DK201070267A - Improved Method and Plant for the Purification of Carbon Dioxide using Liquid Carbon Dioxide - Google Patents
Improved Method and Plant for the Purification of Carbon Dioxide using Liquid Carbon Dioxide Download PDFInfo
- Publication number
- DK201070267A DK201070267A DKPA201070267A DKPA201070267A DK201070267A DK 201070267 A DK201070267 A DK 201070267A DK PA201070267 A DKPA201070267 A DK PA201070267A DK PA201070267 A DKPA201070267 A DK PA201070267A DK 201070267 A DK201070267 A DK 201070267A
- Authority
- DK
- Denmark
- Prior art keywords
- column
- stream
- effluent
- contaminant
- carbon dioxide
- Prior art date
Links
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims 38
- 239000007788 liquid Substances 0.000 title claims 33
- 238000000746 purification Methods 0.000 title claims 32
- 238000000034 method Methods 0.000 title claims 21
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims 19
- 239000001569 carbon dioxide Substances 0.000 title claims 19
- 239000000356 contaminant Substances 0.000 claims 26
- 239000007789 gas Substances 0.000 claims 16
- 239000003112 inhibitor Substances 0.000 claims 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 12
- 239000002516 radical scavenger Substances 0.000 claims 10
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims 6
- 239000002699 waste material Substances 0.000 claims 6
- 238000001816 cooling Methods 0.000 claims 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims 3
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 claims 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims 3
- 238000010521 absorption reaction Methods 0.000 claims 3
- 238000004821 distillation Methods 0.000 claims 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims 2
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 claims 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims 2
- 239000002250 absorbent Substances 0.000 claims 2
- 230000002745 absorbent Effects 0.000 claims 2
- 238000009835 boiling Methods 0.000 claims 2
- 150000001875 compounds Chemical class 0.000 claims 2
- 238000001035 drying Methods 0.000 claims 2
- 229930195733 hydrocarbon Natural products 0.000 claims 2
- 150000002430 hydrocarbons Chemical class 0.000 claims 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 claims 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims 2
- -1 such as N2 Chemical compound 0.000 claims 2
- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 claims 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims 1
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims 1
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 claims 1
- 229910021529 ammonia Inorganic materials 0.000 claims 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims 1
- JJWKPURADFRFRB-UHFFFAOYSA-N carbonyl sulfide Chemical class O=C=S JJWKPURADFRFRB-UHFFFAOYSA-N 0.000 claims 1
- 238000009833 condensation Methods 0.000 claims 1
- 230000005494 condensation Effects 0.000 claims 1
- 230000007423 decrease Effects 0.000 claims 1
- 230000018044 dehydration Effects 0.000 claims 1
- 238000006297 dehydration reaction Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims 1
- 239000007791 liquid phase Substances 0.000 claims 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 claims 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims 1
- 239000001301 oxygen Substances 0.000 claims 1
- 229910052760 oxygen Inorganic materials 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 claims 1
- 150000003568 thioethers Chemical class 0.000 claims 1
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 claims 1
Landscapes
- Gas Separation By Absorption (AREA)
Claims (27)
1. A method for removing at least one contaminant from a feed stream (f) substantially comprising carbon dioxide, said method comprising the step of subjecting the feed stream (f) to a) a purification step in a column having a top, bottom and an intermediate section, the purification step provides a contaminant lean stream (g2) leaving the top section of the column and a contaminant rich liquid stream (12) leaving, optionally the bottom section of, the column and wherein the contaminant lean stream leaving the top section of the column is further subjected to the steps selected from: 1: bl) compressing the contaminant lean stream (g2) providing a compressed gaseous stream (g4) cl) cooling the compressed gaseous stream (g4) in a reboiler providing at least a product stream (p) and a gaseous stream (g3); and dl) feeding the gaseous stream (g3) to the column at the bottom section of the column; and 2: b2) cooling the contaminant lean stream (g2) in a reboiler providing at least a product stream (p) and a gaseous stream (g3); and c2) compressing the gaseous stream (g3) providing a cooled compressed gaseous stream (g4'); d2) feeding the cooled compressed gaseous stream (g4') to the column at the bottom section of the column; and depressurising the contaminant rich liquid stream (12) leaving at the bottom section of the column before entering the reboiler.
2. The method according to claim 1, wherein the feed stream is liquid or gaseous.
3. The method according to claim 2, wherein the feed stream is gaseous and the purification step is an absorption step wherein the absorbent is liquid carbon dioxide.
