materijalna i energetska bilanca kompletni ispis rezultata

22
Unit VUC 1 wellstream WTS 1 VUC 1 zasicen Vapour Fraction 1 0.145481 1 0 0.986927 0.984904 Temperature C 65 340.712425 65 59 62.554211 51.985523 Pressure bar 149 149 149 141 141 111 Molar Flow m3/h_(gas) 10833.333219 70.203488 10903.536707 136.441189 11039.977896 11039.977896 Mass Flow kg/h 15048.499039 53.489239 15101.988278 103.956877 15205.945155 15205.945155 Liquid Volume Flow m3/d 588.535686 1.286332 589.822018 2.5 592.322018 592.322018 Heat Flow kW -32821.082506 -209.255371 -33030.337877 -454.185101 -33484.522978 -33484.522978 VUK 1 plin iz sep Vapour Fraction 1 0 0 0 0.999963 1 Temperature C 31.79454 31.79454 31.79454 32.152122 34.209464 5.200846 Pressure bar 70 70 70 72 68.8 68.8 Molar Flow m3/h_(gas) 10432.652341 0 219.260667 558.637168 31620.529439 10407.730347 Mass Flow kg/h 15921.67803 0 170.512391 505.08748 44020.392498 15896.013544 Liquid Volume Flow m3/d 563.914878 0 4.130007 13.121218 1719.229826 563.234277 Heat Flow kW -36097.54009 0 -739.70684 -1884.559431 -95891.842271 -36269.422936 VUC 5 wellstream WTS 5 VUC 5 zasicen Vapour Fraction 0.984906 0.982449 1 0.133058 1 0 Temperature C 52 32.806375 49 329.8858 49 49 Pressure bar 111 72 130 130 130 130 Molar Flow m3/h_(gas) 11039.977896 11039.977896 6249.999934 23.295658 6273.295592 81.864714 Mass Flow kg/h 15205.945155 15205.945155 8681.826369 17.749361 8699.575729 62.374126 Liquid Volume Flow m3/d 592.322018 592.322018 339.539819 0.426844 339.966663 1.5 Heat Flow kW -33484.387256 -33484.387256 -18985.33197 -69.899837 -19055.231807 -273.274461 VUC 3 wellstream WTS 3 Vapour Fraction 0.98544 0.985073 0.986389 0.984516 1 0.138098 Temperature C 37.563213 32.911053 47 31.931386 59 336.28952 Pressure bar 102 101.890561 101 72 141 141 Molar Flow m3/h_(gas) 6355.160305 6355.160305 6355.160305 6355.160305 14583.333179 78.099481 Mass Flow kg/h 8761.949856 8761.949856 8761.949856 8761.949856 20418.676445 59.505331 Liquid Volume Flow m3/d 341.466663 341.466663 341.466663 341.466663 795.366212 1.43101 Heat Flow kW -19328.506268 -19355.009313 -19274.889146 -19274.889146 -44497.732651 -233.475258 Slojna voda 3 Vapour Fraction 0 0.987352 0.985119 0.983896 0.984803 0.981792 Temperature C 59 58.991386 46.044417 34.178837 44 31.808118 Pressure bar 141 141 106 95.084277 95 72 Molar Flow m3/h_(gas) 185.560017 14846.992677 14846.992677 14846.992677 14846.992677 14846.992677 Mass Flow kg/h 141.381353 20619.563129 20619.563129 20619.563129 20619.563129 20619.563129 Liquid Volume Flow m3/d 3.4 800.197222 800.197222 800.197222 800.197222 800.197222 Heat Flow kW -617.691737 -45348.893026 -45348.893026 -45436.146437 -45310.956395 -45310.956395 VUC 1,3,5 VODA ZEB 2 wellstream WTS Zb 2 ZEB 2 zasicen Vapour Fraction 1 0 0 1 0.249907 1 Temperature C 32.152123 32.152123 32.152123 53 315.732157 53 Pressure bar 72 72 72 108 108 108 Molar Flow m3/h_(gas) 31683.493711 27.872985 530.764183 5333.333277 25.182393 5358.51567 Mass Flow kg/h 44082.370661 93.724442 411.363038 8110.594714 19.186896 8129.78161 Liquid Volume Flow m3/d 1720.864685 3.169205 9.952013 292.080108 0.461415 292.541523 Heat Flow kW -96185.673365 -95.788572 -1788.770859 -17958.278695 -75.26172 -18033.540416 Vapour Fraction 0.965136 0.959524 1 0 0.997139 0.057983 Temperature C 52.981846 39.104169 39.104113 39.104113 32.28425 35.584136 Pressure bar 108 80 80 80 69 7 Molar Flow m3/h_(gas) 5549.533335 5549.533335 5324.911669 224.621666 5324.911669 224.621666 Slojna voda VUC 3 VUC 1 ukupni wellstream VUC 1 1,rusenje tlaka VUK 1 kondenzat iz sep VUK 1 voda iz sep VUC 1,3,5 ukupna tekuca faza prema CV DEHIDRIRAN PLIN VUC 1,3,5 VUK 1 PLIN PREMA CV VUC 1 nakon grijalice VUC 1 nakon 2,rusenja tlaka Slojna voda VUC 5 VUC 5 1,rusenje tlaka VUC 5 prije grijalice VUC 5 nakon grijalice VUC 5 2 rusenje tlaka VUC 3 ukupni wellstream VUC 3 1,rusenje tlaka VUC 3 prije grijalice VUC 3 nakon grijalice VUC 3 nakon 2 rusenje tlaka VUC 1,3,5 PLIN IZ SEP VUC 1,3,5 KONDENZAT ZEB 2 ukupni wellstream ZEB 2 nakon 1,rusenja ZEB 2 plin iz OST ZEB 2 tekuca faza OST ZEB 2 plin 2,rusenje ZEB 2 tekuca faza 2,rusenje tlaka

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M&E balance of gas rafinerry station

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Page 1: Materijalna i Energetska Bilanca Kompletni Ispis Rezultata

UnitVUC 1 wellstream WTS 1 VUC 1 zasicen

Vapour Fraction 1 0.145481 1 0 0.986927 0.984904 0.984416

Temperature C 65 340.712425 65 59 62.554211 51.985523 48.234244

Pressure bar 149 149 149 141 141 111 110.585798

Molar Flow m3/h_(gas) 10833.333219 70.203488 10903.536707 136.441189 11039.977896 11039.977896 11039.977896

Mass Flow kg/h 15048.499039 53.489239 15101.988278 103.956877 15205.945155 15205.945155 15205.945155

Liquid Volume Flow m3/d 588.535686 1.286332 589.822018 2.5 592.322018 592.322018 592.322018

