
Transcript
Page 1: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

File: document.xls NREL Protected Information 05/08/2023 03:29:38

Ethanol Production Process Engineering Analysis

Dilute Acid Prehydrolysis with Saccharification and Co-FermentationAll Values in 2002 $

Annual Ethanol Production Cost #REF! Per GallonNet Operating Cost #REF! Per Gallon

Fuel Ethanol Production (MM Gal. / Year) #REF! Ethanol at 68°F Fuel Ethanol Yield (Gal / Dry US Ton Feedstock) #REF!

Feedstock Cost $/Dry US Ton $40Ethanol Yield (Gal / Bushel Corn) 2.84

Operating Costs ($/gal ethanol)Shelled Corn 0.49

Variables that can be Changed Biomass Feedstock #REF!Cost Year for Analysis 2002 CSL #REF!Life of Equipment 10 Cellulase #REF!Days of Operation per Year 330 Other Raw Materials #REF!% Denaturant in Final Fuel Ethanol 5% Waste Disposal #REF!Feedstock Cost $/Dry US Ton $40 Electricity #REF!Feedstock Cost $/ Bushel $2.80 Fixed Costs #REF!DDGS Price $/ton $115.00 Denaturant #REF!

DDG Co-product 0.00Starch Utilities 0.00Capital Depreciation #REF!Total Product Cost per Gallon #REF!

Capital Costs Feed Handling #REF! Pretreatment #REF! Operating Costs ($/yr) Neutralization/Conditioning #REF! Shelled Corn $24,700,000 Saccharification & Fermentation #REF! Feedstock #REF! Distillation and Solids Recovery #REF! CSL #REF! Wastewater Treatment #REF! Cellulase #REF! Storage #REF! Other Raw Matl. Costs #REF! Boiler/Turbogenerator #REF! Denaturant #REF! Utilities #REF! Waste Disposal #REF!Total Stover Capital Investment #REF! Electricity #REF! Fixed Costs #REF!

DDG Co-product $0Total Starch Capital Investment $9,600,000 Starch Utilities $0

Capital Depreciation #REF!Total Annual Production Cost #REF!

Total Combined Capital Investment #REF!

Page 2: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

NREL Protected Information 05/08/2023 OPCOST

document.xls

Neat Ethanol Production Rate (MM gal/yr) #REF! Feed (Dry tons/yr) #REF!Days per Year 330

Operating Hours per Year 7,920

Denaturant Density (kg/L) 0.6875 #REF!

% V/V Denaturant in Final Fuel Ethanol 5%

Annual Fuel Ethanol Production (MMgal) #REF! #REF!

Variable Operating Costs

Raw Material Stream No. kg/hr lb/hr $/hour MM$/yr (2002)

Feedstock STRM0101 #REF! #REF! #REF! #REF! #REF! #REF! 2000Clarifier Polymer STRM0107 #REF! #REF! 1.2641 #REF! #REF! #REF! 2000Sulfuric Acid STRM0710 #REF! #REF! 0.0500 #REF! #REF! #REF! 2001Hydrated Lime STRM0745 #REF! #REF! 0.0400 #REF! #REF! #REF! 2001Corn Steep Liquor STRM0735 #REF! #REF! 0.0767 #REF! #REF! #REF! 1998Purchased Cellulase Enzyme STRM0750 #REF! #REF! 0.1450 #REF! #REF! #REF! 1999 Diammonium Phosphate STRM0755 #REF! #REF! 0.0714 #REF! #REF! #REF! 2001Purchased Biomass to Burner STRM840A #REF! #REF! #REF! #REF! #REF! #REF! 2000 S840AH2OPropane STRM0723 #REF! #REF! 0.0022 #REF! #REF! #REF! 1999 Makeup Water STRM0903 #REF! #REF! 0.0000 #REF! #REF! #REF! 1990Boiler Chemicals STRM0921 #REF! #REF! 1.4914 #REF! #REF! #REF! 1991Cooling Tower Chems STRM0922 #REF! #REF! 1.0170 #REF! #REF! #REF! 1999WasteWater Chems STRM0630 #REF! #REF! 0.1574 #REF! #REF! #REF! 1999WasteWater Polymer STRM0631 #REF! #REF! 2.5425 #REF! #REF! #REF! 1999Denaturant STRM0701 #REF! #REF! 0.0898 #REF! #REF! #REF! 1999Subtotal #REF! #REF! #REF!

Waste StreamsDisposal of Steam 809 STRM804C #REF! #REF! 0.0096 #REF! #REF! #REF! 1993 Disposal of Stream 229 STRM0229 #REF! #REF! 0.0096 #REF! #REF! #REF! 1993Subtotal #REF! #REF! #REF!

By-Product Credits KW $/kWhElectricity Generated WKBLRNET #REF! na 0.0500 #REF! #REF! #REF! 1999Electricity Consumed #REF! na 0.0500 #REF! #REF! #REF! 1999Starch Plant Electricity Requirements 672 0.0500 34 0.27 #REF! 1999Electricity Required/(Excess) #REF! #REF! #REF! #REF!

Total Variable Operating Costs #REF! #REF! #REF!

Fixed Operating Costs

Direct Labor Hourly Wage Operators per Shift Multiplier $/hour $/yr (2002) Operators $18.31 10 183 $1,449,839 #REF! 2002 Maintenance $18.31 4 73 $579,936 #REF! 2002Indirect Labor

40% of Direct Labor $811,910 #REF!Overhead (Benefits, general plant upkeep) 60% of Total Labor $1,705,011 #REF!Operating Supplies 0.75% #REF! #REF!Maintenance Supplies 1% #REF! #REF!Insurance & Property Taxes 1.5% #REF! #REF!Total Fixed Operating Costs #REF! #REF!

Straight Line Depreciation #REF! #REF!

Total Annual Operating Cost #REF! #REF!

Ethanol Yield (MMgal/dry ton)

Denatured Yield (MMgal/dry ton)

2000 Cost ($/lb)

$/Gallon Denatured

Ethanol (2002)Year of Price

Quote

Cost on a dry basis

Cost on a dry basis

Basis for Multiplier

Cents/Gallon Ethanol (2002)

Direct Supervisory, Lab, Clerical,

of TCI (per year)of TCI (per year)of TCI (per year)

Page 3: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

NREL Protected Information 05/08/2023 Page 3

document.xls

Equip No. Equip Name Scaling Stream Size Ratio Base Year Installed CostNo.

Req'dNo.

SparesNo. Req. Variable

Scaling Stream Flow (Kg/hr)

New Stream Flow

Original Equip Cost (per unit)

Total Original Equip Cost (Req'd &

Spare)Scaling

ExponentScaled Cost in

Base YearInstallation

FactorInstalled Cost in 2002 $

M-800 1 Burner/Boiler/Turbogenerator System BLRCAPTL #REF! #REF! 2.75 #REF! #REF!

A800 Subtotal #REF!

Q160
Bob Wallace: Installed cost for steam/elec. System comes from Aspen with 1.4 installation factor in it. 1.96 factor is used to bring up to 2.75 overall installation factor.
Page 4: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Page 4

05/08/2023K.N. Ibsen I0597A.XLS/INDICES

Plant Cost IndicesSource: (1)Chemical Engineering Magazine, March, 1997

(2)Chemical Engineering Magazine, March, 2000 CE Index for Use in Calcs(3)Chemical Engineering Magazine, JaYear <=1999 Measured, >=2000 Extrapolated

Year CE Annual Index Source 1990 357.6 1990 0 357.6 (1) 1991 361.3

1 361.3 (1) 1992 358.2 2 358.2 (1) 1993 359.2 3 359.2 (1) 1994 368.1 4 368.1 (1) 1995 381.1

1995 5 381.1 (1) 1996 381.7 6 381.7 (1) 1997 386.57 386.5 (2) 1998 389.58 389.5 (2) 1999 390.69 390.6 (3) 2000 397.3

Linear Regression Results 2001 401.6### ### 2002 405.9### ### 2003 410.3### ### 2004 414.6### 8 2005 419.0### ### 2006 423.3

Calculated index 2007 427.71990 0 353.8 2008 432.0

1 358.2 2009 436.32 362.5 2010 440.73 366.94 371.2

1995 5 375.66 379.97 384.28 388.69 392.9

2000 10 397.311 401.612 405.9

2005 13 410.314 414.615 419.016 423.317 427.718 432.019 436.3

0 2 4 6 8 10 12 14 16 320

340

360

380

400

420

440

Chemical Engineering Plant Cost Index

Calculated indexActual index

Year (beginning 1990)

Inde

x

C7
kneeves: For Sept. '00 final cost index
Page 5: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Cost Year for Analysis 2002Total Installed Equipment Cost $9,598,931Life of Equipment 10Ethanol Density (kg/L) 0.78940 Black - Input by UserEthanol Production (kg/h) 8,962 Pure Ethanol Blue - Transferred from another cell in the same or another sheet.Ethanol Production Rate (gal/yr) 23,753,791Days per Year 330Operating Hours per Year 7,920 Denaturant Density (kg/L) 0.6875Denaturant in Final Product 5.0%Ethanol in Final Ethanol Product 95.0%Ethanol Production Rate (gal/yr) 25,003,991

Variable Operating Costs

Raw Material Stream

Corn Feedstock 1GRAIN 28,268 62,330 0.050000Caustic CIP 141 311 0.055000Alpha-Amylase AAMYL 20 43 1.500000Gluco-Amylase GAMYL 28 63 1.500000Gasoline GAS 411 906 0.089800Sulfuric Acid ACID 56 124 0.050000Lime LIME 34 74 0.040000Makeup Water 60,005 132,310 0.000020

Urea UREA 56 124 0.100000Yeast YEAST 5 12 2.500000Subtotal

UtilitiesSteam - 150 PSI kg/hr 26,011 57,355 0.000000CT Water - 85 F kg/hr 1,011,119 2,229,517 0.000000Cool Water 60 F kg/hr 260,481 574,361 0.000020Electricity kW 2,415 0.050000Natural Gas cal/sec 6,787,205 96.9601 6.000000Subtotal

By-Product Credits Stream DDGS DDGS 9,328 20,569 0.057500Carbon Dioxide CO2 8,624 19,015 0.000000Subtotal

kg/hr or cal/sec or

kWlb/hr or

106 BTU/hr

2002 Cost ($/lb or $/kWh or $/106 BTU)

MAKEUP + 5% Steam +5% CT water

Total Variable Operating Costs

E31
use on site steam genration
E32
Use on site coling tower
E34
EIA Dec 02 Industrial Users
E35
EIA 02 Industrial Consumers
Page 6: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Fixed Operating Costs

Calculation BasisCapital Cost $9,598,931 (Total Installed Equipment Cost)Plant Operators' Salaries 5 Operators / ShiftMaintenance Salaries 2.5% Capital CostsSupervision, Etc Salaries 40.0% of Operators & Maintenance LaborFringe Benefits 0 Included in G/A

Supplies Operating Supplies 0.75% of Capital CostMaintenance Supplies 1.0% of Capital Cost

General & Administrative 60.0% of Operators', Maintenance & Supervision SalariesInsurance & Local Taxes 1.5% of Capital Cost

Total Fixed Operating Costs

Depreciation (Straight Line) 10 Years Economic Life

Total Operating Cost

Raw Material Net Cost Cost of Corn less Coproducts Credit

Process Operating Cost

Page 7: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Red - CalculatedBlue - Transferred from another cell in the same or another sheet.

$/hour $/yr (2002)

$3,116.51 $24,682,787 $0.987 $17.09 $135,385 $0.005 $65.03 $515,055 $0.021 $93.93 $743,941 $0.030 $0.00 $0 $0.000 $6.18 $48,965 $0.002 $2.96 $23,405 $0.001 $0.00 $0 $0.000

$12.36 $97,930 $0.004 $29.21 $231,325 $0.009

$3,343.28 $26,478,794 $1.059

$0.00 $0 $0.000 $0.00 $0 $0.000 $0.00 $0 $0.000 $0.00 $0 $0.000 $0.00 $0 $0.000 $0.00 $0 $0.000

$0.00 $0 $0.000 $0.00 $0 $0.000

$0 $0.000

$3,343.28 $26,478,794 $1.059

$/Gallon Ethanol (2002)

Page 8: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

$/hour $/yr (2002)

(Total Installed Equipment Cost)$18.00 $713,000 $0.029

$240,000 $0.010 $381,200 $0.015

$0.000

$72,000 $0.003 $96,000 $0.004

of Operators', Maintenance & Supervision Salaries $800,520 $0.032 $143,984 $0.006

$2,446,704 $0.098

$960,000 $0.038

$29,885,498 1.195

$24,682,787 $0.987

$5,202,711 $0.208

$/Gallon Ethanol (2002)

Page 9: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Equip Name101U Grain Cleaning Equipment $36.3 2.75 $99.9

102U Corn Milling Equipment - Hammer Mills $100.7 2.75 $277.0

103U Grain Handling Equipment $72.8 2.75 $200.2

104T Corn Storage Silo's -10 Day Capacity $742.4 2.75 $2,041.5

$952.2 $2,618.7202T Meal Surge Tank $8.4 2.75 $23.1

203T Batch Weigh Tank $5.3 2.75 $14.5

204T Continuous Weigh Tank $53.1 2.75 $146.0

205E Process Condensate to Slurry Mix Tank $26.4 2.75 $72.6

206E Liquify / Cook Recover Heat Exchanger $69.9 2.75 $192.3

207E Cook Heat Exchanger $32.6 2.75 $89.8

208U Liquification Tank Agitator $25.0 2.75 $68.7

209P Sulfuric Acid Metering Pump $3.0 2.75 $8.3

210P Caustic To Slurry Tank Pump $1.7 2.75 $4.7

211P Slurry Chop & Recirc Pump $13.8 2.75 $37.9

212P Liquified Mash Pump $8.1 2.75 $22.2

213P Saccharified Mash Pump $4.7 2.75 $12.8

214U Saccharification Tank Agitator $13.0 2.75 $35.8

215U Slurry Mixing Tank Agitator $15.4 2.75 $42.3

216T Sulfuric Acid Tank $10.5 2.75 $28.8

217T Slurry Mix Tank $39.6 2.75 $108.8

218T Ammonia Tank $26.1 2.75 $71.8

219T Alpha Amalyse Tank $6.4 2.75 $17.5

220T Gluco Amalyse Tank $9.4 2.75 $25.8

221T Liquification Tank $71.5 2.75 $196.5

222T Saccarification Tank $274.5 2.75 $754.8

223V Cook Retention Tanks $74.1 2.75 $203.8

$792.3 3 $2,179.0401C CO2 Compressor $67.5 2.75 $185.5

402P Fermentor Cooling Pumps $48.0 2.75 $132.0

403E Fermentor Cooling Exchangers $110.6 2.75 $304.1

404T Fermentors $1,225.4 2.75 $3,369.7

405E Saccharified Mash Cooler $82.8 2.75 $227.6

406E Cooked Mash Cooler $34.0 2.75 $93.4

407P Beer Column Feed Pump $5.3 2.75 $14.6

408P Scrubber Bottoms Water Pump $1.4 2.75 $3.9

409P $4.5 2.75 $12.3

410P Clean In Place Return Pump $3.8 2.75 $10.4

411P Yeast Slurry Pmp $2.0 2.75 $5.4

Equip No.

