H26R6ABC6360NspTotalSystemRHYKr7.xls

TRIAL VERSION

NSP-SYSTEM TOTAL SYMULATION

LICENCED NO. : RH-NSP0001 Mr.AAAAAA COPYRIGHT : RYUTA HANAO<exsample> TLC CEMENT PLANT : 6000 T/D MFC KILN

6360

5-stage NSP SYSTEM All link with each other.

NOTE: In this program, abbreviationsof SF, KV, FS, etc., do not meanspecified m MANUAL for 1-5mean only codes or datas on the program execution.

RAW MATERIAL GRINDING SYSTEM

APPLIED DESIGN : bb NO cyclone ba:two BF bb:one BF WITH cyclone ca:two BF cb:one BF

(note) Neglect the warning window of "Link to other file".

Operation: T/D 0a TOTAL GAS FLOW 0b MATERIAL FLOW

MANUAL for 1-5 1 NSP SYSTEM (5-stage)

2 CYCLON PRESSURE DROP (5-stage) 3 DUCT SPRAY & HEAT LOSS

4 AQC SYMULATION 5 SPRAY TOWER

6-1 RAW VERTICAL MILL 6-2 HGG CEMENT GRINDING SYSTEM

7-1 CEMENT BM ba 7-2 CEMENT BM bb 7-3 CEMENT BM ca 7-4 CEMENT BM cb

COAL GRINDING SYSTEM 7-5 PG VERTICAL MILL 8 COAL VERTICAL MILL

RAW MIX CALCULATION 9 RAW MATERIAL MIXTURE

CAPACITY & SPECIFICATION of MAIN MACHINARY 10 CAPACITY BALANCE

3/14/2002

8/8/2002

COPYRIGHT : RYUTA HANAO

RV-12

RV-13

0b MATERIAL FLOW

6-2 HGG

7-2 CEMENT BM bb 7-4 CEMENT BM cb 7-5 PG VERTICAL MILL

NO-PW

04/18/2023--document.xls

12 ABC CEMENT PLANT 6,360 T/D GAS FLOW34 B-maker B-maker 試算 ABC5 CAPACITY: 6,360 T/D COAL BF 3,700 3,040 3,800 3,833 Cement EP6 FUEL CONSUMPTION: 730,000 Kcal/clKg fan 3,700 3,800 ③ ④ Cement BF7 F W. SPRAY EP fan8 COAL FIRING: 100 % BF fan9 CALORIFIC VALUE: 6,200 Kcal/Kg F

10 K-line C-line % ST11 RATIO OF FUEL: 40 60 100 12 ⑤ C fan13 ⑱ ⑲ Leak K fan14 BF F ① ②15 Leak 16 ⑯ Leak17 CM18 ⑰ ⑥ ⑧ ' ⑧19 CY F EP20 ⑮21 NSP Leak ⑩ ⑪2223 ⑬ ⑫ FC W.SPRAY⑳ Leak24 F EP ⑦ RM25 ⑭2627 KILN Leak28 Keak RAW EP29 COOLER ⑨ OPERATION30 B-maker B-maker 試算 ABC STOP31 COOLER EP 315,000 314,764 315,000 370,000 698,640 Nm3/H ← VM fan32 fan 12,500 12,500 VM fan: 698,640 EP fan: 553,450 553,450 Nm3/H ← EP fan33 HGG34 34832 = 17980 1685235 H2O=4.7 % 323275 499319 609469 643214 176044 467170 47361436 B-maker OPERATION H2O=8.0 %NSP 280 323275 0 0 323275 502170 609469 656341 162043 502002 508446 254750 87143 166203738 HGG 1600 16852 94 94 100 99 94 315 230 3039 STOP 359122 405822.640 355620 40186541 280 15042 K-SP C-SP SP ST RM MAIN EP COOLER EP COOL MILL43 ① ② ③ ④ ⑤ ⑥ ⑦ ⑧ '⑧ ⑨ ⑩ ⑪ ⑫ ⑬ ⑭ ⑮ ⑯44 6360T/H 500211 50021145 87 8746 FLOW RATE Nm3/H 132700 206600 339300 339300 516300 593000 593000 177000 416000 416000 254700 254700 170400 84300 10000 47 TEMPERATU 'C 290 290 290 280 211 80 80 80 80 80 315 315 315 315 25 4849 359122 0 0 414421 516263 609500 658,260 101842 567546 567546 244157 244157 155898 88260 28935 50 　試算 291 0 0 281 243 84 80 87 87 87 328 328 318 308 30 5152 （朱記値） EFFERENCE -19822 0 0 -75121 37 -16500 -65260 75158 -151546 -151546 10543 10543 14502 -3960 -18935 53 RATIO 1.0584 1.0278 1.1101 1.3643 54 DUST g/Nm3 70 0 70 70 70 843 70 70 0.025 30 0.025 0.025 0.025 0 55 UNIT VOL. Nm3/clKg 0.531 0.862 1.357 1.357 2.065 2.372 0.708 1.664 1.664 1.019 1.019 0.682 0.337 0.040 56 1.355 57 58 6360T/H 405630 405630 59 150 150 60 FLOW RATE Nm3/H 132700 206600 339300 339300 374600 374600 374600 254700 254700 170400 84300 10000 61 TEMPERATU 'C 290 290 290 290 150 150 150 315 315 315 315 25 62 359122 417117 417117 417117 63 281 150 150 140 646566 DUST g/Nm3 70 70 70 70 62 62 0.025 30 0.025 0.025 0.025 0 67 UNIT VOL. Nm3/clKg 0.531 0.862 1.357 1.357 1.498 1.498 1.498 1.019 1.019 0.682 0.337 0.040

Vapor(8.0→6.3）

(概算）

ABC換算 (概算）


68697071

24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43


123

B-maker B-maker 試算 ABC 433,000 ***** 33,000 B 120,000 5

4,000 ***** 4,000 B 25,000 6900 1,000 7

4,000 4,000 89

10B-maker B-maker 試算 ABC 11

8,700 8,500 8,500 126,700 6,700 6,667 13

14EP: Nm3/H 15BF: m3/min 16fan: m3/min 17

18F 19

2021

Bm3/m mmAq 'C Nm3/H 2217,000 -1000 87 698,636 2312,000 -150 77 553,447 24

252627

B-maker B-maker 試算 ABC 28453,000 556,984 520,000 540,000 29400,000 401,865 440,000 420,000 30

17,000 16,500 3112,000 12,000 32

12,500 333435

111643 128843 142225 3637

80 72 3839

H2O=4.7% 原料 40(T/H) 相当 41

W.SPRAY 42⑰ ⑱ ⑲ ⑳ 43

6360T/H 11.903 6.8% 4420 45

94300 119000 119000 *** 46285 90 90 *** 47

48117195 128880 142283 0.000 6.3% 49

239 80 75 20 5051

-22895 -9880 -23283 521.1957 53

0.020 378 0.025 540.337 0.476 0.476 55

56575859

94300 119000 119000 60285 90 90 61

62636465

0.02 378 0.025 660.377 0.476 0.476 67


68697071

44 45 46 47 48


12 ABC CEMENT PLANT 6,360 T/D MATERIAL BALANCE345 300 10 3000 300 10 3000 300 14 4200 30067 8 CLAY HIGH SILICA9 COAL,LATERITE

10 ITB ITB ITB11 GRIZZLY V.FEEDER -80 90% <70 -80 90% <7012 -80 90% <70 L.S/IPP -25 90% <30 ADDITIVE13 1150 B.S -25 90% <3014 -80 90% <70 COAL15 2,525,391 ITB16 7,600 17 0 IMPACT SHIP UNLOADER1819 -1500 --> -350 90% -800 --> -80 90% -200 --> -25 90% 350 ave 216 20 950 300 300 sea 190 0.51521 3502223 V.SCREEN 603,012 3,576 24 2010 H L.S 7,600 239,900 25 1150 3000 H B.S 0 37 H26 0.67 =WR 11,176 1263 H27 4200 28 0.31 29 -350 -80 90%30 110031 2303 H TRRIPER TRRIPER32 3000 H33 0.77 =WR 300 300 350 35034 35035 1150 358 3381 ---- 760 153293637 8418 2010 12 113 905 25 51138 3.7 8.2 400 50 10.5 38 93940 H.SILICA LATERITE COAL L.S/IPP ADDITIVE41 2000 16000 8000 2500 3000 5000 1000 250042 1 2 2 2 2 2 1 243 2400 16000 8000 3400 4300 5100 1200 250044 0.54 5.11 47.9 1.0053 22.14546 RECLAIMER 406 RECLAIMER 91.2 RECLAIME 53.54748 500 150 20049505152 434 103 0.61 5.775354 LIMESTONE CLAY H.SILICA LATERITE55 500 200 150 13056 500 80 40 20 ITB57 500 80 40 20 A-maker58 500 150 4 2059 RAW MILL60 mm -80 90% --> 0.09 88% 61 4.7% --> 1% 62 500 6364 600065 567546 66 4250 412.5 1650 17000 (698,640Nm3/H)67 4 636068 50021169 600070 420,000 71 55 --> 0.02572 420000 150 359122 73 20000 560000 87 408939 7475 636076 35855477 (553,450Nm3/H) 12000 12500 4056307879 500 A-make 400000 A-mak 35920080 315 21 6615 453000 396600818283

RAW MATERIAL CRUSHING & GRINDING

D/Yx H/Dx H/YLIMESTONE QUARRY CLAY QUARRY CLAY QUARRY & YARD PROCUREMENT

LIMESTONE(L.S) GYPSUM, ADDITIVEBLACKSTONE(B.S) L.S, B.S

required size required size required sizeL.S H.SILICA GYPSUMB.S

T/H(WB) LATERITET/Y CLAY

L.SL.S/IPPB.S

P.CRUSHER ROLL CRUSHER ROLL CRUSHER ROLL Bucket(m3)mm mm

T/H(WB) qu'y T/H(WB) n=

T/Y T/YCLAY H.SILICA sea GYPSUM

ADDITIVET/H(WB) qu'y LATERITE

TOT sea COALTOT

S.CRUSHER IMPACT WR=--> mm

T/H(WB)STACKER

STACKER T/H(WB) T/H(WB)

T/H(WB)

T/D(WB)days

STORAGE YARD STORAGE Y. STORAGE YARDB.S L.S CLAY

T(WB) T(WB)NO. NO.

DUMP TRUCKPREPAIRED L.S CLAY COMMON

BY THE BUYER T/H(WB) T/H(WB) T/H(WB)

T/H(WB)RAW MILL BIN

T(WB)

CFW(T/H)

H2O HOT GAST/H GENERATOR

CYCLONE IDFm3/mNO. m3/m

SAMPLEREP GAS CONDITIONING

BLENDING g/Nm3 TSILO Nm3/Hx'C

T(WB) Nm3/Hx'C

SAMPLER IDFMETERING

DEVICE m3/m D/Yx H/Dx H/Y T/H


8485

3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24


MATERIAL BALANCE

16 4800

200-300COAL,LATERITE 5000-7000

ITB NO/M D/M-30 <30 1.06 1.72-25 90% <30 3.07 4.99-70 <70 0.68 1.1-15 <15 9.96 16.2

14.8 240.71 0.8

SHIP UNLOADER 3412 H4800 H

rated 420t7 60 420

52,800 153,290 229,935

33,810 498,181 738,081

TRRIPER

350

5280 49818

176 75638 10

GYPSUM COAL/IPP3500 4000 ITB

2 23800 5100 A-maker

6.98 30

RECLAIMER60.11

200

359122 281 408939 150

358554405630

359200396600

WR: Working Ratio

D/Yx H/Dx H/YROCUREMENT

DWT, ADDITIVE barge

shipequired size

14H=

WR=

6 & 8T/H(WB)

sec t/hratedT/Y

T/H(WB)

T/M(WB)

T/D(WB)days

T(WB)NO.

T/H(WB)

T/H(WB)COMMON

T/H(WB)

AS CONDITIONINGTOWER(GCT)

Nm3/Hx'CNm3/Hx'C


25 26 27 28 29 30


ABC CEMENT PLANT 6,360 T/D MATERIAL BALANCECLINKER BURNING CEMNT GRINDING

1-226-37

5000 PULVERIZED1.628 D COAL BIN

1.86 25 25

25315 18 5670

PREHEATER PRECALCINER110 110 18.721 T/H

730,000 60%T/D 6,360 6,360

KILN-15 --> 0.09 95% 40% 12.481

18 15% --> 1% T/D 6,360 7.816 45 T/H

SAMPLER 6360 2446073700 6000 244157 370000 350

COOLER EP3800 3800 315000 350

290 -> 0.025 g/Nm3 T/D 6,360 20 0.025 g/Nm3

SAMPLER

CLINKER SILO -30 90% UNBURNT SILO120 120 T 40000 2000 T

215

A-maker

168 24 8

6700 6700 300 200 150250 80 20 ITB250 80 20 A-maker

2008700 8700

33000

33000 95200 300 --> 0.025

N-3500

2000

2000 20002 2

orking Ratio COAL GRINDING

H/unload'g

DWT

T(WB)

D/Yx H/Dx H/Y T/H

RAW COAL BINT(WB) COAL:

Kcal/clKg FUEL RATIOHOT GAS

GENERATOR

COAL MILL DUAL BURNERmm FUEL RATIO COAL:H2O OIL:T/H

BAG FILTER m3/m IDF Nm3/Hx'C

m3/m -->

PULVERIZED SIZECOAL BIN

T(WB)NO.

T/H

T/HCEMENT MILL BIN

IDF CLINKER ADDITIVE GYPSUMTO IPP T(WB)

LIMESTONE,COAL m3/m CFW(T/H)OUT OF SCOPE

OF SUPPLYPREGRINDING MILL

PCB40IDF T/H

m3/m

CEMENT MILL EPPCB40

T/H

AIRSEPARATOR

BAG FILTER IDF m3/mm3/m

NO.

SAMPLER

SCREWPUMP

CF

CF


31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54


FDF550

m3/m

315

OIL BURNER 11.724

T/H

FDF200

m3/m

14500IDF

12500m3/m

TELESCOPIC

100 T/H

900

1000

315 22 6930

D/Yx H/Dx H/Y

OIL:

m3/Hx'C

CHUTE

Nm3/Hx'C IDF

g/Nm3 m3/m

D/Yx H/Dx H/Y


55 56 57 58 59 60


ABC CEMENT PLANT 6,360 T/D MATERIAL BALANCEOIL TANK

DIESEL OILWORKING HOURS

OIL TANK10 300 3000

1000 10 300 300014 300 4200

24 7560 RAW MILLING 21 315 6615RAW MEAL BLENDING 24 315 7560

TO IPP CLINKER BURNING 24 315 7560COAL MILLING 18 315 5670

OUT OF SCOPE CEMENT MILLING 22 315 6930OF SUPPLY CEMENT PACKING 16 300 4800

CEMENT SHIP LOADING 16 300 4800SERVICE TANK

1507

62009900

-80 90% 3 1.35 -80 90% 26 1.20 -25 90% 26 1.30

LATERITE -70 10 1.80 8.70

CLINKER -30 90% 0 1.40 GYPSUM -30 10 1.30

40 ADDITIVE -25 90% 5 1.60 1.06

CLINKER -30 90% 0 1.40 GYPSUM -30 10 1.30

30 ADDITIVE -25 90% 5 1.60 1.37

158 --> 157

78.9 1.01 30

T 150002 BLACKSTONE

600 34.8 0.54 5.11 22.1900

LIMESTON 157BLACKSTO

100 100 60.1 1.01 22.1 6.984 2

100 1001 5

53.5 0.54 5.11

300 16 4800 300 16 4800

CEMENT PACKING & SHIPPING

DEPARTMENT WORKING HOURESH/D D/Y H/Y

LIMESTONE CRUSHINGCLAY CRUSHING

D/Yx H/Dx H/Y m3 UNLOADING AT PIRE

DIESEL OIL

m3

RAW MATERIAL CONDITION & REQUIREMENT

COAL: Kcal/Kg LUMP MOISTURE BULKOIL: Kcal/Kg NAME OF MATERIAL SIZE CONTENT DENCITY

mm x % Max.%(WB) T/m3LIMESTONE

RAW COALCLAYMATERIAL H.SILICA

TOTALmm x % Max.%(WB) T/m9

PCB

CEMENT TOTAL

PCB

TOTAL

T/H

LIM COALEST

CEMENT SILO ONE

NO.

SHIP LOADER H.SILICA LATERITE ADDITIVE

CLINKER T/H T/HCEMENT T/H

ADDITIVE & COAL STRAGE YARD

H.SILICA

PACKER BAG SHIP LOADER from QUARRYT/H T/HNO.

LIM ADDITIVE GYPSUMESTONEBLACKSTONE

BULK LOADER BAG LOADER ADDITIVET/H CRUSHER H.SILICA LATERITENO.

T/H

D/Yx H/Dx H/Y D/Yx H/Dx H/Y

to RAW MILL


61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86


123456789

1011121314

2.26 1.326 1516.00 0.281 1616.00 0.002 17

7.00 0.017 184.70 1.626 19

2021

1.2961 220.2361 230.0014 240.0161 251.5497 26

27282930

T/clT(DB) 311.218 1.256 320.223 0.301 330.081 0.109 340.029 0.032 351.551 1.699 36

T/clT(DB) 370.840 0.840 380.040 0.044 390.120 0.126 401.000 1.011 410.780 0.780 420.040 0.044 430.180 0.189 441.000 1.014 45

464748

47.9 495051525354

BLACKSTONE 55565758

6.98 5960616263646566

30 67686970717273747576

47.9 77787980818283

Nor.%(WB) T/clT(WB)

AW MATERIAL CONDITION & REQUIREMENT

RAW MATERIALREQUIREMENT

T/clT(WB)

T/clT(WB)

COAL

DDITIVE GYPSUM

GYPSUMADDITIVECOALLATERITEfrom JETTY

COAL

COAL

to CEMENT MILL& IPP

to COAL MILL


8485

87 88 89 90###

1

2 MANUAL for NSP SYSTEM TOTAL SIMULATION34 (NOTE) Read the "(note) or comment" described in the each program's <DATAINPUT> table.56 (1) Order to execute NSP-SYSTEM TOTAL SIMULATION7 (2) (3) (4)8 5aqc → 5NSP-sys → 5cy-pd9

10 11 (2) 5aqc12 1. Input all DATA in AQC SIMULATION GAS BALANCE chart at O1:AD42.131415 Q11(=E6),Q12(=M39)Inlet capacity and temperature are given by 5NSP-sys:I6 and M17.16 RAW 26(=K39) Temperature is given by 5NSP-sys:E2117 Q5(=E18),T5(G18) Secondary and tertiary air are given by 5NSP-sys:AA65 and X44.18 If the link with E18&G18 and AA65&X44 cancelled and E18&G18 DATA input by hand,19 5aqc simulation can be executed separately from 5NSP-sys. 20 If 5aqc program goes wrong, try the above method and go to (3) NAP-sys.21 After finishing 5NSP-sys simulation, link with E18&G18 and AA65&X44.22 RAW 7 Number of chamber (min:5-max:7)23 RAW 30 Length of grate or chamber24 RAW 31 Width of grate25 See AA30, the value will become to 1.6-1.8.26 RAW 27 Gas volume at every chamber referring to RAW 33 and O43:X48 AIR LOAD27 See Y24, the value will become to 1.8-2.5.28 RAW 25 See equation in RAW 25, value in RAW 25 is input by equation in RAW 2529 RAW 55 ADJUSTMENT FACTOR OF HEAT TRANSFER FACTOR referring to O50:X5430 RAW 57 ADJUSTMENT FACTOR OF OUTPUT GAS TEMPERATURE referring to O58:X6231 ADJUSTMENT FACTOR has big differences depending on MAKER, TYPE and manufactured year.32 The vest way to get ADJUSTMENT FACTOR is to examine operational DATA of ARC using this33 program.34 Q20,21,22 Number of grate stroke of each grate stage (max:20)35 See RAW 28, the value will become to 0.80-0.25 after program running.3637 X4,Y4 No relation with program38 AA10 No relation with program39 V11:Z11 No relation with program40 T10 No relation with program41 AA36:AB40 No relation with program4243 All input DATA, required for simulation, are transferred to ARC SIMULATION PROGRAM B5:M45.4445 2. Check the all DATA.46 3. Click RUN button.47 Gas volume of secondary, tertiary and exhaust becomes near48 to the target value of 0.3, 0.5 and 1.0-1.5 , and gas temperature49 of secondary, tertiary and exhaust becomes near to the value 50 of TEMPERATURE in Y43:AC48, then go to (3) 5NSP-sys. 51