Heat Flow kW -32821.082506 -209.255371 -33030.337877 -454.185101 -33484.522978 -33484.522978 -33518.192229

VUK 1 plin iz sep

Vapour Fraction 1 0 0 0 0.999963 1 0

Temperature C 31.79454 31.79454 31.79454 32.152122 34.209464 5.200846 31.79454

Pressure bar 70 70 70 72 68.8 68.8 70

Molar Flow m3/h_(gas) 10432.652341 0 219.260667 558.637168 31620.529439 10407.730347 219.260667

Mass Flow kg/h 15921.67803 0 170.512391 505.08748 44020.392498 15896.013544 170.512391

Liquid Volume Flow m3/d 563.914878 0 4.130007 13.121218 1719.229826 563.234277 4.130007

Heat Flow kW -36097.54009 0 -739.70684 -1884.559431 -95891.842271 -36269.422936 -739.70684

WTS 5 VUC 5 zasicen

Vapour Fraction 0.984906 0.982449 1 0.133058 1 0 0.986956

Temperature C 52 32.806375 49 329.8858 49 49 48.992175

Pressure bar 111 72 130 130 130 130 130

Molar Flow m3/h_(gas) 11039.977896 11039.977896 6249.999934 23.295658 6273.295592 81.864714 6355.160305

Mass Flow kg/h 15205.945155 15205.945155 8681.826369 17.749361 8699.575729 62.374126 8761.949856

Liquid Volume Flow m3/d 592.322018 592.322018 339.539819 0.426844 339.966663 1.5 341.466663

Heat Flow kW -33484.387256 -33484.387256 -18985.33197 -69.899837 -19055.231807 -273.274461 -19328.506268

WTS 3 VUC 3 zasicen

Vapour Fraction 0.98544 0.985073 0.986389 0.984516 1 0.138098 1

Temperature C 37.563213 32.911053 47 31.931386 59 336.28952 59

Pressure bar 102 101.890561 101 72 141 141 141

Molar Flow m3/h_(gas) 6355.160305 6355.160305 6355.160305 6355.160305 14583.333179 78.099481 14661.43266

Mass Flow kg/h 8761.949856 8761.949856 8761.949856 8761.949856 20418.676445 59.505331 20478.181776

Liquid Volume Flow m3/d 341.466663 341.466663 341.466663 341.466663 795.366212 1.43101 796.797222

Heat Flow kW -19328.506268 -19355.009313 -19274.889146 -19274.889146 -44497.732651 -233.475258 -44731.201289

Slojna voda 3

Vapour Fraction 0 0.987352 0.985119 0.983896 0.984803 0.981792 0.982674

Temperature C 59 58.991386 46.044417 34.178837 44 31.808118 32.152123

Pressure bar 141 141 106 95.084277 95 72 72

Molar Flow m3/h_(gas) 185.560017 14846.992677 14846.992677 14846.992677 14846.992677 14846.992677 32242.130879

Mass Flow kg/h 141.381353 20619.563129 20619.563129 20619.563129 20619.563129 20619.563129 44587.458141

Liquid Volume Flow m3/d 3.4 800.197222 800.197222 800.197222 800.197222 800.197222 1733.985903

Heat Flow kW -617.691737 -45348.893026 -45348.893026 -45436.146437 -45310.956395 -45310.956395 -98070.232796

VUC 1,3,5 VODA WTS Zb 2 ZEB 2 zasicen

Vapour Fraction 1 0 0 1 0.249907 1 0

Temperature C 32.152123 32.152123 32.152123 53 315.732157 53 53

Pressure bar 72 72 72 108 108 108 108

Molar Flow m3/h_(gas) 31683.493711 27.872985 530.764183 5333.333277 25.182393 5358.51567 191.017665

Mass Flow kg/h 44082.370661 93.724442 411.363038 8110.594714 19.186896 8129.78161 145.539628

Liquid Volume Flow m3/d 1720.864685 3.169205 9.952013 292.080108 0.461415 292.541523 3.5

Heat Flow kW -96185.673365 -95.788572 -1788.770859 -17958.278695 -75.26172 -18033.540416 -637.025999

Vapour Fraction 0.965136 0.959524 1 0 0.997139 0.057983 1

Temperature C 52.981846 39.104169 39.104113 39.104113 32.28425 35.584136 37

Pressure bar 108 80 80 80 69 7 96

Molar Flow m3/h_(gas) 5549.533335 5549.533335 5324.911669 224.621666 5324.911669 224.621666 10416.666557

Mass Flow kg/h 8275.321238 8275.321238 8055.055315 220.265923 8055.055315 220.265923 15912.952123

Liquid Volume Flow m3/d 296.041523 296.041523 290.142067 5.899456 290.142067 5.899456 563.734486

Slojna voda VUC 3

VUC 1 ukupni wellstream

VUC 1 1,rusenje tlaka

VUC1 prije grijalice

VUK 1 kondenzat iz sep

VUK 1 voda iz sep

VUC 1,3,5 ukupna tekuca faza prema CV

DEHIDRIRAN PLIN VUC 1,3,5

VUK 1 PLIN PREMA CV

VUK 1 UKUPNA TEKUCA FAZA

VUC 1 nakon grijalice

VUC 1 nakon 2,rusenja tlaka

VUC 5 wellstream

Slojna voda VUC 5

VUC 5 ukupni wellstream

VUC 5 1,rusenje tlaka

VUC 5 prije grijalice

VUC 5 nakon grijalice

VUC 5 2 rusenje tlaka

VUC 3 wellstream

VUC 3 ukupni wellstream

VUC 3 1,rusenje tlaka

VUC 3 prije grijalice

VUC 3 nakon grijalice

VUC 3 nakon 2 rusenje tlaka

VUC 1,3,5 UKUPNI ULAZ U

SEP

VUC 1,3,5 PLIN IZ SEP

VUC 1,3,5 KONDENZAT

ZEB 2 wellstream

Slojna voda ZEB 2

ZEB 2 ukupni wellstream

ZEB 2 nakon 1,rusenja

ZEB 2 plin iz OST

ZEB 2 tekuca faza OST

ZEB 2 plin 2,rusenje

ZEB 2 tekuca faza 2,rusenje

tlaka

VUK 1 wellstream

Page 2: Materijalna i Energetska Bilanca Kompletni Ispis Rezultata

Heat Flow kW -18670.566414 -18670.566414 -17911.044749 -759.521665 -17911.044749 -759.521665 -36161.434566

Slojna voda VUK 1 WTS VUK 1 VUK 1 zasicen

Vapour Fraction 0 0.156381 1 0.980225 0.979415 0.979229 0.980307

Temperature C 37 307.071529 37 36.992795 29.984985 27.49008 40

Pressure bar 96 96 96 96 84 83.5385 83

Molar Flow m3/h_(gas) 207.390608 27.855843 10444.5224 10651.913008 10651.913008 10651.913008 10651.913008