Revised 2002 Cost

($1,000)Installation

Factor2002 Installed Cost ($1,000)

Beer from Fermenter to Degasser Pump

Page 10: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

412T Clean In Place Tank $30.2 2.75 $83.2

413T 50% Caustic Tank $21.8 2.75 $59.8

414T Yeast Tank With Agitator $42.8 2.75 $117.7

415PT CO2 Scrubber Packed Tower $61.4 2.75 $168.9

416P CIP Supply Pump $4.7 2.75 $12.8

$1,745.9 $4,801.3501V Degasser Drum $25.5 2.75 $0.0

502TT Beer Column Tower $138.0 2.75 $0.0

503TT Rectifier Tower $143.8 2.75 $0.0

504TT Stripper Tower $223.6 2.75 $0.0

505E Beer Column Reboiler $112.9 2.75 $0.0

506E Stripper Col Reboiler $27.5 2.75 $0.0

507E Beer Degas Vent Condeser $85.0 2.75 $0.0

508E Beer/Stillage Recovery Exch. $69.5 2.75 $0.0

509E Reflux Condenser $49.8 2.75 $0.0

510E SAC / Beer Recovery Exchanger $44.7 2.75 $0.0

511E Beer/Cooked Mash Recovery Exch. $102.2 2.75 $0.0

512P Beer Columns Bottom Pump $4.5 2.75 $0.0

513P Rectifier Bottoms Pump $1.5 2.75 $0.0

514P Stripper Bottoms Pump $1.4 2.75 $0.0

515P Regenneration / Ejector Liquid Pump $3.4 2.75 $0.0

516P Reflux Pump $3.5 2.75 $0.0

517U Molesieve Package $1,022.6 2.75 $0.0

525P Final Product Pump $1.9 2.75 $0.0

$1,924.0 $0.0601U Centrifuge $1,403.9 2.75 $0.0

602U Evaporator Incl Turbine Recompressor $1,533.4 2.75 $0.0

603U Grain Dryer $474.1 2.75 $0.0

604P Thin Sillage to Evaporator Pump $1.9 2.75 $0.0

605P Whole Stillage to Pre-Evaporator Pump $3.2 2.75 $0.0

606P Process Condensate Pump $2.9 2.75 $0.0

607T Whole Stillage Tank $137.5 2.75 $0.0

608T Thin Stillage Tank $113.7 2.75 $0.0

609T Process Condensate Tank $71.4 2.75 $0.0

610U Air Pollution Control -Thermal Oxidizer $505.0 2.75 $0.0

$4,246.9 $0.0701U Product Loading & Transfer Pumps $20.9 2.75 $0.0

702P Denaturant Discharge Pump $1.6 2.75 $0.0

703T Ethanol Day Tank $138.5 2.75 $0.0

704T Ethanol Product Storage Tank $334.7 2.75 $0.0

705T Denaturant Tank $52.0 2.75 $0.0

$547.8 $0.0

Page 11: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

801U Wastewater Treatment $256.0 2.75 $0.0

802U Plant Main Air Compressor $48.9 2.75 $0.0

803 U Steam Generator w/ Deaerator & Pumps $413.7 2.75 $0.0

804U Cooling Tower System $253.8 2.75 $0.0

$972.4 $0.0Totals $11,181.5 $9,598.9

(Capital Cost)

Page 12: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424
Page 13: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Equip Name Units

101U Grain Cleaning Equipment 1GRAIN 29,343 kg/h 28,268102U Corn Milling Equipment - Hammer Mills 4GRAIN 29,255 kg/h 28,183103U Grain Handling Equipment 1GRAIN 29,343 kg/h 28,268

Subtotal205E Process Condensate to Slurry Mix Tank 729,467 cal/sec 838,646207E Cook Heat Exchanger EM03 283,103 cal/sec 296,208208U Liquification Tank Agitator 11LMASH 92,715 kg/h 87,069209P Sulfuric Acid Metering Pump none kg/h210P Caustic To Slurry Tank Pump none kg/h211P Slurry Chop & Recirc Pump 11LMASH 92,715 kg/h 87,069212P Liquified Mash Pump 11LMASH 92,715 kg/h 87,069213P Saccharified Mash Pump 21MASH 109,180 kg/h 102,534214U Saccharification Tank Agitator 21MASH 109,180 kg/h 102,534215U Slurry Mixing Tank Agitator 11LMASH 92,715 kg/h 87,069

Subtotal401C CO2 Compressor COMP HP 101 kg/h 100402P Fermentor Cooling Pumps COOL3 953,618 kg/h 890,958403E Fermentor Cooling Exchangers COOLER -833,333 cal/sec -802,795405E Saccharified Mash Cooler EM05 -231,618 cal/sec -249,636407P Beer Column Feed Pump 27BEER 100,080 kg/h 92,924408P Scrubber Bottoms Water Pump 75SW 10,666 kg/h 8,424409P 24BEER 100,381 kg/h 93,785410P Clean In Place Return Pump 21MASH 109,180 kg/h 102,534411P Yeast Slurry Pmp YEAST 6 kg/h 5414T Yeast Tank With Agitator YEAST 6 kg/h 5416P CIP Supply Pump 21MASH 109,180 kg/h 102,534

Subtotal505E Beer Column Reboiler BEERCOL 2,347,496 cal/sec 2,075,804506E Stripper Col Reboiler RECTIFY 360,697 cal/sec 356,732507E Beer Degas Vent Condeser ED07 -18,232 cal/sec -81,933512P Beer Columns Bottom Pump 29STILL 80,339 kg/h 75,982513P Rectifier Bottoms Pump 40SB 10,881 kg/h 8,655514P Stripper Bottoms Pump 40SB 10,881 kg/h 8,655515P Regeneration / Ejector Liquid Pump 40SB 10,881 kg/h 8,655516P Reflux Pump 47REGEN 2,755 kg/h 2,770517U Molesieve Package PURETH 8,960 kg/h 8,962525P Final Product Pump PURETH 8,960 kg/h 8,962

Subtotal601U Centrifuge 53PEWS 67,485 kg/h 61,969602U Evaporator Incl Turbine Recompressor 64EC 40,502 kg/h 40,390603U Grain Dryer 66VENT 13,151 kg/h 10,883604P Thin Sillage to Evaporator Pump 58TS 33,509 kg/h 32,401605P Whole Stillage to Pre-Evaporator Pump 29STILL 80,339 kg/h 75,982

Equip No.

Aspen Reference

Original Size

Scaled Size

EM01DUTY

Beer from Fermenter to Degasser Pump

Page 14: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

606P Process Condensate Pump PC 62,049 kg/h 57,468607T Whole Stillage Tank 29STILL 80,339 kg/h 75,982608T Thin Stillage Tank 55TS 80,339 kg/h 75,982610U Air Pollution Control -Thermal Oxidizer 66VENT 13,151 kg/h 10,883

Subtotal701U Product Loading & Transfer Pumps PURETH 8,960 kg/h 8,962702P Denaturant Discharge Pump PURETH 8,960 kg/h 8,962

Subtotal801U Wastewater Treatment EXTRAPC 165 kg/h 100802U Plant Main Air Compressor PURETH 8,960 kg/h 8,962803U Steam Generator w/ Deaerator & Pump Cell M60 27,211 kg/h 26,011804U Cooling Tower System Cell P60 985,753 kg/h 1,011,119

SubtotalTotals

Page 15: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Base New

Nat Gas Electric CT Water Nat Gas Electrickg/hr cal/sec kW kg/hr kg/hr kg/hr cal/sec kW

0.9634 16.67 16.10.9634 95.00 91.50.9634 58.33 56.2

0 0 170 0 0 0 0 1641.1497 5,117 5,8831.0463 1,986 2,0780.9391 56.67 53.21.0000 0.03 0.01.0000 1.67 1.70.9391 36.55 34.30.9391 55.78 52.40.9391 28.42 26.70.9391 18.33 17.20.9391 25.00 23.5

7,103 0 222 0 0 7,961 0 2090.9947 100.69 100.20.9343 138.87 129.70.9634 270,3901.0778 75,2090.9285 35.21 32.70.7897 2.91 2.30.9343 21.44 20.00.9391 0.62 0.60.9634 4.97 4.80.9634 8.33 8.00.9391 1.02 1.0

0 0 314 75,209 270,390 0 0 2990.8843 16,468 14,5620.9890 2,530 2,5024.4939 5,9200.9458 21.40 20.20.7954 7.27 5.80.7954 4.36 3.50.7954 15.95 12.71.0056 14.47 14.61.0002 193 61 443,766 193 61.21.0002 7.3 7.3

19,191 0 132 449,687 0 17,258 0 1250.9183 294.15 270.10.9972 795 250.47 460,857 793 249.80.8276 2,877,500 473.71 2,381,359 392.00.9669 4.36 4.20.9458 14.47 13.7

Size Ratio

150 PSI Steam Well Water

150 PSI Steam

Page 16: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

0.9262 7.27 6.70.9458 51.67 48.90.9458 16.67 15.80.8276 210,000 226.20 173,792 187.2

795 3,087,500 1,339 460,857 0 793 2,555,151 1,1881.0003 1.67 1.71.0003 2.91 2.9

0 0 5 0 0 0 0 50.9511 34.48 32.81.0003 100.00 100.00.9559 4,427,215 180.92 4,232,054 172.91.0257 116.00 119.0

0 4,427,215 431 0 0 0 4,232,054 42527,089 7,514,715 2,613 985,753 270,390 26,011 6,787,205 2,415

J57
elec based on aspen steam generator model (1/24/97) for 32,600#/hr scaled up
J58
Source Richardson
Page 17: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

CT Waterkg/hr kg/hr

0 0

0 0

###81,060

81,060 260,481

26,604

443,875

470,480 0

459,580

Well Water

Page 18: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

459,580 0

0 0

0 01,011,119 260,481

Page 19: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Shelled Corn to Ethanol Process AnalysisDry Grind Starch Fermentation

All Values in 2002 Dollars

Annual Ethanol Production Cost

Fuel Ethanol Production (MM Gal. / Year) Ethanol Yield (Gal / Bushel Corn)

Feedstock Cost ($/Bushel)

VariablesCost Year for Analysis 2002 Life of Equipment 10 Days of Operation per Year 330 % Denaturant in Final Fuel Ethanol 5.0%Feedstock Cost $/ Bushel $2.38DDGS Price $/ton $95.25

Installed Capital Costs $9,598,931

B18
Oxy Fuel News 12/16/02 Chicago Cash Grain Prices
B19
Oxy Fuel News 12/16/02
Page 20: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Shelled Corn to Ethanol Process AnalysisDry Grind Starch Fermentation

All Values in 2002 Dollars

$1.20 Per Gallon

25.0 Ethanol at 68°F2.84$2.38 15% Moisture Content

Operating Costs ($/gal ethanol)Shelled Corn $0.987Denaturant $0.000Other Raw Materials $0.072Utilities $0.000Labor, Supplies and Overheads $0.098Depreciation $0.038CoProduct Credits $0.000Total Product Cost per gallon $1.195

Operating Costs ($/yr)Shelled Corn $24,682,787Denaturant $0Other Raw Materials $1,796,007Utilities $0Labor, Supplies and Overheads $2,446,704Depreciation $960,000CoProduct Credits $0Total Production Cost $29,885,498

Page 21: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Location of Eq. Numbers

ASPEN d4:IT4Heat Exchanger Surface Area Calculation

Aspen Parameter

Equip No. Equip Name Name Area (sq. ft)

H-200 Hydrolyzate Cooler 250 QLMT0200 #REF! #REF!

H-201 Beer Column Feed Economizer 150 QLMT0201 #REF! #REF!

H-205 Pneumapress Vent Condensor 250 QLMT0205 #REF! #REF!

H-244 Waste Vapor Condensor 150 QLMT0244 #REF! #REF!

H-302 Saccharified Slurry Cooler 300 QLMT0302 #REF! #REF!

E-501-3 Evaporators 170 QLMTE502 #REF! #REF!

H-512 Beer Column Feed Interchanger 200 QLMT0512 #REF! #REF!

INPUT BY USER

CALLED FROM ANOTHER SHEET

CALCULATED

Scaling Material Stream Sheet Name:

Overall Heat Transfer

Coefficient (Btu/hr-F-sq. ft)

Duty / LMTD (Btu/hr-F)

Page 22: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

d12:IT12 ASPEN!d4:IT4 ASPEN!d12:IT12

Location of Mixed Stream Total Mass

Flow

Page 23: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

CALLED FROM ANOTHER SHEET ASPEN

Agitator Power Calculation

Equip No. Equip Name

A-205 Hydrolyzate Mix Tank Agitator 2.95E-04 0.25 1

A-209 Overliming Tank Agitator 9.85E-05 1 1

A-224 Reacidification Tank Agitator 9.85E-05 4 1

A-232 Reslurrying Tank Agitator 2.95E-04 0.25 1

A-300 Ethanol Fermentor Agitator 2.95E-05 -------- --------

A-301 Seed Hold Tank Agitator 1.97E-05 24 1

A-304 4th Seed Vessel Agitator 5.91E-05 24 2

A-305 5th Seed Vessel Agitator 1.97E-05 24 2

A-306 Beer Surge Tank Agitator 5.91E-05 4 1

A-310 Saccharification Tank Agitator 2.95E-05 -------- --------

A-530 Recycled Water Tank Agitator 7.88E-05 0.333 1

A-720 CSL Storage Tank Agitator 1.97E-05 120 1

A-760 CSL/DAP Day Tank Agitator 9.85E-05 28 1

A-910A CIP System Sterilization Tank Agitator 5.92E-01 -------- 1

A-910B CIP System Cleaning Chemical Tank Agitator 2.96E-01 -------- 1

INPUT BY USER

CALCULATED Scaling Material

Stream Sheet Name:

Power Ratio (kW/L)

Residence Time (hr)

Number of Agitators

C5
; Unless Otherwise Stated c THESE POWER REQUIREMENTS WERE OBTAINED FROM THE c 1990 BASE CASE. EXCEPTIONS INCLUDE THOSE FOR c WASTEWATER TREATMENT WHICH WERE OBTAINED FROM c THE 1995 CHEM SYSTEMS STUDY AND THE CH2MHILL c REPORT. They are listed in kW/L. 3.94E-4 kW/L=2 hp/1000 gal.
D5
c THE RESIDENCE TIMES (h) WERE TAKEN FROM THE 1990 BASE c CASE EXCEPT FOR THOSE FOR WASTEWATER TREATMENT c WHICH WERE TAKEN FROM THE 1995 CHEM SYSTEMS STUDY AND c FROM THE CH2MHILL REPORT.
C6
1.5 hp/1000 gal
C7
0.5 hp/1000 gal
D7
Residence time from Delta T
C8
0.5 hp/1000 gal
C9
1.5 hp/1000 gal
C10
0.15 hp/1000 gal
E10
Aspen parameter is for total fermentation volume
C11
0.1 hp/1000 gal
D11
Same as F-305 (Largest Seed)
C12
0.3 hp/1000 gal
D12
One batch turns around each 24 hrs. So this is the effective residence time
C13
0.1 hp/1000 gal
D13
One batch turns around each 24 hrs. So this is the effective residence time
C14
0.3 hp/1000 gal
E14
kibsen: 2 agitators, but 0.3 hp/1000 gal is total power req'd
C15
0.15 hp/1000 gal
E15
Aspen parameter is for total fermentation volume
C16
0.4 hp/1000 gal
D16
Residence time 20 minutes, 0.333 hours
C17
0.1 hp/1000 gal Based on A-301
C18
0.5 hp/1000 gal
C19
1 hp/1000 gal MR estimate; 50000 gal Delta T estimate; 63 kg/hr base flow; Units are Kw/kg/hr
C20
0.5 hp/1000 gal MR estimate; 50000 gal Delta T estimate; 63 kg/hr base flow Units are Kw/kg/hr
Page 24: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Location of Eq. Numbers

d4:IT4 d12:IT12 ASPEN!d4:IT4 ASPEN!d12:IT12

Aspen Parameter

Name

VOLFS205 -------- #REF! #REF!

VOLFM209 #REF! #REF! #REF!

VOLFM239 #REF! #REF! #REF!

VOLFS232 -------- #REF! #REF!

VOLFS300 #REF! -------- #REF!

VOLFS301 -------- #REF! #REF!

VOLFS304 -------- #REF! #REF!

VOLFS305 -------- #REF! #REF!

VOLFM306 #REF! #REF! #REF!

VOLFS310 #REF! -------- #REF!

VOLFM530 #REF! #REF! #REF!

VOLFM720 #REF! #REF! #REF!

VOLFM760 #REF! #REF! #REF!

STRM0914 #REF! -------- #REF!

STRM0914 #REF! -------- #REF!

Total Mixer Power #REF!

