Design og modellering af metanolanlæg til VEnzin-visionen Bilag

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11. Råoliepris Råoliepris fra Bloomberg.com fra d. 5/03-2007. http://www.bloomberg.com/markets/commodities/energyprices.html hentet d. 5/3- 2007.
12. Metanolpris Metanolpriser fra Methanex (verdens største metanolproducent). Månedspriser fra år 2002 frem til marts 2007: http://www.methanex.com/products/documents/MxAvgPrice_Feb262007.pdf hentet d. 6/3-2007. Linket ovenfor bliver ændret hver måned, i takt med at nye månedspriser bliver tilføjet. Det aktuelle link til de historiske månedspriser kan findes på: http://www.methanex.com/products/methanolprice.html
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Design og modellering af metanolanl
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2 Resumé I forbindelse med DONG En
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4 Indholdsfortegnelse 1 Abstract...
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5 Indledning Baggrunden for dette p
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7 Design og statisk modellering af
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Brint er specielt fordelagtig til m
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Ligning 7.1: Den specifikke varmeka
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DNA-navn: DRYER_04 Forgasser Forgas
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T Fordampning Pinch points Figur 7.
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Massestrøm af Metanol/vand-blandin
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Parameter Værdi Komponenter Evt. k
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7.2 Anlægskonfigurationer Den opby
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7.3 Økonomi For at kunne vurdere o
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Input-priser Kilde Elektricitet 18
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7.4 Termoøkonomisk analyse Der er
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Komponent Produkt(er) Spild Elektro
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Tabet i fysisk exergi forekommer ho
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Anlæg 1 Total: 320 MWex (292 MW) 7
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antagelse, da naturgasnettet er try
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246 562 112 Anlæg 1 Total: 1222 mi
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Brændsel Pris Kilde [kr/L] [kr/GJe
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Metanolomkostning [kr/GJex] 500 450
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7.5.2 Parametervariation Nedenfor e
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Udkondenseret metanol [%] 100 95 90
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Metanolrenhed efter destillation [m
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vandkoncentrationen i syngassen fal
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Metanolexergivirkningsgrad [%] 73 7
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Metanolrenhed efter destillation [m
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Dette betyder at den metanolholdige
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Atmosfærisk forgasning (1 bar) Try
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7.6 Diskussion I parametervariation
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7.6.2 Alternative anlægsdesign Ned
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8 Benyttelse af underjordiske gasla
Page 67 and 68: 8.2 Scenarier Der er undersøgt 2 s
Page 69 and 70: Ligning 8.5: Reference-el-omkostnin
Page 71 and 72: Ligning 8.13: Tidskonstant for lage
Page 73 and 74: Brintlagerbeholdning [MWh] 3000 250
Page 75 and 76: Brintlagerbeholdning [MWh] 400 350
Page 77 and 78: den time, hvor regulatorligningen b
Page 79 and 80: El-pris-funktionen [kr/MWh] 500 450
Page 81 and 82: Brintlagerbeholdning [MWh] 100 90 8
Page 83 and 84: Omkostninger [%] 100 90 80 70 60 50
Page 85 and 86: Sparede omkostninger [%] 30 25 20 1
Page 87 and 88: selvstændig investering og de omko
Page 89 and 90: Tilbagebetalingstid (beregnet ud fr
Page 91 and 92: Sparede omkostninger i nutidsværdi
Page 93 and 94: Tilbagebetalingstid [år] 15 10 5 0
Page 95 and 96: 8.4 Diskussion Resultaterne præsen
Page 97 and 98: El-pris [kr/Mwh] 400 350 300 250 20
Page 99 and 100: 9 Konklusion I den første del af r
Page 101 and 102: http://www.energyserver.net/ET1/Def
Page 103 and 104: 11 Nomenklaturliste c omkostning pe
Page 105 and 106: Design og modellering af metanolanl
Page 107 and 108: 25. Flowsheets for metanolanlæg -
Page 109 and 110: 2. Forgasserpris - Choren Choren In
Page 111 and 112: 4. El-afgifter og -tariffer GE-NET
Page 113 and 114: 6. Naturgasafgifter - DONG Energy N
Page 115 and 116: 8. Benzinforbrug til vejtransport E
Page 117: 10. Benzinafgift Benzinafgifter fra
Page 121 and 122: Methanex Non-Discounted Reference P
Page 127 and 128: 14. Metanolproduktion, NZIC New Zea
Page 129 and 130: Maui Gas Supply Kapuni Gas Supply N
Page 131 and 132: Gas metering and letdown The proces
Page 133 and 134: Methanol Distillation Crude methano
Page 135 and 136: Product Gasoline Pipeline (250 mm N
Page 137 and 138: steam, preheat the reactants (steam
Page 139 and 140: As it is very difficult to separate
Page 141 and 142: Operational processes A schematic l
Page 143 and 144: The reaction of the synthesis gas c
Page 145 and 146: Figure 15 - Flowsheet of the MTG pr
Page 147 and 148: 15. Metanolproduktion, Nykomb Nykom
Page 149 and 150: NYKOMB SYNERGETICS 2. Methanol Plan
Page 151 and 152: NYKOMB SYNERGETICS 6. Investment Es
Page 153 and 154: NYKOMB SYNERGETICS 9. Logistics and
Page 155 and 156: 16. Metanolproduktion, Wikipedia Wi
Page 157 and 158: 18. Flowsheet for et metanolanlæg
Page 159 and 160: 20. Flowsheet for metanolanlæg - u
Page 161 and 162: 21. Flowsheet for metanolanlæg - t
Page 163 and 164: 22. Flowsheet for metanolanlæg - t
Page 165 and 166: 23. Flowsheets for metanolanlæg -
Page 167 and 168: 0 1 1 1 P 2 M type NOD* 2 1 type NO
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0 1 1 1 P 2 M type NOD* 9 2 type NO