52 Temperature of CLINKER, COOLING GAS, PRESSURE DROP are shown in CLINKER COOLING CURVE53 graph.54 4. OUTPUTDATA of the simulation55 AQC SIMULARC SIMULATION PROGRAM56 CLINKER COOLING CURVE graph57 CLINKER TEMPERATURE AND GAS TEMPERATURE table5859 (3) 5NSP-sys60 1. Input all DATA in GAS BALANCE OF NSP SYSTEM <DATAINPUT> chart at B5:O45.6162 I2 Base capacity (T/D) It is benchmark capacity against I6 of actual capacity.63 I5 Type of NSP system (SF, KSV, MFC)64 H6,I6 Number of string and actual capacity (T/D)65 RAW 8 Composition of CLINKER66 This program introduces the composition from rawMIX S36:AG36 of RAW MATERIAL MIXTURE67 CALCULATION result.68 The composition can be input by hand, if the link with RAW 8 and rawMIX S36:AG36 is69 canceled.70 E11 Input decarbonation ratio, so as E9 becomes to 60% of NSP fuel firing ratio.71 H11:M11 Dust load 72 E14,F14 Approximate O2 composition in NSP outlet and kiln outlet73 Input approximate O2 value in E4, so as E12 becomes to the target O2 composition of about 2-3%.74 H14,I14 H2O content and temperature of raw material (raw meal)75 M14,N14 ALKALI LOSS in raw material and alkali bypass loss in NSP system76 K14 Normally K14=1.0 Theoretical clinker burning heat value can be changed by the K14 value.7778 E17:M17 Temperature of raw material decomposition, raw material and clinker in kiln79 E21,F21 Ambient temperature and humidity80 H21,I21 Gas temperature of NSP top cyclone outlet and kiln inlet81 Gas temperature of NSP top cyclone outlet is determined by trial calculation of 82 composition of 2-3% and fuel consumption value in M16 becomes no change.83 The method of trial calculation is mentioned hereinafter.84 N17,L21:N21,E24 Gas temperature of AQC The temperatures link with 5aqc output DATA.85 If the link with 5aqc DATA cancelled and the temperatures input by hand,86 5NSP-sys simulation can be executed separately from 5aqc program. 87 If 5NSP-sys program goes wrong, try the above input method.88 After finishing 5NSP-sys simulation, link with 5aqc program.89 H24 See equation in H24. The H24 value comes from I6/24.90 I62:I66 Original capacity (T/D) due to NSP cyclone standard size for HEAT LOSS calculation91 K24:N24 Input HEAT LOSS in NSP system in B61:O67. Output DATA of L62:L65 goes to K24:N24.92 I24,J24 H25,J25 No relation with program93 Kiln diameter and length Kiln unit load and kiln volume94 E25 Name of fuel95 F28:I28 High and low calorific value of fuel, specific heat value and temperature of fuel96 K28,L28 Volume % to theoretical combustion air and temperature of primary air97 M28,N28 Theoretical combustion air and combustion gas 9899 RAW 31 No relation with program

100101 High and low calorific value of fuel and theoretical combustion air and combustion gas, 102 calculated from the composition, are shown in F29&G29 and M29&N29 for reference of

Composition of fuel

103 K28&L28 and M28&N29.104 RAW 34 No relation with program105 CLINKER MODULUS and MINERAL COMPOSITION calculated from CLINKER COMPOSITION106 107108 2. Check the all DATA.109 3. Execute simulation.110 5NSP-sys and 5aqc are linked with each other.111 1) Move on TEMPERATURE BALANCE OF NSP-CYCLONE SYSTEM at Q115:AG141. 112 Input gas temperature of each cyclone inlet at AB123:AB127, so as to balance the input and output heat113 value of each cyclone.114 First, input AB127 and click RUN button so as to become ABS(X129) < 0-0.5.115 Next, input AB126 and click RUN button so as to become ABS(X126) < 0-3.116 Next, input AB125 and click RUN button so as to become ABS(X125) < 0-1.117 Next, input AB124 and click RUN button so as to become ABS(X124) < 0-1.118 Last, input AB123 and click RUN button so as to become ABS(X123) < 0-1.119 Temperature of AB123 is the gas temperature of NSP top cyclone inlet, AB123 is equal to top cyclone120 outlet in this program.121 2) Move on HEAT BALANCE OF NSP SYSTEM <DATAINPUT> chart. 122 Change E14 and repeat a few click RUN <--> RUN by turns so as E12 becomes to the target O2 ② ①123 composition of 2-3% and fuel consumption value in M6 becomes no change.124 Change E11 and repeat a few click RUN <--> RUN by turns so as E9 becomes to the target fuel ② ①125 firing ratio of 60% and fuel consumption value in M6 becomes no change.126 3) Move on TEMPERATURE BALANCE OF NSP-CYCLONE SYSTEM in Q115:AG141. 127 See X123:X127. If the balance becomes out of the above descried tolerance, adjust the balance like 128 the mentioned procedure in 1).129 4) Move on HEAT BALANCE OF NSP SYSTEM <DATAINPUT> chart. 130 Repeat a few click RUN <--> RUN by turns. ② ①131 Stop the simulation, if the value of E12,E14 and M6 occur no change. 132 4. End the simulation of HEAT BALANCE OF NSP SYSTEM.133134 5. OUTPUTDATA of the simulation135 MATERIAL BALANCE chart136 GAS BALANCE chart137 MATERIAL BALANCE and COMPOSITION OF EXHAUST GAS table138 TEMPERATURE BALANCE OF NSP-CYCLONE SYSTEM table139 HEAT BALANCE table THEORETICAL HEAT VALUE OF CLINKER BURNING140 NSP HEAT BALANCE141 KILN HEAT BALANCE142 AQC HEAT BALANCE143 TOTAL HEAT BALANCE144 TOTAL BALANCE OF NSP SYSTEM chart145146147 (4) 5cy-pd148 1. Input basic DATA in 5NSP-sys (CY or DUCT area) table at B68:O73 for calculation of cyclone and duct pressure drop. 149 RAW 70 Diameter (main dimension) of equipment150 H73 Cyclone size will be changed or not by capacity increase (T/H). 0:no change 1:auto change151152 2. Input all DATA in PRESSURE DROP OF NSP-CYCLONE SYSTEM <DATAINPUT> chart at B5:O52.153

154 G17:G19 Initial setting pressure drop (PD) It depends on PLANT MAKER and Type of NAP. 155 K19,K29 PD factor for cyclone and duct Check the factor from actual operation. 156 G29 Duct size up factor Duct size can be changed freely in case of capacity increase to reduce pressure157 drop.158 RAW 8 : RAW 25 All DATA excluding above comes from 5NSP-sys.159 RAW 21 Efficiency of cyclone comes from RAW 39. Therefore the efficiency can be changed according to 160 actual efficiency.161 RAW 26 H26=H18+F18, I26=V21, J26=V16, K26=V12, L26=V7162 RAW 28 : RAW 37 Cyclone and duct size come from (INPUT of DIMENSION) B55:O65.163 C59 Capacity of model NSP cyclone (T/H) It comes from 5NSP-sys (CY or DUCT area) B68:O73 table.164 RAW 57 : RAW 65 Reefing to NSP TYPE:M8 and capacity:C59, the dimension comes from (INPUT of DIMENSION) table B78:o121165 automatically. If actual capacity is bigger than capacity:C59, the dimension will increase according to166 INCREASE ratio of RAW 73. 167 RAW 67, RAW 69 Section area of original dimension and modified dimension168 These come from 5NSP-sys (CY or DUCT area) B68:O73 table.169 RAW 72, RAW 73 Ratio of original and modified dimension Equation of INCREASE latio is shown in H73:L73.170171 3. Check the all DATA.172 4. Execute simulation.173 Click RUN button several times, so as top cyclone pressure U6 occurs no change.174 Because cyclone input pressure I26:L26 refer to output DATA of simulation.175176 5. OUTPUTDATA of the simulation177 PRESSURE DROP OF NSP CYCLONE chart178 GAS SPEED OF NSP CYCLONE table179180 (5) TOTAL BALANCE OF NSP SYSTEM181 Move to 5NSP-sys TOTAL BALANCE OF NSP SYSTEM chart at Q144:AG202.182 This chart shows TOTAL BALANCE OF NSP SYSTEM including NSP, KILN and AQC.183 1. IDF inlet temperature184 X190 Heat loss % in duct = about 4%185 V190 IDF input temperature186 Change the value of V190, so as water spray S161 and S163 become to nearly zero(0). The value of V190187 is the IDF inlet temperature. GAS BALANCE OF DUCT SPRAY in 5spray program is used for the temperature188 calculation.189 2. IDF outlet temperature190 S183 IDF outlet temperature191 3. IDF specification192 W192 Design temperature of IDF inlet193 X192 Design allowance of IDF suction volume 194 Y192 Design allowance of IDF suction pressure 195 T194,V194 Fan and motor efficiency196 S194,W194 Theoretical fan power and necessary motor power at 50% gas volume197 Y194,X194 Rated motor power at 50% gas volume and afford of motor198 R196:Z199 Calculation of IDF for MFC199200 4. Other DATA Other DATA comes from 5NSP-sys, 5cy-pd, 5spray and 5aqc.201202 (6) 5spTower203 1. Input all DATA in GAS BALANCE OF SPRAY TOWER <DATAINPUT> chart at B5:M32.204 Almost DATA comes from 5NSP-sys.

205 F6 Standard temperature for heat balance206 K6 Afford of gas volume Input 1.100 in K6 in case gas volume increases 110%.207 RAW 11 Inlet condition of gas volume, dust, gas temperature and leak air208 RAW 12 Outlet condition of gas volume, dust, gas temperature and leak air209 J13 Temperature drop between IDF outlet and spray tower inlet210 E15 Source of gas ( NSP-oil or NSP-coal )211 F17,K17 Leak air % against inlet hot gas and heat loss %212 F20 Heat transfer factor213 I20 Gas speed in tower214 L20 Diameter of spray droplet215 The reference diameter is shown at <DATAINPUT> B25:B27. The diameter differs significantly216 due to type of nozzle system (water only or water + air).217218 2. Check the all DATA.219 3. Execute simulation.220 Move to GAS BALANCE OF SPRAY TOWER chart at O1:AD42.221 1) Diameter of spray tower222 Input gas speed in T22 referring to <DATAINPUT> B25:B27, so as T25 diameter becomes 223 the targeted diameter224 2) Heat transfer factor225 Input heat transfer factor in AB22 referring to <DATAINPUT> B25:B27, so as AB21 EVAPORATION226 TIME ratio becomes more than 130%.227228 The size of spray tower is determined by suitable combination of gas speed, heat transfer factor and 229 diameter of droplet.230231 4. OUTPUTDATA of the simulation232 GAS BALANCE OF SPRAY TOWER chart233 HEAT BALANCE OF SPRAY TOWER table234235

3 4 4 5 5 6

MANUAL for NSP SYSTEM TOTAL SIMULATION

Read the "(note) or comment" described in the each program's <DATAINPUT> table.

(5) (6)→ TOTAL BALANCE OF NSP SYST → 5spTower

↓↑5spray

Input all DATA in AQC SIMULATION GAS BALANCE chart at O1:AD42.

Inlet capacity and temperature are given by 5NSP-sys:I6 and M17.Temperature is given by 5NSP-sys:E21Secondary and tertiary air are given by 5NSP-sys:AA65 and X44.If the link with E18&G18 and AA65&X44 cancelled and E18&G18 DATA input by hand,5aqc simulation can be executed separately from 5NSP-sys. If 5aqc program goes wrong, try the above method and go to (3) NAP-sys.After finishing 5NSP-sys simulation, link with E18&G18 and AA65&X44.Number of chamber (min:5-max:7)

See AA30, the value will become to 1.6-1.8.Gas volume at every chamber referring to RAW 33 and O43:X48 AIR LOADSee Y24, the value will become to 1.8-2.5.See equation in RAW 25, value in RAW 25 is input by equation in RAW 25ADJUSTMENT FACTOR OF HEAT TRANSFER FACTOR referring to O50:X54ADJUSTMENT FACTOR OF OUTPUT GAS TEMPERATURE referring to O58:X62ADJUSTMENT FACTOR has big differences depending on MAKER, TYPE and manufactured year.The vest way to get ADJUSTMENT FACTOR is to examine operational DATA of ARC using this

Number of grate stroke of each grate stage (max:20)See RAW 28, the value will become to 0.80-0.25 after program running.

Preset pressure drop in exhaust duct for EP fan Power calculationDesign temperature for EP fan Power calculationDesign allowance for EP fan Power calculationFan PowerDesign allowance for cooling fan Power calculation

All input DATA, required for simulation, are transferred to ARC SIMULATION PROGRAM B5:M45.

Gas volume of secondary, tertiary and exhaust becomes nearto the target value of 0.3, 0.5 and 1.0-1.5 , and gas temperatureof secondary, tertiary and exhaust becomes near to the value of TEMPERATURE in Y43:AC48, then go to (3) 5NSP-sys.

Temperature of CLINKER, COOLING GAS, PRESSURE DROP are shown in CLINKER COOLING CURVE

ARC SIMULATION PROGRAMCLINKER COOLING CURVE graphCLINKER TEMPERATURE AND GAS TEMPERATURE table

Input all DATA in GAS BALANCE OF NSP SYSTEM <DATAINPUT> chart at B5:O45.

Base capacity (T/D) It is benchmark capacity against I6 of actual capacity.Type of NSP system (SF, KSV, MFC)Number of string and actual capacity (T/D)

This program introduces the composition from rawMIX S36:AG36 of RAW MATERIAL MIXTURE

The composition can be input by hand, if the link with RAW 8 and rawMIX S36:AG36 is

Input decarbonation ratio, so as E9 becomes to 60% of NSP fuel firing ratio.

Approximate O2 composition in NSP outlet and kiln outletInput approximate O2 value in E4, so as E12 becomes to the target O2 composition of about 2-3%.H2O content and temperature of raw material (raw meal)ALKALI LOSS in raw material and alkali bypass loss in NSP system

Theoretical clinker burning heat value can be changed by the K14 value.

Temperature of raw material decomposition, raw material and clinker in kilnAmbient temperature and humidityGas temperature of NSP top cyclone outlet and kiln inletGas temperature of NSP top cyclone outlet is determined by trial calculation of composition of 2-3% and fuel consumption value in M16 becomes no change.The method of trial calculation is mentioned hereinafter.Gas temperature of AQC The temperatures link with 5aqc output DATA.If the link with 5aqc DATA cancelled and the temperatures input by hand,5NSP-sys simulation can be executed separately from 5aqc program. If 5NSP-sys program goes wrong, try the above input method.After finishing 5NSP-sys simulation, link with 5aqc program.See equation in H24. The H24 value comes from I6/24.Original capacity (T/D) due to NSP cyclone standard size for HEAT LOSS calculationInput HEAT LOSS in NSP system in B61:O67. Output DATA of L62:L65 goes to K24:N24.

Kiln diameter and length Kiln unit load and kiln volume

High and low calorific value of fuel, specific heat value and temperature of fuelVolume % to theoretical combustion air and temperature of primary airTheoretical combustion air and combustion gas

High and low calorific value of fuel and theoretical combustion air and combustion gas, calculated from the composition, are shown in F29&G29 and M29&N29 for reference of

CLINKER MODULUS and MINERAL COMPOSITION calculated from CLINKER COMPOSITION

5NSP-sys and 5aqc are linked with each other.Move on TEMPERATURE BALANCE OF NSP-CYCLONE SYSTEM at Q115:AG141.

Input gas temperature of each cyclone inlet at AB123:AB127, so as to balance the input and output heat

First, input AB127 and click RUN button so as to become ABS(X129) < 0-0.5.Next, input AB126 and click RUN button so as to become ABS(X126) < 0-3.Next, input AB125 and click RUN button so as to become ABS(X125) < 0-1.Next, input AB124 and click RUN button so as to become ABS(X124) < 0-1.Last, input AB123 and click RUN button so as to become ABS(X123) < 0-1.

Temperature of AB123 is the gas temperature of NSP top cyclone inlet, AB123 is equal to top cyclone

Move on HEAT BALANCE OF NSP SYSTEM <DATAINPUT> chart. Change E14 and repeat a few click RUN <--> RUN by turns so as E12 becomes to the target O2 ② ①composition of 2-3% and fuel consumption value in M6 becomes no change.Change E11 and repeat a few click RUN <--> RUN by turns so as E9 becomes to the target fuel ② ①firing ratio of 60% and fuel consumption value in M6 becomes no change.

Move on TEMPERATURE BALANCE OF NSP-CYCLONE SYSTEM in Q115:AG141. If the balance becomes out of the above descried tolerance, adjust the balance like

Move on HEAT BALANCE OF NSP SYSTEM <DATAINPUT> chart. Repeat a few click RUN <--> RUN by turns. ② ①Stop the simulation, if the value of E12,E14 and M6 occur no change.

End the simulation of HEAT BALANCE OF NSP SYSTEM.

MATERIAL BALANCE and COMPOSITION OF EXHAUST GAS tableTEMPERATURE BALANCE OF NSP-CYCLONE SYSTEM table

THEORETICAL HEAT VALUE OF CLINKER BURNINGNSP HEAT BALANCEKILN HEAT BALANCEAQC HEAT BALANCETOTAL HEAT BALANCE

Input basic DATA in 5NSP-sys (CY or DUCT area) table at B68:O73 for calculation of cyclone and duct pressure drop. Diameter (main dimension) of equipmentCyclone size will be changed or not by capacity increase (T/H). 0:no change 1:auto change

Input all DATA in PRESSURE DROP OF NSP-CYCLONE SYSTEM <DATAINPUT> chart at B5:O52.

Initial setting pressure drop (PD) It depends on PLANT MAKER and Type of NAP. PD factor for cyclone and duct Check the factor from actual operation. Duct size up factor Duct size can be changed freely in case of capacity increase to reduce pressure

All DATA excluding above comes from 5NSP-sys.Efficiency of cyclone comes from RAW 39. Therefore the efficiency can be changed according to

H26=H18+F18, I26=V21, J26=V16, K26=V12, L26=V7Cyclone and duct size come from (INPUT of DIMENSION) B55:O65.Capacity of model NSP cyclone (T/H) It comes from 5NSP-sys (CY or DUCT area) B68:O73 table.Reefing to NSP TYPE:M8 and capacity:C59, the dimension comes from (INPUT of DIMENSION) table B78:o121automatically. If actual capacity is bigger than capacity:C59, the dimension will increase according to

Section area of original dimension and modified dimensionThese come from 5NSP-sys (CY or DUCT area) B68:O73 table.Ratio of original and modified dimension Equation of INCREASE latio is shown in H73:L73.

Click RUN button several times, so as top cyclone pressure U6 occurs no change.Because cyclone input pressure I26:L26 refer to output DATA of simulation.

PRESSURE DROP OF NSP CYCLONE chartGAS SPEED OF NSP CYCLONE table

Move to 5NSP-sys TOTAL BALANCE OF NSP SYSTEM chart at Q144:AG202.This chart shows TOTAL BALANCE OF NSP SYSTEM including NSP, KILN and AQC.

Change the value of V190, so as water spray S161 and S163 become to nearly zero(0). The value of V190is the IDF inlet temperature. GAS BALANCE OF DUCT SPRAY in 5spray program is used for the temperature

See equation in S183.

Design allowance of IDF suction volume The design gas volume of 50% is shown in S192.Design allowance of IDF suction pressure The design pressure is shown in T192.

Theoretical fan power and necessary motor power at 50% gas volumeRated motor power at 50% gas volume and afford of motor

Other DATA comes from 5NSP-sys, 5cy-pd, 5spray and 5aqc. See equation in each cell.

Input all DATA in GAS BALANCE OF SPRAY TOWER <DATAINPUT> chart at B5:M32.Almost DATA comes from 5NSP-sys.

Standard temperature for heat balanceAfford of gas volume Input 1.100 in K6 in case gas volume increases 110%.Inlet condition of gas volume, dust, gas temperature and leak airOutlet condition of gas volume, dust, gas temperature and leak airTemperature drop between IDF outlet and spray tower inlet

( NSP-oil or NSP-coal )Leak air % against inlet hot gas and heat loss %

←Input at T22.←Input at AB22.

The reference diameter is shown at <DATAINPUT> B25:B27. The diameter differs significantlydue to type of nozzle system (water only or water + air).

Move to GAS BALANCE OF SPRAY TOWER chart at O1:AD42.

Input gas speed in T22 referring to <DATAINPUT> B25:B27, so as T25 diameter becomes

Input heat transfer factor in AB22 referring to <DATAINPUT> B25:B27, so as AB21 EVAPORATIONTIME ratio becomes more than 130%.