Mass Flow kg/h 158.014454 21.223844 15934.175967 16092.190421 16092.190421 16092.190421 16092.190421

Liquid Volume Flow m3/d 3.8 0.5104 564.244886 568.044886 568.044886 568.044886 568.044886

Heat Flow kW -694.700518 -84.278969 -36245.713535 -36940.414053 -36940.414053 -36963.789505 -36837.24693

Vapour Fraction 0.979416 0.999781 0.993615 0.031205 0.033875 0.008693 0.011705

Temperature C 31.794551 32.130375 4.865465 9.399707 30.765674 4.999997 32.553186

Pressure bar 70 68.623938 68.144214 6.996192 7 6.999808 7

Molar Flow m3/h_(gas) 10651.913008 31620.529439 10407.730347 558.637168 558.637168 219.260667 219.260667

Mass Flow kg/h 16092.190421 44020.392498 15896.013544 505.08748 505.08748 170.512391 170.512391

Liquid Volume Flow m3/d 568.044886 1719.229826 563.234277 13.121218 13.121218 4.130007 4.130007

Heat Flow kW -36837.24693 -95934.692129 -36269.54785 -1896.112465 -1884.559431 -745.267 -739.70684

UKUPNI PLIN CV

Vapour Fraction 0.999735 0.999046 0.995401 0.052969 0.025066 0.024566 0.998711

Temperature C 22.886519 16.314941 25.531299 5.531918 8.180487 5.000317 17.107573

Pressure bar 68.144214 66.280761 68.506619 6.959144 6.996192 6.958902 66.280761

Molar Flow m3/h_(gas) 42028.259786 42028.259786 5324.911669 224.621666 777.897835 777.897835 47353.171456

Mass Flow kg/h 59916.406042 59916.406042 8055.055315 220.265923 675.599871 675.599871 67971.461357

Liquid Volume Flow m3/d 2282.464103 2282.464103 290.142067 5.899456 17.251226 17.251226 2572.60617

Heat Flow kW -132204.239979 -132373.28854 -17939.152923 -766.224569 -2641.379465 -2643.748908 -150312.441463

TEG ulaz TEG 2 ULAZ

Vapour Fraction 0.030922 0.995456 1 0 0 0 0

Temperature C 5.12304 2.874791 4.619554 55 33.946617 55 32.055661

Pressure bar 6.958902 56.741149 3.6 80 69.8 80 69.8

Molar Flow m3/h_(gas) 1002.519501 47353.171456 34.545163 35.624247 98.588518 12.983059 37.905053

Mass Flow kg/h 895.865794 67971.461357 57.902178 225 286.978162 82 107.664486

Liquid Volume Flow m3/d 23.150682 2572.60617 1.903421 4.785801 6.420659 1.744158 2.42476

Heat Flow kW -3409.973477 -150565.118785 -135.822325 -328.255653 -558.632678 -119.630949 -212.230078

izlaz rema baklji

Vapour Fraction 0 1 1 0 1 1 1

Temperature C 4.628515 1.732433 3.096668 3.096668 3.036885 4.628515 2.631407

Pressure bar 2.8 1 1.25 1.25 1.2 2.8 1.2

Molar Flow m3/h_(gas) 945.453464 34.545163 0.866033 21.562049 0.866033 0.092792 0.092792

Mass Flow kg/h 722.764264 57.902178 1.550885 113.476297 1.550885 0.17217 0.17217

Liquid Volume Flow m3/d 17.401859 1.903421 0.049037 3.791359 0.049037 0.005006 0.005006

Heat Flow kW -3199.618748 -135.822325 -3.612688 -70.606143 -3.612688 -0.428137 -0.428137

Vapour Fraction 0 0.038614 0 0.000098 0.030961 0.034458

Temperature C 4.619554 3.096668 4.619554 4.628515 4.998826 4.619554

Pressure bar 3.6 1.25 3.6 2.8 6.899245 3.6

Molar Flow m3/h_(gas) 22.428082 22.428082 945.546256 945.546256 1002.519501 1002.519501

Mass Flow kg/h 115.027182 115.027182 722.936434 722.936434 895.865794 895.865794

Liquid Volume Flow m3/d 3.840396 3.840396 17.406865 17.406865 23.150682 23.150682

Heat Flow kW -74.218831 -74.218831 -3200.046885 -3200.046885 -3410.088041 -3410.088041