Location of Mixed Stream Total Mass Flow

Flow (cu. M/s, L/min,L, kg/hr)

Volumetric Flow (L/hr)

Agitator Electrical Demand (kW)

G10
liters
G15
liters
Page 25: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

CALLED FROM ANOTHER SHEET CALCULATED ASPEN

Pump Power Calculation

Equip No. Equip Name

P-101 Wash Table Pump 50 0.67 0.95

P-102 Wash Water Pump 50 0.67 0.95

P-103 Clarifier Underflow Pump 50 0.169 0.95

P-104 Clarified Water Pump 50 0.67 0.95

P-105 Belt Press Sump Pump 40 0.337 0.95

P-201 Sulfuric Acid Pump 441 0.6 0.95

P-205 PneumaPress Feed Pump 0.00333 -------- --------

P-209 Overlimed Hydrolyzate Pump 150 0.6 0.95

P-211 Primary Filtrate Pump 0.000103 -------- --------

P-213 Wash Filtrate Pump 0.0017 -------- --------

P-222 Filtered Hydrolyzate Pump 150 0.6 0.95

P-224 Saccharification Feed Pump 0.01231 -------- --------

P-239 Reacidified Liquor Pump 100 0.6 0.95

P-300 Fermentation Recirc/Transfer Pump 138.6 0.6 0.95

P-301 Seed Hold Transfer Pump 0.02462 -------- --------

P-302 Seed Transfer Pump 0.02462 -------- --------

P-306 Beer Transfer Pump 170 0.6 0.95

P-310 Saccharification Recirc/Transfer Pump 138.6 0.6 0.95

P-501 Beer Column Bottoms Pump 150 0.6 0.95

P-503 Beer Column Reflux Pump 140 0.6 0.95

P-504 Rectification Column Bottoms Pump 155 0.6 0.95

P-505 Rectification Column Reflux Pump 110 0.6 0.95

P-511 1st Effect Pump 110 0.6 0.95

P-512 2nd Effect Pump 110 0.6 0.95

P-513 3rd Effect Pump 110 0.6 0.95

P-514 Evaporator Condensate Pump 110 0.6 0.95

P-515 Scrubber Bottoms Pump 110 0.6 0.95

P-530 Recycled Water Pump 150 0.6 0.95

P-701 Ethanol Product Pump 112 0.6 0.95

P-703 Sulfuric Acid Pump 150 0.6 0.95

P-710 Gasoline Pump 200 0.6 0.95

P-720 CSL Pump 150 0.6 0.95

P-750 Cellulase Pump 50 0.6 0.95

INPUT BY USER Scaling Material

Stream Sheet Name:

Head (ft) or Kw/L/min or

Kw/kg/hrPump

EfficiencyMotor

Efficiency

C6
The listed pump design is 2500 gpm (0.1578 m^3/s) at 50 ft (21.68 psi) (Harris report, App. A, p3) EPM is the pump efficiencies (set at 67% to get 100hp design like report) EEL is the motor efficiencies Two Units
D6
set at 67% to get 100 hp design like report
C7
The listed pump design is 5000 gpm (0.3155 m^3/s) at 50 ft (21.68 psi) (Harris report, App. A, p5)
C8
The listed pump design is 100 gpm (0.00631 m^3/s) at 50 ft (21.68 psi) (Harris report, App. A, p5)
D8
set at 16.9% to get 7.5 hp design like report
C9
The listed pump design is 5000 gpm (0.3155 m^3/s) at 50 ft (21.68 psi) (Harris report, App. A, p5)
C10
The listed pump design is 100 gpm (0.00631 m^3/s) at 40 ft (17.34 psi) (Harris report, App. A, p6)
D10
set at 33.7% to get 3 hp design like report
C11
Use H2SO4 density of 1.8 to adjust head of 245 ft. to get 191.1 psi used in rigorous model
C12
=3.33E-3 kW/kg/hr Power Required from Harris design (300 hp at 75% power) equals 225 hp / Flow from R0101C (see equip design sheet) Power Required 225 hp / 50299 kg/hr CISOLIDS flow = 4.47E-3 hp/kg/hr
C14
= 1.03E-4 kW/kg/hr Power Required from Harris design (25 hp at 75% power) equals 18.8 hp / Flow from R0101C (see equip design sheet) Power Required 18.8 hp / 136350 kg/hr CISOLIDS flow = 1.38E-4 hp/kg/hr
C15
= 1.70E-3 kW/kg/hr Power Required from Harris design (400 hp at 75% power) equals 300.0 hp / Flow from R0101C (see equip design sheet) Power Required 300.0 hp / 131530 kg/hr CISOLIDS flow = 2.28E-3 hp/kg/hr
C17
This is a rotary lobe pump, so the power req. is not calc. like a cent. pump. It has an input of 1.231E-2 kW/ L/min c (50 hp/800 gpm) Need to double for 2 pumps?
C20
This is a rotary lobe pump, so the power req. is not calc. like a cent. pump. It has an input of 2.462E-2 kW/ L/min c (100 hp/800 gpm)
C21
P-302 is a larger pump, but doesn't run all of the time. On the average it is the same as P-301
Page 26: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

P-760 CSL/DAP Pump 150 0.6 0.95

P-902 Cooling Water Pumps 70 0.6 0.95

P-910A CIP System Pump 288.75 0.6 0.95

P-910B CIP System Pump 138.6 0.6 0.95

P-910C CIP System Pump 138.6 0.6 0.95

P-912 Make-up Water Pump 75 0.6 0.95

P-914 Process Water Circulating Pump 150 0.6 0.95

C41
First pump 600 gpm & 125 psi from Delta-T
C42
Second pump 2000 gpm & 60 psi from Delta-T
C43
Third pump 600 gpm from Delta-T & 60 psi MR estimate
Page 27: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Location of Eq. Numbers

d4:IT4 d12:IT12 ASPEN!d4:IT4 ASPEN!d12:IT12

Aspen Parameter

Name

VOLFM101 #REF! #REF!

VOLFM102 #REF! #REF!

VOLFM103 #REF! #REF!

VOLFM104 #REF! #REF!

VOLFM105 #REF! #REF!

VOLFM201 #REF! #REF!

SOLD0220 #REF! #REF!

VOLFM209 #REF! #REF!

STRM0221 #REF! #REF!

STRM0256 #REF! #REF!

VOLFM222 #REF! #REF!

VOLFL224 #REF! #REF!

VOLFM239 #REF! #REF!

VOLFM300 #REF! #REF!

VOLFL301 #REF! #REF!

VOLFL302 #REF! #REF!

VOLFM306 #REF! #REF!

VOLFM310 #REF! #REF!

VOLFM501 #REF! #REF!

VOLFM503 #REF! #REF!

VOLFM504 #REF! #REF!

VOLFM505 #REF! #REF!

VOLFM511 #REF! #REF!

VOLFM512 #REF! #REF!

VOLFM513 #REF! #REF!

VOLFM514 #REF! #REF!

VOLFM515 #REF! #REF!

VOLFM530 #REF! #REF!

VOLFM701 #REF! #REF!

VOLFM703 #REF! #REF!

VOLFM710 #REF! #REF!

VOLFM720 #REF! #REF!

VOLFM750 #REF! #REF!

Location of Mixed Stream Total Mass Flow

Volumetric Flow (cu. M/s or L/min) of

Mass Flow (kg/hr)Pump Electrical Demand (kW)

Page 28: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

VOLFM760 #REF! #REF!

VOLFM902 #REF! #REF!

STRM0914 #REF! #REF!

STRM0914 #REF! #REF!

STRM0914 #REF! #REF!

VOLFM912 #REF! #REF!

VOLFM914 #REF! #REF!

Total Pump Power #REF!

Page 29: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

CALLED FROM ANOTHER SHEET ASPEN

Miscellaneous Equipment Power CalculationAspen Parameter

Equip No. Equip Name Name

C-101 Bale Transport Conveyor 5.70E-04 STRM0101 #REF!

C-102 Bale Unwrapping Conveyor 1.14E-04 STRM0101 #REF!

C-103 Belt Press Discharge Conveyor 2.85E-05 STRM0101 #REF!

C-104 Shredder Feed Conveyor 1.14E-04 STRM0101 #REF!

M-104 Corn Stover Wash Table 8.56E-04 STRM0101 #REF!

M-105 Shredder 1.14E-02 STRM0101 #REF!

M-107 Polymer Feed System 2.55E-04 STRM0101 #REF!

S-101 Clarifier Thickener 5.70E-05 STRM0101 #REF!

S-102 Belt Press 4.28E-05 STRM0101 #REF!

S-103 Magnetic Separator ---------- ---------- ----------

C-201 Hydrolyzate Screw Conveyor 1.64E-04 STRM0220 #REF!

C-202 Hydrolyzate Washed Solids Belt Conveyor 3.06E-04 STRM0255 #REF!

C-225 Lime Solids Feeder 3.52E-04 STRM0227 #REF!

M-202 Prehydrolysis/Screw Feeder/Reactor 7.14E-03 STRM0101 #REF!

P-223 Lime Unloading Blower 1.17E-02 STRM0227 #REF!

S-205 PneumaPress Filter 2.00E-03 SOLD0220 #REF!

S-222 Hydroclone & Rotary Drum Filter 1.11E-04 STRM0239 #REF!

C-501 Lignin Wet Cake Screw 6.39E-04 STRM0571 #REF!

M-503 Molecular Sieve (9 pieces) 1.94E+04 VOLFM701 #REF!

S-505 PneumaPress Filter 5.05E-03 SOLD0570 #REF!

WWT Waste Water Treatment System ---------- WKWWTRMT ----------

C-755 DAP Solids Feeder 3.52E-04 STRM0755 #REF!

P-755 DAP Unloading Blower 1.17E-02 STRM0755 #REF!

M-902 Cooling Tower System ---------- WKCWTOWR ----------

M-904 Plant Air Compressor ---------- WKAIRCMP ----------

M-910 CIP System Centrifugal Separator 3.97E-01 STRM0914 #REF!

S-904 Instrument Air Dryer 7.50E-05 STRM0101 #REF!

PLANTPOW Miscellaneous additional plant power ---------- ---------- ----------

Total Misc. Power

INPUT BY USER

CALCULATED Scaling Material

Stream Sheet Name:

Power Ratio (kW/kg/hr)

Mass Flow Rate (kg/hr)

C5
;DEFINE THE POWER REQUIREMENTS ( KW / (KG/HR) ) ;UNLESS OTHERWISE NOTED, THE POWER REQUIREMENTS WERE CALCULATED ;FROM THE 1990 BASE CASE. ;THEY ARE SIMPLY RATIOS OF THE POWER REQUIRED AND THE FLOWRATE ;THROUGH THE EQUIPMENT ITEM.
C6
2 motors at 50 hp each = 100 hp Harris stated that power requirements are 75% of connected power and reported connected power for equipment Harris' design was for 2000 bone dry metric tonnes / day at 15% moisture That is equivalent to 2594 short tons as recieved material / day Also equivalent to 98039 kg as received material / hr
C7
2 motors at 10 hp each
C8
1 motor at 5 hp
C9
4 motors at 5 hp each
C10
2 motors at 75 hp each
C11
4 motors at 500 hp each
C12
Minimal Power required so 25 kW Dividing and multiplying by PWRRATE?
C13
1 motor at 10 hp each
C14
1 unit at 7.5 hp each
C16
50 hp/ 250 ton/hr
C17
37.5 hp/91633 kg/hr = 28.0 KW/91633 Kg/hr
C18
Icarus 20 Oct 98 1.5 hp/7000 lb/hr
C19
Anco Eaglin: 0.85 * 1801 hp (motor sizes) = 1531 hp = 1142 kW for total feed of 159948 kg/hr in Stream 101
C21
= 2.00E-3 kW/kg/hr Power Required from Harris design (60 hp for 3 machines at 75% power) equals 135 hp / Flow from R0101C (see equip design sheet) Power Required 135 hp / 50299 kg/hr CISOLIDS flow = 2.68E-3 hp/kg/hr
C24
THE POWER REQUIREMENTS ARE SIMPLE RATIOS FROM A COST QUOTE. .0204 kW/gal/hr
C25
180 hp * (.7457 kW/hp) / 26601 kg/hr Using same power calc as before a PP?
C27
COPY OF C-225 POWER CALCULATION
C28
Copy of P-223 power calculation
C31
25 kW MR estimate; 63 kg/hr base flow
C32
12 kW ratioed from Delta T
Page 30: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Location of Eq. Numbers

d4:IT4 d12:IT12 ASPEN!d4:IT4 ASPEN!d12:IT12

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

0

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

#REF!

1000

#REF!

Location of Mixed Stream Total Mass

Flow

Equipment Electrical Demand (kW)

F15
Power is unknown, but believed to be low; therefore, 0.0 power input
F26
WWT system power is calculated in Fortran WWT in Aspen
F29
CW tower system power is calculated in Fortran CW in Aspen
F30
125 hp & 2 in use + Pneumapress air reqs.
F33
1000 kW requirement is a guess (MR 12 Feb 1998)
Page 31: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Data file created by ASPEN PLUS Rel. 9.2-1 on 16:13:12 Mon Jun 21, 1999Run ID: _UNNAMED Item: MASSFLOW Screen: Sensitivity.Results

VARY 1 BLRCAPTL

bw0404a_scenario_4_burn 0 20 22606961.7

Page 32: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Data file created by ASPEN PLUS Rel. 9.2-1 on 16:13:12 Mon Jun 21, 1999

CODTOTAL DIAMD501 INUMSACA INUMSACC INUMSSCF

512.164924 10.3824936 4 2 2

Page 33: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

INUMSSFA P501FLOW QCHWTOTA QCND0501 QCND0502

CAL/SEC CAL/SEC CAL/SEC 4 3802.15301 -86904.333 56700.3844 3938152.35

Page 34: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

QCWTOTAL QF301-6B QHET0517 QHX300EA QHX310EA

CAL/SEC CAL/SEC CAL/SEC 17100333 38557.0053 7098044.73 426634.816 15847.6856

Page 35: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

QLMT0200 QLMT0201 QLMT0205 QLMT0244 QLMT0301

234409.93 548997.752 35084.4815 199215.811 0

Page 36: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

QLMT0302 QLMT0512 QLMTE502 QRFD0501 QRFD0502

CAL/SEC CAL/SEC

418728.86 245594.099 4095876.95 -5923665.2 -738173.13

Page 37: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

QSTMH301 QTOTM908 S510S521 S840AH2O SOLD0220

CAL/SEC KG/HR KG/HR -460595.72 1502.91199 47989.3089 794 21308.6986

Page 38: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

SOLD0570 STRM0101 STRM0107 STRM0214 STRM0217

KG/HR KG/HR KG/HR KG/HR KG/HR 15867.1085 42353 12.2633189 44433.4882 120237.188

Page 39: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

STRM0220 STRM0221 STRM0225 STRM0227 STRM0228

KG/HR KG/HR KG/HR KG/HR KG/HR 100949.293 62276.6891 38672.6042 1049.94533 121146.536

Page 40: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

STRM0229 STRM0230 STRM0232 STRM0239 STRM0240

KG/HR KG/HR KG/HR KG/HR KG/HR 3167.15844 118508.799 187550.691 121675.957 120096.59

Page 41: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

STRM0250 STRM0255 STRM0256 STRM0257 STRM0304

KG/HR KG/HR KG/HR KG/HR KG/HR 187550.691 38856.5395 57819.9014 4687.01654 18340.3813

Page 42: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

STRM0502 STRM0515 STRM0516 STRM0523 STRM0525

KG/HR KG/HR KG/HR KG/HR KG/HR 190139.009 17597.6583 24449.9205 9021.30278 188954.929

Page 43: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

STRM0528 STRM0531 STRM0551 STRM0557 STRM0571

KG/HR KG/HR KG/HR KG/HR KG/HR 65577.7966 19663.2207 7634.86062 5920.92137 40579.8676

Page 44: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

STRM0572 STRM0612 STRM0630 STRM0631 STRM0701

KG/HR KG/HR KG/HR KG/HR KG/HR 148301.521 45636.3664 18.8220609 0.06411977 725.994914

Page 45: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

STRM0703 STRM0710 STRM0713 STRM0717 STRM0723

KG/HR KG/HR KG/HR KG/HR KG/HR 18323.6532 1441.371 6.47E+03 4.71E-05 14.4072707

Page 46: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

STRM0735 STRM0745 STRM0750 STRM0755 STRM0903

KG/HR KG/HR KG/HR KG/HR KG/HR 572.784439 1049.94533 2955.01214 71.426206 297416.835

Page 47: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

STRM0904 STRM0905 STRM0914 STRM0921 STRM0922

KG/HR KG/HR KG/HR KG/HR KG/HR 297416.835 378245.267 63.04 1 1.36980739

Page 48: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

STRM534A STRM804C STRM840A VOLFL224 VOLFL301

KG/HR KG/HR KG/HR 143342.707 7191.81594 5294 2985.97601 301.035592

Page 49: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

VOLFL302 VOLFM101 VOLFM102 VOLFM103 VOLFM104

301.035592 0.1578 0.3155 0.003155 0.15775

Page 50: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

VOLFM105 VOLFM201 VOLFM209 VOLFM222 VOLFM239

0.003155 0.0002204 0.03280907 0.03248702 0.03297154

Page 51: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

VOLFM300 VOLFM306 VOLFM310 VOLFM501 VOLFM503

0.43125568 0.05634926 0.04486754 0.23987666 0.00069444

Page 52: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

VOLFM504 VOLFM505 VOLFM511 VOLFM512 VOLFM513

0.00750522 0.02222222 0.21079338 0.05393468 0.02004288

Page 53: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

VOLFM514 VOLFM515 VOLFM530 VOLFM701 VOLFM703

0.04214118 0.00215878 0.04134675 6.30E-03 0.0002204

Page 54: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

VOLFM710 VOLFM720 VOLFM750 VOLFM760 VOLFM902

0.000202 0.00015937 0.00079926 0.00015937 1.90251026

Page 55: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

VOLFM912 VOLFM914 VOLFS205 VOLFS232 VOLFS300

0.0832359 0.10671294 93797.0364 179158.653 6440320.37

Page 56: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

VOLFS301 VOLFS304 VOLFS305 VOLFS310 WKAIRCMP

21467.7346 1788.97788 17889.7788 6600373.84 1297.31539

Page 57: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

WKBLRNET WKCWTOWR WKWWTRMT WWTCOSTS Z5101FLW

KG/HR

-16519.264 390.348439 185.775746 1970363.53 798.994899

Page 58: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Z6101FLW ZC101FLW ZW101FLW ZX101FLW ZZDEN515