The size of spray tower is determined by suitable combination of gas speed, heat transfer factor and

GAS BALANCE OF SPRAY TOWER chartHEAT BALANCE OF SPRAY TOWER table

6 7 7 8 8 9 9

1

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101112131415161718192021222324252627282930313233343536373839404142434445464748495051

525354555657585960616263646566676869707172737475767778798081828384858687888990919293949596979899

100101102

103104105106107108109110111112113114115116117118119120121122123124125126127128129130131132133134135136137138139140141142143144145146147148149150151152153

154155156157158159160161162163

Reefing to NSP TYPE:M8 and capacity:C59, the dimension comes from (INPUT of DIMENSION) table B78:o121 164165166167168169170171172173174175176177178179180181182183184185186187188189190191192193194195196197198199200201202203204

205206207208209210211212213214215216217218219220221222223224225226227228229230231232233234235

10

144 All this part is consist of EXCEL-equation, nat VBA. Please customize as you like. 145 NSP TYPE : FS TOTAL BALANCE OF NSP SYSTEM FUEL(Kg)146 CAPA: 6,360 (T/D) ratio147 dust W= 0.1000 (Kg/clKg) O2 %= 3.02 FUEL(T/H)148 B= 6,420 (m3/min) P= -601.8 149 N= 1.3236 (Nm3/clKg) T= 290.0 MATERIAL BALANCE(Kg/cl-Kg)150 Bmax= 6,573 (m3/min) W= -0.0034 IN OUT151 Gmax= 1.3552 (Nm3/clKg) P= -505.2 N= 0.0042 C5 1.9503 0.1000 152 T= 290.0 C4 2.0210 0.3032 153 MW= 1.6538 C3 1.9944 0.2992 154 STREAM C5 * 2 ash W= 0.0000 C2 1.8437 0.2766 155 2 P= -465.7 C1 1.4185 0.0709 156 CAPACITY of ONE STREAM P= -401.4 T= 448.0 157 132.5 T= 448.0 OUT PRESET IN158 3180.0 FUEL consumption ('C) (mmAq)159 P= -366.4 C4 (Kcal/cl-T) C5 290.0 -505.2 160 ( from spray ) T= 581.0 720,793 C4 448.0 -401.4 161 water= 0.0000 T= 581.0 Total heat consumption C3 581.0 -302.4 162 P= -302.4 731,673 C2 701.0 -212.7 163 0.0000 P= -268.3 C1 891.0 -134.8 164 P= -212.7 T= 701.0 FURNACE *** ***165 T= 701.0 166 W= -0.0775 167 D= 3.1 (m) C2 N= 0.0520 168 V= 16.8 (m/s) Pout=169 P= -182.2 W= -0.3862 P in=170 T= 891.0 N= 0.1966 171 T= 280.05 ('C) Tout= 891.0 T= 883.2 172 W= 0.1000 (dust) Tin= 891.0 N= 0.4715 B=173 B= 6,306 (m3/min) C1 P= -134.8 W= 0.0500 Po(KW)=174 N= 1.3236 (Nm3/clKg) Pm(KW)=175 Bmax= 6,457 (m3/min) W= 0.1876 Motor(KW)176 Gmax= 1.3552 (Nm3/clKg) GF= 0.6419 W= -0.1100 W= 0.0330 N=177 Po= 970.33 (KW) N= 0.0560 178 B= 12,914 in (Bm3/m)179 T= 874.0 max N= 244,161 180 IDF W= 1.3476 TGK= 1100.0 GK= 0.4289 max N= 0.9214 181 B= 12,298 out(Bm3/m) P= -56.2 N= 0.9213 182 Pout= 56 (mmAq) NSP KILN T= 327.5 183 Tout= 291.0 ('C) 6,360 (T/D) 6,360 (T/D) W= 0.0750 184 appearance185 P= -630.9 TP= 687 (mmAq) W= 1.1600 W= 1.0500 68.9 186 N= 359,122 (Nm3/H) η(%): 68.4 187188 < IDF inlet-TEMP REDUCTION by heat loss or water spray > AQC189 G:(Kg/Nm3) D:(Kg/Nm3) ratio spray:('C) heat loss:(%) 6,360 190 GAS 1.4546 0.0800 1.0550 280.05 4 ( to 5spray:K17 )191 V:(m3/min) P:(mmAq) Pi:(mmAq) Po:(mmAq) design T:('C) V(α) Pi(α) W= 1.0000 192 IDF 7,700 -750 -690 60 300 1.15 1.092 N= 0.3144 N= 1.7072 193 Pth(KW) Fn(%) Po(KW) Mn(%) Po(KW) afford Motor(KW) T= 1021.6 T= 30.0 194 Motor 968 0.80 1,210 0.96 1260.24 105.14% 1325 FAN N= 1.7073 195 (note) 196 FS gas ratio Nm3/clKg Bm3/min afford Bm3/min Motor(KW) Bm3/H ABC B= Repeat a few click(3-4 times) on ⇔ by ① ②197 C-stream 0.5996 0.7936 7,743 1.124 8700 1497.1 1500 522000 510,000 turns, then click and in order,③ ④198 K-stream 0.4004 0.5300 5,171 1.296 6700 1152.9 1150 402000 400,000 becouse output DATA of 5NSP and 5aqc are linked 199 TOT 1.0000 1.3236 12,914 1.193 15400 2650.0 2650 with each other.200201

18 19 20 21 22 23 24 25 26 27 28 29

(T/H)(T/D)

(T/H)

(Nm3/clKg) C3

NSP KILN TOTAL 1440.0697 0.0465 0.1163 1450.5999 0.4001 1.0000 14618.48 12.33 30.81 147

Coal(Kcal/Kg): 6,200 148MATERIAL BALANCE(Kg/cl-Kg) 149

DOWN n(%) 1501.8503 94.87 1511.7179 85.00 1521.6953 85.00 1531.5672 85.00 1541.3476 95.00 155

156 GAS CYCLON IN 157(Nm3/cl-T) (Bm3/min) (mmAq) 158

1.3552 7,858 -505.2 1591.3510 9,894 -401.4 1601.3510 11,603 -302.4 1611.3510 13,104 -212.7 1621.2990 14,930 -134.8 1631.0708 *** 164

165166

base design 16714 20 (mmAq) 168

-91 -100 (mmAq) 169350 350 ('C) 170

Va=1.3 1719,569 12,500 (m3/min) 172

204 305 Fn=0.8 173213 318 Mn=0.96 174

*** 420 132.16% 175244,157 325,471 (Nm3/H) 176ABC N= 370,000 177

315,000 178179

EP 180Ex.FAN in 181

N= 0.9398 182N= 249,041 183B= 9,070 184

(air only) T= 317.5 185(air+dust) 186

187188

(T/D) 189190

W= 0.9250 1.0000 191T= 87.1 107.2 192

193194195

Repeat a few click(3-4 times) on ⇔ by ① ② 196 turns, then click and in order,③ ④ 197 becouse output DATA of 5NSP and 5aqc are linked 198

199200201

30 31 32

↓ See 5aqc-sheet:X9,Y9,AA10

EP design:

12 ABC CEMENT PLAN 6,360 T/D3 PRESSURE DROP OF NSP CYCLON4 P= -601.8 538.9 MATERIAL BALANCE(Kg/cl-Kg)5 W= -0.0034 DL(Kg/Nm3) IN OUT DOWN6 G= 0.0042 1.439 C5 1.9503 0.1000 1.8503 7 P= -505.2 1.496 C4 2.0210 0.3032 1.7179 8 MW= 1.6505 1.476 C3 1.9944 0.2992 1.6953 9 STREAM C5 * 2 1.365 C2 1.8437 0.2766 1.5672

10 2 1.092 C1 1.4185 0.0709 1.3476 11 NSP CAPACITY P= -465.7 duct dP cyclon dP12 158.9 P= -401.4 (mmAq) (mmAq) OUT PRESET IN IN13 29.1 :C5-IDF ('C) (mmAq) (Nm3/cl-T)14 C4 39.5 96.6 C5 290.0 -505.2 1.3552 15 P= -366.4 35.0 64.3 C4 448.0 -401.4 1.3510 16 P= -302.4 34.1 64.0 C3 581.0 -302.4 1.3510 17 DUCT size up 30.5 55.6 C2 701.0 -212.7 1.3510 18 1.03 C3 134.8 47.3 C1 891.0 -134.8 1.2990 19 P= -268.3 303.0 327.8 FURNACE *** *** 1.0708 20 630.9 21 P= -212.7 W= 0.0775 22 C2 G= 0.0520 2324 W= -0.3862 25 P= -182.2 G= 0.1966 2627 W= 0.1000 (dust) P= -134.8 W= 0.0500 28 Bmax= 7,882 (Bm3/min) C1 W= 0.0750 29 Gmax= 1.3552 (Nm3/cl-Kg) W= 0.1876 W= -0.1100 W= 0.0330 30 GF= 0.6419 G= 0.0560 31 P= -630.9 (mmAq)3233 W= 1.3476 GK= 0.4289 34 P= -56.2 3536 Pout= 56.0 (mmAq)3738 TP= 686.9 (mmAq) NSP KILN AQC3940 604.441 W= 1.1600 W= 1.0500 W= 1.0000 W=4243

18 19 20 21 22 23 24 25 26 27 28 29 30

47 48 PRESSURE DROP OF NSP CYCLON49 DUCT size up DUCT size up50 1.03 INTLET DUCT INLET OPENING51 D(m) L(m) A(m2) V(m/s) W(m) H(m) A(m2)52 DUCT 3.09 118.80 7.50 17.30 DUCT 1.03 1.0353 C5 3.30 10.00 8.53 15.36 TWIN:C5 1.28 2.55 3.26 54 C4 3.61 11.00 10.20 16.22 C4 2.11 4.22 8.92 55 C3 3.71 11.00 10.79 17.98 C3 2.19 4.39 9.63 56 C2 3.86 11.00 11.71 18.73 C2 2.34 4.68 10.93 57 C1 4.25 12.00 14.21 17.61 C1 2.46 4.92 12.12 585960 CYCLON D(m) H1(m) H2(m) A(m2) V(m/s)61 TWIN:C5 4.50 7.87 3.51 15.90 4.08 62 C4 7.20 7.20 5.65 40.69 4.03 63 C3 7.20 7.20 5.65 40.69 4.72 64 C2 7.20 7.20 7.00 40.69 5.34 65 C1 7.50 7.50 9.61 44.16 5.61 6667

18 19 20 21 22 23 24 25 26 27 28 29 30

(T/H)

1234

n(%) 594.87 685.00 785.00 885.00 995.00 10

1112

(Bm3/min) 137,858 149,894 15

11,603 1613,104 1714,930 18

*** 19202122232425262728293031323334353637383940

1.0000 414243

31 32

474849

50V(m/s) 51

5219.88 5318.37 5419.96 5519.87 5620.44 57

58596061626364656667

31 32

GAS BALANCE OF DUCT SPRAY

REGISTERED NO. : DS-0001 Mr. AAAAAA 5 <DATA INPUT> ABC CEMENT PLANT6 STADARD TEMPERSTURE (TS:'C) 3078 GAS CONDITION GAS CONDITION GAS & DUST9 Q Unit Vol Volume

10 (T/H)11 IN 265 1.3552 012 OUT *** *** ***1314 SOURCE OF GAS NSP-coal ( NSP-oil , NSP-coal , HGG-oil )1516 LEAK AIR & HEAT LOSS LEAK AIR: LA(%) 17 0 1819 DIMENTION OF DUCT Ua(UA:Kcal/m3.h.'C)20 120212223 note : If CD( J11 and J12 ) is 0(zero), NSP dust's Cp(Kcal/Kg) is given automaticaly. 2425 ( Evapolation time )26 te= d^2 / 10^(1.83446*((Tin+Tout)/2)^0.37603*(Tin)^-0.23389)27 Tin: 29028 Tout: 280.052930 ( In case of "Volume(Nm3/H)" is given, input 0 (zero) in "CAP(T/H)" cell. ) 31

3 4 5 6 7

Change the bold value, and click the "Run" button.

(Nm3/Kg) (Nm3/H)

ﾟC =ﾟC =

12

( gas conditioning ) 3COPYRIGHT : RYUTA HANAO [ NO COPY ] 4

6,360 T/D 5 5: link with 5NSP-sys. 6 6

7 7GAS & DUST DUST WATER LEAK AIR 8 8

TG DL Cp TW LA 9 9('C) (Kg/Nm3) (Kcal/'C) ('C) ('C) 10 10

290 0.08 0 30 30 11 11280.05 0.08 0 *** 280.05 12 12

13 13( NSP-oil , NSP-coal , HGG-oil ) 14 14

15 15HEAT LOSS: HL(%) 16 16

4 17 1718 18

GAS SPEED (GS:m/s) DIA. OF DROPLET (DDL:1/1000mm) 19 1916.8 120 20 20

21 2122 22

If CD( J11 and J12 ) is 0(zero), NSP dust's Cp(Kcal/Kg) is given automaticaly. 23 2324 2425 25

d^2 / 10^(1.83446*((Tin+Tout)/2)^0.37603*(Tin)^-0.23389) d: 120 μ 26 26554 27 27

536.09 te= 0.48 sec 28 28See AB18 ↑ 29 29

( In case of "Volume(Nm3/H)" is given, input 0 (zero) in "CAP(T/H)" cell. ) 30 3031 31

8 9 10 11 12

ﾟFﾟF

GAS BALANCE OF DUCT SPRAY ABC CEMENT PLANT ( gas conditioning )

Water 6,360 (T/D) 0.000 (H2O:T/H)) 30.0 ('C) 0 (Nm3/H)

DUCT SPRAY

< NSP-coal

Hot Gas359,122 (Nm3/H) Leak air

290.0 ('C) 0 (Nm3/H) 0.080 (Kg/Nm3) 30.0 ('C) 0.352 (Cp) 0.312 (Cp)

HEAT from HOT GAS (Kcal/H): 34,445,735 TRANSFERRED HEANECESSARY RD's VOLUME for HEAT TRANSFER(m3) :DIMENSION OF RD D(m): 3.929 L(m): 0.000

OTHER INPUT DATA STADARD TEMPERATURE ('C) : 30 OTHER DATA LEAK AIR(%) : 0DIMENTION OF RD Ua(Kcal/m3.h.'C) : 120

16 17 18 19 20 21 22

1 GAS BALANCE OF DUCT SPRAY 2

34

Exh. Gas 5 359,122 (Nm3/H) 6 724.1005 =i(Kcal/Kg) 280.1 ('C) 7 0.080 (Kg/Nm3) 8 0.351 (Cp) 9

10 11

DUCT SPRAY 12 13> 14

1516

EVAPOLATION TIME 17 Theoretical(s): 0.48 18 Actual(s) : 0.00 19 <Ratio> 0.00 20

2122

TRANSFERRED HEA (Kcal/H): -8 23 24

L/D: 0.000 2526

27 28

('C) : 30 HEAT LOSS(%) : 4 29L/D: 0.000 DOROPLET(1/1000mm) 120 30

3123 24 25 26 27 28 29

12 GAS BALANCE OF SPRAY TOWER345 <IN> W or V *6 INLET GAS GAS 0 *7 DUST DUST 0 *8 SPRAY WATER H2O 0 *9 LEAK AIR AIR 0 *

10 TOTAL 11 12 13 <OUT> W or V *14 OUTLET GAS GAS 0 *15 DUST DUST 0 *16 VAPOUR H2O 0 *17 LEAK AIR AIR 0 *18 HEAT LOSS 34,445,735 *19 TOTAL 20 212223 HEAT LOSS (Kcal/cl-Kg)2425262728293031

33 34 35 36 37

GAS BALANCE OF SPRAY TOWER( gas conditioning )

* Cp * ( T - Ts ) = Kcal/H* 0.352 * ( 290.0 - 30.0 ) = 32,853,345

0.080 * 0.213 * ( 290.0 - 30.0 ) = 1,592,391 * 1.000 * ( 30.0 - 30.0 ) = 0 * 0.312 * ( 30.0 - 30.0 ) = 0

= 34,445,735

* Cp * ( T - Ts ) = Kcal/H* 0.351 * ( 280.1 - 30.0 ) = 31,540,451

0.080 * 0.213 * ( 280.1 - 30.0 ) = 1,527,463 * 1.000 * ( 724.1 - 30.0 ) = -8 * 0.315 * ( 280.1 - 30.0 ) = 0 * 0.040 * ( - ) = 1,377,829 = 34,445,735

5.20

38 39 40 41 42 43 44 45 46 47 48

123456789

10111213141516171819202122232425262728293031

49

3 260652 0.9129 4 note: Values in green box are linked into "5NSP-sys" sheet.56 KILN 2nd AIR NSP 2nd AIR middle AIR 15 -100 AQC EXHOUST GAS7 0.3144 (Nm3/cl-Kg) 0.4715 (Nm3/cl-Kg) 0.4564 (Nm3/cl-Kg) 0.4649 8 1021.62 ('C) 883.23 ('C) 455.84 ('C) 201.54 9 1186 730 Ex.FAN P (assumption)

10 Motor(KW) afford Pm(KW) Po(KW) out(mmAq) in(mmAq) (Bm3/min)11 CLINKER *** base: 213 204 14 -91 9,569 12 265.0 (T/H) 420 1.3216 318 305 20 -100 12,500 13 1,370 ('C) 0.96 0.80 1.15 1.30 14 Mn= Fn= Pa= Va=15 AQC EFFICIENCY( % ) 16 66.35 4.888 6.720 7.193 17 68.59 eff(%)= 66.35 68.59 FAN:18 CHAMBER ( min : 5 )19 NUMBER: 7 20 10.40 4.20 4.20 4.20 4.20 21 STROKE changing CELL 1 2 3 4 5 6 7 22 first 1 12.8 GRATE L= 27.20 (m)23 second 2 12.8 gross A(m2)= 141.440 B= 2.70 ---- 5.200 (m)24 third 3 12.8 25 CHAMBER 1 2 3 4 5 6 7 TOTAL 26 COOLING AIR 0.118 0.291 0.291 0.291 0.253 0.232 0.232 1.7072 (Nm3/clKg)27 6360 T/H (Nm3/H) 31,200 77,000 77,000 77,000 67,020 61,600 61,600 452,420 28 1.0000 ('C) 30 30 30 30 30 30 30 30 Black29 6000 T/D (Nm3/H) 31,200 77,000 77,000 77,000 67,020 61,600 61,600 1.7072 (Nm3/clKg)30 Bed Depth(m) 0.805 0.548 0.548 0.548 0.548 0.548 0.548 *** 31 P.Drop(mmAq) 589 361 361 339 293 272 270 *** 32 Grate L(m) 2.00 4.20 4.20 4.20 4.20 4.20 4.20 27.20 gross33 B(m) 2.7 5.20 5.20 5.20 5.20 5.20 5.20 5.20 *** net34 net A(m2) 7.90 21.84 21.84 21.84 21.84 21.84 21.84 138.94 35 Air load 66 59 59 59 51 47 47 54 (Nm3/min/m2)36 Air speed 1.22 1.09 1.09 1.09 0.95 0.87 0.87 1.00 (m/s)37 CHAMBER 1 2 3 4 5 6 7 TOTAL 38 F.D.FAN V(Bm3/m) 580 1430 1430 1430 1240 1140 1140 8390 Vα=39 SPEC: P(mmAq) 1070 650 660 620 530 500 490 *** Pα=40 Po(KW) 127 190 193 181 134 116 114 1055 Fn =41 Pm(KW) 170 240 250 230 170 150 150 1360 Mn =42 Mα=43 All this part is consist of EXCEL-equation, not VBA. Please customize as you like.

16 17 18 19 20 21 22 23 24 25 26AIR LOAD : ( for reference ) TEMPERATURE('C)

B-hitach 2.0 158 96 79 50 50 47 47 1370 1186 CP-type 2.0 160 94 76 53 51 46 46 1370 1173

Conventional 2.5 160 95 70 55 60 60 60 1400 962 IKN-type 1.9 160 95 65 45 40 30 35 1370 979 FLS-SF 1.8 63 53 53 53 46 42 42 1370 1027

(Nm3/clKg) (Nm3/min/m2) <------------------------- --------------------> (Nm3/min/M2) CLINKER kiln 2-airB-hitach 1.000 1.400 1.100 1.100 1.100 1.100 1.100 1.100 4000T/D area(m2):CP-type 1.055 1.504 2.154 1.500 1.300 1.300 1.300 1.300 4000T/D area(m2):

Conventional 0.960 0.893 0.905 0.910 0.932 0.932 0.932 0.932 4000T/D area(m2):IKN-type 1.000 1.690 3.650 3.100 1.000 0.950 0.900 0.900 4000T/D area(m2):FLS-SF 1.000 0.586 0.794 1.910 1.910 1.205 1.205 1.205 6000T/D area(m3):

1.000 0.586 0.794 1.910 1.910 1.205 1.205 1.205 : ADJUSTMENT OF HEAT TRANSFER FACTOR(for reference)CHAMBER 1--7 1 2 3 4 5 6 7

1.002 1.024 1.024 1.024 1.025 1.025 1.025 1.025 : ADJUSTMENT OF OUTPUT GAS TEMPERATURE(for reference)FLS-SF 1.001 1.024 1.024 1.024 1.025 1.025 1.025 1.025 W*L(m):IKN-type 1.000 1.024 1.024 1.024 1.025 1.025 1.025 1.025 W*L(m):

Conventional 1.001 1.024 1.024 1.024 1.025 1.025 1.025 1.025 W*L(m):CP-type 0.999 1.024 1.024 1.024 1.025 1.025 1.025 1.025 W*L(m):B-hitach 1.000 1.024 1.024 1.024 1.025 1.025 1.025 1.025 W*L(m):

0ﾟC30ﾟC

0.000 5.000 10.000 15.000 20.000 25.000 30.000 0

100

200

300

400

500

600

700

800

900

1,000

1,100

1,200

1,300

1,400

1,500

1,600

CLINKER COOLING CURVE

GAS in

GAS out

P mmAq

CL(AVE)

Rec'ry Point

Chamber Wall

LENGTH(m)

TE

MP

( 'C

)

0.000 5.000 10.000 15.000 20.000 25.000 30.000 0

100

200

300

400

500

600

700

800

900

1,000

1,100

1,200

1,300

1,400

1,500

1,600


GAS in

GAS out

P mmAq

CL(AVE)

Rec'ry Point

Chamber Wall

LENGTH(m)

TE

MP

( 'C

)

Leak(%)= 2 3dT= 10 4N= 0.9398 5

AQC EXHOUST GAS T= 317.52 6(Nm3/clKg) 7('C) 9,070 8middle + EXHOUST FAN in 9

0.9213 (Nm3/cl-Kg) 10327.52 ('C) 297 11

350 :design('C) 12244,157 (Nm3/H) 249,041 13244,161 (max:Nm3/H) 14

370,000 =N ABC 15315,000 16325,471 :Nm3/H 17

18192021222324

CLINKER 25265.0 (T/H) 26

Kg/cl-Kg ('C) 270.0750 327.52 :dust 280.9250 89.33 :cl' 291.0000 107.19 95 30

311.87 (cl-T/H.m2) 321.91 (cl-T/H.m2) 33

34(Nm3/min/m2) 35

36(#1-2) (#3-7) Nm3/clKg 37

1.00 1.00 1.7115 381.80 1.60 390.80 0.80 400.95 0.95 411.20 1.20 42

4327 28 29

: ( for reference )730 297 93 835 230 90 683 261 121 979 257 amb +65877 315 amb +65

nsp 2-air exh air clinker99.0 eff(%): 67.8 90.6 eff(%): 73.0

112.0 eff(%): < 60.0 90.2 eff(%): 73.8

138.8 eff(%): 70.0 : ADJUSTMENT OF HEAT TRANSFER FACTOR(for reference)

