TWI500601B - 藉蒸餾用於自粗製１，３－丁二烯分離純１，３－丁二烯之方法及裝置 - Google Patents
藉蒸餾用於自粗製１，３－丁二烯分離純１，３－丁二烯之方法及裝置 Download PDFInfo
- Publication number
- TWI500601B TWI500601B TW100108403A TW100108403A TWI500601B TW I500601 B TWI500601 B TW I500601B TW 100108403 A TW100108403 A TW 100108403A TW 100108403 A TW100108403 A TW 100108403A TW I500601 B TWI500601 B TW I500601B
- Authority
- TW
- Taiwan
- Prior art keywords
- butadiene
- column
- fraction
- stream
- selective solvent
- Prior art date
Links
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 title claims description 126
- 238000000034 method Methods 0.000 title claims description 29
- 238000004821 distillation Methods 0.000 title claims description 21
- 239000002904 solvent Substances 0.000 claims description 45
- 238000000895 extractive distillation Methods 0.000 claims description 41
- 238000007872 degassing Methods 0.000 claims description 30
- 238000000746 purification Methods 0.000 claims description 24
- 150000001345 alkine derivatives Chemical class 0.000 claims description 22
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 claims description 18
- MWWATHDPGQKSAR-UHFFFAOYSA-N propyne Chemical compound CC#C MWWATHDPGQKSAR-UHFFFAOYSA-N 0.000 claims description 18
- 229930195733 hydrocarbon Natural products 0.000 claims description 16
- 238000005984 hydrogenation reaction Methods 0.000 claims description 15
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 claims description 13
- 150000002430 hydrocarbons Chemical class 0.000 claims description 11
- 239000004215 Carbon black (E152) Substances 0.000 claims description 6
- 239000001273 butane Substances 0.000 claims description 6
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 6
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims 2
- 238000010521 absorption reaction Methods 0.000 claims 1
- KDKYADYSIPSCCQ-UHFFFAOYSA-N but-1-yne Chemical compound CCC#C KDKYADYSIPSCCQ-UHFFFAOYSA-N 0.000 description 38
- WFYPICNXBKQZGB-UHFFFAOYSA-N butenyne Chemical compound C=CC#C WFYPICNXBKQZGB-UHFFFAOYSA-N 0.000 description 18
- 238000009835 boiling Methods 0.000 description 9
- 238000000605 extraction Methods 0.000 description 7
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000005192 partition Methods 0.000 description 5
- -1 C 4 hydrocarbons Chemical class 0.000 description 4
- QACDWUMHRWJKNJ-UHFFFAOYSA-N but-1-ene but-1-en-3-yne Chemical compound CCC=C.C=CC#C QACDWUMHRWJKNJ-UHFFFAOYSA-N 0.000 description 4
- IAQRGUVFOMOMEM-ARJAWSKDSA-N cis-but-2-ene Chemical compound C\C=C/C IAQRGUVFOMOMEM-ARJAWSKDSA-N 0.000 description 4
- 238000003795 desorption Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 238000011064 split stream procedure Methods 0.000 description 4
- IAQRGUVFOMOMEM-ONEGZZNKSA-N trans-but-2-ene Chemical compound C\C=C\C IAQRGUVFOMOMEM-ONEGZZNKSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 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
- 238000010992 reflux Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 125000000304 alkynyl group Chemical group 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- QNRMTGGDHLBXQZ-UHFFFAOYSA-N buta-1,2-diene Chemical compound CC=C=C QNRMTGGDHLBXQZ-UHFFFAOYSA-N 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 238000004508 fractional distillation Methods 0.000 description 1
- 239000002638 heterogeneous catalyst Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000006200 vaporizer Substances 0.000 description 1
Classifications
-
- 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
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/12—Alkadienes
- C07C11/16—Alkadienes with four carbon atoms
- C07C11/167—1, 3-Butadiene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/04—Purification; Separation; Use of additives by distillation
- C07C7/05—Purification; Separation; Use of additives by distillation with the aid of auxiliary compounds
- C07C7/08—Purification; Separation; Use of additives by distillation with the aid of auxiliary compounds by extractive distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Water Supply & Treatment (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102010011014A DE102010011014A1 (de) | 2010-03-11 | 2010-03-11 | Verfahren und Vorrichtung zur destillativen Gewinnung von Rein-1,3-Butadien aus Roh-1,3-Butadien |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| TW201139368A TW201139368A (en) | 2011-11-16 |
| TWI500601B true TWI500601B (zh) | 2015-09-21 |
Family
ID=43806920
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW100108403A TWI500601B (zh) | 2010-03-11 | 2011-03-11 | 藉蒸餾用於自粗製１，３－丁二烯分離純１，３－丁二烯之方法及裝置 |
Country Status (8)
| Country | Link |
|---|---|
| EP (1) | EP2545019B1 (enExample) |
| JP (1) | JP5758922B2 (enExample) |
