excel baru

Feed Coal 68493.1507 kg/hr DME68.4932 ton/hr DME

Parameter Contents (%)Total moisture 17.8200fixed carbon 41.0000volatile matter 38.1800ash 3.0000

100.0000batu bara 79.1800komponen % berat berat(ton) MR grmolC 75.6000 51.7498 12 4312481.0045H 5.4000 3.6964 1 3696412.2896N 1.5100 1.0336 14 73830.4571O 17.3000 11.8422 16 740138.1089S 0.2500 0.1711 32 5347.8187total 100.0600 68.4932

Fraksi mol keluar gasifier dari IGCCCO 0.6290 62.9000CO2 0.0230 2.3000 H2/COH2 0.2890 28.9000 0.4595H2O 0.0420 4.2000H2S 0.0003 0.0330CH4 0.0004 0.0370N2 0.0156 1.5600NH3 0.0004 0.0380C sisa 0.0003 0.0320

1.0000 100.0000

600000.0000 ton/year68493.1507 kg/hr

C/H grmol14.0000 C tak terkonversi total 43124.8100

C jadi ash 40968.5695C tak terkonversi pada wet scrubber 2048.4285

analisis ultimate massa (kg)moisture + ash 18009.9444moisture 15414.8515ash 2595.0929

steam masuk gasifier 2175.9691kandungan ash keluar waste 3086.7157air dalam batubara masuk gasifier 3741.4865

konversi gasifier konversi dry solid removal konversi splitter0.9900 0.9500 0.7000

komponen molNeraca C 6,544,473.5403 flow aliran 17Neraca H 328,747.5336 N(steam H2O)Neraca N 66,422.0086 N(N2 aliran dari ASU)Neraca O 1,811,750.9429 N(O2 aliran dari ASU)Neraca S 5,347.8187 N(H2S aliran keluar 17)

komposisi aliran keluarangasifier 17 %mol MR grmolCO 62.9000 28 4,116,473.8568CO2 2.3000 44 150,522.8914H2 28.9000 2 1,891,352.8531H2O 4.2000 18 274,867.8887H2S 0.0330 34 2,159.6763CH4 0.0370 18 2,421.4552N2 1.5600 28 102,093.7872NH3 0.0380 17 2,486.8999C sisa 0.0320 12 2,094.2315total 100.0000 6,544,473.5403

komposisi aliran ASU 8komponen mol MR massa(gr)

N2 66,422.0086 28 1,859,816.2421O2 1,811,750.9429 32 57,976,030.1733total 1,878,172.9516 59,835,846.4154

hasil perhitungan neraca massa basis keringaliran masuk aliran keluar

aliran massa (kg) aliran massa(kg)1 68,493.1507 17 133,657.65228 59,835.8464 13 491.6228

ST-01 5,917.4556total 134,246.4527 134,149.2751

massa (gr) massa(kg)115,261,267.9914 115,261.2680

6,623,007.2228 6,623.00723,782,705.7063 3,782.70574,947,621.9965 4,947.6220

73,428.9931 73.429043,586.1938 43.5862

2,858,626.0424 2,858.626042,277.2991 42.277325,130.7784 25.1308

133,657,652.2236

Parameter (ultimate) massa (kg) % massa baruC 51,749.7721 69.1567H 3,696.4123 4.9398N 1,033.6264 1.3813O 11,842.2097 15.8255S 171.1302 0.2287ash 2,595.0929 3.4680moisture 3,741.4865 5.0000total 74,829.7300 100.0000

referensi shel gasifier steam/coal = 0.04

dari perhitungansteam/coal 0.0291

neraca massa gasifier(basis basah)aliran masuk aliran keluar

aliran massa(kg) aliran massa(kg)6 74,829.7300 17 133,657.65228 59,835.8464 13+11 3,578.3385