: ADJUSTMENT OF OUTPUT GAS TEMPERATURE(for reference)2.7*2.0 5.2*25.2 1.3*4 rows4.2*21.6 ** 1-stage4.2*26.7 ** 2-stage3.3*27.5 ** 2-stage3.0*11.1 3.6*15.3 2-stage

EP B=

:EP design

0.000 5.000 10.000 15.000 20.000 25.000 30.000 0

100

200

300

400

500

600

700

800

900

1,000

1,100

1,200

1,300

1,400

1,500

1,600


GAS in

GAS out

P mmAq

CL(AVE)

Rec'ry Point

Chamber Wall

LENGTH(m)

TE

MP

( 'C

)

0.000 5.000 10.000 15.000 20.000 25.000 30.000 0

100

200

300

400

500

600

700

800

900

1,000

1,100

1,200

1,300

1,400

1,500

1,600


GAS in

GAS out

P mmAq

CL(AVE)

Rec'ry Point

Chamber Wall

LENGTH(m)

TE

MP

( 'C

)

12 GAS BALANCE OF SPRAY TOWER3 ( gas conditioning )45 <IN> W or V * * Cp * ( T - Ts ) = Kcal/H6 INLET GAS GAS 359,122 * * 0.356 * ( 281.0 - 30.0 ) = 32,042,113 7 DUST DUST 359,122 * 0.080 * 0.213 * ( 281.0 - 30.0 ) = 1,533,441 8 SPRAY WATER H2O 25,694 * * 1.000 * ( 30.0 - 30.0 ) = 0 9 LEAK AIR AIR 17,956 * * 0.312 * ( 30.0 - 30.0 ) = 0

10 TOTAL = 33,575,554 11 12 13 <OUT> W or V * * Cp * ( T - Ts ) = Kcal/H14 OUTLET GAS GAS 359,122 * * 0.347 * ( 150.0 - 30.0 ) = 14,955,479 15 DUST DUST 359,122 * 0.080 * 0.205 * ( 150.0 - 30.0 ) = 708,022 16 VAPOUR H2O 25,694 * * 1.000 * ( 661.7 - 30.0 ) = 16,231,499 17 LEAK AIR AIR 17,956 * * 0.312 * ( 150.0 - 30.0 ) = 673,287 18 HEAT LOSS 33,575,554 * * 0.030 * ( - ) = 1,007,267 19 TOTAL = 33,575,554 20 21 2223242526 2728293031

33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48

1234

A-maker 533,576 6

70 80 9

33,576 10111213

16,337 1415

16,231 1617

1,007 1833,576 19

202122232425262728293031

49

12 HEAT BALANCE OF RAW VERTICAL MILL345 <IN> W or V * * Cp * ( T - Ts ) = Kcal/H6 INLET GAS GAS 414,421 * * 0.356 * ( 281.0 - 30.0 ) = 36,976,046 7 DUST DUST 414,421 * 0.080 * 0.213 * ( 281.0 - 30.0 ) = 1,769,356 8 LEAK AIR VM VM 45,586 * * 0.312 * ( 30.0 - 30.0 ) = 0 9 CY CY 48,760 * * 0.312 * ( 30.0 - 30.0 ) = 0

10 RAW MATERIAL 500,000 * * 0.202 * ( 20.0 - 30.0 ) = -1,008,809 11 H2O IN MATERIAL H2O 43,478 * * 1.000 * ( 20.0 - 30.0 ) = -434,783 12 CIRCULATION AIR AIR 101,842 * * 0.343 * ( 87.0 - 30.0 ) = 1,989,996 13 GRAINDING HEAT 4,500 * 0.900 * 860 * 1.000 = 3,483,000 14 FAN HEAT 3350 * 0.700 * 860 * 1.000 = 2,016,700 15 TOTAL 44,791,506 1617 <OUT> W or V * * Cp * ( T - Ts ) = Kcal/H18 OUTLET GAS GAS 414,421 * * 0.343 * ( 87.0 30.0 ) = 8,097,759 19 DUST DUST 414,421 * 0.080 * 0.201 * ( 80.0 30.0 ) = 333,950 20 LEAK AIR VM VM 45,586 * * 0.312 * ( 87.0 30.0 ) = 810,470 21 CY CY 48,760 * * 0.312 * ( 87.0 30.0 ) = 866,894 22 MATERIAL 500,000 * * 0.208 * ( 80.0 30.0 ) = 5,189,588 23 H2O IN MATERIAL H2O 5,051 * * 1.000 * ( 80.0 30.0 ) = 252,525 24 CIRCULATION AIR AIR 101,842 * * 0.343 * ( 87.0 30.0 ) = 1,989,996 25 VAPOUR H2O 38,428 * * 1.000 * ( 632.5 30.0 ) = 23,153,069 26 HEAT LOSS VM 4,500 * 0.900 * 860 * 0.800 = 2,786,400 27 HEAT LOSS FAN 3,350 * 0.700 * 860 * 0.650 = 1,310,855 28 TOTAL 44,791,506 29 3031

33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48

1234

A-maker 538,745 6

789

-1,444 1011

0 125,500 13

1442,802 15

1617

10,109 18192021

5,442 2223

0 2423,153 254,097 26

2742,802 28

293031

49

12 HOT GAS GENERETOR3 4 Q: Kcal/H [ 4,933,933 at T= 30 ]5 W: Kg/H EXCESS AIR6 T: 'C (primary air)7 N: Nm3/H HEAT LOSS 20.0 (%) N= 1,475 8 Q= 1,233,483 (Kcal/H) T= 30.0 9

10 11 26,405 12 HGG13 14 15 Hot Gas F.LOSS 0.0 16 N= 41,018 FUEL W= 623.0 17 T= 400.1 Hl= 9900.0 18 Cp= 0.325 COMBUTION GAS 19 HEAT VOLUME N= 8,876 W= 623.0 20 Q= 4,933,933 (Kcal/H) N= 7,121 21 ( 4,933,933 + 0 ) T= 30.0 22 23 2425 H2O in AIR COOLING AIR H2O in AIR COMBUTION AIR26 N= 1,066 N= 31,076 N= 280 N= 6,687 27 T= 30 T= 30.0 T= 30.0 T= 30.0 28 2930 FUEL EFFICIENCY(%): 4,933,933 / 6,167,416 = 80.00%313233

16 17 18 19 20 21 22 23 24 25 26 27

Q=

1234

EXCESS AIR 5(primary air) 6

7 8 9 10 11

121314

(%) 15(Kg/H) 16(Kcal/Kg) 17 18 19 20 21

222324252627282930313233

28 29

GAS & MATERIAL BALANCE OF CEMENT BALL MILL

REGISTERED NO. : CEM-CB0001 Mr. AAAAAAA 5 <DATA INPUT> ABC CEMENT PLANT6 GRINDING PRE.GRINDING or NOT( 1 or 0 ) : 07 SYSTEM Cyclon or Osep( CY or OS ) : OS89 STADARD TEMPERSTURE : (TS:'C) 30 WATER SPRAY(WS) :

10 SPECFICATION BALL MILL11 DIA(m) LENGTH(m) POWER(KW)12 Mill shell size: 5.2 15.5 650013 KSCC 160 4.4 12.5 370014 GAS SPEED(m/s) POWER(%) HEAT LOSS(%)15 0.82 85 251617 CONDITION MATERIAL18 Q(DB) TM CM19 (T/H) ('C) (Kcal/'C)20 CLINKER 168.0 100.0 0.190 21 GYPSUM 8.0 30.0 0.200 22 SLUG/LIME 24.0 30.0 0.200 23 IN TOT 200.0 88.3 0.192 24 OUT 200 0.192 25 dT= 10 2627 GAS SPECFICATION BALL MILL 28 TG DUST 29 ('C) (g/Nm3) 30 IN 30.0 *** 31 OUT 100.0 20032 92 :balance33 CIRCULATION RATIO(MCR) 150 ( CY = 200 , OS = 150 )34 FAN TEMP-UP CALCULATIO dP(mmAq): -520 5035 See Y9 ↑ See Z9 ↑3637 KSCC 160 4.4 12.5 3700(3770)

3 4 5 6 7

41 < LARGE BALL MILL SPEC >4243 KW D(m) L(m) L/D4445 300046 3500 4.3 13.0 3.02 47 3700 4.4 13.0 2.95 48 4000 4.6 13.0 2.83 49 4500 4.6 13.5 2.93 50 5000 4.8 14.5 3.02 51 5500 4.9 15.0 3.06


XX + dT

52 6000 5.0 15.5 3.10 53 6300 5.0 15.8 3.16 54 6500 5.2 15.5 2.98 55 7000 5.3 15.5 2.92 56 7500 5.4 16.0 2.96 57 8000 5.5 16.0 2.91 5859 PG + BM SYSTEM60 CAPA(T/H) PG-SIZE PG(KW) BM(KW)61 120 *** *** 400062 160 180 1350 370063 180 200 1100 430064 200 200 1200 500065 200 220 1400 500066 220 220 1700 580067 240 220 1500 600068 260 220 1700 65006970

3 4 5 6 7

GAS & MATERIAL BALANCE OF CEMENT BALL MILL( O-sep )

COPYRIGHT : RYUTA HANAO [ NO COPY ] 6,360 :T/D unit(T/clT) afford BM(T/H) 5265.0 :T/H 1.192 1.266 400 6

No of BM: 2 200 78

WATER SPRAY(WS) : (WS/Q:%) 0 TEMP('C) 30 9SEPARATOR FAN 10

KW/T Roter:D(m) V(Kg/Nm3) POWER(KW) POWER(KW) 1132.50 2.95 3.07843 300 600 1223.125 N-3500 162,420 13

HEAT LOSS(%) INTAKE AIR(%) HEAT LOSS(% *** POWER(%) 1436 4.4 *** 70 15

16 WATER in MATERIAL FAN TEMP-UP 17

Unit Weight W(WB) TW MAT TOT TE('C) 18T/clT (%) ('C) H2O(T/H) 5 190.8400 0.00 100.0 0.000 200.0400 10.00 30.0 0.889 210.1200 10.00 30.0 2.667 221.0000 1.747 30.0 3.556 231.0000 0.00 *** 24

25 O-sepa 26

SEPRATOR Roter:D(m) 27TG dTG DUST N-250 0.78 28('C) ('C) (g/Nm3) N-500 1.11 29

30 *** *** N-1000 1.56 30XX 0 200 N-1250 1.75 31

N-1500 1.92 32( CY = 200 , OS = 150 ) N-2000 2.22 33

TE('C): 4.9 N-2500 2.50 34N-3000 2.74 35N-3500 2.96 36

23.13 N-4000 3.16 378 9 10 11 12

4142

rpm Media(T) CAPACITY (T/H) 43raw meal cement 44

4514.9 265 90 4614.7 255 95 4714.4 114 4814.0 295 4913.9 335 250 123 5013.7 360 280 136 HTNE 51

TYPE(Bm3/m)

13.5 360 150 5214.4 410 300 175 paki:BCL 5313.5 420 170 AKO#2 5413.3 475 180 5513.1 475 375 190 56

210 575859

OS-SIZE OS(KW) TOT(KW) KW/T 603000 160 613500 200 5250 32.81 KSCC 623500 250 5650 31.39 633500 300 6500 32.50 IHI 643500 300 6700 33.50 KHI 654000 330 7830 35.59 FOMOSA 664000 360 7860 32.75 674000 400 8600 33.08 AKO#2 68

6970

8 9 10 11 12

12 Brown : EXCEL GAS & MATERIAL BALANCE OF CEMENT BALL MILL3 ABC CEMENT PLANT 200 4 N= 58,471 (36%) N= 68,952 5 T= 30.0 T= 84.8 6 C= 0.312 C= 0.312 78 N= 162,420 50 2509 T= 46.8

10 C= 0.312 11 SEP SEP/DL12 N= 162,420 3078 13 MATERIAL B= 209,896 2382 14 Q= 200.0 v= 401.3 15 T= 88.3 16 C= 0.192 Q= 300.0 Water spray17 T= 89.8 H2O=18 Water in MAT. C= 0.192 T=19 H2O= 3.556 20 T= 30.0 BALL MILL21 %= 1.75% 650022 W=23 N= 30,574 N=24 T= 30.0 25 Heat V= C= 0.312 MILL D*L: 5.2

O-sep 26 net: 285,862 Kcal/H PRE GRINDING :(KW) 27 gross: 285,862 Kcal/H

28 Tin= 30.0 ( KW * % + 29 Tout= 100.0 HEAT LOSS BM 650030 HEAT LOSS SP 6500

100 31 MATERIAL T * % 32 clinker 100*0.84 Gas compornent TOT 33 gypsum 30*0.04 BF inlet 100.00% 34 slug/lime 30*0.12

150-250 35200-350 36 ( BM exhoust circulation )300-450 37 V(Bm3/m) V-afford Bm3/m P(mmAq)

38 O-sep 3559 N-3500 -17539 SEP FAN 3684 1.086 4000 65040 BF FAN 2034 1.229 2500 30041 42 KSCC 3800 65043 KSCC 1600 30044 ABC 3833 70045 ABC 2000 35046

16 17 18 19 2048 ( Saturate TEMPERATURE ) Nm3/Nm3= 0.032029 49 Air Humid(%)= 75 50 T('C)= 30.0 CO2 H2O51 Air % 1.0000 0.0000 0.0000

52 Cold air 58,471 1873 53 Hot air 30,574 979 54 55 H2O in MAT 4,423 4423 56 TOTAL 93,469 0 7,275 57 BF inlet 100.00% 0.00% 7.78%58 59 Specific heat value 'C60 BF inlet 84.8 0.028 616263 < APPROXIMATE EQUATION >64 H=0.0062+0.00032912*T+0.000026518*T^2-0.00000015059*T^3+0.0000000084342*T^465 T=-9.3475+1831.24032730894*H-31474.5301726136*H^2+311439.031040743*H^3-1658132.44374535*H^466 +4661155.60293728*T^5-6425597.4301294*H^6+3379407.89167236*H^767

16 17 18 19 20

GAS & MATERIAL BALANCE OF CEMENT BALL MILL(T/H) ( O-sep ) 　　(42%) N= 68,952 N= 93,469

T= 84.8 T= 84.8 C= 0.312 C= 0.312

N-3500 　　 dust= 11.694 200 20 50 50 200

-175 -520 50 -250SEP CY FAN BF FAN

DL BF/DL Bm3/M=N= 162,420 (g/Nm3): 200 T= 79.8 (g/Bm3): 150 i(Kcal/Kg)=C= 0.312 dT=

Water spray0.000 0 0.000

30.0 Q= 493.0 Q= 188.3 dust=T= 103.0 T= 89.8 T=

BALL MILL C= 0.192 C= 0.192 C=(KW)

3.556 V(m/s) dust= 6.999 Q= 200.0 4,423 0.82 N= 34,997 (22%) T= 89.5

T= 100 H2O= 0.000 15.5 C= 0.312

NON

( KW * % + ( KW + KW ) * %) * % =85 300 600 70 25 = 1,323,325 85 300 600 70 4.4 = 232,905

CO2 H2O SO3 N2 O2 Dew point0.00% 7.78% 0.00% 72.85% 19.37% 40.5 'C

TOTAL POWER(KW)Pin Pout T('C) Fn Mn Mo(KW) M-afford

-50 -300 80-600 50 80 0.8 0.96 540.0 1.111 -250 50 80 0.8 0.96 157.9 1.077

21 22 23 24 25 26 27

TEMP HumiditySO3 N2 O2 Dew point 'C %0.0000 0.7900 0.2100 'C 0 100

44713 11886 10 10023380 6215 20 100

30 10030 100

0 68,093 18,101 40 1000.00% 72.85% 19.37% 40.5 50 100

60 100Cp 70 100

0.230 0.060 0.318 80 10090 100

H=0.0062+0.00032912*T+0.000026518*T^2-0.00000015059*T^3+0.0000000084342*T^4T=-9.3475+1831.24032730894*H-31474.5301726136*H^2+311439.031040743*H^3-1658132.44374535*H^4 +4661155.60293728*T^5-6425597.4301294*H^6+3379407.89167236*H^7

21 22 23 24 25 26 27

1 12 2

3 3N= 93,469 4 4T= 74.8 5 5 <IN>C= 0.312 6 6 MATERIAL

drop T= 10.0 7 7 MAT.RETURN50 =dP(mmAq) 8 8 MILL AIR

50 9 9 POWER10 10

2092 11 11 H2O IN MATERIAL 12 12 WATER

637.8 13 13 SEP AIR5.0 14 14 TOTAL

15 1516 16 <OUT>

17 17 MATERIAL11.694 18 18 MAT.RETURN

84.8 19 19 MILL AIR0.192 20 20 HEAT LOSS

21 21 22 22 VAPOUR MATERIA

23 23 WATER24 24 H2O IN MATERIAL 25 25 SEP AIR26 26 DUST27 27

Kcal/H 28 28 TOTAL1,323,325 29 29

232,905 30 3031 3132 33 34333435

7570 36Motor(KW) 37

300 38600 39170 40

41600 42120 43

6030 44132 45

4628 29

48H2O inAir 49Nm3/Nm3(WB) 500.006200 51

0.012077 520.023534 530.042706 540.042706 550.073747 560.122841 570.198192 580.310029 590.470608 600.694204 61

626364656667

28 29

HEAT BALANCE OF CEMENT BALL MILL( O-sep )

W or V * * Cp * ( T - 200,000 * * 0.192 * ( 88.3 - 300,000 * * 0.192 * ( 89.8 -

AIR 30,574 * * 0.312 * ( 30.0 -MILL 6,500 * 0.850 * 860.000 * ( -

SEP 900 * 0.700 * 860.000 * ( -H2O 3,556 * * 1.000 * ( 30.0 -H2O 0 * * 1.000 * ( 30.0 -AIR 58,471 * * 0.312 * 30.0

W or V * * Cp * ( T - 181,306 * * 0.192 * ( 89.8 - 300,000 * * 0.192 * ( 89.8 -

AIR 30,574 * * 0.312 * ( 84.8 -MILL 541,800 + 4,751,500 * ( 0.250 -

SEP 541,800 + 4,751,500 * ( 0.044 -H2O 3,556 * * * ( 637.8 -H2O 0 * * * ( 637.8 -H2O 0 * * 1.000 * ( 84.8 -AIR 58,471 * * 0.312 * ( 84.8

MILL 6,999 * 0.192 * ( 89.8 SEP 11,694 * 0.192 * ( 84.8

35 36 37 38 39 40 41 42 43 44

1234

Ts ) = Kcal/H 530.0 ) = 2,234,400 630.0 ) = 3,437,140 730.0 ) = 0 8

) = 4,751,500 9) = 541,800 10

30.0 ) = 0 1130.0 ) = 0 1230.0 = 0 13

10,964,840 1415

Ts ) = Kcal/H 1630.0 ) = 2,077,250 1730.0 ) = 3,437,140 1830.0 ) = 522,718 19

) = 1,323,325 20) = 232,905 21

30.0 ) = 2,161,067 2230.0 ) = 0 2330.0 ) = 0 2430.0 ) = 998,466 2530.0 ) = 66,783 2630.0 ) = 145,186 27

10,964,840 28293031

45 46 47 48 49

12 HEAT BALANCE OF CEMENT BALL MILL3 ( O-sep )45 <IN> W or V * * Cp * ( T - Ts ) = Kcal/H6 MATERIAL 200,000 * * 0.192 * ( 79.4 - 30.0 ) = 1,893,665 7 MAT.RETURN 300,000 * * 0.192 * ( 92.5 - 30.0 ) = 3,591,876 8 MILL AIR AIR 26,405 * * 0.312 * ( 30.0 - 30.0 ) = 0 9 POWER MILL 5,000 * 0.850 * 860.000 * ( - ) = 3,655,000

10 SEP 900 * 0.700 * 860.000 * ( - ) = 541,800 11 H2O IN MATERIAL H2O 2,695 * * 1.000 * ( 30.0 - 30.0 ) = 0 12 WATER H2O 0 * * 1.000 * ( 30.0 - 30.0 ) = 0 13 SEP AIR AIR 16,242 * * 0.312 * 30.0 30.0 = 0 14 TOTAL 9,682,341 1516 <OUT> W or V * * Cp * ( T - Ts ) = Kcal/H17 MATERIAL 194,048 * * 0.192 * ( 92.5 - 30.0 ) = 2,323,325 18 MAT.RETURN 300,000 * * 0.192 * ( 92.5 - 30.0 ) = 3,591,876 19 MILL AIR AIR 26,405 * * 0.312 * ( 95.0 - 30.0 ) = 535,438 20 HEAT LOSS MILL 541,800 + 3,655,000 * ( 0.250 - ) = 1,049,200 21 SEP 541,800 + 3,655,000 * ( 0.044 - ) = 184,659 22 VAPOUR MATERIA H2O 2,695 * * * ( 635.8 - 30.0 ) = 1,632,743 23 WATER H2O 0 * * * ( 635.8 - 30.0 ) = 0 24 H2O IN MATERIAL H2O 0 * * 1.000 * ( 87.5 - 30.0 ) = 0 25 SEP AIR AIR 16,242 * * 0.312 * ( 87.5 30.0 ) = 290,977 26 DUST MILL 5,952 * 0.192 * ( 95.0 30.0 ) = 74,122 27 SEP 0 * 0.192 * ( 87.5 30.0 ) = 0 28 TOTAL 9,682,341 293031