4. The method according to claim 2, wherein the feed stream is liquid and the purification step is a rectification step and the liquid phase is liquid carbon dioxide.
5. The method according to claim 2 and 4, wherein the feed stream (f) is liquid and the further steps are: bl) compressing the contaminant lean stream (g2) providing a compressed gaseous stream (g4) cl) cooling the compressed gaseous stream (g4) in a reboiler providing at least a product stream (p) and a gaseous stream (g3); and dl) feeding the gaseous stream (g3) to the column at the bottom section of the column.
6. The method according to claim 2 and 3, wherein the feed stream (f) is gaseous.
7. The method according to claim 6, wherein the further steps are: b2) cooling the contaminant lean stream (g2) in a reboiler providing at least a product stream (p) and a gaseous stream (g3); and c2) compressing the gaseous stream (g3) providing a cooled compressed gaseous stream (g4'); d2) feeding the cooled compressed gaseous stream (g4') to the column at the bottom section of the column; and depressurising the contaminant rich liquid stream (12) leaving at the bottom section of the column before entering the reboiler.
8. The method according to any of the preceding claims wherein the at least one contaminant is selected among compounds having a boiling point higher than the boiling point of carbon dioxide at the prevailing conditions and non-polar compounds.
9. The method according to claim 8, wherein the at least one contaminant is selected from the group consisting of: sulfides, such as hydrogen sulfide, carbonyl sulfides and dimethylsulfide; nitrogen containing compounds, such as N2, ammonia and nitrogen dioxide; and hydrocarbons, such as, methane, n-pentane, n-hexane, benzene, toluene and oxygen containing hydrocarbons such as dimethyl ether, acetaldehyde, ethyl acetate, acetone, methanol, ethanol, isobutanol and n-propanol.
10. The method according to any of the preceding claims, wherein ratio of liquid carbon dioxide to the feed stream is 1:3 to 10:1, preferably 1:3 to 3:1.
11. The method according to any of the preceding claims, wherein the purification step further comprises an integrated water inhibitor and/or scavenger step.
12. The method according to claim 11, wherein the water inhibitor and/or scavenger used in the purification step is recirculated in the process.
13. The method according to any of the claims 11 or 12, wherein the water inhibitor and/or scavenger is fed to the intermediate section of the purification column.
14. The method according to any of the claims 11 or 12 wherein the water inhibitor and/or scavenger is mixed with the feed stream (f) or the absorbent liquid (II) prior to being fed to the column.
15. The method according to any of the claims 11-14, wherein a liquid carbon dioxide stream (15) is partially withdrawn from the purification column at a position above the inlet of the water inhibitor and/or scavenger.
16. The method according to any of the claims 11 to 15, wherein the integrated inhibitor step is a dehydration step using a water inhibitor, which decreases the water activity in the feed stream, such as methanol, ethanol, mono ethylene glycol and tri ethylene glycol.
17. The method according to any of the preceding claims further comprising at least one of the steps of: heating or cooling the product stream leaving the reboiler, and/or - purifying the product stream by means of adsorption and/or absorption; and/or - condensing and/or distilling the product stream to provide a high purity liquid carbon dioxide stream; and/or feeding a portion of condensed and/or refluxed carbon dioxide to the purification column.
18. The method according to any of the preceding claims wherein the purification step is preceded by at least one or more of the steps of: - compressing, - adsorbing and/or absorbing; and - liquefying by means of for example condensation or distillation.
19 A carbon dioxide purification unit comprising a purification column (Al) having a top and a bottom and a section intermediate of the top and the bottom, the purification column having a feeding stream influent (f), a contaminant lean gas effluent (g2) situated at the top part of the column, a liquid carbon dioxide influent (II) situated at the top part of the column, and a contaminant rich liquid effluent (12), said contaminant rich liquid effluent (12) optionally being situated at the bottom part of the purification column, wherein the contaminant rich liquid effluent (12) is connected to a reboiler (A3) additionally having a waste liquid effluent (13), a product effluent (p), a compressed gaseous influent (g4), and a gas effluent (g3), the gaseous effluent (g3) being connected to the purification column (Al), wherein a compressing means (A2) is inserted between the reboiler (A3) and the purification column (Al) at a position between the contaminant lean gas purification column effluent (g2) and the compressed gaseous influent (g4); or wherein the contaminant rich liquid effluent (12) is connected to a reboiler (A3) additionally having a waste liquid effluent (13), a product effluent (p), a contaminant lean gas purification column effluent (g2), and a gas effluent (g3), the gas effluent (g3) being connected to a compressing means (A2) inserted between the reboiler (A3) and the purification column (Al) at a position between the gas effluent (g3) and a cooled compressed gaseous influent (g4') and wherein a valve (A4) is positioned on the contaminant rich liquid effluent (12).