KG/HR KG/HR KG/HR KG/HR GM/CC 491.930193 13426.2476 6353 7397.75278 0.79156688

Page 59: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Equipment Number Equipment NameA-201 In-line Sulfuric Acid MixerA-205 Hydrolyzate Mix Tank AgitatorA-209 Overliming Tank AgitatorA-224 Reacidification Tank AgitatorA-232 Reslurrying Tank AgitatorA-300 Ethanol Fermentor AgitatorA-301 Seed Hold Tank AgitatorA-304 4th Seed Vessel AgitatorA-305 5th Seed Vessel AgitatorA-306 Beer Surge Tank AgitatorA-310 Saccharification Tank AgitatorA-530 Recycled Water Tank AgitatorA-602 Equalization Basin AgitatorA-606 Anaerobic AgitatorA-608 Aerobic Lagoon AgitatorA-701 Denaturant In-line MixerA-720 CSL Storage Tank AgitatorA-760 CSL/DAP Day Tank AgitatorC-101 Bale Transport ConveyorC-102 Bale Unwrapping ConveyorC-103 Belt Press Discharge ConveyorC-104 Shredder Feed ConveyorC-201 Hydrolyzate Screw ConveyorC-202 Hydrolysate Washed Solids Belt ConveyorC-225 Lime Solids FeederC-501 Lignin Wet Cake ScrewC-614 Aerobic Sludge ScrewC-755 DAP Solids FeederD-501 Beer ColumnD-502 Rectification ColumnE-501 1st Effect EvaporationE-502 2nd Effect EvaporationE-503 3rd Effect EvaporationF-1 FeedstockF-300 Ethanol FermentorF-301 1st Seed FermentorF-302 2nd Seed FermentorF-303 3rd Seed FermentorF-304 4th Seed FermentorF-305 5th Seed FermentorH-200 Hydrolyzate CoolerH-201 Beer Column Feed EconomizerH-205 Pneumapress Vent CondensorH-244 Waste Vapor CondensorH-300 Fermentation CoolerH-301 Hydrolyzate HeaterH-302 Saccharified Slurry Cooler

Page 60: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

H-304 4th Seed Fermentor CoilH-305 5th Seed Fermentor CoilH-310 Saccharification CoolerH-501 Beer Column ReboilerH-502 Rectification Column ReboilerH-504 Beer Column CondenserH-505 Start-up Rect. Column CondenserH-512 Beer Column Feed InterchangerH-517 Evaporator CondenserH-602 Anaerobic Digestor Feed CoolerH-801 Burner Combustion Air PreheaterH-811 BFW PreheaterM-101 Truck ScalesM-102 Truck Unloading ForkliftM-103 Bale Moving ForkliftM-104 Corn Stover Wash TableM-105 ShredderM-106 Concrete Feedstock-Storage SlabM-107 Polymer Feed SystemM-202 Prehydrolysis/Screw Feeder/Reactor

M-503 Molecular Sieve (9 pieces)M-604 Nutrient Feed SystemM-606 Biogas Emergency FlareM-612 Filter Precoat SystemM-803 Fluidized Bed Combustion ReactorM-804 Combustion Gas BaghouseM-811 Turbine/GeneratorM-820 Hot Process Water Softener SystemM-830 Hydrazine Addition Pkg.M-832 Ammonia Addition PkgM-834 Phosphate Addition Pkg.M-902 Cooling Tower SystemM-904 Plant Air CompressorM-910 CIP SystemP-1 ElectricityP-101 Wash Table PumpP-102 Wash Water PumpP-103 Clarifier Underflow PumpP-104 Clarified Water PumpP-105 Belt Press Sump PumpP-201 Sulfuric Acid PumpP-205 Pneumapress Feed PumpP-209 Overlimed Hydrolyzate PumpP-211 Primary Filtrate PumpP-213 Wash Filtrate PumpP-222 Filtered Hydrolyzate PumpP-223 Lime Unloading BlowerP-224 Saccharification Feed Pump

Page 61: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

P-239 Reacidified Liquor PumpP-300 Fermentation Recirc/Transfer PumpP-301 Seed Hold Transfer PumpP-302 Seed Transfer PumpP-306 Beer Transfer PumpP-310 Saccharification Recirc/Transfer PumpP-501 Beer Column Bottoms PumpP-503 Beer Column Reflux PumpP-504 Rectification Column Bottoms PumpP-505 Rectification Column Reflux PumpP-511 1st Effect PumpP-512 2nd Effect PumpP-513 3rd Effect PumpP-514 Evaporator Condensate PumpP-515 Scrubber Bottoms PumpP-530 Recycled Water PumpP-602 Anaerobic Reactor Feed PumpP-606 Aerobic Digestor Feed PumpP-608 Aerobic Sludge Recycle PumpP-610 Aerobic Sludge PumpP-611 Aerobic Digestion Outlet PumpP-614 Sludge Filtrate Recycle PumpP-616 Treated Water PumpP-701 Ethanol Product PumpP-703 Sulfuric Acid PumpP-704 Firewater PumpP-710 Gasoline PumpP-720 CSL PumpP-750 Cellulase PumpP-755 DAP Unloading BlowerP-760 CSL/DAP PumpP-804 Condensate PumpP-811 Turbine Condensate PumpP-824 Deaerator Feed PumpP-826 BFW PumpP-828 Blowdown PumpP-830 Hydrazine Transfer PumpP-902 Cooling Water PumpP-912 Make-up Water PumpP-914 Process Water Circulating PumpR-3 Corn Steep LiquorR-4 Hydrated LimeR-5 Sulfuric AcidR-7 Purchased Cellulase Enzyme

R-8 Diammonium Phosphate

S-1 Boiler ChemicalsS-10 Bulk Unleaded Gasoline

Page 62: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

S-101 Clarifier ThickenerS-102 Belt PressS-103 Magnetic SeparatorS-11 Clarifier Polymer

S-12 Propane

S-2 Cooling Tower ChemsS-205 Pneumapress FilterS-222 Hydroclone & Rotary Drum FilterS-227 LimeDust Vent Baghouse

S-4 WasteWater ChemsS-5 WasteWater Polymer

S-505 Pneumapress FilterS-600 Bar ScreenS-614 Belt Filter Press

S-7 MethaneS-755 DAP Vent Baghouse

S-8 Makeup WaterS-904 Instrument Air DryerT-101 Wash Water TankT-102 Clarifier Thickener TankT-201 Sulfuric Acid TankT-203 Blowdown TankT-205 Hydrolyzate Mixing TankT-209 Overliming TankT-211 Primary Filtrate TankT-213 Wash Filtrate TankT-220 Lime Storage BinT-224 Reacidification TankT-232 Slurrying TankT-301 Seed Hold TankT-306 Beer Storage TankT-310 Saccharification TankT-503 Beer Column Relfux DrumT-505 Rectification Column Reflux DrumT-512 Vent ScrubberT-514 Evaporator Condensate DrumT-530 Recycled Water TankT-602 Equalization BasinT-606 Anaerobic DigestorT-608 Aerobic DigestorT-610 ClarifierT-701 Ethanol Product Storage Tank

Page 63: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

T-703 Sulfuric Acid Storage TankT-704 Firewater Storage TankT-709 Propane Storage TankT-710 Gasoline Storage TankT-720 CSL Storage TankT-750 Cellulase Storage TankT-755 DAP Storage BinT-760 CSL/DAP Day TankT-804 Condensate Collection TankT-824 Condensate Surge DrumT-826 DeaeratorT-828 Blowdown Flash DrumT-830 Hydrazine DrumT-902 Prehydrolysis Filter Air ReceiverT-904 Plant Air ReceiverT-905 Product Recovery Filter Air ReceiverT-914 Process Water Tank

W-2 Disposal of Steam 809

W-3 Disposal of Stream 229

Page 64: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Equipment DescriptionStatic Mixer, 248 gpm total flow.Top-Mounted, 1800 rpm, 50 hpTop Mounted, 1800 rpm, 25 hpTop-Mounted, 1800 rpm, 93 hpTop-Mounted, 1800 rpm, 50 hpSide Mounted, 2 per vessel, 75 hp each, 0.15 hp/1000 galTop Mounted, 1800 rpm, 23 hp, 0.1 hp/1000 galTop Mounted, 1800 rpm, 6 hp, 0.3 hp/1000 galTop Mounted, 1800 rpm, 19 hp, 0.1 hp/1000 galTop Mounted, 1800 rpm, 4 hp, 0.3 hp/1000 galSide Mounted, 2 per vessel, 75 hp each, 0.15 hp/1000 gal5 hp, 50 rpm,38 hp each, Fixed Prop, 0.1 hp/1000 galFixed Prop, 41 hp, 0.05 hp/1000 galTwister Surface Aerators, 50 HP eaStatic Mixer, total flow 341 gpmTop Mounted, 1800 rpm, 23 hp, 0.1 hp/1000 galTop Mounted, 1800 rpm, 5 hp, 0.5 hp/1000 galBale Transport Conveyor, 400 ft long, 8' wide, 50 HP motorBale Unwrapping Conveyor, 90 bale / hrBelt Press Discharge Conveyor, 3' wide X 50' long.Shredder Feed Conveyor, 8' wide X 30' long. 6001 lbs 31 fpm18" dia. X 33' long, 7600 cfh max flow4' X 60' belt conveyor8" dia., 140 cfh, 7000 lb/hr max flow14" Dia X 100' Long9" Dia X 25' Long8" dia., 140 cfh, 7000 lb/hr max flow13.5' dia, 32 Actual Trays, Nutter V-Grid Trays11.5' dia.(rect)., 4' dia. (strip) x 18" T.S., 60 act. Trays, 60% eff., Nutter V-Grid trays22280 sf each., 135 BTU/hr sf F22278 sf., 170 BTU/hr sf F22278 sf each., 170 BTU/hr sf F $35/TON COST in cents / ton962,651 gal. each, 7 day residence total, 90% wv, API, atmospheric20 gal, jacketed, agitated, 1.3' dia., 2' high, 15 psig194 gal., jacketed, agitated, 3' dia., 4' high, 2.5 psig1950 gal., jacketed, agitated, 6.5' dia, 8' high, 2.5 psig19444 gal., 12' dia x 23' high, atmospheric194500 gal., API, atmosphericFixed Tube Sheet,1990 sf, 27" dia. X 20' longFloating Head, 6266 sf, 48" dia x 23' longFixed Tube Sheet, 120 sf, CS constructionFloating Head, 6266 sf, 48" dia x 23' long2393 sf, 300 BTU/hr sf F256 sf, 400 BTU/hr sf F3765 sf total, 1255 sf each, 300 BTU/hr sf F

Page 65: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

27 sf, 1" sch 40 pipe, 105 BTU/hr sf F307 sf, 3" sch 40 pipe, 92 BTU/hr sf F2393 sf, 300 BTU/hr sf FFixed TS, 13899 sf, 41" dia., 20' long, 178 BTU/hr sf FThermosyphon, 1089 sf, 20" dia., 20' long, 130 BTU/hr sf FFloating Head, 880 sf, 20" dia., 22' long, 92 BTU/hr sf FFixed TS, 4146 sf, 39" dia, 20' long, 157 BTU/hr sf F909 sf, 200 BTU/hr sf FFixed TS, 8223 sf, 39" dia., 20' long, 220 BTU/hr sf FTEMA BES Type, Floating Head37000 sf combustion air/exhaust interchangerFloating Head, 500 SFTruck Scales; 10' X 50' 50tnTruck Unloading Propane Gas ForkliftBale Moving Propane Gas ForkliftCorn Stover Wash Table (55 ton/hr)Shredder (28 ton/hr)Concrete Feedstock-Storage Slab 350' X 538'Polymer Feed SystemHorizontal Screw, Anco-Eaglin quote for Alloy 825-clad

Superheater, twin mole sieve columns, product cooler, condenser, pumps, vacuum source.5 Tanks and PumpsFlare and PilotTank, Agitator, Pump900 to 1250 psig/950F Circ. Fluid BedPulse Shaker, 545000 cfm, 135,135 SF52-61 MW; 281000 KG/HR STEAM1000 gpm flow, 24" dia softener. Includes filters, chemical feeders, piping, valves150 gal tank, agitator, 2 metering pumps150 gal tank, agitator, 2 metering pumps150 gal tank, agitator, 2 metering pumps71000 gpm, 147.8 x E6 kcal/hr, 5 cell3075 cfm, 125 psig outletDesigned by Delta-T. Same cost as sum of previous units.NREL electrical power cost in CENTS / kWhr2500 gpm, 50 ft head.5000 gpm, 50 ft head.Clarifier Underflow Pump MOD SRL 2X3-10 100 GPM -- 50 TDH5000 gpm, 50 ft head.Belt Press Sump Pump VJC 1.5X2.11 100 GPM -- 40 TDH4 gpm, 245 ft. headGoulds Mod 3196 ^X8-13 1000 gpm 60 ft TDH 25 hp 1200 RPM687 gpm, 150 ft. headGoulds Mod 3410 10X12-17 1000 GPM 60 ft TDHGoulds Mod 3410 10X12-17 6000 GPM 200 ft TDH721 gpm, 150 ft head7425 cfm, 6 psi, 22275 lb/hr737 gpm, 200 ft head

Page 66: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

720 gpm, 100 ft head1060 gpm, 150 ft head172 gpm, 150 ft head1231 gpm total, 615 gpm each, 100 ft head1632 gpm each, 171 ft head1060 gpm, 150 ft head5053 gpm, 150 ft head12 gpm, 140 ft head154 gpm, 158 ft head437 gpm, 110 ft head2393 gpm each, 110 ft head1261 gpm, 110 ft head412 gpm each, 110 ft head617 gpm, 125 ft head69 gpm, 104 ft head790 gpm, 150 ft head876 gpm, 150 ft head830 gpm, 150 ft head2.5 gpm, 150 ft head25.3 gpm, 150 ft head828 gpm, 150' head22 gpm, 150' head803 gpm, 100 ft head324 gpm, 112 ft head215 gpm, 150 ft head2500 gpm, 50 ft head17 gpm, 200 ft head431 gpm, 150 ft head2500 gpm, 50 ft head7425 cfm, 6 psi, 22275 lb/hr431 gpm, 150 ft head272 gpm 150' head175 gpm, 150 ft head.650 gpm, 115 ft head.500 gpm, 2740 ft head.29 gpm, 150 ' head5 gpm, 75 ft head41000 gpm, 70 ft head.1083 gpm, 75 ft. head1199 gpm ea, 75 ft. headWhole slurry/ 50% solids: COST CENTS PER TONLime, Chemical, pebble, hydrated bulk, f.o.b. plants$70/Ton COST IN CENTS / TONTanks, works; $25/TON (Higher Price)Base Cost in cents/ton (2500)Cellulase Enzyme

Bulk Unleaded Gasoline, Average 1999; COST CONVERTED TO CENTS PER TON

Ammonium phosphate, fert. Grade, min. 18% N, 20% P bulk, carload, spont, f.o.b., Fla, works $142/ton (high number); COST IS CENTS/TONCost is average of 6 cases in Radian 1991 report, Appendix C. CONVERTED TO CENTS / TON

Page 67: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Clarifier Thickener 5000 GPM mechanismBelt Press 1.5 meterTramp iron magnet separator.COST CENTS PER TON -- As determined from Harris E-Mail

MOD 30-12-316 285 GPM 360 SQ FT AREAHydrocyclone and Vacuum Filter8333 cfm, 1389 sf, 6 cfm/sf

