MXPA02010906A - Metodo y dispositivo para tratar una fraccion de c4. - Google Patents
Metodo y dispositivo para tratar una fraccion de c4.Info
- Publication number
- MXPA02010906A MXPA02010906A MXPA02010906A MXPA02010906A MXPA02010906A MX PA02010906 A MXPA02010906 A MX PA02010906A MX PA02010906 A MXPA02010906 A MX PA02010906A MX PA02010906 A MXPA02010906 A MX PA02010906A MX PA02010906 A MXPA02010906 A MX PA02010906A
- Authority
- MX
- Mexico
- Prior art keywords
- column
- stream
- butadiene
- distillation
- boiling point
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 79
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 claims abstract description 135
- 238000004821 distillation Methods 0.000 claims abstract description 36
- 238000005984 hydrogenation reaction Methods 0.000 claims abstract description 19
- 238000000895 extractive distillation Methods 0.000 claims abstract description 13
- 239000002638 heterogeneous catalyst Substances 0.000 claims abstract description 9
- 230000008569 process Effects 0.000 claims description 64
- 238000009835 boiling Methods 0.000 claims description 46
- 239000002904 solvent Substances 0.000 claims description 32
- 239000000126 substance Substances 0.000 claims description 29
- 239000000203 mixture Substances 0.000 claims description 23
- 239000001257 hydrogen Substances 0.000 claims description 17
- 229910052739 hydrogen Inorganic materials 0.000 claims description 17
- 239000006200 vaporizer Substances 0.000 claims description 15
- 239000002699 waste material Substances 0.000 claims description 15
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 10
- 239000010808 liquid waste Substances 0.000 claims description 10
- 238000000926 separation method Methods 0.000 claims description 8
- BKOOMYPCSUNDGP-UHFFFAOYSA-N 2-methylbut-2-ene Chemical compound CC=C(C)C BKOOMYPCSUNDGP-UHFFFAOYSA-N 0.000 claims description 4
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 4
- 239000007864 aqueous solution Substances 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 125000002534 ethynyl group Chemical class [H]C#C* 0.000 claims description 4
- QWTDNUCVQCZILF-UHFFFAOYSA-N isopentane Chemical compound CCC(C)C QWTDNUCVQCZILF-UHFFFAOYSA-N 0.000 claims description 4
- YWAKXRMUMFPDSH-UHFFFAOYSA-N propyl ethylene Natural products CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 claims description 4
- 230000000779 depleting effect Effects 0.000 claims description 3
- 150000002431 hydrogen Chemical class 0.000 claims description 3
- QMMOXUPEWRXHJS-UHFFFAOYSA-N pent-2-ene Chemical compound CCC=CC QMMOXUPEWRXHJS-UHFFFAOYSA-N 0.000 claims description 3
- YHQXBTXEYZIYOV-UHFFFAOYSA-N 3-methylbut-1-ene Chemical compound CC(C)C=C YHQXBTXEYZIYOV-UHFFFAOYSA-N 0.000 claims description 2
- 150000001335 aliphatic alkanes Chemical class 0.000 claims description 2
- 150000001336 alkenes Chemical class 0.000 claims description 2
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- AFABGHUZZDYHJO-UHFFFAOYSA-N dimethyl butane Natural products CCCC(C)C AFABGHUZZDYHJO-UHFFFAOYSA-N 0.000 claims description 2
- ZFPGARUNNKGOBB-UHFFFAOYSA-N 1-Ethyl-2-pyrrolidinone Chemical compound CCN1CCCC1=O ZFPGARUNNKGOBB-UHFFFAOYSA-N 0.000 claims 1
- 239000003054 catalyst Substances 0.000 description 18