33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48

1234

A-maker 51,894 6

0 78

4,197 91011

0 120 13

6,090 141516

2,397 170 18

535 191,234 20

211,633 22

2324

291 252627

6,090 28293031

49


REGISTERED NO. : CEM-CA0001 Mr. AAAAAAA 5 <DATA INPUT> ABC CEMENT PLANT6 GRINDING PRE.GRINDING or NOT( 1 or 0 ) : 17 SYSTEM Cyclon or Osep( CY or OS ) : OS89 STADARD TEMPERSTURE : (TS:'C) 30 WATER SPRAY(WS) :

10 SPECFICATION BALL MILL11 DIA(m) LENGTH(m) POWER(KW)12 Mill shell size: 4.8 14.5 500013 KSCC 160 4.4 12.5 370014 GAS SPEED(m/s) POWER(%) HEAT LOSS(%)15 0.82 85 2516 28.6317 CONDITION MATERIAL18 Q(DB) TM CM19 (T/H) ('C) (Kcal/'C)20 CLINKER 168.0 88.1 0.190 21 GYPSUM 8.0 30.0 0.200 22 SLUG/LIME 24.0 30.0 0.200 23 IN 200 78.4 0.192 24 OUT 200 0.192 25 dT= 10 2627 GAS SPECFICATION BALL MILL 28 TG DUST 29 ('C) (g/Nm3) 30 IN 30.0 *** 31 OUT 92.0 20032 33 CIRCULATION RATIO(MCR) 150 ( CY = 200 , OS = 150 )34 FAN TEMP-UP CALCULATIO dP(mmAq): -520 5035 See Y9 ↑ See Z9 ↑3637 KSCC 160 4.4 12.5 3700(3770)

3 4 5 6 7


XX + dT


COPYRIGHT : RYUTA HANAO [ NO COPY.] 6,000 :T/D unit(T/clT) afford BM(T/H) 5250.0 :T/H 1.192 1.342 400 6

No of BM: 2 200 78


KW/T Roter:D(m) V(Kg/Nm3) POWER(KW) POWER(KW) 1125.00 2.95 3.07843 300 600 1223.13 N-3500 162,420 200 600 13


79.3495 16 WATER in MATERIAL FAN TEMP-UP 17

Unit Weight W(WB) TW MAT TOT TE('C) 18T/clT (%) ('C) H2O(T/H) 5 190.8400 0.00 88.1 0.000 200.0400 10.00 30.0 0.889 210.1200 7.00 30.0 1.806 221.0000 1.330 30.0 2.695 23

*** 0.00 *** 24 25

O-sepa 26SEPRATOR Roter:D(m) 27

TG dTG DUST N-250 0.78 28('C) ('C) (g/Nm3) N-500 1.11 29

30 *** *** N-1000 1.56 30XX 0 120 N-1250 1.75 31

N-1500 1.92 32( CY = 200 , OS = 150 ) N-2000 2.22 33

TE('C): 4.9 N-2500 2.50 34N-3000 2.74 35N-3500 2.96 36

23.13 N-4000 3.16 378 9 10 11 12

TYPE(Bm3/m)

12 GAS & MATERIAL BALANCE OF CEMENT BALL MILL3 ABC CEMENT PLANT 2004 N= 16,242 N= 146,178 5 T= 30.0 T= 87.3 6 C= 0.312 C= 0.312 78 N= 162,420 50 2509 T= 81.6

10 C= 0.312 11 SEP SEP/DL12 N= 162,420 3078 13 MATERIAL B= 211,374 2365 14 Q= 200.0 v= 404.2 15 T= 78.4 16 C= 0.192 Q= 300.0 Water spray17 T= 92.3 H2O=18 Water in MAT. C= 0.192 T=19 H2O= 2.695 20 T= 30.0 BALL MILL21 %= 1.33% 500022 W=23 N= 26,622 N=24 T= 30.0 25 Heat Value C= 0.312 MILL SIZE D*L:

O-sep 26 net -515,115 Kcal/H PRE GRINDING :(KW) 27 gross 248,913 Kcal/H

28 Tin= 30.0 ( KW * % + 29 Tout= 92.0 HEAT LOSS BM 500030 HEAT LOSS SP 5000

100 31 MATERIAL T * % 32 clinker 88.1*0.84 Gas compornent TOT 33 gypsum 30*0.04 EP inlet 100.00% 34 slug/lime 30*0.12 BF inlet 100.00%

150-250 35 one BF inlet 100.00%200-350 36 one-BF system300-450 37 V(Bm3/m) V-afford Bm3/m P(mmAq)

38 O-sep 3584 N-3500 -17539 SEP FAN 3710 1.078 4000 65040 BF FAN 1022 2.153 2200 30041 KSCC 3800 65042 1600 30043 two-BF system ( BM exhoust NO circulation )44 O-sep 3584 N-3500 -175 45 SEP FAN 3710 1.078 4000 650 46 BF FAN 356 3.371 1200 30047 EP FAN 666 1.652 1100 20048 BF2 FAN 666 1.652 1100 35049 ABC 417 30050 2000 35051

16 17 18 19 2053 ( Saturate TEMPERATURE ) Nm3/Nm3= 0.032029 54 Air Humid(%)= 75 55 T('C)= 30.0 CO2 H2O56 Air % 1.0000 0.0000 0.0000 57 Cold air 16,242 520 58 Hot air 26,622 853 59 H2O in MAT 3,353 3353 60 TOTAL 29,975 0 4,206 61 TOTAL 46,217 0 4,726 62 EP inlet 100.00% 0.00% 14.03%63 BF inlet 100.00% 3.20%64 one BF inlet 100.00% 0.00% 10.23%65 Specific heat value 'C66 EP inlet 92.0 0.000 0.050 67 BF inlet 82.3 0.011 68 one BF inlet 90.3 0.037 6970 < APPROXIMATE EQUATION >71 H=0.0062+0.00032912*T+0.000026518*T^2-0.00000015059*T^3+0.0000000084342*T^472 T=-9.3475+1831.24032730894*H-31474.5301726136*H^2+311439.031040743*H^3-1658132.44374535*H^473 +4661155.60293728*T^5-6425597.4301294*H^6+3379407.89167236*H^774

16 17 18 19 20

GAS & MATERIAL BALANCE OF CEMENT BALL MILL(T/H) ( O-sep ) one-sys

N= 16,242 46,217 N= T= 87.3 90.3 T= C= 0.312 0.312 C=

dust= 1.949 7.9 drop T=200 20 200

-175 -520 50 50 50 -250SEP CY FAN BF FAN

DL BF/DLN= 162,420 (g/Nm3): 172 T= 82.3 (g/Bm3): 129 i(Kcal/Kg)=C= 0.312 dT=

Water spray0.000 H2O= 0.000

30.0 Q= 494.0 Q= 192.1 dust=T= 97.3 T= 92.3 T=

BALL MILL C= 0.192 C= 0.192 C=(KW) 80 50 20

2.695 dust= 5.995 Q= 200.0 3,353 N= 29,975 EP T= 92.2

T= 92.0 BF2 H2O= 0.000 4.8 14.5 C= 0.312

with PG 80 200 20 drop T= 10.0

( KW * % + ( KW + KW ) * %) * % =85 300 600 70 25 = 1,049,200 85 300 600 70 4.4 = 184,659

CO2 H2O SO3 N2 O2 Dew point0.00% 14.03% 0.00% 67.92% 18.05% 53.7 'C0.00% 3.20% 0.00% 76.47% 20.33% 25.7 'C0.00% 10.23% 0.00% 70.92% 18.85% 45.7 'C

Pin Pout T('C) Fn Mn Mo(KW) M-afford-50 -300 80

-600 50 80 0.8 0.96 540.0 1.111 -250 50 80 0.8 0.96 138.9 2.015

600 KW TOTAL POWER(KW)120 KW

( BM exhoust NO circulation )-50 -300 80

-600 50 80 0.8 0.96 540.0 1.111 -250 50 90 0.8 0.96 75.8 1.188 -150 50 100 0.8 0.96 46.5 1.183 -300 50 100 0.8 0.96 80.9 1.113

30 KW TOTAL POER(KW)132 KW

21 22 23 24 25 26 27


12420 3302 10 10020358 5412 20 100

30 1000 20,358 5,412 30 1000 32,778 8,713 40 100

0.00% 67.92% 18.05% 53.7 50 10076.47% 20.33% 25.7 60 100

0.00% 70.92% 18.85% 45.7 70 100Cp 80 100

0.000 0.215 0.056 0.321 90 1000.242 0.063 0.316 0.224 0.059 0.320

H=0.0062+0.00032912*T+0.000026518*T^2-0.00000015059*T^3+0.0000000084342*T^4T=-9.3475+1831.24032730894*H-31474.5301726136*H^2+311439.031040743*H^3-1658132.44374535*H^4 +4661155.60293728*T^5-6425597.4301294*H^6+3379407.89167236*H^7

21 22 23 24 25 26 27

1 12 2

one-sys two-sys 3 346,217 16,242 4 4

80.3 77.3 5 5 <IN>0.312 0.312 6 6 MATERIAL10.0 7 7 MAT.RETURN

50 =dP(mmAq) 8 8 MILL AIR50 9 9 POWER


634.5 13 13 SEP AIR5.0 14 14 TOTAL

15 1516 16 <OUT>

two-sys 17 17 MATERIAL7.944 5.995 18 18 MAT.RETURN

90.3 92.0 19 19 MILL AIR0.192 0.192 20 20 HEAT LOSS

50 21 21 -150 50 22 22 VAPOUR MATERIA

FAN 23 23 WATER24 24 H2O IN MATERIAL

-300 50 25 25 SEP AIR50 26 26 DUST

two-sys 27 27Kcal/H 29,975 28 28 TOTAL

1,049,200 82.0 29 29184,659 0.312 30 30

31 3132 33 3433343536

Motor(KW) PG+BM 37300 38600 39280 40

6180 414243

300 44600 4590 4655 4790 48

6045 495051

28 2953

H2O inAir 54Nm3/Nm3(WB) 550.006200 560.012077 570.023534 580.042706 590.042706 600.073747 610.122841 620.198192 630.310029 640.470608 650.694204 66

6768697071727374

28 29


W or V * * Cp * ( T - 200,000 * * 0.192 * ( 78.4 - 300,000 * * 0.192 * ( 92.3 -

AIR 26,622 * * 0.312 * ( 30.0 -MILL 5,000 * 0.850 * 860.000 * ( -

SEP 900 * 0.700 * 860.000 * ( -H2O 2,695 * * 1.000 * ( 30.0 -H2O 0 * * 1.000 * ( 30.0 -AIR 16,242 * * 0.312 * 30.0

W or V * * Cp * ( T - 192,056 * * 0.192 * ( 92.3 - 300,000 * * 0.192 * ( 92.3 -

AIR 26,622 * * 0.312 * ( 92.0 -MILL 541,800 + 3,655,000 * ( 0.250 -

SEP 541,800 + 3,655,000 * ( 0.044 -H2O 2,695 * * * ( 634.5 -H2O 0 * * * ( 634.5 -H2O 0 * * 1.000 * ( 87.3 -AIR 16,242 * * 0.312 * ( 87.3

MILL 5,995 * 0.192 * ( 92.0 SEP 1,949 * 0.192 * ( 87.3

35 36 37 38 39 40 41 42 43 44

1234

Ts ) = Kcal/H 530.0 ) = 1,855,792 630.0 ) = 3,579,981 730.0 ) = 0 8

) = 3,655,000 9) = 541,800 10

30.0 ) = 0 1130.0 ) = 0 1230.0 = 0 13

9,632,573 1415

Ts ) = Kcal/H 1630.0 ) = 2,291,855 1730.0 ) = 3,579,981 1830.0 ) = 514,888 19

) = 1,049,200 20) = 184,659 21

30.0 ) = 1,629,452 2230.0 ) = 0 2330.0 ) = 0 2430.0 ) = 289,930 2530.0 ) = 71,217 2630.0 ) = 21,391 27

9,632,573 28293031

45 46 47 48 49


REGISTERED NO. : CEM-BB0001 Mr. AAAAAAA 5 <DATA INPUT> ABC CEMENT PLANT6 GRINDING PRE.GRINDING or NOT( 1 or 0 ) : 07 SYSTEM Cyclon or Osep( CY or OS ) : OS89 STADARD TEMPERSTURE : (TS:'C) 30 WATER SPRAY(WS) :

10 SPECFICATION BALL MILL11 DIA(m) LENGTH(m) POWER(KW)12 Mill shell size: 5.2 15.5 650013 KSCC 160 4.4 12.5 370014 GAS SPEED(m/s) POWER(%) HEAT LOSS(%)15 0.82 85 2516 28.6317 CONDITION MATERIAL18 Q(DB) TM CM19 (T/H) ('C) (Kcal/'C)20 CLINKER 168.0 100.0 0.190 21 GYPSUM 8.0 30.0 0.200 22 SLUG/LIME 24.0 30.0 0.200 23 IN 200.0 88.3 0.192 24 OUT 200.0 0.192 25 dT= 10 2627 GAS SPECFICATION BALL MILL 28 TG DUST 29 ('C) (g/Nm3) 30 IN 30.0 *** 31 OUT 100.0 20032 33 CIRCULATION RATIO(MCR) 150 ( CY = 200 , OS = 150 )34 FAN TEMP-UP CALCULATIO dP(mmAq): -550 5035 See Y9 ↑ See Z9 ↑3637 KSCC 160 4.4 12.5 3700(3770)

3 4 5 6 7

41 < LARGE BALL MILL SPEC >42 BM SYSTEM43 KW D(m) L(m) L/D4445 300046 3500 4.3 13.0 3.02 47 3700 4.4 13.0 2.95 48 4000 4.6 13.0 2.83 49 4500 4.6 13.5 2.93 50 5000 4.8 14.5 3.02 51 CS55-8 5500 4.9 15.0 3.06


XX + dT

↑　from Q28:Q29

52 6000 5.0 15.5 3.10 53 6300 5.0 15.8 3.16 54 CS62-8 6500 5.2 15.5 2.98 55 7000 5.3 15.5 2.92 56 SEPAX500 7200 5.4 15.5 2.87 57 7500 5.4 16.0 2.96 58 8000 5.5 16.0 2.91 5960 PG + BM SYSTEM61 CAPA(T/H) PG-SIZE PG(KW) BM(KW)62 120 *** *** 400063 160 180 1350 370064 180 200 1100 430065 200 200 1200 500066 200 220 1400 500067 220 220 1700 580068 240 220 1500 600069 260 220 1700 650070

3 4 5 6 7

PC base MIX base0 0 0

9000 225 253

0 1000 2000 3000 4000 5000 6000 7000 8000 9000 100000

50

100

150

200

250

300

0

253

0

225

f(x) = 0.0304444444444444 x

f(x) = 0.0281111111111111 x

f(x) = 0.025 x

CEMENT MILL SYSTEM

BM

PG+BM

PC base

Linear (PC base)

MIX base

Linear (MIX base)

PG+BM

Linear (PG+BM)

KW

T/H

PC base

MIX base

200T/H x 6,500KW

0 1000 2000 3000 4000 5000 6000 7000 8000 9000 100000

50

100

150

200

250

300

0

253

0

225

f(x) = 0.0304444444444444 x

f(x) = 0.0281111111111111 x

f(x) = 0.025 x

CEMENT MILL SYSTEM

BM

PG+BM

PC base

Linear (PC base)

MIX base

Linear (MIX base)

PG+BM

Linear (PG+BM)

KW

T/H

PC base

MIX base


COPYRIGHT : RYUTA HANAO [ NO COPY.] 6,360 :T/D unit(T/clT) afford BM(T/H) 5265.0 :T/H 1.192 0.633 200 6

No of BM: 1 200 78


KW/T Roter:D(m) V(Kg/Nm3) POWER(KW) POWER(KW) 1132.50 2.95 3.07843 300 600 1223.13 N-3500 162,420 200 600 13


0.97 16 WATER in MATERIAL FAN TEMP-UP 17

Unit Weight W(WB) TW MAT TOT TE('C) 18T/clT (%) ('C) H2O(T/H) 5 190.8400 0.00 100.0 0.000 200.0400 10.00 30.0 0.889 210.1200 10.00 30.0 2.667 221.0000 1.747 30.0 3.556 23

*** 0.00 *** 2425

O-sepa 26SEPRATOR Roter:D(m) 27

TG dTG DUST N-250 0.78 28('C) ('C) (g/Nm3) N-500 1.11 29

30 *** *** N-1000 1.56 30XX 0 0 N-1250 1.75 31

N-1500 1.92 32( CY = 200 , OS = 150 ) N-2000 2.22 33

TE('C): 5.2 N-2500 2.50 34N-3000 2.74 35N-3500 2.96 36

23.13 N-4000 3.16 378 9 10 11 12

4142

rpm Media(T) CAPACITY (T/H) 43raw meal cement 44

76 4514.9 265 90 4614.7 255 95 4714.4 114 4814.0 295 112 4913.9 335 250 123 5013.7 360 280 136 HTNE 51

TYPE(Bm3/m)

13.5 360 150 5214.4 410 300 175 paki:BCL 5313.5 420 167 AKO#2 5413.3 475 180 55

200 ABC/FLS 5613.1 475 375 190 57

205 585960

OS-SIZE OS(KW) TOT(KW) KW/T 613000 160 623500 200 5250 32.81 KSCC 633500 250 5650 31.39 643500 300 6500 32.50 IHI 653500 300 6700 33.50 KHI 664000 330 7830 35.59 FOMOSA 674000 360 7860 32.75 684000 400 8600 33.08 AKO#2 69

708 9 10 11 12

PG+BM0

274

0 1000 2000 3000 4000 5000 6000 7000 8000 9000 100000

50

100

150

200

250

300

0

253

0

225

f(x) = 0.0304444444444444 x

f(x) = 0.0281111111111111 x

f(x) = 0.025 x

CEMENT MILL SYSTEM

BM

PG+BM

PC base

Linear (PC base)

MIX base

Linear (MIX base)

PG+BM

Linear (PG+BM)

KW

T/H

PC base

MIX base

200T/H x 6,500KW

0 1000 2000 3000 4000 5000 6000 7000 8000 9000 100000

50

100

150

200

250

300

0

253

0

225

f(x) = 0.0304444444444444 x

f(x) = 0.0281111111111111 x

f(x) = 0.025 x

CEMENT MILL SYSTEM

BM

PG+BM

PC base

Linear (PC base)

MIX base

Linear (MIX base)

PG+BM

Linear (PG+BM)

KW

T/H

PC base

MIX base

12 GAS & MATERIAL BALANCE OF CEMENT BALL MILL3 ABC CEMENT PLANT 2004 N= 58,471 (36%) N= 68,952 5 T= 30.0 T= 85.0 6 C= 0.312 C= 0.312 78 N= 162,420 509 T= 68.4 -50

10 C= 0.312 B=3600 11 SEP SEP/DL

3.07843 12 N= 162,420 3078 B=3200 13 MATERIAL B= 209,996 2381

2.5 14 Q= 200.0 v= 402 15 T= 88.3 16 C= 0.192 Q= 300.0 Water spray17 T= 90.0 H2O=18 Water in MAT. C= 0.192 T=19 H2O= 3.556 20 T= 30.0 BALL MILL21 %= 1.75% 650022 W=23 N= 30,574 N=

O-sep 24 T= 30.0 (KW) 25 Heat Value C= 0.312 MILL SIZE D*L:

26 net -668,054 Kcal/H PRE GRINDING :27 gross 285,862 Kcal/H28 Tin= 30.0 ( KW * % + 29 Tout= 100.0 HEAT LOSS BM 650030 HEAT LOSS SP 6500

100 31 MATERIAL T * % 32 clinker 100*0.84 Gas compornent TOT 33 gypsum 30*0.04 BF inlet 100.00% 34 slug/lime 30*0.12

150-250 35200-350 36300-450 37 V(Bm3/m) V-afford Bm3/m P(mmAq)

38 O-sep 3560 N-3500 -17539 SEP FAN 3697 1.082 4000 65040 BF FAN #VALUE! #VALUE! 0 041 42 KSCC 3800 65043 KSCC 1600 30044 ABC 3833 70045 ABC 2000 35046

16 17 18 19 2048 ( Saturate TEMPERATURE ) Nm3/Nm3= 0.032029 49 Air Humid(%)= 75 50 T('C)= 30.0 CO2 H2O51 Air % 1.0000 0.0000 0.0000

(NO mill exhoust BF system)

52 Cold air 58,471 1873 53 Hot air 30,574 979 54 Return air 68,952 2208 55 H2O in MAT 4,423 4423 56 TOTAL 162,420 0 9,484 57 BF inlet 100.00% 0.00% 5.84%58 59 Specific heat value 'C60 BF inlet 80.0 0.021 616263 < APPROXIMATE EQUATION >64 H=0.0062+0.00032912*T+0.000026518*T^2-0.00000015059*T^3+0.0000000084342*T^465 T=-9.3475+1831.24032730894*H-31474.5301726136*H^2+311439.031040743*H^3-1658132.44374535*H^466 +4661155.60293728*T^5-6425597.4301294*H^6+3379407.89167236*H^767

16 17 18 19 20

0 1000 2000 3000 4000 5000 6000 7000 8000 9000 100000

50

100

150

200

250

300

0

253

0

225

f(x) = 0.0304444444444444 x

f(x) = 0.0281111111111111 x

f(x) = 0.025 x

CEMENT MILL SYSTEM

BM

PG+BM

PC base

Linear (PC base)

MIX base

Linear (MIX base)

PG+BM

Linear (PG+BM)

KW

T/H

PC base

MIX base

0 1000 2000 3000 4000 5000 6000 7000 8000 9000 100000

50

100

150

200

250

300

0

253

0

225

f(x) = 0.0304444444444444 x

f(x) = 0.0281111111111111 x

f(x) = 0.025 x

CEMENT MILL SYSTEM

BM

PG+BM

PC base

Linear (PC base)

MIX base

Linear (MIX base)

PG+BM

Linear (PG+BM)

KW

T/H

PC base

MIX base

GAS & MATERIAL BALANCE OF CEMENT BALL MILL(T/H) ( O-sep )(42%) N= 68,952 N=

T= 85.0 T= C= 0.312 C=

250 30 200 20

-175 -330 -550 50SEP BF FAN

N= 162,420 T= 80.0 i(Kcal/Kg)=C= 0.312 dT=

Water spray0.000

30.0 Q= 493.0 T= 103.0

BALL MILL C= 0.192 (KW)

3.556 V(m/s) dust= 6.999 Q= 200.0 4,423 0.82 N= 34,997 (22%) T= 90.0

T= 100.0 H2O= 0.000 5.2 15.5 C= 0.312

NON

( KW * % + ( KW + KW ) * %) * % =85 300 600 70 25 = 1,323,325 85 300 600 70 4.4 = 232,905

CO2 H2O SO3 N2 O2 Dew point0.00% 5.84% 0.00% 74.39% 19.77% 35.9 'C

TOTAL POWER(KW)Pin Pout T('C) Fn Mn Mo(KW) M-afford

-50 -300 80-600 50 80 0.8 0.96 540.0 1.111

0 0 0 0.8 0.96 0.0 #DIV/0!