COST CENTS PER TONAs determined in merrick & co report app g

0.5" Mech. cleaned ScreenBELT THICKNESS

8333 cfm, 1389 sf, 6 cfm/sf

400 SCFM Air Dryer, -40F DewpointWash Water Tank (20' Diameter X 22' Tall, 50,000 gal)Clarifier Thickener Tank (80' diameter)6444 gal., 24 hr. residence time, 90% wv14500 gal., 11' dia x 30' high, 10 min. res. time, 75% wv, 15 psigModeled after Tank T-232 in Enzyme Process. 15 min. res. Time46200 gal., 16' dia. X 32' high, 1 hr. res. time, 90% wv, 15 psig12'6" D X 13' high 12,000 gal10' D X 11' high 6000 gal4455 cf, 14' dia x 25' high, 1.5x rail car vol., atmospheric185200 gal., 32' dia x 32' high, 4 hr. res. time, 90% wv, atmospheric24770 gal., 13' dia. X 25' high, 15 min. res. time, 90% wv, atmospheric233,333 gal., API atmospheric456617 gal., 45' dia x 40' high, 4 hr res. Time, 90% wv, atmospheric962,651 gal. each, 7 day residence total, 90% wv, API, atmospheric346 gal, 15 min res. Time, 50% wv, 3' dia., 6.5' long, 25 psig13106 gal, 15 min res time, 50% wv, 9' dia, 27.5' long, 25 psig7' dia x 25' high, 4 stages, plastic Jaeger Tri-Packing10233 gal, 10 min res. Time, 75% wv, 9' dia., 21.5' long, 1 psig13218 gal, Residence time 20 min, 2.5 psig377516 gal, Residence time 7.2 hr,810250 gal each, space velocity 12g COD/L/DAY19500000 gal, 16.3 day residence time195289 gal, Residence time 3.9 hr.604,133 gal, 7 day res time total, 90% wv, 51' dia x 40' high, atmospheric

Propane, consumer grade, industrial price, DOE/EIA 1999 annual average $0.734/gal, COST CENTS PER TONNo reference at this time - used previously recorded data from spreadsheetCONVERTED TO $/100 LBS

urea, agricultural, granular, f.o.b., MW terminals;phosphate, rock, Fla, land pebble, 66-68% b.p.l. bulk, c.l.soda, caustic, liq, 50% f.o.b.micronutrients (merrick, app G.)COST CENT PER TON

3@MOD 30-10-316 285 GPM 300 SQ FT AREA & 1@MOD 30-11-316 314 GPM 314 SQ FT AREA

methane, electric utilities price; 1999 annual average - $2.57/1000 cu.ft.COST CENTS PER TON

Makeup WaterCONVERTED TO CENTS / TON

Page 68: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

18697 gal, 120 hr res time, 90% wv, 12' dia x 22' high, atmospheric600,000 gal, 4 hr res time, 51' dia x 40' high, atmospheric3435 gal, 10 day res time, 50% extra, 4' dia x 23.6' length, 250 psig63,593 gal, 168 hr res time, 90% wv, 19' dia x 32' high, atmospheric71,918 gal, 120 hr res time, 90% wv, 20' dia x 32' high, atmospheric130,115 gal, 48 hr res time, 90% wv, 27' dia x 32' high, atmospheric1425 cf, 9' dia x 19.5' high, 1.5x vessel vol. Req. for 7-day res time, atmospheric10,000 gal, 24 hr res time, 90% wv, 9.5' dia x 18.9' high, atmospheric1600 gal, Residence time 1.5 minutes, atmospheric11,400 gal, 24' x 9'dia, 15psig, Residence time 11 min.18,170 gal hold tank, 150 psig design pressure, 10 min residence time424 gal, 4.5' x 4'dia, 15 psig260 gal, 4.9' x 3'dia., 10psig1000 gal900 gal., 200 psig1000 gal756000 gal. 8 hr res timeCost of solid waste disposal - Chem Systems Report 1993, pg. VI-9. Reported cost is $20/tonne.COST CENTS PER TONCost of solid waste disposal - Chem Systems Report 1993, pg. VI-9. Reported cost is $20/tonneCOST CENTS PER TON

Page 69: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Equipment Type Base Cost Cost BasisMIXER 1 0 1900 ICARUSAGITATOR FIXED-PROP 1 0 36000 ICARUSAGITATOR FIXED-PROP 1 0 19800 ICARUSAGITATOR FIXED-PROP 1 0 65200 ICARUSAGITATOR FIXED-PROP 1 0 36000 ICARUSAGITATOR FIXED-PROP 34 0 19676 DELTA-T98AGITATOR FIXED-PROP 1 0 12551 DELTA-T98AGITATOR FIXED-PROP 2 0 11700 ICARUSAGITATOR FIXED-PROP 2 0 10340 DELTA-T98AGITATOR FIXED-PROP 2 0 48700 ICARUSAGITATOR FIXED-PROP 34 0 19676 DELTA-T98AGITATOR FIXED-PROP 1 0 5963 VENDORAGITATOR FIXED-PROP 1 0 28400 ICARUSAGITATOR FIXED-PROP 4 0 30300 ICARUSAGITATOR SURFACE-AERATOR 16 0 31250 VENDORMIXER STATIC 1 0 1900 ICARUSAGITATOR FIXED-PROP 1 0 12551 DELTA-T98AGITATOR FIXED-PROP 1 0 12795 ICARUSCONVEYOR BELT 2 0 400000 HARRIS00CONVEYOR BELT 2 0 150000 HARRIS00CONVEYOR BELT 1 50000 HARRIS00CONVEYOR BELT 4 0 60000 HARRIS00CONVEYOR SCREW 1 0 59400 ICARUSCONVEYOR BELT 1 0 80000 HARRIS00CONVEYOR ROTARY-VALVE 1 0 3900 ICARUSCONVEYOR SCREW 1 0 31700 ICARUSCONVEYOR SCREW 1 0 5700 ICARUSCONVEYOR ROTARY-VALVE 1 0 3900 ICARUSCOLUMN DISTILLATION 1 0 478100 ICARUSCOLUMN DISTILLATION 1 0 525800 DELTA-T98HEATX SHELL-TUBE 2 0 544595 DELTA-T98HEATX SHELL-TUBE 1 0 435650 DELTA-T98HEATX SHELL-TUBE 2 0 435650 DELTA-T98

3500 UNKNOWNTANK FLAT-BTM-STORAGE 17 0 493391 VENDORREACTOR VERTICAL-VESSEL 2 0 14700 ICARUSREACTOR VERTICAL-VESSEL 2 0 32600 ICARUSREACTOR VERTICAL-VESSEL 2 0 81100 ICARUSREACTOR FLAT-BTM-STORAGE 2 0 39500 ICARUSREACTOR FLAT-BTM-STORAGE 2 0 147245 VENDORHEATX SHELL-TUBE 1 0 45000 ICARUSHEATX SHELL-TUBE 2 1 132800 ICARUSHEATX SHELL-TUBE 1 0 15385 ICARUSHEATX SHELL-TUBE 2 1 132800 ICARUSHEATX PLATE-FRAME 17 1 4000 ICARUSHEATX SHELL-TUBE 1 1 22400 QUESTIMATEHEATX PLATE-FRAME 3 0 25409 DELTA-T98

Equipment Category

Num Required

Num Spares

Page 70: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

HEATX IMMERSED-COIL 1 0 3300 ICARUSHEATX IMMERSED-COIL 1 0 18800 ICARUSHEATX PLATE-FRAME 17 1 4000 ICARUSHEATX SHELL-TUBE 1 1 158374 DELTA-T98HEATX SHELL-TUBE 1 0 29600 ICARUSHEATX SHELL-TUBE 1 0 29544 DELTA-T98HEATX SHELL-TUBE 1 0 86174 DELTA-T98HEATX PLATE-FRAME 1 1 19040 DELTA-T98HEATX SHELL-TUBE 1 1 121576 DELTA-T98HEATX SHELL-TUBE 1 0 128600 ICARUSMISCELLANEOUS MISCELLANEOUS 1 0 1049900 ICARUSHEATX SHELL-TUBE 1 0 58400 ICARUSSCALE TRUCK-SCALE 2 0 34000 HARRIS00VEHICLE LOADER 4 1 18000 HARRIS00VEHICLE LOADER 4 0 18000 HARRIS00SIZE-REDUCTION 2 0 104000 HARRIS00SIZE-REDUCTION 4 0 302000 HARRIS00MISCELLANEOUS CONCRETE-SLAB 1 0 450655 HARRIS00MISCELLANEOUS MISCELLANEOUS 1 0 30000 HARRIS00REACTOR VESSEL W/ PADDLE 3 0 2505084 VENDOR

MISCELLANEOUS PACKAGE 1 0 2700000 VENDORMISCELLANEOUS PACKAGE 1 0 31400 VENDORMISCELLANEOUS MISCELLANEOUS 1 0 20739 VENDORMISCELLANEOUS MISCELLANEOUS 1 0 3000 MERRICK98MISCELLANEOUS MISCELLANEOUS 1 0 24900000 VENDORSEPARATOR FABRIC-FILTER 1 0 2536300 VENDORGENERATOR STEAM-TURBINE 1 0 10000000 VENDORMISCELLANEOUS PACKAGE 1 0 1381300 RICHARDSONMISCELLANEOUS PACKAGE 1 0 19000 CHEMSYST94MISCELLANEOUS PACKAGE 1 0 19000 CHEMSYST94MISCELLANEOUS PACKAGE 1 0 19000 CHEMSYST94COOLING-TOWER INDUCED-DRAFT 1 0 1659000 DELTA-T98COMPRESSOR CENTRIFUGAL 2 1 278200 ICARUSMISCELLANEOUS MISCELLANEOUS 1 0 95000 DELTA-T98

4 CHEMSYST94PUMP CENTRIFUGAL 2 1 20000 HARRIS00PUMP CENTRIFUGAL 2 1 15000 HARRIS00PUMP RECIPROCATING 1 1 6000 HARRIS00PUMP CENTRIFUGAL 1 1 15000 HARRIS00PUMP SLURRY 1 1 19000 HARRIS00PUMP CENTRIFUGAL 1 1 4800 ICARUSPUMP CENTRIFUGAL 2 1 15416 HARRIS00PUMP CENTRIFUGAL 1 1 10700 ICARUSPUMP CENTRIFUGAL 1 1 32549 HARRIS00PUMP CENTRIFUGAL 1 1 49803 HARRIS00PUMP CENTRIFUGAL 1 1 10800 ICARUSFAN CENTRIFUGAL 1 0 47600 DELTA-T98PUMP ROTARY-LOBE 2 1 61368 VENDOR

Page 71: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

PUMP CENTRIFUGAL 1 1 10800 ICARUSPUMP CENTRIFUGAL 17 1 8000 ICARUSPUMP ROTARY-LOBE 1 1 22194 VENDORPUMP ROTARY-LOBE 2 0 54088 VENDORPUMP CENTRIFUGAL 1 1 17300 ICARUSPUMP CENTRIFUGAL 17 1 8000 ICARUSPUMP CENTRIFUGAL 1 1 42300 ICARUSPUMP CENTRIFUGAL 1 1 1357 DELTA-T98PUMP CENTRIFUGAL 1 1 4916 DELTA-T98PUMP CENTRIFUGAL 1 1 4782 DELTA-T98PUMP CENTRIFUGAL 2 1 19700 ICARUSPUMP CENTRIFUGAL 1 1 13900 ICARUSPUMP CENTRIFUGAL 2 1 8000 ICARUSPUMP CENTRIFUGAL 1 1 12300 ICARUSPUMP CENTRIFUGAL 1 0 2793 DELTA-T98PUMP CENTRIFUGAL 1 1 10600 ICARUSPUMP CENTRIFUGAL 1 1 11400 ICARUSPUMP CENTRIFUGAL 1 1 10700 ICARUSPUMP SLURRY 1 0 11100 ICARUSPUMP SLURRY 1 0 11100 ICARUSPUMP CENTRIFUGAL 1 1 10700 ICARUSPUMP CENTRIFUGAL 1 1 6100 ICARUSPUMP CENTRIFUGAL 1 1 10600 ICARUSPUMP CENTRIFUGAL 2 1 7500 ICARUSPUMP CENTRIFUGAL 1 1 8000 ICARUSPUMP CENTRIFUGAL 1 1 18400 ICARUSPUMP CENTRIFUGAL 1 1 4500 ICARUSPUMP CENTRIFUGAL 1 1 8800 ICARUSPUMP CENTRIFUGAL 1 1 18400 ICARUSFAN CENTRIFUGAL 1 0 47600 DELTA-T98PUMP CENTRIFUGAL 1 1 8800 ICARUSPUMP CENTRIFUGAL 2 0 7100 ICARUSPUMP CENTRIFUGAL 2 0 7800 ICARUSPUMP CENTRIFUGAL 2 0 9500 ICARUSPUMP CENTRIFUGAL 5 0 52501 VENDORPUMP CENTRIFUGAL 2 0 5100 ICARUSPUMP CENTRIFUGAL 1 0 5500 DELTA-T98PUMP CENTRIFUGAL 1 1 332300 ICARUSPUMP CENTRIFUGAL 1 1 10800 ICARUSPUMP CENTRIFUGAL 2 1 11100 ICARUS

15000 VENDOR7000 CMR2500 CMR

10823.22 DEFINED

14200 CMR

280000 RADIAN9118955 UNKNOWN

Page 72: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

SEPARATOR 1 0 135000 HARRIS00S/L SEPARATION FILTER-PRESS 1 0 100000 HARRIS00SEPARATOR MAGNET 1 0 13863 VENDOR

250000 HARRIS00

436 DOE/EIA

200000 UNKNOWNSEPARATOR PNEUMAPRESS 3 0 1575000 HARRIS00S/L SEPARATOR ROTARY-DRUM 1 0 165000 VENDORSEPARATOR FABRIC-FILTER 1 0 32200 ICARUS

30956 CMR;MERRICK98500000 CMR;MERRICK98

SEPARATOR PNEUMAPRESS 4 0 1418750 HARRIS00SEPARATOR SCREEN 1 0 117818 CH2MHL91S/L SEPARATOR FILTER-PRESS 1 0 650223 VENDOR

11900 DOE/EIASEPARATOR FABRIC-FILTER 1 0 32200 ICARUS

24 UNKNOWNDRYER PACKAGE 1 1 15498 RICHARDSONTANK VERTICAL-VESSEL 1 0 50000 HARRIS00TANK CLARIFER 1 0 135000 HARRIS00TANK VERTICAL-VESSEL 1 0 5760 DELTA-T98TANK VERTICAL-VESSEL 1 0 64100 ICARUSTANK FLAT-BTM-STORAGE 1 0 44800 ICARUSTANK VERTICAL-VESSEL 1 0 71000 ICARUSTANK VERTICAL-VESSEL 1 0 36000 HARRIS00TANK VERTICAL-VESSEL 1 0 18000 HARRIS00TANK LIVE-BTM-BIN 1 0 69200 ICARUSTANK FLAT-BTM-STORAGE 1 0 147800 ICARUSTANK FLAT-BTM-STORAGE 1 0 44800 ICARUSTANK FLAT-BTM-STORAGE 1 0 161593 VENDORTANK FLAT-BTM-STORAGE 1 0 237700 ICARUSTANK FLAT-BTM-STORAGE 17 0 493391 VENDORTANK HORIZONTAL-VESSE 1 0 11900 ICARUSTANK HORIZONTAL-VESSE 1 0 45600 ICARUSCOLUMN ABSORBER 1 0 99000 DELTA-T98TANK HORIZONTAL-VESSE 1 0 37200 ICARUSTANK FLAT-BTM-STORAGE 1 0 14515 VENDORTANK FLAT-BTM-STORAGE 1 0 350800 VENDORTANK FLAT-BTM-STORAGE 4 0 881081 VENDORREACTOR LINED-PIT 1 0 635173 MERRICK98SEPARATOR CLARIFIER 1 0 174385 VENDORTANK FLAT-BTM-STORAGE 2 0 165800 ICARUS

Page 73: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

TANK FLAT-BTM-STORAGE 1 0 42500 ICARUSTANK FLAT-BTM-STORAGE 1 0 166100 ICARUSTANK HORIZONTAL STOR 1 0 24834 ICARUSTANK FLAT-BTM-STORAGE 1 0 43500 ICARUSTANK FLAT-BTM-STORAGE 1 0 88100 ICARUSTANK FLAT-BTM-STORAGE 2 0 125900 ICARUSTANK LIVE-BTM-BIN 1 0 33384 ICARUSTANK FLAT-BTM-STORAGE 1 0 30084 ICARUSTANK VERTICAL-VESSEL 1 0 7100 ICARUSTANK HORIZONTAL-VESSE 1 0 49600 ICARUSTANK HORIZONTAL-VESSE 1 0 165000 VENDORTANK HORIZONTAL-VESSE 1 0 9200 ICARUSTANK VERTICAL-VESSEL 1 0 12400 ICARUSTANK HORIZONTAL-PRES 3 0 17000 HARRIS00TANK HORIZONTAL-VESSE 1 0 13000 ICARUSTANK HORIZONTAL-PRES 4 0 17000 HARRIS00TANK FLAT-BTM-STORAGE 1 0 195500 ICARUS