- 229930195733 hydrocarbon Natural products 0.000 description 15
- 150000002430 hydrocarbons Chemical class 0.000 description 15
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 10
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 9
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 9
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical class CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 9
- 235000013844 butane Nutrition 0.000 description 7
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 6
- 238000012856 packing Methods 0.000 description 5
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 4
- KDKYADYSIPSCCQ-UHFFFAOYSA-N but-1-yne Chemical compound CCC#C KDKYADYSIPSCCQ-UHFFFAOYSA-N 0.000 description 4
- WFYPICNXBKQZGB-UHFFFAOYSA-N butenyne Chemical group C=CC#C WFYPICNXBKQZGB-UHFFFAOYSA-N 0.000 description 4
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 239000003990 capacitor Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000005194 fractionation Methods 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- MHNNAWXXUZQSNM-UHFFFAOYSA-N 2-methylbut-1-ene Chemical compound CCC(C)=C MHNNAWXXUZQSNM-UHFFFAOYSA-N 0.000 description 2
- YEJRWHAVMIAJKC-UHFFFAOYSA-N 4-Butyrolactone Chemical compound O=C1CCCO1 YEJRWHAVMIAJKC-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- SUAKHGWARZSWIH-UHFFFAOYSA-N N,N‐diethylformamide Chemical compound CCN(CC)C=O SUAKHGWARZSWIH-UHFFFAOYSA-N 0.000 description 2
- 239000013543 active substance Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- HHEMIMSLFVBJMH-UHFFFAOYSA-N but-1-yne Chemical compound C#CCC.C(C)C#C HHEMIMSLFVBJMH-UHFFFAOYSA-N 0.000 description 2
- QNRMTGGDHLBXQZ-UHFFFAOYSA-N buta-1,2-diene Chemical compound CC=C=C QNRMTGGDHLBXQZ-UHFFFAOYSA-N 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- LCEDQNDDFOCWGG-UHFFFAOYSA-N morpholine-4-carbaldehyde Chemical compound O=CN1CCOCC1 LCEDQNDDFOCWGG-UHFFFAOYSA-N 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 229910052763 palladium Inorganic materials 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 238000000859 sublimation Methods 0.000 description 2
- 230000008022 sublimation Effects 0.000 description 2
- 238000007740 vapor deposition Methods 0.000 description 2
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 1
- DURPTKYDGMDSBL-UHFFFAOYSA-N 1-butoxybutane Chemical compound CCCCOCCCC DURPTKYDGMDSBL-UHFFFAOYSA-N 0.000 description 1
- SFPQDYSOPQHZAQ-UHFFFAOYSA-N 2-methoxypropanenitrile Chemical compound COC(C)C#N SFPQDYSOPQHZAQ-UHFFFAOYSA-N 0.000 description 1
- UPOMCDPCTBJJDA-UHFFFAOYSA-N 2-methyl-1-[(2-methylpropan-2-yl)oxy]propane Chemical compound CC(C)COC(C)(C)C UPOMCDPCTBJJDA-UHFFFAOYSA-N 0.000 description 1
- FITVQUMLGWRKKG-UHFFFAOYSA-N 2-methyl-2-propoxypropane Chemical compound CCCOC(C)(C)C FITVQUMLGWRKKG-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 1
- BZLVMXJERCGZMT-UHFFFAOYSA-N Methyl tert-butyl ether Chemical compound COC(C)(C)C BZLVMXJERCGZMT-UHFFFAOYSA-N 0.000 description 1
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 239000000010 aprotic solvent Substances 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- SSNYFFFCLVXSPK-UHFFFAOYSA-N buta-1,2-diene;buta-1,3-diene Chemical compound CC=C=C.C=CC=C SSNYFFFCLVXSPK-UHFFFAOYSA-N 0.000 description 1