ST-01 2,175.9691jumlah(ton) 136,841.5456 jumlah(ton) 137,235.9907

komponen splitterket

aliran splitter N14=N17+N15 aliran 17 70%aliran 15 30%

N14 9,349,247.9147 kgmolN15 2,804,774.3744 kgmol

komposisi aliran dari dry solid removal (cyclone)aliran masuk 14

komponen MR grmol kgmol kgCO 28 5,880,676.9383 5,880.6769 164,658.9543CO2 44 215,032.7020 215.0327 9,461.4389H2 2 2,701,932.6473 2,701.9326 5,403.8653H2O 18 392,668.4124 392.6684 7,068.0314H2S 34 3,085.2518 3.0853 104.8986CH4 18 3,459.2217 3.4592 62.2660N2 28 145,848.2675 145.8483 4,083.7515NH3 17 3,552.7142 3.5527 60.3961C sisa 12 2,991.7593 2.9918 35.9011

total 9,349,247.9147 9,349.2479 190,939.5032

aliran syngas ke recycle dan ke HEaliran keluar 15komponen MR grmol kgmol massa(kg)

CO 28 1,764,203.0815 1,764.2031 49,397.6863CO2 44 64,509.8106 64.5098 2,838.4317H2 2 810,579.7942 810.5798 1,621.1596H2O 18 117,800.5237 117.8005 2,120.4094H2S 34 925.5755 0.9256 31.4696CH4 18 1,037.7665 1.0378 18.6798N2 28 43,754.4802 43.7545 1,225.1254NH3 17 1,065.8143 1.0658 18.1188C sisa 12 897.5278 0.8975 10.7703

total 2,804,774.3744 2,804.7744 57,281.8510total massa 190,939.5032

17grmol kgmol massa(kg)

4,116,473.8568 4,116.4739 115,261.2680150,522.8914 150.5229 6,623.0072

1,891,352.8531 1,891.3529 3,782.7057274,867.8887 274.8679 4,947.6220

2,159.6763 2.1597 73.42902,421.4552 2.4215 43.5862

102,093.7872 102.0938 2,858.62602,486.8999 2.4869 42.27732,094.2315 2.0942 25.1308

6,544,473.5403 6,544.4735 133,657.6522190,939.5032

komponen cyclone

aliran masuk12

komponen MR grmol kgmol massa (kg)CO 28 5,880,676.9383 5,880.6769 164,658.9543CO2 44 215,032.7020 215.0327 9,461.4389H2 2 2,701,932.6473 2,701.9326 5,403.8653H2O 18 392,668.4124 392.6684 7,068.0314H2S 34 3,085.2518 3.0853 104.8986CH4 18 3,459.2217 3.4592 62.2660N2 28 145,848.2675 145.8483 4,083.7515NH3 17 3,552.7142 3.5527 60.3961C sisa 12 43,960.3289 43.9603 527.5239

total 9,390,216.4842 9,390.2165 191,431.1260

komponen aliran keluar cyclonealiran keluar

komponen MR14 13

grmol kgmol massa(kg) grmolCO 28 5,880,676.9383 5,880.6769 164,658.9543 0.0000CO2 44 215,032.7020 215.0327 9,461.4389 0.0000H2 2 2,701,932.6473 2,701.9326 5,403.8653 0.0000H2O 18 392,668.4124 392.6684 7,068.0314 0.0000H2S 34 3,085.2518 3.0853 104.8986 0.0000CH4 18 3,459.2217 3.4592 62.2660 0.0000N2 28 145,848.2675 145.8483 4,083.7515 0.0000NH3 17 3,552.7142 3.5527 60.3961 0.0000C sisa 12 2,991.7593 2.9918 35.9011 40,968.5695

total 9,349,247.9147 9,349.2479 190,939.5032 40,968.5695jumlah massa 191,431.1260

aliran keluar13

kgmol massa(kg)0.0000 0.00000.0000 0.00000.0000 0.00000.0000 0.00000.0000 0.00000.0000 0.00000.0000 0.00000.0000 0.0000