VUK 1 ukupni wellstream

VUK 1 nakon 1,rusenja

VUK 1 nakon 1,plinovoda

VUK 1 nakon grijalice

VUK 1 nakon 2,rusenja

PLIN BRP 1,3,5 NA CV

VUK 1 PLIN NA CV

VUC 1,3,5 TEKUCA FAZA

NA CV

VUC 1,3,5 TEKUCA FAZA

NAKON RUSENJA

TLAKA

VUK 1 TEKUCA FAZA NA CV

VUK 1 TEKUCA FAZA, RUSENJE

TLAKA

PLIN S CV NA CM

ZEB 2 PLIN NA CM

ZEB 2 TEKUCA FAZA NA CM

VUC, VUK TEKUCA FAZA

NA CV

VUC, VUK TEKUCA FAZA

NA CM

UKUPNI PLIN NA CM

UKUPNA TEKUCA FAZA NA CM

PLIN NA CPS MOLVE

PLIN PV 13200-01

TEG na regeneraciju

TEG 2 na regenerator

KAPLJ, XV-13300-01

plinska faza prema baklji

ukapljeni kondenzat

izlaz na baklju MIH

plinska faza u mjesaliste struja

izlaz prema mjesalistu struja

Plinski kondenzat na LV 13200-02

kondenzat prema

spremniku kondenzata

Slojna voda LV 13200- 01

voda prema spremniku slojne vode

Visefazni fluid prema CPS

MIHOVLJAN

Ulaz 3-fazni separator CPS MIHOVLJAN

Page 3: Materijalna i Energetska Bilanca Kompletni Ispis Rezultata

VUC 1 wellstream WTS 1 VUC 1 zasicen Slojna voda VUC 3 VUC 1 ukupni wellstream

Comp Mole Frac (Nitrogen) 0.028407 0 0.028225 0 0.027876

Comp Mole Frac (CO2) 0.571749 0 0.568067 0 0.561047

Comp Mole Frac (Methane) 0.386715 0 0.384225 0 0.379477

Comp Mole Frac (Ethane) 0.006219 0 0.006179 0 0.006103

Comp Mole Frac (Propane) 0.00258 0 0.002563 0 0.002531

Comp Mole Frac (i-Butane) 0.00058 0 0.000576 0 0.000569

Comp Mole Frac (n-Butane) 0.00084 0 0.000835 0 0.000824

Comp Mole Frac (i-Pentane) 0.00035 0 0.000348 0 0.000343

Comp Mole Frac (n-Pentane) 0.00031 0 0.000308 0 0.000304

Comp Mole Frac (n-Hexane) 0.00038 0 0.000378 0 0.000373

Comp Mole Frac (n-Heptane) 0.00055 0 0.000546 0 0.00054

Comp Mole Frac (n-Octane) 0.00041 0 0.000407 0 0.000402

Comp Mole Frac (n-Nonane) 0.00016 0 0.000159 0 0.000157

Comp Mole Frac (n-Decane) 0.00065 0 0.000646 0 0.000638

Comp Mole Frac (H2S) 0.0001 0 0.000099 0 0.000098

Comp Mole Frac (H2O) 0 1 0.006439 1 0.018718

Comp Mole Frac (TEGlycol) 0 0 0 0 0

Comp Mole Frac (Air) 0 0 0 0 0

VUK 1 plin iz sep VUK 1 kondenzat iz sep VUK 1 voda iz sep

Comp Mole Frac (Nitrogen) 0.035143 0.035141 0.000034 0.000215 0.027829

Comp Mole Frac (CO2) 0.687044 0.687046 0.014308 0.030341 0.573362

Comp Mole Frac (Methane) 0.26104 0.261039 0 0.006195 0.385211

Comp Mole Frac (Ethane) 0.007865 0.007865 0 0.000323 0.006079

Comp Mole Frac (Propane) 0.001991 0.001991 0 0.000332 0.002614

Comp Mole Frac (i-Butane) 0.002987 0.002987 0 0.000141 0.000597

Comp Mole Frac (n-Butane) 0.000697 0.000697 0 0.000265 0.000873

Comp Mole Frac (i-Pentane) 0.000199 0.000199 0 0.00021 0.000374

Comp Mole Frac (n-Pentane) 0.000199 0.000199 0 0.000237 0.000343

Comp Mole Frac (n-Hexane) 0.000796 0.000797 0 0.000724 0.000474

Comp Mole Frac (n-Heptane) 0 0 0 0.002738 0.000839

Comp Mole Frac (n-Octane) 0 0 0 0.004295 0.000621

Comp Mole Frac (n-Nonane) 0 0 0 0.00292 0.000205

Comp Mole Frac (n-Decane) 0 0 0 0.012242 0.000435

Comp Mole Frac (H2S) 0.000205 0.000205 0.000012 0.000011 0.000086

Comp Mole Frac (H2O) 0.001834 0.001833 0.985646 0.938809 0.000055

Comp Mole Frac (TEGlycol) 0 0 0 0 0.000002

Comp Mole Frac (Air) 0 0 0 0 0

VUC 1 1,rusenje tlaka VUC1 prije grijalice VUC 1 nakon grijalice VUC 5 wellstream

Comp Mole Frac (Nitrogen) 0.027876 0.027876 0.027876 0.027876 0.028407

Comp Mole Frac (CO2) 0.561047 0.561047 0.561047 0.561047 0.571749

Comp Mole Frac (Methane) 0.379477 0.379477 0.379477 0.379477 0.386715

Comp Mole Frac (Ethane) 0.006103 0.006103 0.006103 0.006103 0.006219

Comp Mole Frac (Propane) 0.002531 0.002531 0.002531 0.002531 0.00258

Comp Mole Frac (i-Butane) 0.000569 0.000569 0.000569 0.000569 0.00058

Comp Mole Frac (n-Butane) 0.000824 0.000824 0.000824 0.000824 0.00084

Comp Mole Frac (i-Pentane) 0.000343 0.000343 0.000343 0.000343 0.00035

Comp Mole Frac (n-Pentane) 0.000304 0.000304 0.000304 0.000304 0.00031

Comp Mole Frac (n-Hexane) 0.000373 0.000373 0.000373 0.000373 0.00038

Comp Mole Frac (n-Heptane) 0.00054 0.00054 0.00054 0.00054 0.00055

Comp Mole Frac (n-Octane) 0.000402 0.000402 0.000402 0.000402 0.00041

Comp Mole Frac (n-Nonane) 0.000157 0.000157 0.000157 0.000157 0.00016

Comp Mole Frac (n-Decane) 0.000638 0.000638 0.000638 0.000638 0.00065

Comp Mole Frac (H2S) 0.000098 0.000098 0.000098 0.000098 0.0001

Comp Mole Frac (H2O) 0.018718 0.018718 0.018718 0.018718 0

VUC 1,3,5 ukupna tekuca faza prema CV

DEHIDRIRAN PLIN VUC 1,3,5

VUC 1 nakon 2,rusenja tlaka

Page 4: Materijalna i Energetska Bilanca Kompletni Ispis Rezultata

Comp Mole Frac (TEGlycol) 0 0 0 0 0

Comp Mole Frac (Air) 0 0 0 0 0

WTS 5 VUC 5 zasicen Slojna voda VUC 5 VUC 5 ukupni wellstream VUC 5 1,rusenje tlaka

Comp Mole Frac (Nitrogen) 0 0.028302 0 0.027937 0.027937

Comp Mole Frac (CO2) 0 0.569625 0 0.562288 0.562288

Comp Mole Frac (Methane) 0 0.385279 0 0.380316 0.380316

Comp Mole Frac (Ethane) 0 0.006196 0 0.006117 0.006117

Comp Mole Frac (Propane) 0 0.00257 0 0.002537 0.002537

Comp Mole Frac (i-Butane) 0 0.000578 0 0.00057 0.00057

Comp Mole Frac (n-Butane) 0 0.000837 0 0.000826 0.000826

Comp Mole Frac (i-Pentane) 0 0.000349 0 0.000344 0.000344

Comp Mole Frac (n-Pentane) 0 0.000309 0 0.000305 0.000305

Comp Mole Frac (n-Hexane) 0 0.000379 0 0.000374 0.000374

Comp Mole Frac (n-Heptane) 0 0.000548 0 0.000541 0.000541

Comp Mole Frac (n-Octane) 0 0.000408 0 0.000403 0.000403

Comp Mole Frac (n-Nonane) 0 0.000159 0 0.000157 0.000157

Comp Mole Frac (n-Decane) 0 0.000648 0 0.000639 0.000639

Comp Mole Frac (H2S) 0 0.0001 0 0.000098 0.000098

Comp Mole Frac (H2O) 1 0.003713 1 0.016547 0.016547

Comp Mole Frac (TEGlycol) 0 0 0 0 0

Comp Mole Frac (Air) 0 0 0 0 0

VUC 5 prije grijalice VUC 5 nakon grijalice VUC 5 2 rusenje tlaka VUC 3 wellstream WTS 3