20. The unit according to claim 19, wherein the feeding influent (f) is situated at the bottom section of the purification column (Al) and the contaminant rich liquid effluent (12) is connected to a reboiler (A3) additionally having a waste liquid effluent (13), a product effluent (p), a compressed gaseous influent (g4), and a gas effluent (g3), the gas effluent (g3) being connected to the purification column (Al), wherein a compressing means (A2) is inserted between the reboiler (A3) and the purification column (Al) at a position between the contaminant lean gas purification column effluent (g2) and the compressed gaseous influent (g4) and wherein the purification column is an absorption column.
21. The unit according to claim 19, wherein the feeding influent (f) is situated at the top section of the purification column (Al) and the contaminant rich liquid effluent (12) is connected to a reboiler (A3) additionally having a waste liquid effluent (13), a product effluent (p), a contaminant lean gas purification column effluent (g2), and a gas effluent (g3), the gas effluent (g3) being connected to a compressing means (A2) inserted between the reboiler (A3) and the purification column (Al) at a position between the gas effluent (g3) and the cooled compressed gaseous influent (g4') and wherein a valve (A4) is positioned on the contaminant rich liquid effluent (12) and wherein the purification column is a rectification column.
22. The unit according to any of the claims 19 to 21, wherein the purification column further comprises a water inhibitor and/or scavenger influent (10) situated at the intermediate section of the column.
23. The unit according to any of the claims 19 to 22, wherein the contaminant rich liquid effluent (12) situated at the bottom section of the column is split in two at a position outside the column and a first liquid effluent (12') is connected to the water inhibitor and/or scavenger influent (10) and a second liquid effluent (12") is connected to the reboiler (A3).
24. The unit according to any of the claims 19 to 23, wherein the purification column is further provided with a carbon dioxide effluent (15) situated at a position of the purification column between the water and/or scavenger inhibitor influent (10) and the liquid carbon dioxide influent (II).
25. The unit according to any of the claims 19 to 24, wherein the feeding influent (f) is connected to a feeding gas source, preferably partially purified carbon dioxide; and/or the product effluent (p) is connected to a carbon dioxide processing unit, such as a heat exchanger and/or a filter and/or a distillation column; and/or the liquid carbon dioxide influent (II) is connected to a liquid carbon dioxide reservoir, e.g. a distillation column connected to the product gas outlet; and/or the waste liquid effluent (13) is connected to a waste reservoir ; and/or the water inhibitor and/or scavenger influent (10) is connected to the water inhibitor/scavenger reservoir.
26. The unit according to any of the claims 19 to 25, wherein the feeding influent (f) up stream is optionally connected to a drying filter, which optional drying filter is connected to a compressor.
27. The unit according to any of the claims 19 to 26 wherein the carbon dioxide effluent (15) is connected to the feeding influent (f).
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DKPA201070267A DK201070267A (en) | 2010-06-17 | 2010-06-17 | Improved Method and Plant for the Purification of Carbon Dioxide using Liquid Carbon Dioxide |
| ARP110102062A AR081924A1 (en) | 2010-06-17 | 2011-06-14 | IMPROVED METHOD AND PLANT TO PURIFY CARBON DIOXIDE USING LIQUID CARBON DIOXIDE |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DKPA201070267A DK201070267A (en) | 2010-06-17 | 2010-06-17 | Improved Method and Plant for the Purification of Carbon Dioxide using Liquid Carbon Dioxide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DK201070267A true DK201070267A (en) | 2010-06-17 |
Family
ID=42315579
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DKPA201070267A DK201070267A (en) | 2010-06-17 | 2010-06-17 | Improved Method and Plant for the Purification of Carbon Dioxide using Liquid Carbon Dioxide |
Country Status (1)
| Country | Link |
|---|---|
| DK (1) | DK201070267A (en) |
-
2010
- 2010-06-17 DK DKPA201070267A patent/DK201070267A/en not_active Application Discontinuation
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AHS | Application shelved for other reasons than non-payment |