21 22 23 24 25 26 27


44713 11886 10 10023380 6215 20 100

52727 14016 30 10030 100

0 120,820 32,117 40 1000.00% 74.39% 19.77% 35.9 50 100

60 100Cp 70 100

0.235 0.061 0.317 80 10090 100

H=0.0062+0.00032912*T+0.000026518*T^2-0.00000015059*T^3+0.0000000084342*T^4T=-9.3475+1831.24032730894*H-31474.5301726136*H^2+311439.031040743*H^3-1658132.44374535*H^4 +4661155.60293728*T^5-6425597.4301294*H^6+3379407.89167236*H^7

21 22 23 24 25 26 27

1 12 23 3

93,469 4 485.0 5 5 <IN>

0.312 6 6 MATERIAL 7 7 MAT.RETURN

50 =dP(mmAq) 8 8 MILL AIR9 9 POWER


637.8 13 13 SEP AIR5.0 14 14 TOTAL

15 1516 16 <OUT>17 17 MATERIAL18 18 MAT.RETURN19 19 MILL AIR20 20 HEAT LOSS

21 21 22 22 VAPOUR MATERIA

23 23 WATER 24 24 H2O IN MATERIAL

25 25 SEP AIR26 26 DUST27 27

Kcal/H 28 28 TOTAL1,323,325 29 29

232,905 30 3031 3132 33 34333435

7400 36Motor(KW) 37

300 38600 39

0 4041

600 42120 43

6030 44132 45

4628 29

48H2O inAir 49Nm3/Nm3(WB) 500.006200 51

0.012077 520.023534 530.042706 540.042706 550.073747 560.122841 570.198192 580.310029 590.470608 600.694204 61

626364656667

28 29


W or V * * Cp * ( T - 200,000 * * 0.192 * ( 88.3 - 300,000 * * 0.192 * ( 90.0 -

AIR 30,574 * * 0.312 * ( 30.0 -MILL 6,500 * 0.850 * 860.000 * ( -

SEP 900 * 0.700 * 860.000 * ( -H2O 3,556 * * 1.000 * ( 30.0 -H2O 0 * * 1.000 * ( 30.0 -AIR 58,471 * * 0.312 * 30.0

W or V * * Cp * ( T - 193,001 * * 0.192 * ( 90.0 - 300,000 * * 0.192 * ( 90.0 -

AIR 30,574 * * 0.312 * ( 85.0 -MILL 541,800 + 4,751,500 * ( 0.250 -

SEP 541,800 + 4,751,500 * ( 0.044 -H2O 3,556 * * * ( 637.8 -H2O 0 * * * ( 637.8 -H2O 0 * * 1.000 * ( 85.0 -AIR 58,471 * * 0.312 * ( 85.0

MILL 6,999 * 0.192 * ( 90.0 SEP 0 * 0.192 * ( 85.0

35 36 37 38 39 40 41 42 43 44

1234

Ts ) = Kcal/H A-maker 530.0 ) = 2,234,400 2,234 630.0 ) = 3,446,885 0 730.0 ) = 0 8

) = 4,751,500 5,293 9) = 541,800 10

30.0 ) = 0 1130.0 ) = 0 0 1230.0 = 0 0 13

10,974,585 7,528 1415

Ts ) = Kcal/H 1630.0 ) = 2,217,502 2,285 1730.0 ) = 3,446,885 0 1830.0 ) = 524,336 524 19

) = 1,323,325 1,556 20) = 232,905 21

30.0 ) = 2,161,067 2,161 2230.0 ) = 0 2330.0 ) = 0 2430.0 ) = 1,001,555 1,002 2530.0 ) = 67,010 2630.0 ) = 0 27

10,974,585 7,528 28293031

45 46 47 48 49

12 HEAT BALANCE OF PRE-GRINDING MILL345 <IN> W or V * * Cp * ( T - Ts ) = Kcal/H6 MATERIAL 168,000 * * 0.190 * ( 90.0 - 30.0 ) = 1,915,200 7 MAT.RETURN 50,400 * * 0.190 * ( 89.3 - 30.0 ) = 568,099 8 MILL AIR AIR 11,315 * * 0.312 * ( 30.0 - 30.0 ) = 0 9 POWER MILL 1,200 * 0.800 * 860.000 * ( - ) = 825,600

10 SEP 0 * 0.000 * 860.000 * ( - ) = 0 11 H2O IN MATERIAL H2O 0 * * 1.000 * ( 0.0 - 30.0 ) = 0 12 WATER H2O 0 * * 1.000 * ( 30.0 - 30.0 ) = 0 13 SEP AIR AIR 14,400 * * 0.312 * 30.0 30.0 = 0 14 TOTAL 3,308,899 1516 <OUT> W or V * * Cp * ( T - Ts ) = Kcal/H17 MATERIAL 166,149 * * 0.190 * ( 89.3 - 30.0 ) = 1,872,795 18 MAT.RETURN 50,400 * * 0.190 * ( 89.3 - 30.0 ) = 568,099 19 MILL AIR AIR 11,315 * * 0.312 * ( 90.7 - 30.0 ) = 214,075 20 HEAT LOSS MILL 0 + 825,600 * ( 0.500 - ) = 412,800 21 SEP 0 + 825,600 * ( 0.000 - ) = 0 22 VAPOUR MATERIA H2O 0 * * * ( 634.0 - 30.0 ) = 0 23 WATER H2O 0 * * * ( 634.0 - 30.0 ) = 0 24 H2O IN MATERIAL H2O 0 * * 1.000 * ( 89.3 - 30.0 ) = 0 25 SEP AIR AIR 14,400 * * 0.312 * ( 79.3 30.0 ) = 221,342 26 DUST MILL 1,131 * 0.190 * ( 90.7 30.0 ) = 13,039 27 SEP 720 * 0.190 * ( 79.3 30.0 ) = 6,748 28 TOTAL 3,308,899 293031

33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48

1234

A-maker 51,915 6

0 78

826 91011

0 120 13

2,741 141516

1,886 170 18

214 19413 20

210 22

2324

228 252627

2,741 28293031

49

12 HEAT BALANCE OF COAL VERTICAL MILL345 <IN> W or V * * Cp * ( T - Ts ) =6 INLET GAS GAS 88,260 * * 0.315 * ( 307.5 - 30.0 ) =7 DUST DUST 88,260 * 0.050 * 0.207 * ( 307.5 - 30.0 ) =8 LEAK AIR VM VM 28,935 * * 0.312 * ( 30.0 - 30.0 ) =9 BF BF 13,404 * * 0.312 * ( 30.0 - 30.0 ) =

10 RAW MATERIAL 45,000 * * 0.250 * ( 20.0 - 30.0 ) =11 H2O IN MATERIAL H2O 9,878 * * 1.000 * ( 20.0 - 30.0 ) =12 CIRCULATION AI AIR 0 * * 0.312 * ( 83.3 - 30.0 ) =13 GRAINDING HEAT 1,050 * 0.900 * 860 * ( 1.0 ) =14 FAN HEAT 1,000 * 0.700 * 860 * ( 1.0 ) =15 TOTAL =1617 <OUT> W or V * * Cp * ( T - Ts ) =18 OUTLET GAS GAS 88,260 * * * ( 75.3 - 30.0 ) =19 DUST DUST 88,260 * 0.050 * 0.184 * ( 75.3 - 30.0 ) =20 LEAK AIR VM VM 28,935 * * 0.312 * ( 75.3 - 30.0 ) =21 BF BF 13,404 * * 0.312 * ( 75.3 - 30.0 ) =22 MATERIAL 45,000 * * 0.250 * ( 75.3 - 30.0 ) =23 H2O IN MATERIAL H2O 455 * * 1.000 * ( 75.3 - 30.0 ) =24 CIRCULATION AI AIR 0 * * 0.312 * ( 83.3 - 30.0 ) =25 VAPOUR H2O 9,424 * * 1.000 * ( 627.7 - 30.0 ) =26 HEAT LOSS VM 1,050 * 0.900 * 860 * ( 0.8 ) =27 HEAT LOSS FAN 1,000 * 0.700 * 860 * ( 0.8 ) =28 TOTAL =293031

33 34 35 36 37 38 39 40 41 42 43 44 45 46 47

1234

Kcal/H A-maker 57,719,782 7,973 6

253,330 70 80 9

-112,500 -211 10-98,780 11

3 0 12812,700 1,415 13602,000 14

9,176,534 9,177 1516

Kcal/H 171,246,777 1,882 18

36,822 19408,743 20189,341 21509,625 530 2220,591 23

3 0 245,632,872 5,633 25

650,160 1,132 26481,600 27

9,176,534 9,177 28293031

48 49

RAW MATERIAL MIXTURE CALCULATION

6 <INPUT DATA> ABC CEMENT PLANT7 MAIN RAW MATERIAL NO. 4 ADDITIVE: 0 RAW MATERIAL LOSS (LS:%)89 COMPOSITION SiO2 Al2O3 Fe2O3 CaO MgO SO3 R2O OTHER Ig.Loss

10 * LIME 3.90 0.22 0.26 48.64 4.12 0.01 0.03 0.03 42.67 11 * CLAY 64.52 16.45 8.86 0.43 0.60 0.01 1.90 0.70 5.87 12 * IRON 26.36 11.27 54.01 0.10 0.12 0.01 1.30 0.41 7.21 13 * SAND 94.70 0.89 3.07 0.04 0.02 0.01 0.07 0.05 0.64 14 MAGN15 +16 ADDITIV ADTV-mix17 :ABC SPEC18 FUEL COAL 60.00 25.99 7.96 0.20 0.73 0.10 3.25 0.88 0.00 19 FUEL COAL COAL ASH20 MODULUS CLINKER HM SM IM MG(%) W1(Kg/T-cl) W2(%)21 2.09 2.65 1.4 1.7 110.439 16.72223 <OUTPUT DATA>24 L(n,1) L(n,2) L(n,3) L(n,4) L(n,5) L(n,6) L(n,7) L(n,8) L(n,9)25 RAW MAT. MIXTURE SiO2 Al2O3 Fe2O3 CaO MgO SO3 R2O OTHER Ig.Loss26 * LIME 5.06 0.29 0.34 63.05 5.34 0.01 0.04 0.04 55.31 27 * CLAY 15.23 3.88 2.09 0.10 0.14 0.00 0.45 0.17 1.39 28 * IRON 0.42 0.18 0.87 0.00 0.00 0.00 0.02 0.01 0.12 29 * SAND 0.13 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 30 MAGN31 ADTV-mix 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 32 n=8 sub-T 20.83 4.35 3.30 63.15 5.48 0.02 0.51 0.21 56.81 33 COAL 1.11 0.48 0.15 0.00 0.01 0.00 0.06 0.02 0.00 34 TOTAL 21.94 4.83 3.45 63.16 5.50 0.02 0.57 0.23 56.81 3536 n=9 CLINKER 21.94 4.83 3.45 63.16 5.50 0.02 0.57 0.23 3738 2.6-2.8 1.4-1.8 94-9639 HM SM IM AI LSF(BS) CLINKER OXIDE(%)40 RAW MIX MODULUS 2.217 2.722 1.317 4.789 0.9625 C3S C2S41 CLINKER MODULUS 2.090 2.650 1.400 4.543 0.9104 52.94 22.96 42 See at E18:G18 → 2.090 2.650 1.400 *** 43 ABC SPEC: *** 2.7 1.6 96 65.83 12.8344 UNIT CONSUMPTION LIME CLAY IRON SAND MANG ADTV TOTAL LIQUID PHASE RATIO(%)45 DRY BASE 1.2947 0.2344 0.01625 0.00133 0.0000 1.5467 46 WET BASE 1.3446 0.3168 0.01806 0.00179 0.0000 0.0000 1.6812 47 LOSS OF RAW MATERIALE(%) : 0.00 H2O: 0.1345 48 H2O(%): 8.00%49 MAIN RAW MATERIAL NO. 4 ADDITIVE: 0 RAW MATERIAL LOSS (LS:%)50 ( 0:non or 1 )51 DRY BASE % 0.8371 0.1516 0.0105 0.0009 0.0000 0.0000 1.0000 52 ( for reference )53 'RAW MIX MODULUS54 1370 RHM = L(8, 4) / (L(8, 1) + L(8, 2) + L(8, 3))55 1380 RSM = L(8, 1) / (L(8, 2) + L(8, 3))56 1390 RIM = L(8, 2) / L(8, 3)57 1400 RAI = L(8, 1) / L(8, 2)58 1410 RLSF(K) = L(8, 4) / (2.8 * L(8, 1) + 1.18 * L(8, 2) + 0.65 * L(8, 3)) :BS(raw mix)59 'CLINCAR MODULUS60 1430 CHM = L(9, 4) / (L(9, 1) + L(9, 2) + L(9, 3))61 1440 CSM = L(9, 1) / (L(9, 2) + L(9, 3))62 1450 CIM = L(9, 2) / L(9, 3)63 1460 CAI = L(9, 1) / L(9, 2)64 1470 CLSF(K) = L(9, 4) / (2.8 * L(9, 1) + 1.18 * L(9, 2) + 0.65 * L(9, 3)) :BS(raw mix)65 'MINERAL COMPOSITION66 1480 C3S = (4.071 * L(9, 4)) - (7.6 * L(9, 1)) - (6.718 * L(9, 2)) - (1.43 * L(9, 3)) _67 - (2.852 * L(9, 6))68 1490 C2S = (2.867 * L(9, 1)) - (0.7544 * C3S)69 1500 C3A = (2.65 * L(9, 2)) - (1.692 * L(9, 3)) : C4AF = 3.043 * L(9, 3)70 'LIQUID PHASE RATIO71 LPR= 6.10*F + M + R (A/F>=1.38)72 LPR= 8.20*A - 5.22*F + M + R (A/F<=1.38)73 LPR= 2.95*A + 2.20*F + M + R74 LPR= 3.00*A + 2.25*F + M + R R= K + N75

20 21 22 23 24 25 26 27 28 29 30

　　　TCVN 2682-1999　：

1338ﾟC1338ﾟC1400ﾟC1450ﾟC

60 7

8TOTAL H2O 9

99.88 3.71 1099.34 26.00 11

100.79 10.00 1299.49 26.00 13

14151617

99.11 0.00 18 COAL ASH 19

(Kg/T-cl) 200.0184 21

2223

L(n,10) 24TOTAL H2O 25

129.47 3.71 2623.44 26.00 27

1.63 10.00 280.13 26.00 29

300.00 8.00 31

154.67 0.00 321.83 33

156.50 3435

99.68 363738

CLINKER OXIDE(%) 39C3A C4AF 40

6.96 10.50 41 42

7.9 9.44 43LIQUID PHASE RATIO(%) 44

27.1 4527.9 4628.3 47

480 49

505152535455565758596061626364

6566676869707172737475

31 32

1338ﾟC1400ﾟC1450ﾟC

1 note: This sheet linkes with ABCcConveyer-DATA.2 1 2 3 4 5 6 7 8 9 10 1 2 334 SPECIFICATION OF CONVEYOR, BAG FILTER/FAN and AS/BLOWER, and LARGE FAN note:5 ( excluded : majour machinary, duct damper, miscellaneous and piping material )6 CODE Section NO MATERIAL Q W L H speed Mo Accesary NO V area7 main BC BE EF FC RV AS T/H(WB) m m m,deg m/min KW BF m3/min m28 03 Limestone crushing 03SS101 limestone 115 :m3 6*6.5*69 03 vibration feeder 03VF101 limestone 1150 1.8 7 5' 55 03BF101 600.0 360

10 03 1500->350 first crusher 03CR101 limestone 950 *** *** *** *** 220*2 25T OH.crane 03HO101/10211 03 03BC101 limestone 1150 1.4 24.5 1.5 79 22 mag.sepa 03MG10112 03 03BC102 limestone 1150 1.4 42.2 11.3 88 75 03BF102 1250.0 80013 03 vibrating screen 03VS101 limestone 1150 2 5 15' 3014 03 350-80 second crusher 03CR102 limestone 1100 *** *** *** *** 85015 03 03BC103 limestone 1150 1.4 26 0 78 15 b.scale 03SB101 03BF103 100.0 6016 03 03BC104 limestone 1150 0.8 3001.5 -13 40/270 160*217 03 03BC105 limestone 1150 1.2 300 9 109 9018 03 Limestone transport 19 03 & storage stacker 03PM101 limestone 1150 7.5*2+1.5*220 03 03BC1 limestone 1150 1.2 22 9 5521 03 limestone22 03 46*240*11 storage 27*106*9.45 limestone 16000*223 03 27*27*9.45 blackstone 2400*124 03 reclaimer 03PM102 limestone 500 32 11,5.5,7.5*325 03 03PM1 limestone 500 1.8*0.5 31 0 7526 03 03BC106 limestone 500 0.8 340.2 10 112 45 b.scale 03SB102 03BF104 60.0 4527 03 03BC107 limestone 500 0.8 162 11 112 3728 03 limestone29 04 Shale crushing 04SS101 clay 55 :m3 5*5*5 (15')30 04 apron: 04FE101 clay 350 1.7 6.5 1.5 30+2.2 mag.sepa 04MG101 04BF101 250.0 15031 04 800-80 crusher 04CR101 clay 300 *** *** *** *** 110+90 15T OH.crane 04HO10132 04 04BC101 clay 350 1 11.3 0 57 5.5 b.scale 04SB101 04BF102 60.0 4533 04 04BC102 clay 350 0.8 117.7 11.5 94 3034 04 04BC103 clay 350 0.8 78.7 9.15 95 2235 05 04BC104 clay 350 1 6.5 0 57 5.536 06 04BC105 clay 350 0.8 63.5 0 92 7.537 04 Shale transport stacker 04ST101/102 300->350 clay 350 3*4,0.37*238 04 & stacking 04BC1 300->350 clay 350 0.8 11.2 0 92 5.539 04 04BC2 300->350 clay 350 0.8 9.2 0 92 5.5 b.scale 04SB10240 04 44.8*110*14 storage 19.4*50 clay 8000*241 04 reclaimer 04PM103 clay 150 3*2,7.5,3,1.5*342 04 04PM1 clay 150 0.7 15 9 28 3743 04 04BC106 clay 150 0.65 212.5 12 62 1544 05 Additive unloading 05SU101 raw coal 350 200-300Tbarge, 5000-7000DWTship 110*2,55,22 45 05 & Cement&Clinker loading 05SS101 raw coal 75 :m3 5*5.5*5.546 05 200> apron: 05FE101 raw coal 350 1 6.5 0 8.6 22 mag.sepa 05MG10147 05 05BC101 raw coal 350 0.8 173 2.4 113 18.5 b.scale 05SB101 05BF101 170.0 13048 05 raw coal 05FE102 raw coal 350 1 2.5 6' 2.2*2 05BF102 100.0 8049 05 cement 900 05BC102' cement 900 1.2 4517 2.5 40/60/130 200*3,30 water tank 05SS10250 05 clinker 600 05BC102'' clinker 600 1.2 4517 2.5 40/60/130 200*3,30 20m3*2 05SS10351 05 diatmite additive 350 05BC102 raw coal 350 1.2 4517 2.5 40/60/130 200*3,30 water pump 05WP101 05BF103 70.0 6052 05 gypsum 05BC103 raw coal 350 1 11.7 1.2 71 7.5 14&9m3/h 05WP102 05BF104 70.0 6053 05 silica stacker 05BC104 raw coal 350 0.8 290.5 20.9 114 5554 06 iron ore 05BC1 raw coal 350 1 5.5 0 70 5.555 05 Additive crushing 05SS106 additive 50 :m3 5*5*5 (10')56 05 200->25 apron: 05FE103 additive 350 1.2 6.5 1 7.2 30+5.5 damper 05GA201 05BF105 250.0 18057 05 crusher 05CR101 additive 300 110*2 b.scale 05SB10258 05 05BC105 additive 350 1 11.3 0 52 5.5 10T E hoist 05CR10159 05 stacker 05BC106 additive 350 0.8 468 21.1 85 7560 05 05BC2 additive 350 1 5.5 0 52 5.561 05 mag.sepa 05MG10262 0563 05 storage 54.5*140*12 coal, silica, laterite 5000*2, 3000*2, 5000*164 05 coal, gypsum, additive, limestone 4000*2, 3500*2, 5000*1, 1000*165 05 Additive storage reclaimer 05PM201 raw coal 200 3,1.5,7.1,5.566 05 raw coal 05PM2 raw coal 200 0.9 19.6 3 3767 05 gypsum 05BC201 raw coal 200 0.65 280 7.5 102 18.5 b.scale 05SB20168 05 additive 05BC202 gypsum 200 0.65 170.5 29 79 3069 05 05BC203 gypsum 200 0.8 10.15 0 48 3.7 05BF201 50.0 3870 05 reclaimer 05PM301 raw coal 200 3,1.5,7.1,5.5 05BF202 50.0 3871 05 05PM3 raw coal 200 0.9 19.6 3 3772 05 silica 05BC301 silica 200 0.65 266 2.5 76 15 05BF301 50.0 38