Comp Mole Frac (Nitrogen) 0.027937 0.027937 0.027937 0.027089 0

Comp Mole Frac (CO2) 0.562288 0.562288 0.562288 0.575491 0

Comp Mole Frac (Methane) 0.380316 0.380316 0.380316 0.382501 0

Comp Mole Frac (Ethane) 0.006117 0.006117 0.006117 0.00591 0

Comp Mole Frac (Propane) 0.002537 0.002537 0.002537 0.00266 0

Comp Mole Frac (i-Butane) 0.00057 0.00057 0.00057 0.00062 0

Comp Mole Frac (n-Butane) 0.000826 0.000826 0.000826 0.00092 0

Comp Mole Frac (i-Pentane) 0.000344 0.000344 0.000344 0.00041 0

Comp Mole Frac (n-Pentane) 0.000305 0.000305 0.000305 0.00039 0

Comp Mole Frac (n-Hexane) 0.000374 0.000374 0.000374 0.00061 0

Comp Mole Frac (n-Heptane) 0.000541 0.000541 0.000541 0.00128 0

Comp Mole Frac (n-Octane) 0.000403 0.000403 0.000403 0.00103 0

Comp Mole Frac (n-Nonane) 0.000157 0.000157 0.000157 0.00037 0

Comp Mole Frac (n-Decane) 0.000639 0.000639 0.000639 0.00065 0

Comp Mole Frac (H2S) 0.000098 0.000098 0.000098 0.00007 0

Comp Mole Frac (H2O) 0.016547 0.016547 0.016547 0 1

Comp Mole Frac (TEGlycol) 0 0 0 0 0

Comp Mole Frac (Air) 0 0 0 0 0

VUC 3 zasicen Slojna voda 3 VUC 3 ukupni wellstream VUC 3 1,rusenje tlaka VUC 3 prije grijalice

Comp Mole Frac (Nitrogen) 0.026944 0 0.026608 0.026608 0.026608

Comp Mole Frac (CO2) 0.572426 0 0.565271 0.565271 0.565271

Comp Mole Frac (Methane) 0.380463 0 0.375708 0.375708 0.375708

Comp Mole Frac (Ethane) 0.005878 0 0.005805 0.005805 0.005805

Comp Mole Frac (Propane) 0.002646 0 0.002613 0.002613 0.002613

Comp Mole Frac (i-Butane) 0.000617 0 0.000609 0.000609 0.000609

Comp Mole Frac (n-Butane) 0.000915 0 0.000904 0.000904 0.000904

Comp Mole Frac (i-Pentane) 0.000408 0 0.000403 0.000403 0.000403

Comp Mole Frac (n-Pentane) 0.000388 0 0.000383 0.000383 0.000383

Comp Mole Frac (n-Hexane) 0.000607 0 0.000599 0.000599 0.000599

Comp Mole Frac (n-Heptane) 0.001273 0 0.001257 0.001257 0.001257

Comp Mole Frac (n-Octane) 0.001024 0 0.001012 0.001012 0.001012

Comp Mole Frac (n-Nonane) 0.000368 0 0.000363 0.000363 0.000363

Comp Mole Frac (n-Decane) 0.000647 0 0.000638 0.000638 0.000638

Comp Mole Frac (H2S) 0.00007 0 0.000069 0.000069 0.000069

Comp Mole Frac (H2O) 0.005327 1 0.017758 0.017758 0.017758

Comp Mole Frac (TEGlycol) 0 0 0 0 0

Page 5: Materijalna i Energetska Bilanca Kompletni Ispis Rezultata

Comp Mole Frac (Air) 0 0 0 0 0

VUC 3 nakon grijalice VUC 1,3,5 PLIN IZ SEP VUC 1,3,5 KONDENZAT

Comp Mole Frac (Nitrogen) 0.026608 0.026608 0.027304 0.027782 0.003828

Comp Mole Frac (CO2) 0.565271 0.565271 0.563237 0.572633 0.381063

Comp Mole Frac (Methane) 0.375708 0.375708 0.377907 0.384461 0.124158

Comp Mole Frac (Ethane) 0.005805 0.005805 0.005968 0.006068 0.006465

Comp Mole Frac (Propane) 0.002613 0.002613 0.00257 0.002609 0.006659

Comp Mole Frac (i-Butane) 0.000609 0.000609 0.000588 0.000596 0.002827

Comp Mole Frac (n-Butane) 0.000904 0.000904 0.000861 0.000872 0.005315

Comp Mole Frac (i-Pentane) 0.000403 0.000403 0.000371 0.000374 0.004213

Comp Mole Frac (n-Pentane) 0.000383 0.000383 0.000341 0.000342 0.004757

Comp Mole Frac (n-Hexane) 0.000599 0.000599 0.000477 0.000473 0.014513

Comp Mole Frac (n-Heptane) 0.001257 0.001257 0.00087 0.000837 0.054875

Comp Mole Frac (n-Octane) 0.001012 0.001012 0.000683 0.000619 0.086081

Comp Mole Frac (n-Nonane) 0.000363 0.000363 0.000252 0.000205 0.058528

Comp Mole Frac (n-Decane) 0.000638 0.000638 0.000638 0.000434 0.245367

Comp Mole Frac (H2S) 0.000069 0.000069 0.000085 0.000086 0.000127

Comp Mole Frac (H2O) 0.017758 0.017758 0.017848 0.00161 0.001225

Comp Mole Frac (TEGlycol) 0 0 0 0 0

Comp Mole Frac (Air) 0 0 0 0 0

VUC 1,3,5 VODA ZEB 2 wellstream WTS Zb 2 ZEB 2 zasicen Slojna voda ZEB 2

Comp Mole Frac (Nitrogen) 0.000026 0.037643 0 0.037466 0

Comp Mole Frac (CO2) 0.011923 0.661133 0 0.658026 0

Comp Mole Frac (Methane) 0 0.277221 0 0.275918 0

Comp Mole Frac (Ethane) 0 0.010938 0 0.010887 0

Comp Mole Frac (Propane) 0 0.003579 0 0.003563 0

Comp Mole Frac (i-Butane) 0 0.00118 0 0.001174 0

Comp Mole Frac (n-Butane) 0 0.00145 0 0.001443 0

Comp Mole Frac (i-Pentane) 0 0.00065 0 0.000647 0

Comp Mole Frac (n-Pentane) 0 0.00071 0 0.000707 0

Comp Mole Frac (n-Hexane) 0 0.00097 0 0.000965 0

Comp Mole Frac (n-Heptane) 0 0.00121 0 0.001204 0

Comp Mole Frac (n-Octane) 0 0.00097 0 0.000965 0

Comp Mole Frac (n-Nonane) 0 0.00066 0 0.000657 0

Comp Mole Frac (n-Decane) 0 0.00151 0 0.001503 0

Comp Mole Frac (H2S) 0.000005 0.000176 0 0.000176 0

Comp Mole Frac (H2O) 0.988046 0 1 0.0047 1

Comp Mole Frac (TEGlycol) 0 0 0 0 0

Comp Mole Frac (Air) 0 0 0 0 0

ZEB 2 ukupni wellstream ZEB 2 nakon 1,rusenja ZEB 2 plin iz OST ZEB 2 tekuca faza OST ZEB 2 plin 2,rusenje