- 229930188620 butyrolactone Natural products 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000006184 cosolvent Substances 0.000 description 1
- -1 cyclic acid amides Chemical class 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- AQEFLFZSWDEAIP-UHFFFAOYSA-N di-tert-butyl ether Chemical class CC(C)(C)OC(C)(C)C AQEFLFZSWDEAIP-UHFFFAOYSA-N 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000002815 homogeneous catalyst Substances 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 150000003951 lactams Chemical class 0.000 description 1
- 239000003915 liquefied petroleum gas Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- AJFDBNQQDYLMJN-UHFFFAOYSA-N n,n-diethylacetamide Chemical compound CCN(CC)C(C)=O AJFDBNQQDYLMJN-UHFFFAOYSA-N 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- FVSKHRXBFJPNKK-UHFFFAOYSA-N propionitrile Chemical compound CCC#N FVSKHRXBFJPNKK-UHFFFAOYSA-N 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- MWWATHDPGQKSAR-UHFFFAOYSA-N propyne Chemical compound CC#C MWWATHDPGQKSAR-UHFFFAOYSA-N 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- NUMQCACRALPSHD-UHFFFAOYSA-N tert-butyl ethyl ether Chemical compound CCOC(C)(C)C NUMQCACRALPSHD-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G70/00—Working-up undefined normally gaseous mixtures obtained by processes covered by groups C10G9/00, C10G11/00, C10G15/00, C10G47/00, C10G51/00
- C10G70/02—Working-up undefined normally gaseous mixtures obtained by processes covered by groups C10G9/00, C10G11/00, C10G15/00, C10G47/00, C10G51/00 by hydrogenation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/141—Fractional distillation or use of a fractionation or rectification column where at least one distillation column contains at least one dividing wall
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/143—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
- B01D3/146—Multiple effect distillation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
- B01D3/40—Extractive distillation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/005—Processes comprising at least two steps in series
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G70/00—Working-up undefined normally gaseous mixtures obtained by processes covered by groups C10G9/00, C10G11/00, C10G15/00, C10G47/00, C10G51/00
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1088—Olefins
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/44—Solvents
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/80—Additives
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/20—C2-C4 olefins
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE10022465A DE10022465A1 (de) | 2000-05-09 | 2000-05-09 | Verfahren und Vorrichtung zur Aufarbeitung eines C4-Schnitts aus der Fraktionierung von Erdöl |
| PCT/EP2001/005279 WO2001085656A1 (de) | 2000-05-09 | 2001-05-09 | Verfahren und vorrichtung zur aufarbeitung eines c4-schnitts |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| MXPA02010906A true MXPA02010906A (es) | 2003-04-14 |
Family
ID=7641246
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| MXPA02010906A MXPA02010906A (es) | 2000-05-09 | 2001-05-09 | Metodo y dispositivo para tratar una fraccion de c4. |