40.9686 491.622840.9686 491.6228

191,431.1260

komponen scrubber aliran masuk

komponen MR 18 W-03grmol kgmol massa(kg) grmol

CO 28 4,116,473.8568 4,116.4739 115,261.2680 0.0000CO2 44 150,522.8914 150.5229 6,623.0072 0.0000H2 2 1,891,352.8531 1,891.3529 3,782.7057 0.0000H2O 18 274,867.8887 274.8679 4,947.6220 7,425,425.1235H2S 34 2,159.6763 2.1597 73.4290 0.0000CH4 18 2,421.4552 2.4215 43.5862 0.0000N2 28 102,093.7872 102.0938 2,858.6260 0.0000NH3 17 2,486.8999 2.4869 42.2773 0.0000C sisa 12 2,094.2315 2.0942 25.1308 0.0000

total 6,544,473.5403 6,544.4735 133,657.6522 7,425,425.1235jumlah massa 267,315.3044

aliran keluar

komponen MR 20grmol kgmol massa(kg) %mol

CO 28 4,116,473.8568 4,116.4739 115,261.2680 0.629440608CO2 44 150,522.8914 150.5229 6,623.0072 0.023016111H2 2 1,891,352.8531 1,891.3529 3,782.7057 0.289202442H2O 18 274,867.8887 274.8679 4,947.6220 0.042029421H2S 34 2,159.6763 2.1597 73.4290 0.000330231CH4 18 2,421.4552 2.4215 43.5862 0.000370259N2 28 102,093.7872 102.0938 2,858.6260 0.015610928NH3 17 0.0000 0.0000 0.0000 0.000000000C sisa 12 0.0000 0.0000 0.0000 0.000000000

total 6,539,892.4088 6,539.8924 133,590.2441 1.0000jumlah massa 267,315.3044

aliran masukW-03

kgmol massa(kg)0.0000 0.00000.0000 0.00000.0000 0.0000

7,425.4251 133,657.65220.0000 0.00000.0000 0.00000.0000 0.00000.0000 0.00000.0000 0.0000

7,425.4251 133,657.6522267,315.3044

aliran keluar19

grmol kgmol massa(kg)0.0000 0.0000 0.00000.0000 0.0000 0.00000.0000 0.0000 0.0000

7,425,425.1235 7,425.4251 133,657.65220.0000 0.0000 0.00000.0000 0.0000 0.00000.0000 0.0000 0.0000

2,486.8999 2.4869 42.27732,094.2315 2.0942 25.1308

7,430,006.2550 7,430.0063 133,725.0603267,315.3044

komponen separator

komposisi aliran 20komponen %mol kgmol massa(kg)

CO 62.9441 4,116.4739 115,261.2680CO2 2.3016 150.5229 6,623.0072H2 28.9202 1,891.3529 3,782.7057H2O 4.2029 274.8679 4,947.6220H2S 0.0330 2.1597 73.4290CH4 0.0370 2.4215 43.5862N2 1.5611 102.0938 2,858.6260DEAmine 0.0000 0.0000 0.0000total 100.0000 6,539.8924 133,590.2441

komposisi aliran 21komponen %mol kgmol massa(kg) MR

CO 40.99923398 3,068.2190 85,910.13102073 28CO2 2.07544527 155.3180 6,833.99363426 44H2 52.28673629 3,912.9306 7,825.86113550 2H2O 0.14143046 10.5841 190.51363607 18H2S 0.10049423 7.5206 255.69996472 34CH4 0.04522723 3.3846 60.92324919 18N2 4.35143253 325.6438 9,118.02740240 28DEAmine 0.00000000 0.0000 0.00000000total 100.00000000 7,483.60070876 110,195.15004288

total massa keluaran 110,411.7427 110,291.0497


CO 0.00266154 0.00032010 0.00896282 28CO2 0.03156253 0.00379599 0.16702356 44H2 0.00267481 0.00032170 0.00064339 2H2O 99.95618126 12.02161705 216.38910691 18H2S 0.00497014 0.00059775 0.02032361 34CH4 0.00000001 0.00000000 0.00000003 18N2 0.00194970 0.00023449 0.00656568 28DEAmine 0.00000000 0.00000000 0.00000000total 100.00000000 12.02688708 216.59262599

216.7743

komponen absorber


CO 40.99923398 3,068.2190 85,910.13102073 28CO2 2.07544527 155.3180 6,833.99363426 44H2 52.28673629 3,912.9306 7,825.86113550 2H2O 0.14143046 10.5841 190.51363607 18H2S 0.10049423 7.5206 255.69996472 34CH4 0.04522723 3.3846 60.92324919 18N2 4.35143253 325.6438 9,118.02740240 28DEAmine 0.00000000 0.0000 0.00000000total 100.00000000 7,483.60070876 110,195.15004288