Comp Mole Frac (Nitrogen) 0.036177 0.036177 0.037679 0.00057 0.037679

Comp Mole Frac (CO2) 0.635377 0.635377 0.66005 0.050457 0.66005

Comp Mole Frac (Methane) 0.266421 0.266421 0.2773 0.008531 0.2773

Comp Mole Frac (Ethane) 0.010512 0.010512 0.010914 0.000979 0.010914

Comp Mole Frac (Propane) 0.00344 0.00344 0.003556 0.000696 0.003556

Comp Mole Frac (i-Butane) 0.001134 0.001134 0.001165 0.000396 0.001165

Comp Mole Frac (n-Butane) 0.001393 0.001393 0.001426 0.000608 0.001426

Comp Mole Frac (i-Pentane) 0.000625 0.000625 0.000631 0.000464 0.000631

Comp Mole Frac (n-Pentane) 0.000682 0.000682 0.000685 0.000607 0.000685

Comp Mole Frac (n-Hexane) 0.000932 0.000932 0.000903 0.00162 0.000903

Comp Mole Frac (n-Heptane) 0.001163 0.001163 0.001055 0.003708 0.001055

Comp Mole Frac (n-Octane) 0.000932 0.000932 0.000754 0.005148 0.000754

Comp Mole Frac (n-Nonane) 0.000634 0.000634 0.000428 0.005518 0.000428

Comp Mole Frac (n-Decane) 0.001451 0.001451 0.000758 0.017887 0.000758

Comp Mole Frac (H2S) 0.00017 0.00017 0.000175 0.000031 0.000175

Comp Mole Frac (H2O) 0.038958 0.038958 0.002519 0.90278 0.002519

Comp Mole Frac (TEGlycol) 0 0 0 0 0

VUC 3 nakon 2 rusenje tlaka

VUC 1,3,5 UKUPNI ULAZ U SEP

Page 6: Materijalna i Energetska Bilanca Kompletni Ispis Rezultata

Comp Mole Frac (Air) 0 0 0 0 0

VUK 1 wellstream Slojna voda VUK 1 WTS VUK 1 VUK 1 zasicen

Comp Mole Frac (Nitrogen) 0.00057 0.035198 0 0 0.035104

Comp Mole Frac (CO2) 0.050457 0.6884 0 0 0.686564

Comp Mole Frac (Methane) 0.008531 0.26144 0 0 0.260743

Comp Mole Frac (Ethane) 0.000979 0.007877 0 0 0.007856

Comp Mole Frac (Propane) 0.000696 0.001994 0 0 0.001989

Comp Mole Frac (i-Butane) 0.000396 0.002991 0 0 0.002983

Comp Mole Frac (n-Butane) 0.000608 0.000698 0 0 0.000696

Comp Mole Frac (i-Pentane) 0.000464 0.000199 0 0 0.000199

Comp Mole Frac (n-Pentane) 0.000607 0.000199 0 0 0.000199

Comp Mole Frac (n-Hexane) 0.00162 0.000798 0 0 0.000796

Comp Mole Frac (n-Heptane) 0.003708 0 0 0 0

Comp Mole Frac (n-Octane) 0.005148 0 0 0 0

Comp Mole Frac (n-Nonane) 0.005518 0 0 0 0

Comp Mole Frac (n-Decane) 0.017887 0 0 0 0

Comp Mole Frac (H2S) 0.000031 0.000205 0 0 0.000205

Comp Mole Frac (H2O) 0.90278 0 1 1 0.002667

Comp Mole Frac (TEGlycol) 0 0 0 0 0

Comp Mole Frac (Air) 0 0 0 0 0

VUK 1 ukupni wellstream VUK 1 nakon 1,rusenja VUK 1 nakon 1,plinovoda VUK 1 nakon grijalice VUK 1 nakon 2,rusenja