1820 CHEMSYST94

1820 CHEMSYST94

Page 74: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Cost Year Base Type Base Units Installation Factor1997 55308 FLOW KG/HR 1 1997 358810 FLOW KG/HR 1.2 1997 167050 FLOW KG/HR 1.3 1997 167280 FLOW KG/HR 1.2 1997 358810 FLOW KG/HR 1.2 1996 1.2 1996 41777 FLOW KG/HR 1.2 1997 41777 FLOW KG/HR 1.2 1996 41777 FLOW KG/HR 1.2 1998 381700 FLOW KG/HR 1.2 1996 1.2 1998 179446 FLOW KG/HR 1.3 1997 188129 FLOW KG/HR 1.2 1997 810250 SIZE GAL 1.2 1998 812 SIZE HP 1.4 1997 19436 FLOW KG/HR 1 1996 41777 FLOW KG/HR 1.2 2001 1400 FLOW KG/HR 1.2 2000 98040 FLOW KG/HR 1.62 2000 98040 FLOW KG/HR 1.19 2000 98040 FLOW KG/HR 1.89 2000 98040 FLOW KG/HR 1.38 1997 225140 FLOW KG/HR 1.3 2000 91633 FLOW KG/HR 1.45 1997 1.3 1997 99199 FLOW KG/HR 1.4 1997 978 FLOW KG/HR 1.4 1997 1.3 1998 16.892 SIZE SQM 2.1 1996 56477 FLOW KG/HR 2.1 1996 22278 SIZE SQF 2.1 1996 22278 SIZE SQF 2.1 1996 22278 SIZE SQF 2.1 2000 LB1998 1.2 1997 2.8 1997 2.8 1997 2.8 1997 41777 FLOW KG/HR 1.2 1998 41777 FLOW KG/HR 1.2 1997 1988 SIZE SQF 2.1 1997 12532 SIZE SQF 2.1 2000 120 SIZE SQF 2.1 1997 12532 SIZE SQF 2.1 1997 67820 DUTY CAL/S 2.1 2001 256 SIZE SQF 2.1 1998 3765 SIZE SQF 2.1

Base For Scaling

Page 75: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

1997 38339 DUTY CAL/S 1.2 1997 38339 DUTY CAL/S 1.2 1997 67820 DUTY CAL/S 2.1 1996 -7863670 DUTY CAL/S 2.1 1997 -987427 DUTY CAL/S 2.1 1996 277820 DUTY CAL/S 2.1 1996 4905410 DUTY CAL/S 2.1 1996 909 SIZE SQF 2.1 1996 6764222 DUTY CAL/S 2.1 1997 7627 SIZE SQF 2.1 1997 6676015 DUTY CAL/S 1.5 1997 415 SIZE SQF 2.1 2000 98040 FLOW KG/HR 2.47 2000 98040 FLOW KG/HR 1 2000 98040 FLOW KG/HR 1 2000 98040 FLOW KG/HR 2.39 2000 98040 FLOW KG/HR 1.38 2000 98040 FLOW KG/HR 2.2 2000 98040 FLOW KG/HR 2.28 2000 271313 FLOW KG/HR 2.29

1998 20491 FLOW KG/HR 1 1998 2.58 1998 2572 FLOW KG/HR 1.68 1998 1.4 1998 341270 FLOW KG/HR 1.3 1998 652517 FLOW KG/HR 1.5 1998 281179 FLOW KG/HR 1.5 1999 225889 FLOW KG/HR 1.3 1994 229386 FLOW KG/HR 1 1994 229386 FLOW KG/HR 1 1994 229386 FLOW KG/HR 1 1998 41100000 DUTY CAL/S 1.2 2000 98040 FLOW KG/HR 1.3 1995 63 FLOW KG/HR 1.2 1999 LB2000 98040 FLOW KG/HR 3.87 2000 98040 FLOW KG/HR 5.19 2000 98040 FLOW KG/HR 13.41 2000 98040 FLOW KG/HR 7.07 2000 98040 FLOW KG/HR 2.92 1997 1647 FLOW KG/HR 2.8 2000 50299 FLOW KG/HR 3.34 1997 167050 FLOW KG/HR 2.8 2000 136350 FLOW KG/HR 3.56 2000 131530 FLOW KG/HR 2.71 1997 162090 FLOW KG/HR 2.8 1998 547 FLOW KG/HR 1.4 1998 358810 FLOW KG/HR 2.8

Page 76: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

1997 167280 FLOW KG/HR 2.8 1997 67737 DUTY CAL/S 2.8 1998 41777 FLOW KG/HR 1.4 1998 41777 FLOW KG/HR 1.4 1997 381701 FLOW KG/HR 2.8 1997 67737 DUTY CAL/S 2.8 1997 5053 FLOW 2.8 1998 277820 DUTY CAL/S 2.8 1998 31507 FLOW KG/HR 2.8 1998 4906301 DUTY CAL/S 2.8 1997 278645 FLOW KG/HR 2.8 1997 91111 FLOW KG/HR 2.8 1997 48001 FLOW KG/HR 2.8 1997 140220 FLOW KG/HR 2.8 1998 15377 FLOW KG/HR 2.8 1997 179446 FLOW KG/HR 2.8 1997 188129 FLOW KG/HR 2.8 1997 185782 FLOW KG/HR 2.8 1997 5862 FLOW KG/HR 1.4 1997 5862 FLOW KG/HR 1.4 1997 187827 FLOW KG/HR 2.8 1997 4885 FLOW KG/HR 2.8 1997 181965 FLOW KG/HR 2.8 1997 18549 FLOW KG/HR 2.8 1997 1647 FLOW KG/HR 2.8 1997 6823 FLOW KG/HR 2.8 1997 887 FLOW KG/HR 2.8 1997 2039 FLOW KG/HR 2.8 1997 6823 FLOW KG/HR 2.8 1998 154 FLOW KG/HR 1.4 1997 2039 FLOW KG/HR 2.8 1997 61471 FLOW KG/HR 2.8 1997 39524 FLOW KG/HR 2.8 1997 293605 FLOW KG/HR 2.8 1998 564626 FLOW KG/HR 2.8 1997 6613 FLOW KG/HR 2.8 1997 229386 FLOW KG/HR 2.8 1997 18290000 FLOW KG/HR 2.8 1997 244160 FLOW KG/HR 2.8 1997 352710 FLOW KG/HR 2.8 1998 2039 LB2001 LB2001 1647 LB1999 0

2001 356 LB

1991 LB1999 LB

Page 77: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

2000 98040 FLOW KG/HR 1.51 2000 98040 FLOW KG/HR 1.25 1998 159948 FLOW KG/HR 1.3 2000 LB

1999 1.87 FLOW KG/HR

1999 2000 50299 FLOW KG/HR 1.05 1998 5195 FLOW KG/HR 1.4 1997 548 FLOW KG/HR 1.5

1999 LB1999 LB

2000 26601 FLOW KG/HR 1.04 1991 188129 FLOW KG/HR 1.2 1998 438 FLOW KG/HR 1.8

1999 LB1997 548 FLOW KG/HR 1.5

1990 1999 159950 FLOW KG/HR 1.3 2000 98040 FLOW KG/HR 2.8 2000 98040 FLOW KG/HR 3.04 1996 1647 FLOW KG/HR 1.4 1997 270300 FLOW KG/HR 1.2 1997 358810 FLOW KG/HR 1.2 1997 167050 FLOW KG/HR 1.4 2000 136350 FLOW KG/HR 2.45 2000 131530 FLOW KG/HR 3.68 1997 548 FLOW KG/HR 1.3 1997 167280 FLOW KG/HR 1.2 1997 358810 FLOW KG/HR 1.2 1998 41777 FLOW KG/HR 1.2 1998 381700 FLOW KG/HR 1.2 1998 1.2 1997 277820 DUTY CAL/S 2.1 1997 4906301 DUTY CAL/S 2.1 1998 18523 FLOW KG/HR 2.1 1998 164760 FLOW KG/HR 2.1 1998 179446 FLOW KG/HR 1.4 1998 188129 FLOW KG/HR 1.42 1998 810250 SIZE GAL 1.04 1998 19506756 SIZE GAL 1 1998 185782 FLOW KG/HR 1.96 1997 18549 FLOW KG/HR 1.4

Page 78: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

1997 1647 FLOW KG/HR 1.2 1997 6822 FLOW KG/HR 1.4 2001 14.97 FLOW KG/HR 1.4 1997 887 FLOW KG/HR 1.4 1997 2039 FLOW KG/HR 1.4 2001 9234 FLOW KG/HR 1.4 2001 154 FLOW KG/HR 1.3 2001 1400 FLOW KG/HR 1.4 1997 228862 FLOW KG/HR 1.4 1997 222360 FLOW KG/HR 1.7 1998 266213 FLOW KG/HR 2.8 1997 6563 FLOW KG/HR 2.8 1997 229386 FLOW KG/HR 1.7 2000 5259 FLOW KG/HR 1.2 1997 159950 FLOW KG/HR 1.3 2000 5700 FLOW KG/HR 1.2 1997 352710 FLOW KG/HR 1.4

1993 LB

1993 LB

Page 79: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Installation Factor Basis Scale Factor Exp Scale Factor BasisDELTA-T98 0.48 ICARUSDELTA-T98 0.51 GARRETTDELTA-T98 0.51 GARRETTDELTA-T98 0.51 GARRETTDELTA-T98 0.51 GARRETTDELTA-T98DELTA-T98 0.51 GARRETTDELTA-T98 0.51 GARRETTDELTA-T98 0.51 GARRETTDELTA-T98 0.51 GARRETTDELTA-T98DELTA-T98 0.51 GARRETTDELTA-T98 0.51 GARRETTDELTA-T98 0.51 GARRETTMERRICK98 0.51 GARRETTDELTA-T98 0.48 ICARUSDELTA-T98 0.51 GARRETTDELTA-T98 0.51 GARRETTHARRIS00 0.6 DEFAULTHARRIS00 0.6 DEFAULTHARRIS00 0.6 DEFAULTHARRIS00 0.6 DEFAULTDELTA-T98 0.78 GARRETTHARRIS00 0.76 GARRETTDELTA-T98DELTA-T98 0.78 GARRETTDELTA-T98 0.78 GARRETTDELTA-T98DELTA-T98 0.68 ICARUSDELTA-T98 0.68 ICARUSDELTA-T98 0.68 GARRETTDELTA-T98 0.68 GARRETTDELTA-T98 0.68 GARRETT

DELTA-T98 MULTI-UNITDELTA-T98ICARUSDELTA-T98DELTA-T98 0.93 GARRETTDELTA-T98 0.51 GARRETTDELTA-T98 0.51 GARRETTDELTA-T98 0.68 GARRETTDELTA-T98 0.68 GARRETTDELTA-T98 0.68 GARRETTDELTA-T98 0.78 GARRETTDELTA-T98 0.68 GARRETTDELTA-T98 0.78 GARRETT

Page 80: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

DELTA-T98 0.83 ICARUSDELTA-T98 0.98 ICARUSDELTA-T98 0.78 GARRETTDELTA-T98 0.68 GARRETTDELTA-T98 0.68 GARRETTDELTA-T98 0.68 GARRETTDELTA-T98 0.68 GARRETTDELTA-T98 0.68 GARRETTDELTA-T98 0.68 GARRETTDELTA-T98 0.74 VENDORNREL-ESTM 0.6 DEFAULTDELTA-T98 0.68 GARRETTHARRIS00 0.6 DEFAULTHARRIS00 1 ASSUMEDHARRIS00 1 ASSUMEDHARRIS00 0.6 DEFAULTHARRIS00 0.6 DEFAULTHARRIS00 1 HARRIS00HARRIS00 0.6 DEFAULTHARRIS00 0.6 DEFAULT

DELTA-T98 0.7 VENDORVENDOR 0.6 DEFAULT

DELTA-T98 0.75 VENDORVENDOR 0.58 MULTI-UNITDELTA-T98 0.71 VENDORNREL-ESTM 0.82 MULTI-UNITCHEMSYST94 0.6 DEFAULTCHEMSYST94 0.6 DEFAULTCHEMSYST94 0.6 DEFAULTDELTA-T98 0.78 GARRETTDELTA-T98 0.34 GARRETTDELTA-T98 0.6 NREL-ESTM

HARRIS00 0.79 GARRETTHARRIS00 0.79 GARRETTHARRIS00 0.79 GARRETTHARRIS00 0.79 GARRETTHARRIS00 0.79 GARRETTDELTA-T98 0.79 GARRETTHARRIS00 0.79 GARRETTDELTA-T98 0.79 GARRETTHARRIS00 0.79 GARRETTHARRIS00 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.5 GARRETTICARUS 0.7 VENDOR

Page 81: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

DELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTCHEMSYST94 0.7 VENDORCHEMSYST94 0.7 VENDORDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTICARUS 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.5 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETTDELTA-T98 0.79 GARRETT

Page 82: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

HARRIS00 0.6 DEFAULTHARRIS00 0.6 DEFAULTDELTA-T98 0.6 DEFAULT

HARRIS00 0.6 DEFAULTDELTA-T98 0.39 GARRETTDELTA-T98 1 ICARUS

HARRIS00 0.6 DEFAULTDELTA-T98 0.3 ASSUMEDVENDOR 0.72 VENDOR

DELTA-T98 1 ICARUS

DELTA-T98 0.6 DEFAULTHARRIS00 0.51 GARRETTHARRIS00 0.51 GARRETTDELTA-T98 0.71 GARRETTICARUS 0.93 GARRETTDELTA-T98 0.71 GARRETTDELTA-T98 0.71 GARRETTHARRIS00 0.71 GARRETTHARRIS00 0.71 GARRETTDELTA-T98 0.46 ICARUSDELTA-T98 0.51 GARRETTDELTA-T98 0.71 GARRETTDELTA-T98 0.51 GARRETTDELTA-T98 0.71 GARRETTDELTA-T98 MULTI-UNITDELTA-T98 0.93 GARRETTDELTA-T98 0.72 GARRETTDELTA-T98 0.78 GARRETTDELTA-T98 0.93 GARRETTDELTA-T98 0.745 VENDORVENDOR 0.51 GARRETTVENDOR 0.51 GARRETTMERRICK98 1 VENDOR 0.51 GARRETTDELTA-T98 0.51 GARRETT

Page 83: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

ICARUS 0.51 GARRETTDELTA-T98 0.51 GARRETTDELTA-T98 0.72 GARRETTDELTA-T98 0.51 GARRETTICARUS 0.79 GARRETTICARUS 0.79 GARRETTDELTA-T98 0.44 ICARUSICARUS 0.79 GARRETTDELTA-T98 0.71 GARRETTDELTA-T98 0.72 GARRETTCHEMSYST94 0.72 GARRETTDELTA-T98 0.72 GARRETTDELTA-T98 0.93 GARRETTHARRIS00 0.72 GARRETTDELTA-T98 0.72 GARRETTHARRIS00 0.72 GARRETTDELTA-T98 0.51 GARRETT

Page 84: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Process Stream For Scaling Materials of Construction ObsoleteSTRM0214 SS304 NSTRM0220 SS NSTRM0228 SS NSTRM0239 SS NSTRM0250 SS N

SS304 NSTRM0304 SS304 NSTRM0304 SS NSTRM0304 SS NSTRM0502 SS304 N

SS304 NSTRM0572 CS NSTRM0612 SS NANEROVOL SS NAEROBCHP CS NSTRM0703 SS304 NSTRM0735 SS304 NSTRM0735 SS304 NSTRM0101 CS NSTRM0101 CS NSTRM0101 CS NSTRM0101 CS NSTRM0220 SS316 NSTRM0255 CS N

A285C NSTRM0571 CS NSTRM0623 CS N

A285C NDIAMD501 SS304 NS510S521 SS NAREA0502 SS316 NAREA0502 SS316 NAREA0502 SS316 NSTRM0101 N

SS304 NSS304 NSS304 NSS304 N

STRM0304 SS304 NSTRM0304 SS304 NAREA0200 304SS;CS NAREA0201 304SS NAREA0205 CS NAREA0244 304SS NQHX300EA SS304 NAREA0301 SS NAREA0302 SS304 N

Page 85: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

QF301-6B SS NQF301-6B SS NQHX310EA SS304 NQRD501 SS304;CS NQRD502 SS304;CS NQCD501 SS304;CS NQCD502 SS304;CS NAREA0512 SS NQH517 SS304;CS NAREA0602 SS316;CS NQH801 NAREA0811 SS304 NSTRM0101 CONCRETE NSTRM0101 NSTRM0101 NSTRM0101 A283 NSTRM0101 ALLOY STEEL NSTRM0101 CONCRETE NSTRM0101 CS NSTRM0217 ALLOY 825-CLAD; SS316L N

STRM0515 SS NCS N

STRM0615 SS NCS N

STRM0812 CS NSTRM809A A285C;FABRIC NSTRM0812 NSTRM811B NSTRM813A NSTRM813A NSTRM813A NQCWCAP FIBERGLASS NSTRM0101 NSTRM0914 CS NWKNET NSTRM0101 CS; RUBBER NSTRM0101 CS; SS316 NSTRM0101 CS; RUBBER NSTRM0101 CS; SS316 NSTRM0101 CS NSTRM0710 SS304 NSTRM0220SS SS316 NSTRM0228 304SS NSTRM0221 SS316 NSTRM0256 SS316 NSTRM0230 304SS NSTRM0227 C.S. NSTRM0232 304SS N