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24. Flowsheets for metanolanlæg -
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27. Flowsheet for metanolanlæg - f
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28. Flowsheet for metanolanlæg - f
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29. Matlab-kode til Scenarie 1
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18-03-07 23:10 D:\DTU\Eksamensproje
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Sparede omkostninger i nutidsværdi
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Sparede omkostninger i nutidsværdi
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32. DNA-kode for metanolanlæg
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metanolanlaeg.dna d:/DTU/Eksamenspr
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metanolanlaeg.dna d:/DTU/Eksamenspr
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33. Dokumentation for tilføjede DN
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17.121.4 Conditions ˙m1 > 0 ˙m2 <
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9. - 10. - 11. - 12. - 13. - 14. -
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17.123 GASIFI_3_VENZIN Gasifier wit
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13. - 14. - 15. - 16. - 17. - 18. -
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17.124 GASCLE_2 Syngas cleaning. Th
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38. Compound number 39. Compound nu
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43. - 44. - 45. - 46. - 47. - 48. -
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17.124.5 Example struc Cleaner GASC
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10. - 11. - 12. - 13. - 17.125.4 Co
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7. - 8. - 9. - 10. - 11. - 12. - 13
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17.126.4 Conditions ˙m1 > 0 ˙m2 <
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11. - 12. - 13. - 14. - 15. - 16. -
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17.128 SET_M Utility component for
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4. - 5. - 6. - 7. - 8. - 9. - 10. -
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17.129.4 Conditions ˙m1 > 0 ˙m2 <
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17.130.4 Conditions ˙m1 > 0 ˙m2 <
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17.131.2 Equations Number of equati
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17.132 EL-MOTOR Motor with efficien
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8. - 9. - 17.133.3 Conditions ˙m1
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17.135 MIXER_03 Mixer for ideal gas
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33. - 34. - 35. - 36. - 37. - 38. -
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17.137 SET_X Utility component for
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17.138.4 Conditions ˙m1 > 0 ˙m2 <
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17.140 SET_FLOW Utillity component
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17.142 SET_TEMP2 Utillity component
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34. Tilføjede komponenter til DNA
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VEnzin.for c:/dna/source/ C C Param
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VEnzin.for c:/dna/source/ CA ANTED
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VEnzin.for c:/dna/source/ IF (MDOT(
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VEnzin.for c:/dna/source/ MMVAR(1)
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VEnzin.for c:/dna/source/ ENDDO DO
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VEnzin.for c:/dna/source/ $fluid O2
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VEnzin.for c:/dna/source/ C−−
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VEnzin.for c:/dna/source/ CA FKOMP
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VEnzin.for c:/dna/source/ ENDDO NIN
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VEnzin.for c:/dna/source/ C Subrout
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VEnzin.for c:/dna/source/ CALL STAT
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VEnzin.for c:/dna/source/ CA 3: Flu
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VEnzin.for c:/dna/source/ C C C M_B
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VEnzin.for c:/dna/source/ C C SETFL
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VEnzin.for c:/dna/source/ C C GASCO
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VEnzin.for c:/dna/source/ RES(5) =
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VEnzin.for c:/dna/source/ c c c E2=
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VEnzin.for c:/dna/source/ C C HEATE
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VEnzin.for c:/dna/source/ $ ’$\\d
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VEnzin.for c:/dna/source/ c 1 = Wat
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VEnzin.for c:/dna/source/ CA 4: Fin
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VEnzin.for c:/dna/source/ CL K_MED
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VEnzin.for c:/dna/source/ CA MEDIE
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VEnzin.for c:/dna/source/ CA −4 :
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VEnzin.for c:/dna/source/ C ENDDO E
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VEnzin.for c:/dna/source/ MEDIE(2)
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VEnzin.for c:/dna/source/ C C 400 C
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VEnzin.for c:/dna/source/ GOTO 9999
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VEnzin.for c:/dna/source/ MEDIE(1)
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VEnzin.for c:/dna/source/ RES(1) =
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35. Metanol (fluid) til DNA - Fortr
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methanol.for d:/DTU/Eksamensprojekt
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Design og modellering af metanolanlæg til VEnzin-visionen Bilag

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