Comp Mole Frac (Nitrogen) 0.03442 0.03442 0.03442 0.03442 0.03442

Comp Mole Frac (CO2) 0.673196 0.673196 0.673196 0.673196 0.673196

Comp Mole Frac (Methane) 0.255666 0.255666 0.255666 0.255666 0.255666

Comp Mole Frac (Ethane) 0.007703 0.007703 0.007703 0.007703 0.007703

Comp Mole Frac (Propane) 0.00195 0.00195 0.00195 0.00195 0.00195

Comp Mole Frac (i-Butane) 0.002925 0.002925 0.002925 0.002925 0.002925

Comp Mole Frac (n-Butane) 0.000683 0.000683 0.000683 0.000683 0.000683

Comp Mole Frac (i-Pentane) 0.000195 0.000195 0.000195 0.000195 0.000195

Comp Mole Frac (n-Pentane) 0.000195 0.000195 0.000195 0.000195 0.000195

Comp Mole Frac (n-Hexane) 0.00078 0.00078 0.00078 0.00078 0.00078

Comp Mole Frac (n-Heptane) 0 0 0 0 0

Comp Mole Frac (n-Octane) 0 0 0 0 0

Comp Mole Frac (n-Nonane) 0 0 0 0 0

Comp Mole Frac (n-Decane) 0 0 0 0 0

Comp Mole Frac (H2S) 0.000201 0.000201 0.000201 0.000201 0.000201

Comp Mole Frac (H2O) 0.022085 0.022085 0.022085 0.022085 0.022085

Comp Mole Frac (TEGlycol) 0 0 0 0 0

Comp Mole Frac (Air) 0 0 0 0 0

VUK 1 PLIN PREMA CV PLIN BRP 1,3,5 NA CV VUK 1 PLIN NA CV

Comp Mole Frac (Nitrogen) 0.035215 0.000034 0.027829 0.035215 0.000215

Comp Mole Frac (CO2) 0.688107 0.014308 0.573362 0.688107 0.030341

Comp Mole Frac (Methane) 0.261652 0 0.385211 0.261652 0.006195

Comp Mole Frac (Ethane) 0.007883 0 0.006079 0.007883 0.000323

Comp Mole Frac (Propane) 0.001996 0 0.002614 0.001996 0.000332

Comp Mole Frac (i-Butane) 0.002994 0 0.000597 0.002994 0.000141

Comp Mole Frac (n-Butane) 0.000699 0 0.000873 0.000699 0.000265

Comp Mole Frac (i-Pentane) 0.0002 0 0.000374 0.0002 0.00021

Comp Mole Frac (n-Pentane) 0.0002 0 0.000343 0.0002 0.000237

Comp Mole Frac (n-Hexane) 0.000798 0 0.000474 0.000798 0.000724

Comp Mole Frac (n-Heptane) 0 0 0.000839 0 0.002738

Comp Mole Frac (n-Octane) 0 0 0.000621 0 0.004295

Comp Mole Frac (n-Nonane) 0 0 0.000205 0 0.00292

Comp Mole Frac (n-Decane) 0 0 0.000435 0 0.012242

Comp Mole Frac (H2S) 0.000204 0.000012 0.000086 0.000204 0.000011

ZEB 2 tekuca faza 2,rusenje tlaka

VUK 1 UKUPNA TEKUCA FAZA

VUC 1,3,5 TEKUCA FAZA NA CV

Page 7: Materijalna i Energetska Bilanca Kompletni Ispis Rezultata

Comp Mole Frac (H2O) 0.000052 0.985646 0.000055 0.000052 0.938809

Comp Mole Frac (TEGlycol) 0.000001 0 0.000002 0.000001 0

Comp Mole Frac (Air) 0 0 0 0 0

UKUPNI PLIN CV PLIN S CV NA CM

Comp Mole Frac (Nitrogen) 0.000215 0.000034 0.000034 0.029658 0.029658

Comp Mole Frac (CO2) 0.030341 0.014308 0.014308 0.601777 0.601777

Comp Mole Frac (Methane) 0.006195 0 0 0.354613 0.354613

Comp Mole Frac (Ethane) 0.000323 0 0 0.006526 0.006526

Comp Mole Frac (Propane) 0.000332 0 0 0.002461 0.002461

Comp Mole Frac (i-Butane) 0.000141 0 0 0.00119 0.00119

Comp Mole Frac (n-Butane) 0.000265 0 0 0.00083 0.00083

Comp Mole Frac (i-Pentane) 0.00021 0 0 0.000331 0.000331

Comp Mole Frac (n-Pentane) 0.000237 0 0 0.000308 0.000308

Comp Mole Frac (n-Hexane) 0.000724 0 0 0.000554 0.000554

Comp Mole Frac (n-Heptane) 0.002738 0 0 0.000631 0.000631

Comp Mole Frac (n-Octane) 0.004295 0 0 0.000467 0.000467

Comp Mole Frac (n-Nonane) 0.00292 0 0 0.000155 0.000155

Comp Mole Frac (n-Decane) 0.012242 0 0 0.000327 0.000327

Comp Mole Frac (H2S) 0.000011 0.000012 0.000012 0.000115 0.000115

Comp Mole Frac (H2O) 0.938809 0.985646 0.985646 0.000054 0.000054

Comp Mole Frac (TEGlycol) 0 0 0 0.000002 0.000002

Comp Mole Frac (Air) 0 0 0 0 0

ZEB 2 PLIN NA CM UKUPNI PLIN NA CM

Comp Mole Frac (Nitrogen) 0.037679 0.00057 0.000164 0.000164 0.03056

Comp Mole Frac (CO2) 0.66005 0.050457 0.025822 0.025822 0.60833

Comp Mole Frac (Methane) 0.2773 0.008531 0.004449 0.004449 0.345919

Comp Mole Frac (Ethane) 0.010914 0.000979 0.000232 0.000232 0.00702

Comp Mole Frac (Propane) 0.003556 0.000696 0.000239 0.000239 0.002584

Comp Mole Frac (i-Butane) 0.001165 0.000396 0.000101 0.000101 0.001187

Comp Mole Frac (n-Butane) 0.001426 0.000608 0.00019 0.00019 0.000897

Comp Mole Frac (i-Pentane) 0.000631 0.000464 0.000151 0.000151 0.000365

Comp Mole Frac (n-Pentane) 0.000685 0.000607 0.00017 0.00017 0.00035

Comp Mole Frac (n-Hexane) 0.000903 0.00162 0.00052 0.00052 0.000593

Comp Mole Frac (n-Heptane) 0.001055 0.003708 0.001966 0.001966 0.000679

Comp Mole Frac (n-Octane) 0.000754 0.005148 0.003084 0.003084 0.000499

Comp Mole Frac (n-Nonane) 0.000428 0.005518 0.002097 0.002097 0.000185

Comp Mole Frac (n-Decane) 0.000758 0.017887 0.008792 0.008792 0.000375

Comp Mole Frac (H2S) 0.000175 0.000031 0.000012 0.000012 0.000122

Comp Mole Frac (H2O) 0.002519 0.90278 0.952011 0.952011 0.000332

Comp Mole Frac (TEGlycol) 0 0 0 0 0.000002

Comp Mole Frac (Air) 0 0 0 0 0

PLIN NA CPS MOLVE PLIN PV 13200-01 TEG ulaz TEG na regeneraciju

Comp Mole Frac (Nitrogen) 0.000255 0.03056 0.007362 0 0.00261

Comp Mole Frac (CO2) 0.031341 0.60833 0.809056 0 0.131664

Comp Mole Frac (Methane) 0.005363 0.345919 0.153568 0 0.004948

Comp Mole Frac (Ethane) 0.000399 0.00702 0.010601 0 0.000157

Comp Mole Frac (Propane) 0.000341 0.002584 0.007106 0 0.000079

Comp Mole Frac (i-Butane) 0.000167 0.001187 0.002279 0 0.000006

Comp Mole Frac (n-Butane) 0.000284 0.000897 0.003094 0 0.00001

Comp Mole Frac (i-Pentane) 0.000221 0.000365 0.001119 0 0.000003

Comp Mole Frac (n-Pentane) 0.000268 0.00035 0.00102 0 0.000002

Comp Mole Frac (n-Hexane) 0.000766 0.000593 0.000845 0 0.000002

Comp Mole Frac (n-Heptane) 0.002356 0.000679 0.000729 0 0.000002

Comp Mole Frac (n-Octane) 0.003547 0.000499 0.000302 0 0.000001

VUC 1,3,5 TEKUCA FAZA NAKON RUSENJA

TLAKA

VUK 1 TEKUCA FAZA NA CV

VUK 1 TEKUCA FAZA, RUSENJE TLAKA

ZEB 2 TEKUCA FAZA NA CM

VUC, VUK TEKUCA FAZA NA CV

VUC, VUK TEKUCA FAZA NA CM

UKUPNA TEKUCA FAZA NA CM

Page 8: Materijalna i Energetska Bilanca Kompletni Ispis Rezultata

Comp Mole Frac (n-Nonane) 0.002864 0.000185 0.000071 0 0

Comp Mole Frac (n-Decane) 0.01083 0.000375 0.00008 0 0

Comp Mole Frac (H2S) 0.000016 0.000122 0.000336 0 0.000078

Comp Mole Frac (H2O) 0.94098 0.000332 0.002432 0.0063 0.502027

Comp Mole Frac (TEGlycol) 0 0.000002 0 0.9937 0.35841

Comp Mole Frac (Air) 0 0 0 0 0

TEG 2 ULAZ TEG 2 na regenerator KAPLJ, XV-13300-01 izlaz rema baklji plinska faza prema baklji

