Design og modellering af metanolanlæg til VEnzin-visionen Bilag

More documents

Recommendations

Info

methanol.for d:/DTU/Eksamensprojekt/bilag/ 17/19 19−03−2007 N_i(4)=3.26593134060d0 N_i(5)=−4.11425343805d0 N_i(6)=3.46397741254d0 N_i(7)=−0.0836443967590d0 N_i(8)=−0.369240098923d0 N_i(9)=0.00313180842152d0 N_i(10)=0.603201474111d0 N_i(11)=−0.231158593638d0 N_i(12)=0.106114844945d0 N_i(13)=−0.0792228164995d0 N_i(14)=−0.0000422419150975d0 N_i(15)=0.00758196739214d0 N_i(16)=−0.0000244617434701d0 N_i(17)=0.00000115080328802d0 N_i(18)=−12.5099747447d0 N_i(19)=27.0392835391d0 N_i(20)=−21.2070717086d0 N_i(21)=6.32799472270d0 N_i(22)=14.3687921636d0 N_i(23)=−28.7450766617d0 N_i(24)=18.5397216068d0 N_i(25)=−3.88720372879d0 N_i(26)=−4.16602487963d0 N_i(27)=5.29665875982d0 N_i(28)=0.509360272812d0 N_i(29)=−3.30257604839d0 N_i(30)=−0.311045210826d0 N_i(31)=0.273460830583d0 N_i(32)=0.518916583979d0 N_i(33)=−0.00227570803104d0 N_i(34)=0.0211658196182d0 N_i(35)=−0.0114335123221d0 N_i(36)=0.00249860798459d0 N_i(37)=−8.19291988442d0 N_i(38)=0.478601004557d0 N_i(39)=−0.444161392885d0 N_i(40)=0.179621810410d0 N_i(41)=−0.687602278259d0 N_i(42)=2.40459848295d0 N_i(43)=−6.88463987466d0 N_i(44)=1.13992982501d0 r_i(1)=1 r_i(2)=1 r_i(3)=1 r_i(4)=1 r_i(5)=2 r_i(6)=2 r_i(7)=2 r_i(8)=2 r_i(9)=2 r_i(10)=3 r_i(11)=3 r_i(12)=3 r_i(13)=4 r_i(14)=4 r_i(15)=5 r_i(16)=6 r_i(17)=7 r_i(18)=1 r_i(19)=1 r_i(20)=1 r_i(21)=1 r_i(22)=2 r_i(23)=2 r_i(24)=2 r_i(25)=2 r_i(26)=3 r_i(27)=4 r_i(28)=5 r_i(29)=5 r_i(30)=5 r_i(31)=5 r_i(32)=6 r_i(33)=9 r_i(34)=6 r_i(35)=6 r_i(36)=4
methanol.for d:/DTU/Eksamensprojekt/bilag/ 18/19 19−03−2007 r_i(37)=1 r_i(38)=1 r_i(39)=1 r_i(40)=1 r_i(41)=1 r_i(42)=3 r_i(43)=3 r_i(44)=3 s_i(1)=0 s_i(2)=1 s_i(3)=2 s_i(4)=3 s_i(5)=1 s_i(6)=2 s_i(7)=3 s_i(8)=4 s_i(9)=6 s_i(10)=0 s_i(11)=3 s_i(12)=4 s_i(13)=0 s_i(14)=7 s_i(15)=1 s_i(16)=6 s_i(17)=7 s_i(18)=1 s_i(19)=2 s_i(20)=3 s_i(21)=4 s_i(22)=1 s_i(23)=2 s_i(24)=3 s_i(25)=5 s_i(26)=1 s_i(27)=2 s_i(28)=1 s_i(29)=2 s_i(30)=4 s_i(31)=5 s_i(32)=2 s_i(33)=5 s_i(34)=9 s_i(35)=14 s_i(36)=19 k_i(18)=2 k_i(19)=2 k_i(20)=2 k_i(21)=2 k_i(22)=2 k_i(23)=2 k_i(24)=2 k_i(25)=2 k_i(26)=2 k_i(27)=2 k_i(28)=2 k_i(29)=2 k_i(30)=2 k_i(31)=2 k_i(32)=2 k_i(33)=2 k_i(34)=4 k_i(35)=4 k_i(36)=6 k_i(37)=2 k_i(38)=3 k_i(39)=2 k_i(40)=4 k_i(41)=2 k_i(42)=3 k_i(43)=2 k_i(44)=4 j_i(37)=2 j_i(38)=2 j_i(39)=3 j_i(40)=3
Page 1 and 2:
Design og modellering af metanolanl
Page 3 and 4:
2 Resumé I forbindelse med DONG En
Page 5 and 6:
4 Indholdsfortegnelse 1 Abstract...
Page 7 and 8:
5 Indledning Baggrunden for dette p
Page 9 and 10:
7 Design og statisk modellering af
Page 11 and 12:
Brint er specielt fordelagtig til m
Page 13 and 14:
Ligning 7.1: Den specifikke varmeka
Page 15 and 16:
DNA-navn: DRYER_04 Forgasser Forgas
Page 17 and 18:
T Fordampning Pinch points Figur 7.
Page 19 and 20:
Massestrøm af Metanol/vand-blandin
Page 21 and 22:
Parameter Værdi Komponenter Evt. k
Page 23 and 24:
7.2 Anlægskonfigurationer Den opby
Page 25 and 26:
7.3 Økonomi For at kunne vurdere o
Page 27 and 28:
Input-priser Kilde Elektricitet 18
Page 29 and 30:
7.4 Termoøkonomisk analyse Der er
Page 31 and 32:
Komponent Produkt(er) Spild Elektro
Page 33 and 34:
Tabet i fysisk exergi forekommer ho
Page 35 and 36:
Anlæg 1 Total: 320 MWex (292 MW) 7
Page 37 and 38:
antagelse, da naturgasnettet er try
Page 39 and 40:
246 562 112 Anlæg 1 Total: 1222 mi
Page 41 and 42:
Brændsel Pris Kilde [kr/L] [kr/GJe
Page 43 and 44:
Metanolomkostning [kr/GJex] 500 450
Page 45 and 46:
7.5.2 Parametervariation Nedenfor e
Page 47 and 48:
Udkondenseret metanol [%] 100 95 90
Page 49 and 50:
Metanolrenhed efter destillation [m
Page 51 and 52:
vandkoncentrationen i syngassen fal
Page 53 and 54:
Metanolexergivirkningsgrad [%] 73 7
Page 55 and 56:
Metanolrenhed efter destillation [m
Page 57 and 58:
Dette betyder at den metanolholdige
Page 59 and 60:
Atmosfærisk forgasning (1 bar) Try
Page 61 and 62:
7.6 Diskussion I parametervariation
Page 63 and 64:
7.6.2 Alternative anlægsdesign Ned
Page 65 and 66:
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 and 118:
10. Benzinafgift Benzinafgifter fra
Page 119 and 120:
12. Metanolpris Metanolpriser fra M
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:
Page 167 and 168:
0 1 1 1 P 2 M type NOD* 2 1 type NO
Page 169 and 170:
Page 171 and 172:
Page 173 and 174:
Page 175 and 176:
Page 177 and 178:
Page 179 and 180:
Page 181 and 182:
Page 183 and 184:
Page 185 and 186:
27. Flowsheet for metanolanlæg - f
Page 187 and 188:
28. Flowsheet for metanolanlæg - f
Page 189 and 190:
29. Matlab-kode til Scenarie 1
Page 191 and 192:
18-03-07 23:10 D:\DTU\Eksamensproje
Page 193 and 194:
Page 195 and 196:
Page 197 and 198:
Page 199 and 200:
Page 201 and 202:
Page 203 and 204:
Page 205 and 206:
Page 207 and 208:
Page 209 and 210:
Page 211 and 212:
Page 213 and 214:
32. DNA-kode for metanolanlæg
Page 215 and 216:
metanolanlaeg.dna d:/DTU/Eksamenspr
Page 217 and 218:
metanolanlaeg.dna d:/DTU/Eksamenspr
Page 219 and 220:
33. Dokumentation for tilføjede DN
Page 221 and 222:
17.121.4 Conditions ˙m1 > 0 ˙m2 <
Page 223 and 224:
9. - 10. - 11. - 12. - 13. - 14. -
Page 225 and 226:
17.123 GASIFI_3_VENZIN Gasifier wit
Page 227 and 228:
13. - 14. - 15. - 16. - 17. - 18. -
Page 229 and 230:
17.124 GASCLE_2 Syngas cleaning. Th
Page 231 and 232:
38. Compound number 39. Compound nu
Page 233 and 234:
43. - 44. - 45. - 46. - 47. - 48. -
Page 235 and 236:
17.124.5 Example struc Cleaner GASC
Page 237 and 238:
10. - 11. - 12. - 13. - 17.125.4 Co
Page 239 and 240:
7. - 8. - 9. - 10. - 11. - 12. - 13
Page 241 and 242:
17.126.4 Conditions ˙m1 > 0 ˙m2 <
Page 243 and 244:
11. - 12. - 13. - 14. - 15. - 16. -
Page 245 and 246:
17.128 SET_M Utility component for
Page 247 and 248:
4. - 5. - 6. - 7. - 8. - 9. - 10. -
Page 249 and 250:
17.129.4 Conditions ˙m1 > 0 ˙m2 <
Page 251 and 252:
17.130.4 Conditions ˙m1 > 0 ˙m2 <
Page 253 and 254:
17.131.2 Equations Number of equati
Page 255 and 256:
17.132 EL-MOTOR Motor with efficien
Page 257 and 258:
8. - 9. - 17.133.3 Conditions ˙m1
Page 259 and 260:
17.135 MIXER_03 Mixer for ideal gas
Page 261 and 262:
33. - 34. - 35. - 36. - 37. - 38. -
Page 263 and 264:
17.137 SET_X Utility component for
Page 265 and 266:
17.138.4 Conditions ˙m1 > 0 ˙m2 <
Page 267 and 268:
17.140 SET_FLOW Utillity component
Page 269 and 270:
17.142 SET_TEMP2 Utillity component
Page 271 and 272:
34. Tilføjede komponenter til DNA
Page 273 and 274:
VEnzin.for c:/dna/source/ C C Param
Page 275 and 276:
VEnzin.for c:/dna/source/ CA ANTED
Page 277 and 278:
VEnzin.for c:/dna/source/ IF (MDOT(
Page 279 and 280:
VEnzin.for c:/dna/source/ MMVAR(1)
Page 281 and 282:
VEnzin.for c:/dna/source/ ENDDO DO
Page 283 and 284:
VEnzin.for c:/dna/source/ $fluid O2
Page 285 and 286:
VEnzin.for c:/dna/source/ C−−
Page 287 and 288:
VEnzin.for c:/dna/source/ CA FKOMP
Page 289 and 290:
VEnzin.for c:/dna/source/ ENDDO NIN
Page 291 and 292:
VEnzin.for c:/dna/source/ C Subrout
Page 293 and 294:
VEnzin.for c:/dna/source/ CALL STAT
Page 295 and 296:
VEnzin.for c:/dna/source/ CA 3: Flu
Page 297 and 298:
VEnzin.for c:/dna/source/ C C C M_B
Page 299 and 300:
VEnzin.for c:/dna/source/ C C SETFL
Page 301 and 302:
VEnzin.for c:/dna/source/ C C GASCO
Page 303 and 304:
VEnzin.for c:/dna/source/ RES(5) =
Page 305 and 306: VEnzin.for c:/dna/source/ c c c E2=
Page 307 and 308: VEnzin.for c:/dna/source/ C C HEATE
Page 309 and 310: VEnzin.for c:/dna/source/ $ ’$\\d
Page 311 and 312: VEnzin.for c:/dna/source/ c 1 = Wat
Page 313 and 314: VEnzin.for c:/dna/source/ CA 4: Fin
Page 315 and 316: VEnzin.for c:/dna/source/ CL K_MED
Page 317 and 318: VEnzin.for c:/dna/source/ CA MEDIE
Page 319 and 320: VEnzin.for c:/dna/source/ CA −4 :
Page 321 and 322: VEnzin.for c:/dna/source/ C ENDDO E
Page 323 and 324: VEnzin.for c:/dna/source/ MEDIE(2)
Page 325 and 326: VEnzin.for c:/dna/source/ C C 400 C
Page 327 and 328: VEnzin.for c:/dna/source/ GOTO 9999
Page 329 and 330: VEnzin.for c:/dna/source/ MEDIE(1)
Page 331 and 332: VEnzin.for c:/dna/source/ C−−
Page 333 and 334: VEnzin.for c:/dna/source/ RES(1) =
Page 339 and 340: 35. Metanol (fluid) til DNA - Fortr
Page 341 and 342: methanol.for d:/DTU/Eksamensprojekt
Page 355: methanol.for d:/DTU/Eksamensprojekt
show all

Design og modellering af metanolanlæg til VEnzin-visionen Bilag

Create successful ePaper yourself

Delete template?

Save as template?