Page 86: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

STRM0239 SS304 NQHX300EA SS304 NSTRM0304 SS304 NSTRM0304 SS304 NSTRM0502 SS304 NQHX310EA SS304 NP501FLOW SS NQCD501 SS NSTRM0516 SS NQCD502 SS NSTRM0525 SS NSTRM0528 SS NSTRM0531 SS NSTRM534A SS304 NSTRM0551 SS NSTRM0572 CS NSTRM0612 CS NSTRM0618 CS NSTRM0625 SS316 NSTRM0625 SS316 NSTRM0621 CS NSTRM0627 CS NSTRM0624 CS NSTRM0515 CS NSTRM0710 SS316 NSTRM0713 CS NSTRM0701 CS NSTRM0735 CS NSTRM0750 CS NSTRM0755 CS NSTRM0735 CS NSTRM811A SS316 NSTRM816A SS304 NSTRM811B SS304 NSTRM0813 SS316 NSTRM0821 CS NSTRM813A CS NSTRM0940 CS NSTRM0904 CS NSTRM0905 CS NSTRM0735 NSTRM0745 NSTRM0710 NSTRM0750 N

STRM0755 N

STRM0921 NSTRM0701 N

Page 87: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

STRM0101 CS NSTRM0101 304SS; FILTER NSTRM0101 NSTRM0107 N

STRM0723 N

STRM0922 NSTRM0220SS SS316 NSTRM0229 EPOXY LINED NSTRM0227 A285C;POLYESTER N

STRM0630 NSTRM0631 N

STRM0570SS SS316 NSTRM0612 CS NAEROBCOD 304SS;BUNA N N

STRM0840 NSTRM0755 A285C;POLYESTER N

STRM0903 NSTRM0101 CS NSTRM0101 CS NSTRM0101 CEMENT NSTRM0710 PLASTIC NSTRM0217 SS316 NSTRM0220 SS304 NSTRM0228 SS304 NSTRM0221 SS316 NSTRM0256 SS316 NSTRM0227 CS NSTRM0239 SS304 NSTRM0250 SS304 NSTRM0304 SS304 NSTRM0502 SS304 N

SS304 NQCD501 SS304 NQCD502 SS304 NSTRM0523 SS304;PLASTIC NSTRM534A SS304 NSTRM0572 CS NSTRM0612 CONCRETE NANEROVOL EPOXY-LINED NAEROBVOL POLYMER LINED NSTRM0618 CONCRETE NSTRM0515 A285C N

Page 88: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

STRM0710 SS316 NSTRM0713 A285C NSTRM0723 A515 NSTRM0701 A285C NSTRM0735 SS304 NSTRM0750 SS304 NSTRM0755 CS NSTRM0735 SS304 NSTRM811A A285C NSTRM811B SS304 NSTRM0813 CS;SS316 NSTRM0821 CS NSTRM813A SS316 NSTRM0257 CS NSTRM0101 CS NSTRM0557 CS NSTRM0905 CS N

STRM0809 N

STRM0229 N

Page 89: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Associated PFDPFD-P100-A201;PFD-P300-A201;PFD-P303-A201; PFD-P105-A201;PFD-P110-A201PFD-P100-A202; PFD-P105-A202;PFD-P110-A202PFD-P100-A204;PFD-P300-A203; PFD-P105-A203;PFD-P110-A203PFD-P100-A204;PFD-P300-A203; PFD-P105-A203;PFD-P110-A203PFD-P100-A202;PFD-P300-A202; PFD-P105-A202;PFD-P110-A202PFD-P105-A302;PFD-P110-A302PFD-P100-A301;PFD-P202-A301;PFD-P300-A301;PFD-P201-A301; PFD-P105-A301;PFD-P110-A301PFD-P100-A301;PFD-P202-A301;PFD-P300-A301;PFD-P201-A301; PFD-P105-A301;PFD-P110-A301PFD-P100-A301;PFD-P202-A301;PFD-P300-A301;PFD-P201-A301; PFD-P105-A301;PFD-P110-A301PFD-P100-A302;PFD-P202-A302;PFD-P300-A302;PFD-P201-A302;PFD-P303-A302; PFD-P105-A302;PFD-P110-A302PFD-P105-A302;PFD-P110-A302PFD-P100-A505;PFD-P301-A601;PFD-P300-A601;PFD-P302-A601;PFD-P310-A601;PFD-P303-A505; PFD-P105-A505;PFD-P110-A505PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A603PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P303-A701; PFD-P105-A701;PFD-P110-A701PFD-P105-A701;PFD-P110-A701PFD-P105-A701;PFD-P110-A701PFD-P100-A101; PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101; PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A201;PFD-P300-A201;PFD-P900-A201; PFD-P105-A201;PFD-P110-A201PFD-P100-A202; PFD-P105-A202;PFD-P110-A202PFD-P100-A204;PFD-P202-A203;PFD-P300-A203;PFD-P201-A203;PFD-P900-A202;PFD-P901-A202; PFD-P105-A203;PFD-P110-A203PFD-P100-A505;PFD-P301-A601;PFD-P300-A601;PFD-P302-A601;PFD-P303-A505; PFD-P105-A505;PFD-P110-A505PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P105-A701; PFD-P110-A701PFD-P100-A501;PFD-P202-A501;PFD-P301-A501;PFD-P300-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEMPFD-P105-A302;PFD-P110-A302PFD-P100-A301;PFD-P202-A301;PFD-P300-A301;PFD-P201-A301; PFD-P105-A301;PFD-P110-A301PFD-P100-A301;PFD-P202-A301;PFD-P300-A301;PFD-P201-A301; PFD-P105-A301;PFD-P110-A301PFD-P100-A301;PFD-P202-A301;PFD-P300-A301;PFD-P201-A301; PFD-P105-A301;PFD-P110-A301PFD-P100-A301;PFD-P202-A301;PFD-P300-A301;PFD-P201-A301; PFD-P105-A301;PFD-P110-A301PFD-P100-A301;PFD-P202-A301;PFD-P300-A301;PFD-P201-A301; PFD-P105-A301;PFD-P110-A301PFD-P100-A202;PFD-P300-A202; PFD-P105-A202;PFD-P110-A202PFD-P100-A201;PFD-P202-A204;PFD-P300-A201;PFD-P201-A204; PFD-P105-A201;PFD-P110-A201PFD-P105-A202;PFD-P110-A202PFD-P105-A201;PFD-P110-A201PFD-P100-A302;PFD-P202-A302;PFD-P300-A302;PFD-P201-A302;PFD-P900-A301;PFD-P901-A301; PFD-P105-A302;PFD-P110-A302 PFD-P105-A302;PFD-P110-A302 PFD-P105-A302;PFD-P110-A302

Page 90: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

PFD-P100-A301;PFD-P202-A301;PFD-P300-A301;PFD-P201-A301; PFD-P105-A301;PFD-P110-A301PFD-P100-A301;PFD-P202-A301;PFD-P300-A301;PFD-P201-A301; PFD-P105-A301;PFD-P110-A301PFD-P105-A302;PFD-P110-A302PFD-P100-A501;PFD-P301-A501;PFD-P202-A501;PFD-P300-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A501;PFD-P301-A501;PFD-P202-A501;PFD-P300-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A501;PFD-P301-A501;PFD-P202-A501;PFD-P300-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A801;PFD-P301-A801;PFD-P900-A801;PFD-P303-A801;PFD-P901-A801; PFD-P105-A801; PFD-P110-A801PFD-P100-A802;PFD-P301-A802;PFD-P202-A802;PFD-P300-A802;PFD-P201-A802;PFD-P302-A802;PFD-P900-A802;PFD-P303-A802;PFD-P901-A802; PFD-P105-A802; PFD-P110-A802PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A201;PFD-P900-A201;PFD-P901-A201; PFD-P105-A201;PFD-P110-A201

PFD-P100-A503;PFD-P301-A503;PFD-P202-A503;PFD-P300-A503;PFD-P201-A503;PFD-P302-A503;PFD-P303-A503; PFD-P105-A503;PFD-P110-A503PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A802;PFD-P301-A802;PFD-P202-A802;PFD-P300-A802;PFD-P201-A802;PFD-P302-A802;PFD-P900-A802;PFD-P303-A802;PFD-P901-A802; PFD-P105-A802; PFD-P110-A802PFD-P100-A801;PFD-P301-A802;PFD-P202-A802;PFD-P201-A802;PFD-P302-A802;PFD-P900-A801;PFD-P303-A802;PFD-P901-A801; PFD-P105-A801; PFD-P110-A801PFD-P100-A802;PFD-P301-A802;PFD-P202-A802;PFD-P300-A802;PFD-P201-A802;PFD-P302-A802;PFD-P900-A802;PFD-P303-A802;PFD-P901-A802; PFD-P105-A802; PFD-P110-A802PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A804;PFD-P301-A804;PFD-P202-A804;PFD-P300-A804;PFD-P201-A804;PFD-P302-A804;PFD-P900-A804;PFD-P303-A804;PFD-P901-A804; PFD-P105-A804; PFD-P110-A804PFD-P100-A804;PFD-P301-A804;PFD-P202-A804;PFD-P300-A804;PFD-P201-A804;PFD-P302-A804;PFD-P900-A804;PFD-P303-A804;PFD-P901-A804; PFD-P105-A804; PFD-P110-A804PFD-P100-A804;PFD-P301-A804;PFD-P202-A804;PFD-P300-A804;PFD-P201-A804;PFD-P302-A804;PFD-P900-A804;PFD-P303-A804;PFD-P901-A804; PFD-P105-A804; PFD-P110-A804PFD-P100-A901;PFD-P301-A901;PFD-P202-A901;PFD-P300-A901;PFD-P201-A901;PFD-P302-A901;PFD-P900-A901;PFD-P303-A901;PFD-P901-A901; PFD-P105-A901; PFD-P110-A901PFD-P100-A901;PFD-P303-A901; PFD-P105-A901; PFD-P110-A901PFD-P100-A903;PFD-P301-A903;PFD-P202-A903;PFD-P300-A903;PFD-P201-A903;PFD-P302-A903;PFD-P900-A903;PFD-P303-A903;PFD-P901-A903; PFD-P105-A903; PFD-P110-A903PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEMPFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A201;PFD-P202-A201;PFD-P300-A201;PFD-P201-A201;PFD-P901-A201; PFD-P105-A201;PFD-P110-A201PFD-P100-A202; PFD-P105-A202;PFD-P110-A202PFD-P100-A204;PFD-P300-A203; PFD-P105-A203;PFD-P110-A203PFD-P100-A202;PFD-P303-A202; PFD-P105-A202;PFD-P110-A202PFD-P100-A202; PFD-P105-A202;PFD-P110-A202PFD-P100-A204;PFD-P300-A203; PFD-P105-A203;PFD-P110-A203PFD-P100-A204;PFD-P202-A203;PFD-P300-A203;PFD-P201-A203;PFD-P900-A202;PFD-P901-A202; PFD-P105-A203;PFD-P110-A203 PFD-P105-A202;PFD-P110-A202

Page 91: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

PFD-P100-A204;PFD-P300-A203; PFD-P105-A203;PFD-P110-A203 PFD-P105-A302;PFD-P110-A302PFD-P100-A301;PFD-P202-A301;PFD-P300-A301;PFD-P201-A301; PFD-P105-A301;PFD-P110-A301PFD-P100-A301;PFD-P202-A301;PFD-P300-A301;PFD-P201-A301; PFD-P105-A301;PFD-P110-A301PFD-P100-A302;PFD-P202-A302;PFD-P300-A302;PFD-P201-A302; PFD-P105-A302;PFD-P110-A302 PFD-P105-A302;PFD-P110-A302PFD-P100-A501;PFD-P301-A501;PFD-P202-A501;PFD-P300-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A501;PFD-P301-A501;PFD-P202-A501;PFD-P300-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A504;PFD-P303-A504; PFD-P105-A502;PFD-P110-A502PFD-P100-A505;PFD-P301-A601;PFD-P300-A601;PFD-P303-A505; PFD-P105-A505;PFD-P110-A505PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P303-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P900-A701;PFD-P303-A701;PFD-P901-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P900-A701;PFD-P303-A701;PFD-P901-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P303-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P900-A701;PFD-P303-A701;PFD-P901-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701; PFD-P105-A701;PFD-P110-A701PFD-P105-A701; PFD-P110-A701PFD-P105-A701; PFD-P110-A701PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A802;PFD-P301-A802;PFD-P202-A802;PFD-P300-A802;PFD-P201-A802;PFD-P302-A802;PFD-P900-A802;PFD-P303-A802;PFD-P901-A802; PFD-P105-A802; PFD-P110-A802PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A804;PFD-P301-A804;PFD-P202-A804;PFD-P300-A804;PFD-P201-A804;PFD-P302-A804;PFD-P900-A804;PFD-P303-A804;PFD-P901-A804; PFD-P105-A804; PFD-P110-A804PFD-P100-A901;PFD-P301-A901;PFD-P202-A901;PFD-P300-A901;PFD-P201-A901;PFD-P302-A901;PFD-P900-A901;PFD-P303-A901;PFD-P901-A901; PFD-P105-A901; PFD-P110-A901PFD-P100-A902;PFD-P301-A902;PFD-P202-A902;PFD-P300-A902;PFD-P201-A902;PFD-P302-A902;PFD-P900-A902;PFD-P303-A902;PFD-P901-A902; PFD-P105-A902; PFD-P110-A902PFD-P100-A902;PFD-P301-A902;PFD-P202-A902;PFD-P300-A902;PFD-P201-A902;PFD-P302-A902;PFD-P900-A902;PFD-P303-A902;PFD-P901-A902; PFD-P105-A902; PFD-P110-A902PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEMPFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEMPFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P600-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEMPFD-P100-CHEM;PFD-P303-CHEM;PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEMPFD-P100-CHEM;PFD-P303-CHEM;PFD-P105-CHEM;PFD-P110-CHEM

Page 92: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEMPFD-P100-A202; PFD-P105-A202;PFD-P110-A202PFD-P100-A204;PFD-P202-A203;PFD-P300-A203;PFD-P201-A203; PFD-P105-A203;PFD-P110-A203PFD-P100-A204;PFD-P202-A203;PFD-P300-A203;PFD-P201-A203;PFD-P900-A202;PFD-P901-A202; PFD-P105-A203;PFD-P110-A203

PFD-P100-CHEM;PFD-P202-CHEM;PFD-P303-CHEM; PFD-P105-CHEM; PFD-P110-CHEMPFD-P100-CHEM;PFD-P202-CHEM;PFD-P303-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-A505; PFD-P105-A505;PFD-P110-A505PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A603; PFD-P105-A601;PFD-P110-A601PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602

PFD-P100-CHEM;PFD-P202-CHEM;PFD-P303-CHEM;PFD-P900-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEMPFD-P105-A701;PFD-P110-A701

PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM; PFD-P600-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEMPFD-P100-A901;PFD-P301-A901;PFD-P202-A901;PFD-P300-A901;PFD-P201-A901;PFD-P302-A901;PFD-P900-A901;PFD-P303-A901;PFD-P901-A901; PFD-P105-A901; PFD-P110-A901PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A101;PFD-P900-A101;PFD-P901-A101; PFD-P105-A101;PFD-P110-A101PFD-P100-A201;PFD-P202-A201;PFD-P300-A201;PFD-P201-A201;PFD-P901-A201; PFD-P105-A201;PFD-P110-A201PFD-P100-A201;PFD-P300-A201;PFD-P900-A201; PFD-P105-A201;PFD-P110-A201PFD-P100-A202; PFD-P105-A202;PFD-P110-A202PFD-P100-A204;PFD-P300-A203; PFD-P105-A203;PFD-P110-A203PFD-P100-A202;PFD-P303-A202; PFD-P105-A202;PFD-P110-A202PFD-P100-A202; PFD-P105-A202;PFD-P110-A202PFD-P100-A204;PFD-P202-A203;PFD-P300-A203;PFD-P201-A203;PFD-P900-A202;PFD-P901-A202; PFD-P105-A203;PFD-P110-A203PFD-P100-A204;PFD-P300-A203; PFD-P105-A203;PFD-P110-A203PFD-P100-A202;PFD-P300-A202; PFD-P105-A202;PFD-P110-A202PFD-P100-A301;PFD-P202-A301;PFD-P300-A301;PFD-P201-A301; PFD-P105-A301;PFD-P110-A301PFD-P100-A302;PFD-P202-A302;PFD-P300-A302;PFD-P201-A302; PFD-P105-A302;PFD-P110-A302PFD-P105-A302;PFD-P110-A302PFD-P100-A501;PFD-P301-A501;PFD-P300-A501;PFD-P202-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A504;PFD-P301-A501;PFD-P300-A501;PFD-P202-A504;PFD-P201-A504;PFD-P303-A501; PFD-P105-A504;PFD-P110-A504PFD-P100-A505;PFD-P301-A601;PFD-P300-A601;PFD-P302-A601;PFD-P303-A505; PFD-P105-A505;PFD-P110-A505PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A602;PFD-P303-A602; PFD-P105-A602;PFD-P110-A602PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P303-A701; PFD-P105-A701;PFD-P110-A701