CO 41.891564125 3046.465680153 85301.0390442893 28CO2 0.000032631 0.002373006417 0.10441228232801 44H2 53.452934389 3887.23919764 7774.47839527991 2H2O 0.154007607 11.19984176698 201.59715180572 18H2S 0.000000154 1.12028826E-05 0.00038089800831 34CH4 0.046085867 3.351486517446 60.3267573140209 18N2 4.455269155 323.998992656 9071.97179436841 28DEAmine 0.000000000 0 0total 99.999893928 7272.257582943 102409.517936238


CO 0.00000000 0 0 28CO2 0.08338911 72.503972886019 3190.17480698485 44H2 0.00000000 0 0 2H2O 89.22017494 77573.884033784 1396329.91260812 18H2S 0.00015536 0.135082957371 4.59282055061414 34CH4 0.00000000 0 0 18N2 0.00000000 0 0 28DEAmine 10.69628059 9300.0493514489 972993.568386total 100.00000000 86,946.57244108 2,372,518.24862165


CO 0.02488900 21.692702785408 607.39567799 28CO2 0.26150110 227.91858412782 10028.41770162 44H2 0.02938818 25.614088719678 51.22817744 2H2O 89.00327200 77573.286448825 1396319.15607885 18H2S 0.00877436 7.64753405716 260.01615794 34CH4 0.00003800 0.0331214425425 0.59618597 18N2 0.00178722 1.5577036182322 43.61570131 28DEAmine 10.67035000 9300.0414306029 972993.10000000total 99.99999986 87,157.79161418 2,380,303.52568112

komponen separator 2

komponen aliran 23komponen %mol kgmol massa(kg) MR

CO 0.02488725 21.69117815 607.35298822 28CO2 0.26150118 227.91865425 10,028.42078711 44H2 0.02938765 25.61362280 51.22724561 2H2O 89.00327382 77,573.28765077 1,396,319.17771389 18H2S 0.00877436 7.64753452 260.01617377 34CH4 0.00003800 0.03311940 0.59614924 18N2 0.00178710 1.55759772 43.61273606 28DEAmine 10.67035100 9,300.04225656 972,993.10000000total 100.00000035 87,157.79161418 2,380,303.50379389

aliran komponen 28komponen %mol kgmol massa(kg) MR


total 2,380,303.41143926

komponen 29komponen %mol kgmol massa(kg) MR

CO 43.51213973 18.20209749 509.65872985 28CO2 0.00048766 0.00020400 0.00897592 44H2 52.25335427 21.85874229 43.71748458 2H2O 0.87449885 0.36582235 6.58480232 18H2S 0.00013423 0.00005615 0.00190914 34CH4 0.06230476 0.02606347 0.46914241 18N2 3.29648068 1.37899131 38.61175681 28DEAmine 0.00059983 0.00025092 0.01660901total 100.00000000 41.83222799 599.06941003

komponen HE keluar dari separator





komponen regenerator





total 2,379,221.15937424


CO 0.01897172 3.48907992 97.69423764 28CO2 0.95087931 174.87579156 7,694.53482864 44H2 0.02041699 3.75487964 7.50975928 2H2O 98.93807326 18,195.65716855 327,521.82903381 18H2S 0.02764306 5.08382321 172.84998901 34CH4 0.00003837 0.00705593 0.12700680 18N2 0.00097116 0.17860635 5.00097772 28DEAmine 0.00000000 0.00000000 0.00000000total 100.00000000 18,390.95564400 335,499.54583291

komponen mixer

komponen aliran 33 W-01komponen %mol kgmol massa(kg) MR komponen

CO 0.00000000 0.00000000 0.00000000 28 COCO2 0.07718101 53.04265122 2,333.87665353 44 CO2H2 0.00000000 0.00000000 0.00000000 2 H2H2O 86.39834356 59,377.26202966 1,068,790.71653395 18 H2OH2S 0.00373031 2.56365491 87.16426681 34 H2SCH4 0.00000000 0.00000000 0.00000000 18 CH4N2 0.00000000 0.00000000 0.00000000 28 N2DEAmine 13.52074512 9,292.13214649 972,509.90840000 DEAminetotal 100.00000000 68,725.00048228 2,043,721.66585429 total