| KR (1) | KR101850562B1 (enExample) |
| CN (1) | CN102781892B (enExample) |
| DE (1) | DE102010011014A1 (enExample) |
| PL (1) | PL2545019T3 (enExample) |
| TW (1) | TWI500601B (enExample) |
| WO (1) | WO2011110562A1 (enExample) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103958647B (zh) * | 2011-12-05 | 2017-07-21 | 巴斯夫欧洲公司 | 提供气态经纯化的c4粗馏分作为进料流用于使用选择性溶剂的萃取蒸馏工艺的方法 |
| US8642828B2 (en) | 2012-01-03 | 2014-02-04 | Basf Se | Process for purifying a recycle stream from a 1,3-butadiene processing plant |
| TWI564288B (zh) * | 2012-01-03 | 2017-01-01 | 巴地斯顏料化工廠 | 從１，３－丁二烯之處理設備純化循環流的方法 |
| 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 |
| PT2897928T (pt) | 2012-09-20 | 2019-01-17 | Lummus Technology Inc | Pré-absorvedor de extração de butadieno |
| CN102942437A (zh) * | 2012-11-22 | 2013-02-27 | 万达集团股份有限公司 | Nmp法丁二烯一段抽提方法 |
| US10125063B2 (en) | 2014-07-08 | 2018-11-13 | Basf Se | Column with separative installations for separating a mixture of hydrocarbons and/or hydrocarbon derivatives by means of an extractive distillation using a selective solvent |
| US11034631B2 (en) | 2017-01-25 | 2021-06-15 | Basf Se | Method for obtaining pure 1,3-butadiene |
| JP7076465B2 (ja) * | 2017-03-13 | 2022-05-27 | ビーエーエスエフ ソシエタス・ヨーロピア | 純粋な１，３－ブタジエンを単離するための簡素化された方法 |
| 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 |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4277313A (en) * | 1980-03-27 | 1981-07-07 | El Paso Products Company | Recovery of 1,3-butadiene |
| US7226527B2 (en) * | 2001-02-08 | 2007-06-05 | Basf Aktiengesellschaft | Method for recovering crude 1,3-butadiene by extractive distillation from a C4 cut |
| WO2010008109A1 (en) * | 2008-07-17 | 2010-01-21 | Sk Energy Co., Ltd. | Process for 1,3-butadiene separation from a crude c4 stream with acetylene converter |
| CN101665399A (zh) * | 2008-09-05 | 2010-03-10 | 中国石油化工股份有限公司 | 丁二烯生产方法 |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4277311A (en) | 1976-06-14 | 1981-07-07 | Bethlehem Steel Corporation | Apparatus for distillation |
| FR2440984A1 (fr) * | 1978-11-10 | 1980-06-06 | Inst Francais Du Petrole | Procede de traitement d'une coupe d'hydrocarbures c4 en vue de la recuperation du butadiene |
| JPS5754129A (ja) * | 1980-09-18 | 1982-03-31 | Japan Synthetic Rubber Co Ltd | Butajenmatahaisopurennoseiseihoho |
| JPS57123123A (en) * | 1981-01-23 | 1982-07-31 | Nippon Oil Co Ltd | Preparation of high purity butadiene |
| DE19818810A1 (de) | 1998-04-27 | 1999-10-28 | Basf Ag | Verfahren zum Trennen eines C4-Kohlenwasserstoffgemisches |
| DE10056841A1 (de) * | 2000-11-16 | 2002-05-23 | Basf Ag | Verfahren und Vorrichtung zur destillativen Gewinnung von 1,3-Reinbutadien aus 1,3-Rohbutadien |
| DE10233621A1 (de) * | 2002-07-24 | 2004-02-19 | Basf Ag | Verfahren zur Aufarbeitung von Roh-1,3-Butadien |
| DE10322655A1 (de) | 2003-05-20 | 2004-12-09 | Basf Ag | Verfahren zur Gewinnung von Roh-1,3-Butadien aus einem C4-Schnitt |
| CN101172929B (zh) | 2006-10-31 | 2010-05-19 | 中国石油化工股份有限公司 | Nmp法丁二烯一段抽提方法 |
-
2010
- 2010-03-11 DE DE102010011014A patent/DE102010011014A1/de not_active Withdrawn
-
2011
- 2011-03-08 KR KR1020127026467A patent/KR101850562B1/ko active Active
- 2011-03-08 CN CN201180012423.XA patent/CN102781892B/zh active Active
- 2011-03-08 JP JP2012556488A patent/JP5758922B2/ja active Active
- 2011-03-08 EP EP11709361.7A patent/EP2545019B1/de active Active
- 2011-03-08 PL PL11709361T patent/PL2545019T3/pl unknown
- 2011-03-08 WO PCT/EP2011/053473 patent/WO2011110562A1/de not_active Ceased
- 2011-03-11 TW TW100108403A patent/TWI500601B/zh not_active IP Right Cessation
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4277313A (en) * | 1980-03-27 | 1981-07-07 | El Paso Products Company | Recovery of 1,3-butadiene |
| US7226527B2 (en) * | 2001-02-08 | 2007-06-05 | Basf Aktiengesellschaft | Method for recovering crude 1,3-butadiene by extractive distillation from a C4 cut |
| WO2010008109A1 (en) * | 2008-07-17 | 2010-01-21 | Sk Energy Co., Ltd. | Process for 1,3-butadiene separation from a crude c4 stream with acetylene converter |
| CN101665399A (zh) * | 2008-09-05 | 2010-03-10 | 中国石油化工股份有限公司 | 丁二烯生产方法 |
Also Published As
| Publication number | Publication date |
|---|---|
| TW201139368A (en) | 2011-11-16 |
| KR20130016264A (ko) | 2013-02-14 |
| PL2545019T3 (pl) | 2014-08-29 |
| CN102781892A (zh) | 2012-11-14 |
| EP2545019B1 (de) | 2014-03-05 |
| KR101850562B1 (ko) | 2018-04-19 |
| WO2011110562A1 (de) | 2011-09-15 |
| DE102010011014A1 (de) | 2011-09-15 |
| EP2545019A1 (de) | 2013-01-16 |
| JP5758922B2 (ja) | 2015-08-05 |
| JP2013522175A (ja) | 2013-06-13 |
| CN102781892B (zh) | 2016-05-04 |
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| MM4A | Annulment or lapse of patent due to non-payment of fees |