WF BB PC SC

73 05 laterite 05BC302 silica 200 0.65 139.65 20.5 79 1.1 b.scale 05SB301 05BF302 50.0 3874 05 05BC303 silica 200 0.8 4 0 48 2.2 mag.sepa 05MG301 05BF303 60.0 4575 05 raw coal 05BC304 raw coal 200 0.8 103.7 2 65 7.5 metal de. 05MG301 05BF304 60.0 4576 05 05BC305 raw coal 200 0.8 16.7 2.2 66 5.5 05BF305 60.0 4577 05 05BC306 raw coal 200 0.8 84.2 13.2 68 1578 05 05BC307 raw coal 200 0.8 79 21 72 22 damper 05GA30179 05 80 05

81 06 Raw mat. dosing limestone 06SS104 limestone 500 7.6*7.6*12.2 06BF104 50.0 3082 06 06WF104 limestone 500 1.8 5 *** *** 18.583 06 iron 06SS103 iron ore 130 3.2*5.85*12.2 VM:2.2*2 06BF103 50.0 3084 06 06WF103 1.5->1.4 iron ore 20 1.4 5 *** *** 5.585 06 silica 06SS101 silica 150 3.9*5.85*12.2 VM:2.2*286 06 apron: 06FE101 1.5->1.0 silica 4 1 2.5 0 8 7.5 06BF101 50.0 3087 06 06WF101 40->4 1.5->1.4 silica 4 1.4 5 *** *** 3.7 5T hoist 06HO10188 06 shale 06SS102 clay 200 5.1*5.85*12.2 VM:2.2*2 damper 06GA10189 06 apron: 06FE102 1.5->1.0 clay 150 1 2.5 0 8 7.5 mag.sepa 06MG101 06BF102 50.0 3090 06 06WF102 80->150 1.5->1.4 clay 150 1.4 5 *** *** 1.5 m.detect 06MD10191 06 hoist 06HO10292 06 06BC101 limestone 600 1.05 126.1 25.5 84 75 06BF105 160.0 11593 06 06BC102 limestone 750 1.2 9.2 0 71 1194 06 Raw mat. grinding triple gate 06RV101 limestone 750 65T OH.crane 06HO10195 06 vertical mill 06RM101 limestone 500 :ATOX52.5 4500 2w.damper 06GA10296 06 vibration feeder 06FE103 limestone 150 3.7 air damper 06DA10197 06 limestone air damper 06DA10698 06 06BC103 limestone 150 0.6 11.5 1.5 64 5.5 air damper 06DA102 06BF106 200.0 14099 06 06BE101 limestone 150 *** *** 38 *** 30+3.7 air damper 06DA104

100 06 Bm3/H 1020000 cyclon 06CY101-104 raw meal 500 5.6*16*4 *** *** *** *** air damper 06DA105101 06 4250*4 06RV101-104 raw meal 150 *** *** *** 3 06BF107 100.0 68102 06 06AS101 raw meal 300 0.508 8 7 *** *** water tank 06WT101103 06 06AS102 raw meal 300 0.508 8 7 *** *** water spray 06WP102/103104 06 0.763->.7 06AS103 raw meal 600 0.736 21 7 *** *** 25m3/H105 06 Bm3/H 1020000 mill fan 06FA103 raw meal 17000.0 106 06 gas chamber 06SS105 raw meal 6.5*16.5 m.detect 06MD102107 06 06RV107 raw meal 30 3.7 air damper 06DA107108 06 396600 GCT 06ST101 raw meal 30 :t/h 9.5*30 75*2 mag.sepa 06MG103109 06 06AC101-103 raw meal 22.5110 06 06SC101 raw meal 11 3.6 7.5 slide gate 06GA103/104111 06 06RV108 raw meal 11 1.1 flap.damper 06GA109112 06 Nm3/H 453000 EP 06EP101 raw meal 7500 :m2*2 0.8m/s113 06 400000 06FC101/102 raw meal 10 0.15 20 4114 06 80/150 06RV105/106 raw meal 20 4115 06 06FC103 raw meal 50 0.27 37.5 5 17 11116 06 06FC104 raw meal 50 0.27 10 5 22 5.5 louver dam 06DA108117 06 06FC105 raw meal 50 0.27 25 0 34 37118 06 raw meal119 06 Bm3/H 720000 EP fan 06FA104 raw meal sampling 06SA101 12000.0 120 06 80/150 chimney 06SK101 raw meal 4.66*105 *** *** *** ***121 06 raw meal 5T hoist 06HO102122 06 06BB102 raw meal 600 1.39 0 70 200+11123 06 0.6->0.7 06AS104 raw meal 600 0.65 11.5 7 124 06 distibution box 06AS105 raw meal 600 *** *** 125 06 10mAS*4 06AS1 raw meal 600 0.7 8 7 12.0 126 06 raw meal 6+2127 07 Raw meal blending silo 07SS101 raw meal 20000*1 25*39*65 07BF101 350.0 (240)128 07 homogenizing aearation unit 07AE101 raw meal :m2 gate 07GA101/102 129 07 outlet gate raw meal :unit 6.7 130 07 raw meal 20.8 131 07 Kiln feeding cont.gate 07RV101/102 raw meal 500 *** *** flow gate 07RV101/102132 07 feed bin 07SS102 raw meal 140 :m3 5*7 *** ***133 07 cont.gate 07RV103/104 raw meal flow gate 07RV103 134 07 flow meter 07IF101 raw meal 500 *** *** *** ***135 07 raw meal 136 07 0.5->0.65 07AS101 raw meal 500 0.5 20 7 *** *** sampling 07SA101 20.0 137 07 07BB101 raw meal 500 0 58 *** 132+5.5 2T hoist 07HO101138 07 07BB102 raw meal 500 0 53 132+5.5139 07 raw meal 3T hoist 07HO121 07BF102 250.0 153140 07 0.5->0.65 07AS102 raw meal 500 0.5 5 7 3T hoist 07HO103 15.0

141 07 distribution box 07DI101 raw meal 250*2 2w gate 07GA105 142 07 0.5->0.65 07AS103 raw meal 500 0.5 5 7 flow gate 07RV105/106 143 07 0.5->0.65 07AS104 raw meal 500 0.5 15 7 25.0 144 07 07RV107 raw meal 200 7.5145 07 07RV108 raw meal 300 7.5 07BF103 100.0 84146 07147 07148 08 NSP & Rotary kiln NSP 08SP101 250.0 *** *** *** *** ***149 08 K-IDF 08FA101 TOWER 26*17*97 2w damper 08GA101/102 6700.0 150 08 max: C-IDF 08FA102 aux damper 08DA101/102 8700.0 151 08 6000 T/H152 08 6360 T/H air blaster 08AC101153 08 60/40 calciner 08MF101 6.2*37.6 Fluid. Bed=16.61 m2 water gan 08WP102154 08 22T/H burner 08BU101 30.0 T/H 27.65 155 08 3T elevator 08PE101156 08 KILN 08RK101 2-3 support,4%, 3.5-0.2rpm 5.2*82 820 ev tower 08TW102157 08 08RG101/102 790-27.6, 970-54.96rpm 100 air damper 08DA103 shell cooling158 08 lub unit 08LP101/102 10T hoist 08HO101 shell cooling159 08 lub unit 08LP103-106 *4 sealing fan160 08 lub unit 08LP107/108 lining 08RF101/102 shell cooling161 08 13T/H burner 08BU102 OIL 10 T/H 7.374 lining 08RF103/104 kiln burner162 08 (1-15TT/H) COAL 15 T/H 11.774 lining 08RF105/106163 08 lining 08RF107164 08 Clinker cooler AQC 08CC101 1370->65+amb., Area=138.8m2 *** *** 75*5 580.0 165 08 6000 T/H <1.7Nm3/clKg, AQC eff>72% 720.0 166 08 max: 6360 T/H FAN eff>78% 720.0 167 08 crusher 110 lining 08RF108 720.0 168 08 65'C+env.temp 22 720.0 169 08 1.8 Nm3/clKg 37*2 1425.0 170 08 1235.0 171 08 1140.0 172 08 sampling 08SA101 1140.0 173 08174 08 water spray 08WP101 water pump175 08176 08 Nm3/H 315000 EP 08EP101 clinker 350(max400)'C, <0.9m/s177 08 08RV101-104 clinker 18 0.75178 08 08FC101 clinker 18 0.3 19.5 2.2 lining 08RF109 08BF501 200.0 119179 08 08FC102 clinker 18 0.3 19.5 2.2 08BF502/503 250.0 305180 08 08FC103 clinker 25 0.27 10.1 3.7 08BF504 100.0 59181 08 08FC104/105 clinker 25 0.27 10.1 0.665 3.7 　　182 08 Bm3/H 750000 AQC EPfan 08FA120 clinker 250(max400)'C, eff>78% 12500.0 183 08 chimney 08SK101 clinker 3.8*35184 08 08PC501 clinker 400 1.2 92.68 55.85 *** 110 3w.damper 08GA501185 08 08PC502 clinker 400 1.2 41 0 15 3T hoist 08HO501186 08187 09 Off-clinker silo silo 09SS101 clinker 2000 12*17.5*25 G. damper 09GA101188 09 telescopic chute 09TC101 clinker 100 G. damper 09GA102189 09 clinker190 09 09SS102 clinker 10 :m3 3*3*4191 09 09BC101 clinker 300 0.8 8 1.5 72 5.5192 09193 09 Crinker transport silo 09SS201/301 clinker 40000*2 35*38*45.5 flow gate:150T/H*7 *** G. damper 09GA201-210194 09 09BC201/202 clinker 300 0.8 29.5 0 70 5.5 G. damper 09GA301-310 09BF201/301 300.0 300195 09 09BC301/302 clinker 300 0.8 29.5 0 70 5.5 6*2w damper 09GA208-310196 09 09BC203/303 clinker 400 0.8 34 0 90 7.5 09BF302 300.0 300197 09 clinker198 09 09BC102 clinker 300 0.8 123.7 4.25 70 15 09BF101-104 70.0 50199 09 09BE101 clinker 300 1 0 36 82 75+3 2T hoist 09HO101 200 09 09BC103 clinker 600 0.8 172.3 5 130 37201 09 09BC104 clinker 600 1.2 368.5 5 150 90202 09 09BC104' cement 900 1.2 368.5 5 150 90 09BF105 400.0 400

203 09 09BE102 clinker 600 0 18 82 90+3204 09 09BE102' cement 900 0 18 82 90+3 2T hoist 09HO102 09BF106 70.0 50205 09 loader 09SL101 09BC1 clinker 600 1.2 10 0 150 18.5 09BF107 150.0 80206 09 09BC1' cement 900 1.2 10 0 150 18.5207 10 Cement dosing Clinker 10SS101 Clinker 300 9*7*9.6 load cell*1208 10 10WF101 Clinker 250 1.4 5.2 *** 20 15209 10 Gypsum 10SS301 Gypsum 150 7*5.5*9.6 2w damper 10GA101 10BF101 50.0 45210 10 10WF301 Gypsum 20 0.6 4.5 *** *** 3.7 10BF201 50.0 45211 10 Additive 10SS201 additive 200 57*7*9.6 10BF301 50.0 45212 10 apron: 10FE101 additive 80 1 2.5 7.5 mag.sepa 10MG101213 10 10WF201 0.75->0.8 additive 80 0.8 3 *** 24 7.5 m.detect 10MG102 10BF102 200.0 120214 10 2w damper 10GA102215 10 10BC101 Clinker 300 0.9 23 4 55 11 216 10 Pre grinder pregrinder 10PG101 Clinker 200 :CKP-200 equivalent 1200 12.5T hoist 10HO101 10BF103 600.0 500217 10 10BE101 Clinker 450 0.63 0 23 24 55+7.5 3.2T hoist 10HO102218 10 10BC102 Clinker 300 0.9 32 0 52 5.5 Class.damper 10GA103219 10 10BC103 Clinker 100 0.75 10 0 26 1.5220 10221 10 Cement mill Cement mill 10FM101 cement 200 <90'C 3600Blaine *** *** 5000 2w valve 10GA104222 10 lub unit 10LP101-103 *3 cement223 10 gear reducer 10GR102 224 10 grinding medea 10GM101 225 10 water spray 10WS101 cement water tank 10SS104 2m3226 10 cement 2T hoist 10HO103227 10 10AS101 cement 650 0.65 6 18 *** 50T OH.crane 10HO101 10.0 228 10 10BE102 cement 650 0 45 132+7.5 4T hoist 10HO104 10BF104 2000.0 1700229 10 10AS102 cement 650 0.65 20 18 *** *** 36.0 230 10 10AS103 cement 450 0.55 6 18 *** ***231 10 10AS104 cement 220 0.4 15 8 *** *** m.detect 10MT101232 10 10AS105 cement 220 0.4 50 8 *** damper 10GA104 233 10 vibrating screen 10VS101 cement 10 flow meter 10IF101234 10 Bm3/H 210000 O-SEP 10SE101 cement 200 :N-3500 650T/H 300 air dampr 10DA103 material trap235 10 air dampr 10DA104236 10 cement 10BF105/106 300.0 180237 10 cement air valve 10DA105238 10 cement air valve 10DA107239 10 Bm3/H 240000 O-SEP fan 10FA105/106 cement eff>80% (112)240 10 cement241 10 Nm3/H 33000 EP 10EP101 cement 3000 :m2 3 chamber 20mmAq 2w damper 10GA107242 10 120000 fan 10FA104 cement eff>80% sampling 10SA101 900.0 243 10 chimney 10SK101 cement 3*43 2T hoist 10HO105244 10 10SC103 cement 30 0.4 11 15 2w damper 10GA106245 10 10RV103 cement 30 0.4 0.35 2.2 3T hoist 10HO107246 10 10BB103 cement 220 0 49.4 90 75 2T hoist 10HO108247 10 10AS106 cement 220 0.4 15 8 insulating 10RF101248 10 10AS107 cement 220 0.4 15 8249 11 Coal Grinding hopper 11SS101 raw coal 110 5*10 load cell*3 11BF101 50.0 45250 11 circle feeder 11FE101 raw coal 60 D=2.48 11251 11 double-SC 11FE102 11SC101 raw coal 30 0.4 3.5 2.2*2252 11 coal VM 11RM101 raw coal 45 H2O: 15->1%, 15%>90u Atox KM30 1050+115253 11 water spray 11WT101 20T OH crain 11HO101254 11 11BC101 45': raw coal 5 0.45 10.35 2.2 20 0.75255 11 256 11 coal rotor scale 11EF201 coal powder 25 7.5 rotor scale257 11 Nm3/H 222000 BF 11BF102 coal powder air dampr 11DA101 11BF102 1850.0 1292.5258 11 11SC201 coal powder 60 0.25 10 1.1 air dampr 11DA102 11BF103 50.0 45259 11 11RV202 coal powder 10 0.55 CO2 11NN101260 11 hopper 11SS102 coal powder 120 6*11.7 CO3 11NN201261 11 AGITATOR 11EF103 coal powder 4 sampling 11SA101 11BF201 100.0 85262 11 screw pump 11PP201 coal powder 30 screw pump

263 11 coal powder air dampr 11DA103/104264 11 hopper 11SS201 coal powder 25 4*3.6265 11 11RV302 coal powder 30 2.2 insulating 11RF101266 11 coal rotor scale 11EF301 coal powder 20 rotor scale267 11 268 11269 11270 12 Cement silo silo 12SS101/102 cement 15000*2 22*35*53.5271 12 aeration unit 12AE101/201 cement272 12 cont.gate 12GA101-202 *4 cement 360273 12274 12 hopper cement 20 3*3 275 12 12AS101/201 cement 360 0.458 18 7 *** ***276 12 12AS102/202 cement 360 0.458 18 7 *** ***277 12 12AS103/203 cement 360 0.458 15 7 *** ***278 12 12BF101/201 150.0 150279 12 12BB101/201 cement 360 0.8 0 24 40+5 belt scale 12SB204280 12 screen 12VS101/201 cement 360 *** 7.5281 12 12AS104 cement 360 0.458 31 7 *** *** 282 12 hopper 12SS102-402 *4 cement 40 :m3 2w gate 12GA104/204283 12 12AS204 cement 360 0.458 13 7 2w gate 12GA304284 12285 12 Cement packing packer 12PA101-401 *4 100*4286 12 bag feeder 12BA101-401 *4 12BF102-402 300.0 300287 12 12SC101-401 *4 cement 10 0.25 13.5 0.5 4288 12 12SC102/302 cement 10 0.25 10 0 4289 12 12BC101-401 *4 bagged 110 0.65 33 0 60 3.7 5T hoist 12HO101/102290 12 2T hoist 12HO103/104291 12 12BC102-502 *5 bagged 110 0.65 26 0 60 3.7292 12 5T hoist 12HO105/106293 12 truck loader 12TL101-501 *5 bagged 100 0.65 12.5 60 1.5 5T hoist 12HO107/108294 12 5T hoist 12HO109/110295 12 Bulk cement loading 296 12 Truck hopper 12SS103 cement 50 :m3 297 12 telescopic shute 12BL101 cement 100298 12 12BF103 50.0 38299 12 Bulk ship cont.gate 12RV601/701 cement 900 300 12301 12 12AS601 cement 900 0.762 13 7

302 12 12AS701 cement 900 0.762 13 7303 12 12BC203 cement 900 1.2 165 9 150 75304 12 12BC203' clinker 600 1.2 165 9 150 75 12BF601 150.0 150305 12 belt scale 12SB203 12BF701 150.0 150306 12 Bag ship 12BC106 bagged 100 0.8 170 4 60 11 belt scale 12SB204307 12 12BC107 bagged 100 0.8 170 4 60 11308 12 12BC108 bagged 100 0.8 4450 3.3 40-60 75309 12 12BC109 bagged 100 0.8 10 0 60 3.7 roller con 12RC101310 12 12BC110 bagged 100 0.8 140 0 60 7.5311 12 12BC111 bagged 100 0.8 6 0 60 2.2 roller con 12RC102 12BF801 150.0 150312 12 12BC112 bagged 100 0.8 6 0 60 2.2313 12 12BC113 bagged 100 0.8 140 0 60 7.5314 12 315 12 Transport 316 12 equipment 12SL101/102 bagged 100 22317 12 &318 12 plant jetty weigh bridge 12WB101/102 truck 60 :T 3*18319 12320 12 321 12322 12323 12324 12325 12 326 327

27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46

cement ship loader

14 5 6 7 8 2

3FA:suction fan -mmAq 4TB:turbo fan +mmAq 5NO V P T Mo 6FA,TB RB m3/H mmAq 'C KW 7

803FA101 36000 -300 30 55 9

1011

03FA102 75000 -300 30 110 121314

6000 -300 30 11 1516171819202122232425

3600 -300 30 5.5 26272829

04FA101 15000 -300 30 22 3031

3600 -300 30 5.5 323334353637383940414243

444546

05FA101 10200 -300 30 15 4705FA102 6000 -300 30 11 48

4950

4200 -300 30 7.5 514200 -300 30 7.5 52

535455

05FA103 15000 -300 30 22 56575859606162636465666768

3000 -230 30 5.5 693000 -230 30 5.5 70

713000 -230 30 5.5 72

3000 -230 30 5.5 733600 -230 30 5.5 743600 -230 30 5.5 753600 -230 30 5.5 76

77787980

3000 -230 30 5.5 8182

3000 -230 30 5.5 838485

3000 -230 30 5.5 868788

3000 -230 30 5.5 899091

06FA101 9600 -250 30 15 929394959697

06FA102 12000 -250 30 18.5 9899

10006FA105 6000 -250 30 15 101

06AS103 10206AS103 103

06TB103 3000 630 30 15 10406FA103 1020000 -1100 80 4150 105

106107108

1350 750000 30 150 109110111112113114115116117118

06FA104 720000 -250 80 670 119950 550 30 2.2 120

1200 550 30 3.7 121122

1500 550 30 5.5 123 124

720 630 30 3 125126

07FA101 21000 -300 30 30 12707RB101 400 5000 30 11 128

12907RB102/103 1250 5000 30 30 130

13107RB104 640 6000 30 18.5 132

133134135

07TB101 1200 630 30 4 136 137

13807FA102 15000 -300 30 22 139

07TB102 900 800 30 5.5 140

141 07AS104 142

07TB103 1500 550 30 5.5 143144

07FA103 6000 -300 30 11 145146147

08TB103 33000 1500 30 200 14808FA101 402000 -750 300 1150 14908FA102 522000 -750 300 1500 150

151air blaster 320 70000 30 30 152water gan 2.7 750 75 153

154155156

08TB106/107 15000 50 30 5.5 *2 15708TB108/109 15000 50 30 5.5 *2 158

08TB104 27000 200 30 30 15908TB110/111 9000 250 30 15 *2 160

08TB105 12000 2000 30 132 161162163

08TB201 34800 940 30 132 16408TB202 43200 940 30 160 16508TB203 43200 940 30 160 16608TB204 43200 760 30 132 16708TB205 43200 760 30 132 16808TB206 85500 700 30 250 16908TB207 74100 640 30 185 17008TB208 68400 580 30 160 17108TB209 68400 580 30 160 172

