slutrapport - Kemiteknik

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6.6. Totalkostnad för anläggningen ...................................................................................... 446.7. Investeringskalkyl ......................................................................................................... 446.8. Känslighetsanalys .......................................................................................................... 456.8.1. Elpriset ................................................................................................................... 466.8.2. Metanpriset ............................................................................................................. 466.8.3. Koldioxidskatten .................................................................................................... 476.9. Slutsats .......................................................................................................................... 48Bilaga 1 .................................................................................................................................... 55Bilaga 2 .................................................................................................................................... 57Bilaga 3 .................................................................................................................................... 58Skriptfil: Angref.m ................................................................................................................ 58Skriptfil: prim.m ................................................................................................................... 59Skriptfil: sek.m ..................................................................................................................... 60Skriptfil: comb.m .................................................................................................................. 61Skriptfil: comb_prim.m ........................................................................................................ 62Skriptfil: n_eff_prim.m ......................................................................................................... 62Skriptfil: n_eff_sek.m ........................................................................................................... 63Skriptfil: vvx.m ..................................................................................................................... 64Bilaga 4 .................................................................................................................................... 65Primärreformering ................................................................................................................ 65Sekundärreformering ............................................................................................................ 66Driftskomponenter ............................................................................................................... 66Bilaga 5 .................................................................................................................................... 68Bilaga 6 .................................................................................................................................... 69Skriptfil för HT-reaktor: vgas.m ........................................................................................... 69Skriptfil för LT-reaktor: vgas2.m ......................................................................................... 71Bilaga 7 .................................................................................................................................... 74WGS-HT .............................................................................................................................. 74Dimensionering .................................................................................................................... 74Ekonomi ................................................................................................................................ 74WGS-LT ............................................................................................................................... 75Dimensionering .................................................................................................................... 75Ekonomi ................................................................................................................................ 75
Driftskomponenter ............................................................................................................... 76Bilaga 8 .................................................................................................................................... 77Bilaga 9 .................................................................................................................................... 79Bilaga 10 .................................................................................................................................. 81Bilaga 11 .................................................................................................................................. 82
Page 2 and 3: SammanfattningAmmoniak är en av de
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Page 8 and 9: 1. IntroduktionI pappersmassaindust
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Page 14 and 15: tillverkade 2000 ton/dag. I priset
Page 16 and 17: Men detta betydde inte att kobolt f
Page 18 and 19: Diagram 2-1 | Uppdelning av kloralk
Page 20 and 21: 3.1. Primär- och sekundärreformer
Page 22 and 23: Figur 3-2 | Gibbs fria energi för
Page 24 and 25: Reaktorerna består av packade bäd
Page 26 and 27: 3.2.4. KinetikEftersom mekanismen b
Page 28 and 29: Genom att utföra reaktionen kataly
Page 30 and 31: (3.4.3.3)Ekvation (3.4.3.4) nedan b
Page 32 and 33: Det ökande behovet av konstgödsel
Page 34 and 35: 5.1.2. SäkerhetsaspekterDet finns
Page 36 and 37: 100% MetanÅngaPrimär-reformerJack
Page 38 and 39: Figur 6-4 | Profiler för sekundär
Page 40 and 41: Material- och energibalanser har sa
Page 42 and 43: I tabell 6-4 återfinns de data som
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Page 48 and 49: Tabell 6-11 | Koncentrationer av ko
Page 50 and 51: Kompressor 5 149 107 500Pump 5 0 *P
Page 52 and 53: Figur 6-9 | Arrangering av årliga
Page 54 and 55: Pris (USD/ton)Pris (USD/ton)680.006
Page 56 and 57:
Figur 6-13 | Resultat av känslighe
Page 58 and 59:
[20] http://www.ne.se/lang/metan (2
Page 60 and 61:
[52] http://www.ted.com/talks/lang/
Page 62 and 63:
Bilaga 1Tabell 1: Fysikaliska egens
Page 64:
Bilaga 2Konstanterna a, b, c, d och
Page 67 and 68:
kh2=(6.12e-9)*exp(82.90e3/(R*Tk));D
Page 69 and 70:
Skriptfil: comb_prim.mfunction [ut]
Page 71 and 72:
Skriptfil: vvx.mfunction [] = vvx(W
Page 73 and 74:
SekundärreformeringDimensioneringV
Page 75 and 76:
Bilaga 568
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% legend('metan','Kolmonoxid','kold
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xlabel('Katalysatormängd (kg)');su
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Bilaga 7WGS-HTDimensioneringFör at
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Katalysatorpriset är baserat på 2
Page 86 and 87:
Bilaga 9Processteg Kostnad (SEK) Pr
Page 88 and 89:
Bilaga 1081
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