Page 93: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P900-A701;PFD-P303-A701;PFD-P901-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P900-A701;PFD-P303-A701;PFD-P901-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P900-A701;PFD-P901-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P303-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P900-A701;PFD-P303-A701;PFD-P901-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701; PFD-P105-A701;PFD-P110-A701PFD-P105-A701; PFD-P110-A701PFD-P105-A701; PFD-P110-A701PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A804;PFD-P301-A804;PFD-P202-A804;PFD-P300-A804;PFD-P201-A804;PFD-P302-A804;PFD-P900-A804;PFD-P303-A804;PFD-P901-A804; PFD-P105-A804; PFD-P110-A804PFD-P100-A202;PFD-P303-A202; PFD-P105-A901; PFD-P110-A901PFD-P100-A901;PFD-P301-A901;PFD-P202-A901;PFD-P300-A901;PFD-P201-A901;PFD-P302-A901;PFD-P900-A901;PFD-P303-A901;PFD-P901-A901; PFD-P105-A901; PFD-P110-A901PFD-P100-A505;PFD-P303-A505; PFD-P105-A901; PFD-P110-A901PFD-P100-A902;PFD-P301-A902;PFD-P202-A902;PFD-P300-A902;PFD-P201-A902;PFD-P302-A902;PFD-P900-A902;PFD-P303-A902;PFD-P901-A902; PFD-P105-A902; PFD-P110-A902

PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-CHEM;PFD-P202-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

Page 94: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

PFD-P100-A302;PFD-P202-A302;PFD-P300-A302;PFD-P201-A302;PFD-P303-A302; PFD-P105-A302;PFD-P110-A302

PFD-P100-A505;PFD-P301-A601;PFD-P300-A601;PFD-P302-A601;PFD-P310-A601;PFD-P303-A505; PFD-P105-A505;PFD-P110-A505PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A603PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P303-A701; PFD-P105-A701;PFD-P110-A701

PFD-P100-A204;PFD-P202-A203;PFD-P300-A203;PFD-P201-A203;PFD-P900-A202;PFD-P901-A202; PFD-P105-A203;PFD-P110-A203PFD-P100-A505;PFD-P301-A601;PFD-P300-A601;PFD-P302-A601;PFD-P303-A505; PFD-P105-A505;PFD-P110-A505PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602

PFD-P100-A501;PFD-P202-A501;PFD-P301-A501;PFD-P300-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-A302;PFD-P202-A302;PFD-P300-A302;PFD-P201-A302;PFD-P900-A301;PFD-P901-A301; PFD-P105-A302;PFD-P110-A302

Page 95: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

PFD-P100-A501;PFD-P301-A501;PFD-P202-A501;PFD-P300-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A501;PFD-P301-A501;PFD-P202-A501;PFD-P300-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A501;PFD-P301-A501;PFD-P202-A501;PFD-P300-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A801;PFD-P301-A801;PFD-P900-A801;PFD-P303-A801;PFD-P901-A801; PFD-P105-A801; PFD-P110-A801PFD-P100-A802;PFD-P301-A802;PFD-P202-A802;PFD-P300-A802;PFD-P201-A802;PFD-P302-A802;PFD-P900-A802;PFD-P303-A802;PFD-P901-A802; PFD-P105-A802; PFD-P110-A802

PFD-P100-A503;PFD-P301-A503;PFD-P202-A503;PFD-P300-A503;PFD-P201-A503;PFD-P302-A503;PFD-P303-A503; PFD-P105-A503;PFD-P110-A503PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A802;PFD-P301-A802;PFD-P202-A802;PFD-P300-A802;PFD-P201-A802;PFD-P302-A802;PFD-P900-A802;PFD-P303-A802;PFD-P901-A802; PFD-P105-A802; PFD-P110-A802PFD-P100-A801;PFD-P301-A802;PFD-P202-A802;PFD-P201-A802;PFD-P302-A802;PFD-P900-A801;PFD-P303-A802;PFD-P901-A801; PFD-P105-A801; PFD-P110-A801PFD-P100-A802;PFD-P301-A802;PFD-P202-A802;PFD-P300-A802;PFD-P201-A802;PFD-P302-A802;PFD-P900-A802;PFD-P303-A802;PFD-P901-A802; PFD-P105-A802; PFD-P110-A802PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A804;PFD-P301-A804;PFD-P202-A804;PFD-P300-A804;PFD-P201-A804;PFD-P302-A804;PFD-P900-A804;PFD-P303-A804;PFD-P901-A804; PFD-P105-A804; PFD-P110-A804PFD-P100-A804;PFD-P301-A804;PFD-P202-A804;PFD-P300-A804;PFD-P201-A804;PFD-P302-A804;PFD-P900-A804;PFD-P303-A804;PFD-P901-A804; PFD-P105-A804; PFD-P110-A804PFD-P100-A804;PFD-P301-A804;PFD-P202-A804;PFD-P300-A804;PFD-P201-A804;PFD-P302-A804;PFD-P900-A804;PFD-P303-A804;PFD-P901-A804; PFD-P105-A804; PFD-P110-A804PFD-P100-A901;PFD-P301-A901;PFD-P202-A901;PFD-P300-A901;PFD-P201-A901;PFD-P302-A901;PFD-P900-A901;PFD-P303-A901;PFD-P901-A901; PFD-P105-A901; PFD-P110-A901

PFD-P100-A903;PFD-P301-A903;PFD-P202-A903;PFD-P300-A903;PFD-P201-A903;PFD-P302-A903;PFD-P900-A903;PFD-P303-A903;PFD-P901-A903; PFD-P105-A903; PFD-P110-A903PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-A201;PFD-P202-A201;PFD-P300-A201;PFD-P201-A201;PFD-P901-A201; PFD-P105-A201;PFD-P110-A201

PFD-P100-A204;PFD-P202-A203;PFD-P300-A203;PFD-P201-A203;PFD-P900-A202;PFD-P901-A202; PFD-P105-A203;PFD-P110-A203

Page 96: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

PFD-P100-A501;PFD-P301-A501;PFD-P202-A501;PFD-P300-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A501;PFD-P301-A501;PFD-P202-A501;PFD-P300-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A504;PFD-P301-A504;PFD-P202-A504;PFD-P300-A504;PFD-P201-A504;PFD-P302-A504;PFD-P303-A504; PFD-P105-A504;PFD-P110-A504PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A504;PFD-P303-A504; PFD-P105-A502;PFD-P110-A502

PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P303-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P900-A701;PFD-P303-A701;PFD-P901-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P900-A701;PFD-P303-A701;PFD-P901-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P303-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P900-A701;PFD-P303-A701;PFD-P901-A701; PFD-P105-A701;PFD-P110-A701

PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A802;PFD-P301-A802;PFD-P202-A802;PFD-P300-A802;PFD-P201-A802;PFD-P302-A802;PFD-P900-A802;PFD-P303-A802;PFD-P901-A802; PFD-P105-A802; PFD-P110-A802PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A804;PFD-P301-A804;PFD-P202-A804;PFD-P300-A804;PFD-P201-A804;PFD-P302-A804;PFD-P900-A804;PFD-P303-A804;PFD-P901-A804; PFD-P105-A804; PFD-P110-A804PFD-P100-A901;PFD-P301-A901;PFD-P202-A901;PFD-P300-A901;PFD-P201-A901;PFD-P302-A901;PFD-P900-A901;PFD-P303-A901;PFD-P901-A901; PFD-P105-A901; PFD-P110-A901PFD-P100-A902;PFD-P301-A902;PFD-P202-A902;PFD-P300-A902;PFD-P201-A902;PFD-P302-A902;PFD-P900-A902;PFD-P303-A902;PFD-P901-A902; PFD-P105-A902; PFD-P110-A902PFD-P100-A902;PFD-P301-A902;PFD-P202-A902;PFD-P300-A902;PFD-P201-A902;PFD-P302-A902;PFD-P900-A902;PFD-P303-A902;PFD-P901-A902; PFD-P105-A902; PFD-P110-A902PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEMPFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEMPFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P600-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

Page 97: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

PFD-P100-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-A204;PFD-P202-A203;PFD-P300-A203;PFD-P201-A203;PFD-P900-A202;PFD-P901-A202; PFD-P105-A203;PFD-P110-A203

PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A603; PFD-P105-A601;PFD-P110-A601PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602

PFD-P100-CHEM;PFD-P202-CHEM;PFD-P303-CHEM;PFD-P900-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM; PFD-P600-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEMPFD-P100-A901;PFD-P301-A901;PFD-P202-A901;PFD-P300-A901;PFD-P201-A901;PFD-P302-A901;PFD-P900-A901;PFD-P303-A901;PFD-P901-A901; PFD-P105-A901; PFD-P110-A901

PFD-P100-A201;PFD-P202-A201;PFD-P300-A201;PFD-P201-A201;PFD-P901-A201; PFD-P105-A201;PFD-P110-A201

PFD-P100-A204;PFD-P202-A203;PFD-P300-A203;PFD-P201-A203;PFD-P900-A202;PFD-P901-A202; PFD-P105-A203;PFD-P110-A203

PFD-P100-A501;PFD-P301-A501;PFD-P300-A501;PFD-P202-A501;PFD-P201-A501;PFD-P302-A501;PFD-P303-A501; PFD-P105-A501;PFD-P110-A501PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A502;PFD-P301-A502;PFD-P202-A502;PFD-P300-A502;PFD-P201-A502;PFD-P302-A502;PFD-P303-A502; PFD-P105-A502;PFD-P110-A502PFD-P100-A504;PFD-P301-A501;PFD-P300-A501;PFD-P202-A504;PFD-P201-A504;PFD-P303-A501; PFD-P105-A504;PFD-P110-A504PFD-P100-A505;PFD-P301-A601;PFD-P300-A601;PFD-P302-A601;PFD-P303-A505; PFD-P105-A505;PFD-P110-A505PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A601;PFD-P301-A602;PFD-P202-A602;PFD-P300-A602;PFD-P201-A602;PFD-P302-A602;PFD-P303-A602; PFD-P105-A601;PFD-P110-A601PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A602;PFD-P303-A602; PFD-P105-A602;PFD-P110-A602PFD-P100-A602;PFD-P301-A603;PFD-P202-A603;PFD-P300-A603;PFD-P201-A603;PFD-P302-A603;PFD-P303-A603; PFD-P105-A602;PFD-P110-A602PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P303-A701; PFD-P105-A701;PFD-P110-A701

Page 98: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P900-A701;PFD-P303-A701;PFD-P901-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P900-A701;PFD-P303-A701;PFD-P901-A701; PFD-P105-A701;PFD-P110-A701

PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P303-A701; PFD-P105-A701;PFD-P110-A701PFD-P100-A701;PFD-P301-A701;PFD-P202-A701;PFD-P300-A701;PFD-P201-A701;PFD-P302-A701;PFD-P900-A701;PFD-P303-A701;PFD-P901-A701; PFD-P105-A701;PFD-P110-A701

PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A803;PFD-P301-A803;PFD-P202-A803;PFD-P300-A803;PFD-P201-A803;PFD-P302-A803;PFD-P900-A803;PFD-P303-A803;PFD-P901-A803; PFD-P105-A803; PFD-P110-A803PFD-P100-A804;PFD-P301-A804;PFD-P202-A804;PFD-P300-A804;PFD-P201-A804;PFD-P302-A804;PFD-P900-A804;PFD-P303-A804;PFD-P901-A804; PFD-P105-A804; PFD-P110-A804

PFD-P100-A901;PFD-P301-A901;PFD-P202-A901;PFD-P300-A901;PFD-P201-A901;PFD-P302-A901;PFD-P900-A901;PFD-P303-A901;PFD-P901-A901; PFD-P105-A901; PFD-P110-A901

PFD-P100-A902;PFD-P301-A902;PFD-P202-A902;PFD-P300-A902;PFD-P201-A902;PFD-P302-A902;PFD-P900-A902;PFD-P303-A902;PFD-P901-A902; PFD-P105-A902; PFD-P110-A902

PFD-P100-CHEM;PFD-P202-CHEM;PFD-P900-CHEM;PFD-P303-CHEM;PFD-P901-CHEM; PFD-P105-CHEM; PFD-P110-CHEM

Page 99: €¦ · XLS file · Web view · 2017-10-05Reslurrying Tank Agitator SS Hydrolyzate Cooler 304SS;CS Filtered Hydrolyzate ... 150 psig design pressure, 10 min residence time 424

Calculations for BOILECON fortran blockBOILECON calculates power output, operating and capital costs for Area 800 based on ratios from a rigorous sister modelPower used in Area 800 is subtracted from the work generated before reporting net work generated for use in Excel

Rigorous Model: I0302B

Work streams consumed (KW) Work streams generated (KW) Heat streams (MMKcal/hr) Steam flows (kg/hr) Area 800 Cost ($)WM801 0 WM811H 22294 QM803T 121.2226 812 185010 EQUIP TIC $38,288,734WM804 176 WM811I 6135 812B 14259 WM830 10 WM811L 1074 814 54765 664 WM832 10 WM811VL 15 814B 115990 514 WM834 10 815 74710 514 WP804 25 815A 14458 WP811 0.062 815C 2680 529 WP824 11.6 815E 158 499 WP826 720 860 26662 529 WP828 1.8 WP830 0.0228 Total Used 964.4848

Simplified Model: I0301CS

Work streams consumed Heat streams (MMKcal/hr) Area 800 CostWUSED 0.0000286427223966488 WHITRB 0.1205 QBOIL Heat Stream QM803 QSTMHI 5.4943E-03 BCOST 1.1371WCFAN Work Stream WCOMBFAN WMTRB 0.0529 QDUTY Heat Stream QM811 QSTM_M 5.4217E-03 CAPCST Parameter 4WLOSS 4% WLOTRB 0.4007 QMDMDH Heat Stream QRD502 QSTMLO 7.0039E-03WNET Parameter 8 WVLTRB 0.0949 QLDMDH Heat Stream QHXLOW QSTMVL 6.8053E-03

QVLDMD Heat Stream QVLOW QCOND 7.2144E-03Ratios of steam used/steam producedPMREC ###PLREC ###

Steam flows (kg/hr)STM215 Matl Stream 215STM216 Matl Stream 216

Latent heat (Kcal/kg)

Ratios of work generated/steam flow (KW/kg/hr)

Ratios of steam flows/heat content (kg/hr/cal/s)

G8
kibsen: 86 atm steam (Hi P) 510 C
G9
kibsen: 13 atm steam (Med P) 268 C to BFW HX
G10
kibsen: 13 atm steam (Med P) 268 C
G11
kibsen: 4.4 atm steam (Low P) 163.5 C
G12
kibsen: 4.4 atm steam (Low P) 163.5 C
G13
kibsen: 4.4 atm steam (Low P) 163.5 C to deaerator
G14
kibsen: 1.7 atm steam (Very Low P) 115.2 C
G15
kibsen: 0.1 atm (vacuum P) 46.1 C
G16
kibsen: 1.7 atm steam (Very Low P) 115.2 C
A22
kibsen: Work used in Area 800 divided by QM803T KW/cal/s
E22
kibsen: Total heat generated from combustion
G22
kibsen: Ratio of flow to heat (QM803T) in stream 812 (kg/hr/cal/s)
J22
kibsen: Ratio of Area 800 TIC to boiler heat ($/cal/s)
E23
kibsen: Calculated in BOILECON, passed out as QM811 - condensor duty to CW load summing block
G23
kibsen: Ratio of flow to heat in stream 814 (kg/hr/cal/s)
J23
kibsen: Calculated in BOILECON
A24
kibsen: Calculated
G24
kibsen: Ratio of flow to heat in stream 815 (kg/hr/cal/s)
A25
kibsen: Calculated in BOILECON
G25
kibsen: Ratio of flow to heat in stream 860 (kg/hr/cal/s)
G26
kibsen: Ratio of flow to heat in stream 815E (kg/hr/cal/s)
G28
kibsen: Ratio of med P steam 812B to steam produced, 812
G29
kibsen: Ratio of med P steam 815A to steam produced, 812

Recommended