Country Status (14)
| Country | Link |
|---|---|
| US (1) | US20030181772A1 (enExample) |
| EP (1) | EP1282586B1 (enExample) |
| JP (1) | JP5038573B2 (enExample) |
| CN (1) | CN100478318C (enExample) |
| AU (2) | AU6741901A (enExample) |
| BR (1) | BR0110721B1 (enExample) |
| CA (1) | CA2408325C (enExample) |
| CZ (1) | CZ20023681A3 (enExample) |
| DE (2) | DE10022465A1 (enExample) |
| DK (1) | DK1282586T3 (enExample) |
| ES (1) | ES2279821T3 (enExample) |
| HU (1) | HUP0302011A3 (enExample) |
| MX (1) | MXPA02010906A (enExample) |
| WO (1) | WO2001085656A1 (enExample) |
Families Citing this family (60)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10056841A1 (de) | 2000-11-16 | 2002-05-23 | Basf Ag | Verfahren und Vorrichtung zur destillativen Gewinnung von 1,3-Reinbutadien aus 1,3-Rohbutadien |
| DE10102168A1 (de) * | 2000-12-08 | 2002-06-20 | Linde Ag | Verfahren und Vorrichtung zur Auftrennung eines Stoffgemisches in seine Bestandteile durch Extraktivdestillation in einer Trennwandkolonne |
| DE10105660A1 (de) * | 2001-02-08 | 2002-08-14 | Basf Ag | Verfahren zur Gewinnung von Roh-1,3-Butadien durch Extraktivdestillation aus einem C4-Schnitt |
| US6930206B1 (en) * | 2001-07-05 | 2005-08-16 | Catalytic Distillation Technologies | Process and apparatus for catalytic distillations |
| DE10233385A1 (de) * | 2002-07-23 | 2004-02-12 | Basf Ag | Verfahren zur kontinuierlichen Herstellung von Propylenglykolen |
| DE10233620A1 (de) * | 2002-07-24 | 2004-02-12 | Basf Ag | Kontinuierliches Verfahren zur Auftrennung eines C4-Schnittes |
| DE10233621A1 (de) * | 2002-07-24 | 2004-02-19 | Basf Ag | Verfahren zur Aufarbeitung von Roh-1,3-Butadien |
| DE10258160A1 (de) * | 2002-12-12 | 2004-06-24 | Basf Ag | Verfahren und Vorrichtung zur Extraktivdestillation |
| DE10333756A1 (de) * | 2003-07-24 | 2005-02-17 | Basf Ag | Verfahren zur Auftrennung eines Roh-C4-Schnittes |
| DE102004005930A1 (de) * | 2004-02-06 | 2005-08-25 | Basf Ag | Verfahren zur Gewinnung von Roh-1,3-Butadien |
| FR2868789B1 (fr) * | 2004-04-09 | 2008-09-26 | Inst Francais Du Petrole | Procede et dispositif de traitement d'une charge comportant du butadiene |
| US20060155154A1 (en) * | 2005-01-07 | 2006-07-13 | Catalytic Distillation Technologies | Process for the selective hydrogenation of alkynes |
| FR2895417B1 (fr) | 2005-12-23 | 2011-10-14 | Inst Francais Du Petrole | Procede de desulfurisation comprenant une etape de transformation et une etape d'extraction des composes soufres |
| RU2304133C1 (ru) * | 2006-02-26 | 2007-08-10 | Олег Станиславович Павлов | Способ извлечения и очистки 1,3-бутадиена |
| US7528290B2 (en) * | 2006-12-28 | 2009-05-05 | Uop Llc | Apparatuses and methods for separating butene-1 from a mixed C4 feed |
| CA2674618C (en) * | 2007-01-19 | 2015-02-10 | Exxonmobil Upstream Research Company | Integrated controlled freeze zone (cfz) tower and dividing wall (dwc) for enhanced hydrocarbon recovery |
| US20100018248A1 (en) * | 2007-01-19 | 2010-01-28 | Eleanor R Fieler | Controlled Freeze Zone Tower |
| CN101665399B (zh) * | 2008-09-05 | 2012-07-25 | 中国石油化工股份有限公司 | 丁二烯生产方法 |