Comp Mole Frac (Nitrogen) 0 0.003438 0 0.007362 0.001044

Comp Mole Frac (CO2) 0 0.159931 0.002314 0.809056 0.867056

Comp Mole Frac (Methane) 0 0.003433 0 0.153568 0.07025

Comp Mole Frac (Ethane) 0 0.000202 0 0.010601 0.01707

Comp Mole Frac (Propane) 0 0.000059 0 0.007106 0.016738

Comp Mole Frac (i-Butane) 0 0.00003 0 0.002279 0.005833

Comp Mole Frac (n-Butane) 0 0.000008 0 0.003094 0.008017

Comp Mole Frac (i-Pentane) 0 0.000001 0 0.001119 0.002915

Comp Mole Frac (n-Pentane) 0 0.000001 0 0.00102 0.00265

Comp Mole Frac (n-Hexane) 0 0.000003 0 0.000845 0.002153

Comp Mole Frac (n-Heptane) 0 0 0 0.000729 0.001812

Comp Mole Frac (n-Octane) 0 0 0 0.000302 0.000732

Comp Mole Frac (n-Nonane) 0 0 0 0.000071 0.000167

Comp Mole Frac (n-Decane) 0 0 0 0.00008 0.000184

Comp Mole Frac (H2S) 0 0.000189 0.000003 0.000336 0.000624

Comp Mole Frac (H2O) 0.0063 0.492569 0.997683 0.002432 0.002755

Comp Mole Frac (TEGlycol) 0.9937 0.340134 0 0 0

Comp Mole Frac (Air) 0 0 0 0 0

ukapljeni kondenzat izlaz na baklju MIH

Comp Mole Frac (Nitrogen) 0.000002 0.001044 0.003357 0.003357 0.000042

Comp Mole Frac (CO2) 0.020435 0.867056 0.993105 0.993105 0.053127

Comp Mole Frac (Methane) 0.000517 0.07025 0.000008 0.000008 0.00321

Comp Mole Frac (Ethane) 0.00089 0.01707 0 0 0.001515

Comp Mole Frac (Propane) 0.003803 0.016738 0 0 0.004303

Comp Mole Frac (i-Butane) 0.003894 0.005833 0 0 0.003969

Comp Mole Frac (n-Butane) 0.007921 0.008017 0 0 0.007924

Comp Mole Frac (i-Pentane) 0.008374 0.002915 0 0 0.008163

Comp Mole Frac (n-Pentane) 0.010735 0.00265 0 0 0.010422

Comp Mole Frac (n-Hexane) 0.034196 0.002153 0 0 0.032959

Comp Mole Frac (n-Heptane) 0.10832 0.001812 0 0 0.104207

Comp Mole Frac (n-Octane) 0.164391 0.000732 0 0 0.158071

Comp Mole Frac (n-Nonane) 0.133025 0.000167 0 0 0.127894

Comp Mole Frac (n-Decane) 0.503381 0.000184 0 0 0.483951

Comp Mole Frac (H2S) 0.000047 0.000624 0.000423 0.000423 0.000069

Comp Mole Frac (H2O) 0.000069 0.002755 0.003106 0.003106 0.000173

Comp Mole Frac (TEGlycol) 0 0 0 0 0

Comp Mole Frac (Air) 0 0 0 0 0

Slojna voda LV 13200- 01

Comp Mole Frac (Nitrogen) 0.000042 0.000001 0.000001 0.000255 0.000255

Comp Mole Frac (CO2) 0.053127 0.002411 0.002411 0.031341 0.031341

Comp Mole Frac (Methane) 0.00321 0 0 0.005363 0.005363

Comp Mole Frac (Ethane) 0.001515 0 0 0.000399 0.000399

Comp Mole Frac (Propane) 0.004303 0 0 0.000341 0.000341

Comp Mole Frac (i-Butane) 0.003969 0 0 0.000167 0.000167

Comp Mole Frac (n-Butane) 0.007924 0 0 0.000284 0.000284

Comp Mole Frac (i-Pentane) 0.008163 0 0 0.000221 0.000221

Comp Mole Frac (n-Pentane) 0.010422 0 0 0.000268 0.000268

Comp Mole Frac (n-Hexane) 0.032959 0 0 0.000766 0.000766

Comp Mole Frac (n-Heptane) 0.104207 0 0 0.002356 0.002356

plinska faza u mjesaliste struja

izlaz prema mjesalistu struja

Plinski kondenzat na LV 13200-02

kondenzat prema spremniku kondenzata

voda prema spremniku slojne vode

Visefazni fluid prema CPS MIHOVLJAN

Ulaz 3-fazni separator CPS MIHOVLJAN

Page 9: Materijalna i Energetska Bilanca Kompletni Ispis Rezultata

Comp Mole Frac (n-Octane) 0.158071 0 0 0.003547 0.003547

Comp Mole Frac (n-Nonane) 0.127894 0 0 0.002864 0.002864

Comp Mole Frac (n-Decane) 0.483951 0 0 0.01083 0.01083

Comp Mole Frac (H2S) 0.000069 0.000003 0.000003 0.000016 0.000016

Comp Mole Frac (H2O) 0.000173 0.997585 0.997585 0.94098 0.94098

Comp Mole Frac (TEGlycol) 0 0 0 0 0

Comp Mole Frac (Air) 0 0 0 0 0

Page 10: Materijalna i Energetska Bilanca Kompletni Ispis Rezultata

Unit Qpli5 Q gr5 Qcj3 Qgrij3 Qgr1 Qpl1 QplVuk1

Heat Flow kW 26.503044 80.120167 87.253411 125.190042 33.804973 33.669251 23.375452

Q gr VUk1 Q CJ135 QPLVUC1 QKOND VUC135 QCJ VUK,KTEK QCJUKPL QSDF QASS

Heat Flow 126.542575 42.849858 0.124914 11.553034 5.56016 169.048561 28.108173 6.702904

ASD ASDF FGH Grijanje 2 Grijanje spremnika kondenzata

Heat Flow 2.369444 252.677323 0.114564 0 0