17330 85 30 174

175176177

08FA501 12000 -300 30 18.5 17808FA502/503 15000 -300 80 22 *2 17908FA504 6000 -300 80 15 180

18108FA120 750000 -150 350 460 182

183184185186187188189190191192193

09FA201/301 18000 -300 80 30 194195

09FA302 18000 -300 80 30 196197

4200 -220 30 7.5 198 199

200201

09FA101 24000 -350 30 37 202

2034200 -220 30 7.5 204

OPTION 9000 -250 30 11 205206207208

3000 -220 30 5.5 2093000 -220 30 5.5 2103000 -220 30 5.5 211

21210FA101 12000 -300 30 22 213

214 21510FA103 36000 -400 80 65 216

217218219220221222223224

pump 8 710 7.5 225226

10TB101 600 600 30 3.7 22710FA105/106 120000 -650 80 300 *2 228

10TB102 2160 600 30 7.5 22910TB103 600 600 30 3.7 23010TB104 900 600 30 3.7 23110TB105 3300 600 30 11 232

23310RB101 120 2000 30 7.5 234

23510FA107/108 18000 -300 30 30 236

500 600 30 1.5 2372500 600 30 7.5 238

10FA105/106 120000 -650 80 300 239240241

10FA104 54000 -250 120 75 242243244245246

10TB106 900 600 30 3.7 24710TB107 900 600 30 3.7 248

3000 -230 30 5.5 249250251252

pump 2 50 7.7 *2 253254255

11RB203/204 4560 3500 75 *2 25611FA101 111000 -1200 80 970 *2 257

3000 -230 80 5.5 258259260

11FA201 6000 -250 30 11 26111RB201/202 1800 7000 75 *2 262

263264265

11RB301/302 4860 7000 30 160 *2 266267268269270

12RB101-301 400 5000 30 11 *3 27112RB102/202 350 5000 30 11 *2 272

273274

12TB101/201 1080 550 30 5.5 *2 27512TB102/202 1080 550 30 5.5 *2 27612TB103/203 1080 550 30 5.5 *2 277

9000 -300 30 15 278279280

12TB104 1980 550 30 7.5 281282

12TB204 900 550 30 3.7 283284285

18000 -300 80 30 *4 286287288289290291292293294

29512RB103 150 5000 30 4 296

297 3000 -240 80 5.5 298

299300

12TB601 1620 550 30 7.5 301

12TB701 1620 550 30 7.5 302303

12FA601 9000 -300 30 15 30412FA701 9000 -300 30 15 305

306307308309310

12FA801 9000 -300 30 15 311312313314315316317318319320321322323324325

326 32747 48 49 50 51 52

1 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 2 23 34 ABC CEMENT PLANT 45 56 67 78 PRODUCTION CAPACITY D/Y H/D H/Y clT/D clT/Y T/H M/Y clT/M ABC KSCC 89 9

10 CEMENT PLANT 315 24 7560 1011 1112 CLINKER PRODUCTION in ABC PLANT 6000 1,890,000 250 12 157,500 5800 1213 For Cement plant 0.50 945,000 12 78,750 1314 12 78,750 1415 For Grinding plant 0.50 945,000 1516 Clinker Import 0.10 94,500 1617 TOT 1,039,500 12 86,625 1718 1819 GRINDING PLANT CEMENT SHIPPING 1,039,500 0.810 1,283,333 12 106,944 1920 2021 CLINKER SHIPPING 0.00 0 2122 2223 2324 MAIN MACHINARY BALANCE Working BASE Capa Working Ratio DESIGN 2425 D/Y H/D H/Y Ratio clT/H Unit T/clT ratio B:T/H D/B D:T/H 2526 2627 CEMENT MILL 315 22 6,930 0.92 136.36 1.235 168.35 1.19 200 200 *** 160 2728 ( 315 24 7,560 1.00 125.00 1.235 154.32 1.30 200 ) 2829 clinker cement 2930 PC40 0.870 446,600 0.40 513,333 Pro.ratio CLINKER GYPSUM ADDITIVE TOT 3031 PC30 0.770 592,900 0.60 770,000 1.00 CEMENT 0.810 0.040 0.150 1.000 3132 TOT 0.810 1,039,500 1.00 1,283,333 0.40 PC40 0.870 0.040 0.090 1.000 3233 CLINKER 0 0.00 0.60 PC30 0.770 0.040 0.190 1.000 3334 TOT 1,039,500 H2O % 0.0% 5.0% 10.0% 3435 3536 D/Y H/D H/Y % 3637 UNLOADING 14 4410 63.6% TRANSPORTATION CAPACITY BALANCE 3738 GRINDING 315 22 6930 100.0% 3839 PACKING 16 5040 72.7% 3940 BASE Capa Afford Working Ratio DESIGN 4041 Working hour B:clT/H ratio T/H D/B D:T/H ABC KSCC 4142 D/Y H/D H/Y 4243 4344 UNLOADING & STORAGE 315 14 4410 4445 (DB) (WB) (WB) (WB) 4546 UNLOADE CLINKER 0.810 0.810 1039500 235.71 4647 GYPSUM 0.040 0.042 54035 12.25 4748 ADDITIVE 0.150 0.167 213889 48.50 4849 TOT 1.000 1.019 1307424 296.47 0.50 592.94 2.02 600 600 4950 5051 HOPPER 70 m3 5152 5253 FEEDER 600 1 600.00 1.00 600 600 5354 5455 5556 COMMON TRANSPORT 600 1 600.00 1.00 600 600 5657 5758 TRANSPORCLINKER 600 1 600.00 1.00 600 600 5859 GYP & ADD 600 1 600.00 1.00 600 600 5960 6061 YARD GYPSUM 35 171.54 6003.90 6003.90 1.00 6000 6000 3000*2 6162 ADDITIVE 14.5 679.01 9845.68 9845.68 1.02 10000 10000 5000*2 6263 6364 CLINLER SILO 9 3300 29700.00 29700.00 1.01 30000 30000 6465 6566 6667 6768 CEMENT GRINGING 315 22 6930 6869 69

D:TonDB/WB DB/WB DB/WB

70 RECLAIMING GYPSUM max 8.00 7071 ADDTIVE max 38.00 7172 TOT TOT 46.00 0.2 230.00 3.26 150 150 7273 7374 TRANSPORT 150 1 150 1.00 150 150 7475 7576 CLINKER EXRACTING max 174.00 0.2 870.00 5.17 900 900 300*3 7677 7778 TRANSPORT max 174.00 1.5 261.00 1.44 250 300 7879 7980 FEED BIN clinker 1.6 ave 174.00 278.40 278.40 1.08 300 300 190*2 8081 gypsum 18 ave 8.00 144.00 144.00 1.04 150 150 80*2 8182 additive 5 ave 38.00 190.00 190.00 1.05 200 200 170*2 8283 others 8384 gorss eff.stock T T/H H H 8485 <CHECK> gypsum 150 0.20 30.00 150 0.200 8586 blackstone 140 0.20 28.00 150 0.187 8687 cem limesetone 60 0.20 12.00 150 0.080 8788 TOT 0.467 < 0.50 8889 8990 CFW clinker 315 22 ave 0.870 174.00 1.2 208.80 1.44 250 250 200*2 9091 gypsum 315 22 ave 0.040 8.00 1.5 12.00 2.50 20 20 10*2 9192 additive 315 22 ave 0.190 38.00 1.5 57.00 2.11 80 80 50*2 9293 others 315 22 9394 9495 TRANSPORT 315 22 200 1.2 240.00 1.20 240 200 200*2 9596 9697 PRE GRINDING VM 315 22 200 200 200 160*2 9798 9899 TRANSPORT 315 22 CL= 60 320 1.2 384.00 1.25 400 450 290*2 99

100 100101 CEMENT MILL 315 22 200 200 200 160*2 101102 102103 TRANSPORMILL EXIT 315 22 CL= 200 > 150 600 1 600 1.00 600 650 540*2 103104 RETURN 315 22 400 1 400 1.00 400 450 540*2 104105 FINISH 315 22 200 1.2 240 1.10 220 240 190*2 105106 106107 STORAGE PC40 12.0 0 1630 19556 19556 1.02 20000 20000 20000 107108 PC30 8.0 0 2444 19556 19556 1.02 20000 20000 30000 108109 TOT 9.8 4074 40000 40000 50000 109110 110111 111112 112113 CEMENT & CLINKER SHIPPING 113114 TRANSPOR PACKING 315 16 4800 0 213.89 267.36 0.31 862.46 2.24 600 600 300*2 300 114115 BULK TRUCK 300 16 4800 0 53.47 100 100 100 115116 BULK SHIPPING 116117 117118 PACKER PACKING LAND 0.40 0.00 513333 106.94 213.89 0.38 562.87 1.87 400 400 100*4 118119 PACKER PACKING SEA 0.40 0.00 513333 106.94 119120 BULK TRUCK LAND 0.20 0.00 256667 53.47 53.47 0.19 281.43 3.74 200 200 100*2 120121 BULK SHIPPING SEA 0 0 121122 TOT 1.00 1283333 267.36 122123 123124 TRANSPORT & BAG TRUCK LOADER max 213.89 0.38 562.87 1.87 400 400 124125 TRANSPORT & BULK TRUCK LOADER max 53.47 0.19 281.43 3.74 200 200 125126 126127 TRANSPORT to BAG SHIP LOADER max 106.94 0.38 281.43 1.87 200 200 100*2 127128 TRANSPORT to BULK SHIP LOADER 0 0 128129 129130 TRANSPORT to CLINKER SHIP LOADER 0 0 130131 131132 BIRTH 132133 BAG SHIP LOADER 0 0 4800 max 106.94 0.38 281.43 1.87 200 200 100*2 133134 BULK SHIP LOADER 0 0 134135 135136 CLINKER SHIP LOAD 0 0 4800 0 0 136137 137138 138139 UNLOADE CLINKER 300 16 4800 1039500 235.71 139140 gypsum 300 16 4800 54035 12.25 140141 additive 300 16 4800 213889 48.50 141

142 142143 143144 TOT 14 4200 1307424 296.47 0.50 592.94 2.02 600 600 144145 145146 146147 147148 MATERIAL DIAGRAM T/Y T/H T/H T/Y T/H STOCK(T) 148149 149150 150151 151152 152153 153154 154155 155156 156157 157158 158159 159160 160161 161162 TOT 1,307,424 birth 162163 g.plant 163164 CLINKER 1,039,500 SHIP UNLOADER C.SILO 30000 164165 g.plant 165166 GYPSUM 54,035 SHIP A.YARD 5000*2 166167 600 g.plant 167168 ADDITIVE 213889 SHIP G.YARD 3000*2 168169 169170 170171 171172 172173 SHIPMENT DIAGRAM T/Y T/Y CEMENT SHIPMENT 1,283,333 T/H 173174 174175 CLINKER 1,039,500 1,039,500 1,283,333 LAND BULK 256,667 200 BULK TRUCK LOADER 175176 176177 BULK 256,667 SEA BULK 0 0 BULK SHIP LOADER 177178 178179 PACKER 1,026,667 LAND BAG 513,333 400 BAG TRUCK LOADER 179180 180181 SEA BAG 513,333 200 BAG SHIP LOADER 181182 182183 0 SEA CLINKER 0 0 CKINKER SHIP LOADER 183184 184185 185

23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41

1 note: This sheet linkes with ABCgConveyer-DATA.2 1 2 3 4 5 6 7 8 9 1 2 334 SPECIFICATION OF CONVEYOR, BAG FILTER/FAN and AS/BLOWER, and LARGE FAN note:5 ( excluded : majour machinary, duct damper, miscellaneous and piping material )6 SECTION NAME CODE WF Q W L H SP Mo Accesary CODE V area7 BC BE EF FC RV AS MATERIAL T/H(WB) m m m,deg m/min KW m3/min m28 21 Unloading,Stock & Discharging9 21 Unloader 21SU101 600

10 21 Hopper 21HP101 70(m3)11 21 21FC101 clinker 600 1 6.5 0 22 2way damper 21GA101 21BF101 166.7 12512 21 21BC101 clinker 600 1.05 62 6 30 21BF102 75.0 5513 21 21BC102 clinker 600 1.05 95 0 22 belt scale 21BS101 21BF103 75.0 5514 21 ITB 1.00 15 21 Gyp + Add 21BC103 additive 600 1.05 71 1.5 7.5 21BF104 75.0 5516 21 Stacker 21ST101 21BC01 additive 600 1.05 222 9 55 17 21 21BC02 additive 600 1.05 20 6.1 7.5 18 21 ITB 0.80 7.5*2 2.2 19 21 Gyp yard 21W/H13 3000*2(T) 20 21 Add yard 5000*2(T) 21 21 Reclaimer 21RE101 150 1.05 21 0 37 22 21 3*2 1.5*2 7.5 23 21 21BC104 additive 150 0.6 190 0 18.5 24 21 21BC105 additive 150 0.6 42 2.5 7.5 25 21 21BE101 additive 150 400 0 39 30 1.5T hoist 21HO101 21BF105 50.0 3726 21 21BC106 additive 150 0.6 8 0 2.2 21BF106 50.0 3727 21 21BC107 additive 150 0.6 11 0 3 28 21 21BC108 additive 150 0.6 7 0 2.2 29 21 30 21 Clinker 21BC109 clinker 600 1.05 245 47 132 31 21 Silo 21SS101 clinker 30000(T) gate damper GA102-108 21BF108 500.0 4232 21 21BC110 clinker 300 0.75 35 0 5.5 21BF109 58.3 4233 21 21BC111 clinker 300 0.75 40 0 5.5 21BF110 58.3 4234 21 21BC112 clinker 300 0.75 35 0 5.5 21BF111 58.3 4235 21 21BC113 clinker 300 0.75 34 0 7.536 21 21BE102 clinker 300 500 0 39 55 1.5T hoist 21HO10237 2138 22 Cement Grinding39 22 Hopper Clinker 22HP101 300(T) 22BF101 50.0 4940 22 Additive 22HP201 200(T) 22BF201 50.0 4941 22 Gypsum 22HP301 150(T) 80 2way damper 22GA101 22BF301 50.0 3242 22 Dosing Clinker 22WF101 clinker 250 1.4 5 0 ** 300 2way damper 22GA102 43 22 Additive 22FC201 additive 80 1 2.5 0 11 300 2way damper 22GA103 44 22 22WF201 additive 80 0.75 5 0 ** 45 22 Gypsum 22WF301 gypsum 20 0.6 3 0 ** 6.2KW m.sepa 22MG101 46 22 22BC101 clinker 300 0.9 24 5 7.5 m.detector 22MD101 22BF102 100.0 7447 22 PG 22PG101 200 10T foist 22HO101 22BF103 500.0 12448 22 22BE101 clinker 450 900 0 23 75 3.2T foist 22HO102 49 22 22BC102 clinker 300 0.9 22 0 5.5 650 2way damper 22GA104 50 22 inpact scale 22WF102 51 22 Cement mill 22FM101 cement 200 <90'C 3600Bln< 2T foist 22HO103 52 22 cement 22 42T crane 22CR101 53 22 22AS101s cement 650 0.63 6 18 4T foist 22HO104 10.0 54 22 22BE102 cement 650 1000 0 45 132 2T foist 22HO105 22BF104 75.0 5055 22 22AS102s cement 650 0.63 20 18 (14+6) 120 metal trap 22MT101 36.0 56 22 22AS103s cement 450 0.55 6 18 10 vib.screen 22VS101 10.0 57 22 O-sep N-3500 22SE101 cement 200 0.2 air damper 22DA105 58 22 flap damper GA105s 59 22 30 2way damper 22GA106 60 22 22AS104s cement 220 0.4 15 8 air damper 22DA106 15.0 61 22 0.2 air damper 22DA101 2000.0 62 22 22RV101/102s cement 110 0.5 0.44 0 2.5 air damper DA103 63 22 22AS105s cement 220 0.4 50 8 air damper DA104 55.0 64 22 22AS106s cement 220 0.4 15 8 15.0 65 22 22AS107s cement 220 0.4 25 8 30.0 66 22 22BB103 cement 220 0.63 0 60 75 sample 22SA101 22BF105 58.3 4267 22 cement 68 22 cement BF 22RV103s cement 20 nor 8 22BF106 4000.0 310069 22 22SC101/102s cement 110 0.5 10 0

PC SC

70 22 cement EP 22EP101 1000.0 300071 2272 22 chimny 22SK10173 22 22SC103S cement 20 0.3 20 074 2275 2276 2277 2278 2279 2280 23 Cement silo & Transport cement 308.3 81 23 Cement silo 23SS101 cement 20000(T) 23BF101 466.7 38082 23 23SS201 cement 20000(T) 23BF201 466.7 38083 23 aearation cement 12.5 23RB101/10284 23 cement 12.5 23RB201/20285 23 cement 12.5 86 23 23AS101/102 cement 300 0.4 18 8 flow gate GA101/102 AS 16.7 87 23 23AS201/202 cement 300 0.4 18 8 flow gate GA201/202 AS 16.7 88 23 23AS103 cement 300 0.4 12 8 AS 13.3 89 23 23AS203 cement 300 0.4 12 8 AS 13.3 90 23 cement 23BF102 150.0 12091 23 cement 23BF202 150.0 12092 23 23BE101/201 cement 300 630 0 29 37 hoist HO101/201 93 23 Vib. screen VS101/201 232 * cement 300 2way damper GA103/203 94 23 23AS104 cement 300 0.4 37.8 6 AS 41.7 95 23 23AS105 cement 300 0.4 5 6 AS 3.3 96 23 23AS204 cement 300 0.4 43.5 6 AS 50.0 97 23 23AS205 cement 300 0.4 3 6 AS 3.3 98 23 Hopper HP101 cement 50(m3) 23BF103 250.0 20099 23 HP102 cement 50(m3) 23BF104 50.0 37

100 23 HP201 cement 50(m3) 23BF203 250.0 200101 23 HP202 cement 50(m3) 23BF204 50.0 37102 23 23AS106/107 cement 120 0.3 2 6 flow gate GA104/105 AS 8.3 103 23 23AS206/207 cement 120 0.3 2 6 flow gate GA204/205 AS 8.3 104 23 cement 3.0 105 23 Truck bulk loader BL101/201 232 * cement 100 2 0.75106 23107 23 Cement packing & Shipping108 23 Packer PA101-401 234 * cement 100 1.5 5.5*8 23BF105/205 300.0 220109 23 BC cement 1.1 23BF301/401 300.0 220110 23 BC cement 1.1 111 23 Bag trap cement 1.1 41.7 112 23 Bag feeder BA101-401 235 * cement 100113 23 cement bag counter BCt101-401114 23 23SC101-401 cement 10 0.25 12 0 2.2115 23 23SC101/102 cement 10 0.25 7 0 2.2116 23 23BC101-401 bagged 100 0.6 23.7 0 2.2117 23 23BC102-402 bagged 100 0.6 15.3 0 1.5118 23 Truck bag loader TL101-401 23BC 234 * bagged 100 0.6 5 + 8 2.2119 23 bagged 1.5 1.1 7.5120 23 23BC105 bagged 100 0.6 146 6 9121 23 23BC106 bagged 100 0.6 138 7 9 hoist HO101/102122 23 23BC107 bagged 100 0.6 56 0 5 hoist HO103/104123 23 bagged124 23 SL101/102 232 * bagged 100 0.6 5.5 truck scale WB102/202125 23 bagged 22 0.75 1.1126 23127 23128 23129 130 ### 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44

Cement ship loader

1 4 5 6 7 8 2

3FA:suction fan -mmAq 4TB:turbo fan +mmAq 5

CODE V P T Mo 6m3/H mmAq 'C KW 7

89

1010000 -300 30 11 114500 -250 30 7.5 124500 -250 30 7.5 13

144500 -250 30 7.5 15

16 17 18 19 20 21 22 23 24

3000 -250 30 4 253000 -250 30 5.5 26

27 28 29 30

30000 -300 30 37 313500 -250 30 5.5 323500 -250 30 5.5 333500 -250 30 5.5 34

35363738

3000 -220 30 3.7 393000 -220 30 3.7 403000 -220 30 3.7 41

42434445

6000 -300 30 7.5 4630000 -300 30 18.5 47

4849505152

AS 600 600 30 2.2 534500 -300 30 7.5 54

AS 2160 600 30 7.5 55AS 600 600 30 3.7 56

575859

AS 900 600 30 3.7 6022FA101 120000 -650 80 610 61

62AS 3300 600 30 11 63AS 900 600 30 3.7 64AS 1800 600 30 7.5 65

3500 -300 30 5.5 66 67

240000 -300 60 30 68SC: 15 69

22FA102 60000 -250 110 132 70SC: 5.5*2 71

7273747576777879

23FA101/201 18500 -30 30 2.2 8028000 -300 30 37 8128000 -300 30 37 82

23RB101/102 750 6000 30 22 8323RB201/202 750 6000 30 22 84

23RB103 750 6000 30 22 85AS 1000 500 30 1.5 86AS 1000 500 30 1.5 87AS 800 550 30 4 88AS 800 550 30 4 89

9000 -300 30 15 909000 -300 30 15 91

92 93

AS 2500 600 30 15 94AS 200 600 30 2.2 95AS 3000 600 30 15 96AS 200 600 30 1.1 97

15000 -300 30 18.5 983000 -250 30 4 99

15000 -300 30 18.5 1003000 -300 30 4 101

AS 500 600 30 1.5 102AS 500 600 30 1.5 103

23RB301/302 180 6000 30 5.5 104105106107

18000 -300 30 22 10818000 -300 30 22 109

11023TB333 2500 750 30 2.2 111

112113114115116117118119120121122123124125126127128129130

45 46 47 48 49###

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