| US9423174B2 (en) | 2009-04-20 | 2016-08-23 | Exxonmobil Upstream Research Company | Cryogenic system for removing acid gases from a hydrocarbon gas stream, and method of removing acid gases |
| AU2010307274B2 (en) | 2009-09-09 | 2016-02-18 | Exxonmobil Upstream Research Company | Cryogenic system for removing acid gasses from a hydrocarbon gas stream |
| CA2786574C (en) | 2010-01-22 | 2016-06-28 | Exxonmobil Upstream Research Company | Removal of acid gases from a gas stream, with co2 capture and sequestration |
| EA025708B1 (ru) | 2010-02-03 | 2017-01-30 | Эксонмобил Апстрим Рисерч Компани | Способ отделения способных затвердевать газовых компонентов от технологических газовых потоков с использованием холодной жидкости |
| CA2805513C (en) | 2010-07-30 | 2016-10-04 | Exxonmobil Upstream Research Company | Cryogenic systems for removing acid gases from a hydrocarbon gas stream using co-current separation devices |
| EP2502655B1 (en) * | 2011-03-25 | 2014-05-14 | Sulzer Chemtech AG | Reactive distillation process and plant for obtaining acetic acid and alcohol from the hydrolysis of methyl acetate |
| CN103086831B (zh) * | 2011-11-02 | 2016-02-24 | 中国石油化工股份有限公司 | 一种提高丁二烯收率和充分利用碳四烃的丁二烯生产系统及方法 |
| US8766029B2 (en) * | 2012-01-11 | 2014-07-01 | Basf Se | Process for providing a vaporous purified crude C4 cut as a feed steam for an extractive distillation with a selective solvent |
| WO2013104692A1 (de) * | 2012-01-11 | 2013-07-18 | Basf Se | Verfahren zur bereitstellung eines dampfförmigen gereinigten roh-c4-schnittes als einsatzstrom für eine extraktivdestillation mit einem selektiven lösungsmittel |
| WO2013142100A1 (en) | 2012-03-21 | 2013-09-26 | Exxonmobil Upstream Research Company | Separating carbon dioxide and ethane from a mixed stream |
| HUE039224T2 (hu) * | 2012-10-04 | 2018-12-28 | Lummus Technology Inc | Butadién-extrakciós eljárás |
| JP5793157B2 (ja) * | 2013-03-04 | 2015-10-14 | 日本リファイン株式会社 | 溶液処理装置 |
| DE102013214765A1 (de) * | 2013-07-29 | 2015-01-29 | Wacker Chemie Ag | Verfahren und Vorrichtung zur destillativen Trennung eines Drei- oder Mehrkomponentengemisches |
| US9937437B2 (en) * | 2013-08-23 | 2018-04-10 | Uop Llc | Fractionation system having rectifying and stripping columns in a single vessel with a uniform diameter |
| AU2014357667B2 (en) | 2013-12-06 | 2017-10-05 | Exxonmobil Upstream Research Company | Method and system for separating a feed stream with a feed stream distribution mechanism |
| US9869511B2 (en) | 2013-12-06 | 2018-01-16 | Exxonmobil Upstream Research Company | Method and device for separating hydrocarbons and contaminants with a spray assembly |
| WO2015084499A2 (en) | 2013-12-06 | 2015-06-11 | Exxonmobil Upstream Research Company | Method and system of modifying a liquid level during start-up operations |
| US9752827B2 (en) | 2013-12-06 | 2017-09-05 | Exxonmobil Upstream Research Company | Method and system of maintaining a liquid level in a distillation tower |
| US9874395B2 (en) | 2013-12-06 | 2018-01-23 | Exxonmobil Upstream Research Company | Method and system for preventing accumulation of solids in a distillation tower |
| WO2015084500A1 (en) | 2013-12-06 | 2015-06-11 | Exxonmobil Upstream Research Company | Method and device for separating hydrocarbons and contaminants with a heating mechanism to destabilize and/or prevent adhesion of solids |