%mol kgmol massa(kg) MR0.00000000 0.00000000 0.00000000 280.00000000 0.00000000 0.00000000 440.00000000 0.00000000 0.00000000 2

100.00000000 18,266.39145152 328,795.04612742 180.00000000 0.00000000 0.00000000 340.00000000 0.00000000 0.00000000 180.00000000 0.00000000 0.00000000 280.00000000 0.00000000 0.00000000

100.00000000 18,266.39145152 328,795.04612742

komponen HE





komponen pump





komponen WGS


CO 41.89156413 3,046.46568015 85,301.03904429 28.00000000CO2 0.00003263 0.00237301 0.10441228 44.00000000H2 53.45293439 3,887.23919764 7,774.47839528 2.00000000H2O 0.15400761 11.19984177 201.59715181 18.00000000H2S 0.00000015 0.00001120 0.00038090 34.00000000CH4 0.04608587 3.35148652 60.32675731 18.00000000N2 4.45526916 323.99899266 9,071.97179437 28.00000000DEAmine 0.00000000 0.00000000 0.00000000total 99.99989393 7,272.25758294 102,409.51793624

total 192,409.53916483

komponen 24akomponen %mol kgmol massa(kg) MR

CO 0.12356353 14.16119446 396.51344482 28.00000000CO2 26.45004014 3,031.34876393 133,379.34561289 44.00000000H2 60.37484779 6,919.35510415 13,838.71020830 2.00000000H2O 10.19531105 1,168.44977826 21,032.09600863 18.00000000H2S 0.00000000 0.00000000 0.00000000 34.00000000CH4 0.02924336 3.35148208 60.32667739 18.00000000N2 2.82699413 323.99214160 9,071.77996491 28.00000000DEAmine 0.00000000 0.00000000 0.00000000total 100.00000000 11,460.65846447 177,778.77191693

total 192,409.53916483

steamkomponen %mol kgmol massa(kg) MR

CO 0.00000000 0.00000000 0.00000000 28.00000000CO2 0.00000000 0.00000000 0.00000000 44.00000000H2 0.00000000 0.00000000 0.00000000 2.00000000H2O 100.00000000 5,000.00117937 90,000.02122859 18.00000000H2S 0.00000000 0.00000000 0.00000000 34.00000000CH4 0.00000000 0.00000000 0.00000000 18.00000000N2 0.00000000 0.00000000 0.00000000 28.00000000DEAmine 0.00000000 0.00000000 0.00000000total 100.00000000 5,000.00117937 90,000.02122859

keluaran WGSkomponen %mol kgmol massa(kg) MR

CO 0.00003944 0.00032006 0.00896161 28.00000000CO2 0.11802881 0.95792076 42.14851328 44.00000000H2 0.02305761 0.18713535 0.37427070 2.00000000H2O 99.85803416 810.44692597 14,588.04466755 18.00000000H2S 0.00000000 0.00000000 0.00000000 34.00000000CH4 0.00000061 0.00000499 0.00008977 18.00000000N2 0.00083937 0.00681232 0.19074500 28.00000000DEAmine 0.00000000 0.00000000 0.00000000total 100.00000000 811.59911945 14,630.76724790

komponen HE 3

komponen 24akomponen %mol kgmol massa(kg) MR




CO2 removal


CO 0.12356353 14.16119446 396.51344482 28CO2 26.45004014 3,031.34876393 133,379.34561289 44H2 60.37484779 6,919.35510415 13,838.71020830 2H2O 10.19531105 1,168.44977826 21,032.09600863 18H2S 0.00000000 0.00000000 0.00000000 34CH4 0.02924336 3.35148208 60.32667739 18N2 2.82699413 323.99214160 9,071.77996491 28DEAmine 0.00000000 0.00000000 0.00000000total 100.00000000 11,460.65846447 177,778.77191693

excel baru

Documents

komponen 24a

mol kgmol

kgmol massa

komponen 25

mol 41

mol 62

kgmol 0

massa