| WO2015084497A2 (en) | 2013-12-06 | 2015-06-11 | Exxonmobil Upstream Research Company | Method and system of dehydrating a feed stream processed in a distillation tower |
| US9562719B2 (en) | 2013-12-06 | 2017-02-07 | Exxonmobil Upstream Research Company | Method of removing solids by modifying a liquid level in a distillation tower |
| MY177751A (en) | 2013-12-06 | 2020-09-23 | Exxonmobil Upstream Res Co | Method and device for separating a feed stream using radiation detectors |
| DE102014220539A1 (de) | 2014-10-09 | 2016-04-14 | Wacker Chemie Ag | Reinigung von Chlorsilanen mittels Destillation und Adsorption |
| SG11201705162SA (en) | 2015-02-27 | 2017-09-28 | Exxonmobil Upstream Res Co | Reducing refrigeration and dehydration load for a feed stream entering a cryogenic distillation process |
| US10365037B2 (en) | 2015-09-18 | 2019-07-30 | Exxonmobil Upstream Research Company | Heating component to reduce solidification in a cryogenic distillation system |
| WO2017052922A2 (en) | 2015-09-24 | 2017-03-30 | Exxonmobil Upstream Research Company | Treatment plant for hydrocarbon gas having variable contaminant levels |
| CN108349850A (zh) * | 2015-11-11 | 2018-07-31 | 沙特基础全球技术有限公司 | 用于从c4烃流纯化1,3-丁二烯的方法和系统 |
| US10323495B2 (en) | 2016-03-30 | 2019-06-18 | Exxonmobil Upstream Research Company | Self-sourced reservoir fluid for enhanced oil recovery |
| US10173951B2 (en) * | 2016-09-13 | 2019-01-08 | Chevron Phillips Chemical Company Lp | Side rectifier column for olefin and diluent recovery |
| WO2018138100A1 (de) * | 2017-01-25 | 2018-08-02 | Basf Se | Verfahren zur gewinnung von rein-1,3-butadien |
| KR102086048B1 (ko) * | 2017-07-07 | 2020-03-06 | 주식회사 엘지화학 | 분산판 및 이를 포함하는 정제탑 |
| US11306267B2 (en) | 2018-06-29 | 2022-04-19 | Exxonmobil Upstream Research Company | Hybrid tray for introducing a low CO2 feed stream into a distillation tower |
| WO2020005553A1 (en) | 2018-06-29 | 2020-01-02 | Exxonmobil Upstream Research Company (Emhc-N1.4A.607) | Mixing and heat integration of melt tray liquids in a cryogenic distillation tower |
| US11952333B2 (en) | 2019-09-13 | 2024-04-09 | Sabic Global Technologies B.V. | Integrated systems and methods for producing 1,3-butadiene via extractive distillation, distillation, and/or selective hydrogenation |
| CN114478161B (zh) * | 2020-10-23 | 2024-09-17 | 中国石油化工股份有限公司 | 混合c4物流选择加氢的装置和方法 |
| CN114471375B (zh) * | 2020-10-23 | 2023-02-24 | 中国石油化工股份有限公司 | 混合c4物流全加氢的装置和方法 |
| EP4251593A1 (de) * | 2021-01-27 | 2023-10-04 | Evonik Operations GmbH | Verfahren zur abtrennung von butenen aus c4-kohlenwasserstoffströmen mit zweistufiger verdampfung |
| KR102670910B1 (ko) * | 2021-03-16 | 2024-05-29 | 한화솔루션 주식회사 | 증발기 및 이를 이용한 분리 방법 |
| CN114011341B (zh) * | 2021-11-15 | 2024-12-06 | 丹东明珠特种树脂有限公司 | 催化精馏塔和深脱除异丁烯之高纯度mtbe制备系统 |
| CN115888159B (zh) * | 2022-12-22 | 2023-08-01 | 安徽瑞柏新材料有限公司 | 一种防静电的醋酸甲酯低温分馏提纯装置 |
| CN117732097B (zh) * | 2023-11-09 | 2024-07-23 | 华陆工程科技有限责任公司 | 一种分离方法 |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4215011A (en) * | 1979-02-21 | 1980-07-29 | Chemical Research And Licensing Company | Catalyst system for separating isobutene from C4 streams |
| US4277313A (en) * | 1980-03-27 | 1981-07-07 | El Paso Products Company | Recovery of 1,3-butadiene |
| US4493906A (en) * | 1983-03-08 | 1985-01-15 | The Dow Chemical Company | Catalyst for the selective hydrogenation of acetylenes |
| DE3314395A1 (de) * | 1983-04-21 | 1984-10-25 | Basf Ag, 6700 Ludwigshafen | Verfahren zur durchfuehrung von chemischen reaktionen und gleichzeitiger destillativer zerlegung eines produktgemisches in mehrere fraktionen mittels einer destillationskolonne |
| FR2553760B1 (fr) * | 1983-10-25 | 1986-05-02 | Inst Francais Du Petrole | Procede d'hydrogenation selective en presence de solvant des composes acetyleniques d'une coupe d'hydrocarbures c4 riche en butadiene |
| US4704492A (en) * | 1986-12-24 | 1987-11-03 | Mobil Oil Corporation | Selective hydrogenation of acetylenic impurities in crude butadiene |
| US6169218B1 (en) * | 1992-02-10 | 2001-01-02 | Catalytic Distillation Technologies | Selective hydrogenation of highly unsaturated compounds in hydrocarbon streams |
| DE19624130A1 (de) * | 1996-06-17 | 1997-12-18 | Basf Ag | Verfahren zur katalytischen Destillation |
| US6040489A (en) * | 1998-12-09 | 2000-03-21 | Uop Llc | 1,3-Butadiene separation from a crude C4 stream using catalytic extractive distillation |
-
2000
- 2000-05-09 DE DE10022465A patent/DE10022465A1/de not_active Withdrawn
-
2001
- 2001-05-09 JP JP2001582258A patent/JP5038573B2/ja not_active Expired - Fee Related
- 2001-05-09 HU HU0302011A patent/HUP0302011A3/hu unknown
- 2001-05-09 ES ES01945105T patent/ES2279821T3/es not_active Expired - Lifetime
- 2001-05-09 EP EP01945105A patent/EP1282586B1/de not_active Expired - Lifetime
- 2001-05-09 CA CA002408325A patent/CA2408325C/en not_active Expired - Fee Related
- 2001-05-09 DK DK01945105T patent/DK1282586T3/da active
- 2001-05-09 DE DE50111854T patent/DE50111854D1/de not_active Expired - Lifetime
- 2001-05-09 CZ CZ20023681A patent/CZ20023681A3/cs unknown
- 2001-05-09 MX MXPA02010906A patent/MXPA02010906A/es active IP Right Grant
- 2001-05-09 WO PCT/EP2001/005279 patent/WO2001085656A1/de not_active Ceased
- 2001-05-09 AU AU6741901A patent/AU6741901A/xx active Pending
- 2001-05-09 CN CNB018107273A patent/CN100478318C/zh not_active Expired - Lifetime
- 2001-05-09 BR BRPI0110721-6A patent/BR0110721B1/pt not_active IP Right Cessation
- 2001-05-09 AU AU2001267419A patent/AU2001267419B2/en not_active Ceased
- 2001-05-09 US US10/275,898 patent/US20030181772A1/en not_active Abandoned
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|---|---|
| JP2004514647A (ja) | 2004-05-20 |
| CZ20023681A3 (cs) | 2003-04-16 |
| WO2001085656A1 (de) | 2001-11-15 |
| CA2408325A1 (en) | 2001-11-07 |
| EP1282586A1 (de) | 2003-02-12 |
| US20030181772A1 (en) | 2003-09-25 |
| HUP0302011A3 (en) | 2007-09-28 |
| ES2279821T3 (es) | 2007-09-01 |
| BR0110721A (pt) | 2004-02-10 |
| AU2001267419B2 (en) | 2006-08-03 |
| CN1433392A (zh) | 2003-07-30 |
| HUP0302011A2 (hu) | 2003-09-29 |
| DK1282586T3 (da) | 2007-03-19 |
| BR0110721B1 (pt) | 2012-01-10 |
| AU6741901A (en) | 2001-11-20 |
| CA2408325C (en) | 2009-08-11 |
| EP1282586B1 (de) | 2007-01-10 |
| DE50111854D1 (de) | 2007-02-22 |
| DE10022465A1 (de) | 2001-11-15 |
| JP5038573B2 (ja) | 2012-10-03 |
| CN100478318C (zh) | 2009-04-15 |
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