GB1113279A - Isoprene purification process - Google Patents
Isoprene purification processInfo
- Publication number
- GB1113279A GB1113279A GB4404165A GB4404165A GB1113279A GB 1113279 A GB1113279 A GB 1113279A GB 4404165 A GB4404165 A GB 4404165A GB 4404165 A GB4404165 A GB 4404165A GB 1113279 A GB1113279 A GB 1113279A
- Authority
- GB
- United Kingdom
- Prior art keywords
- solvent
- extract
- separated
- isoprene
- methylethylacetylene
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (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)
Abstract
Isoprene is separated from a C5 hydrocarbon mixture by a straight distillation followed by two extraction distillations; in the straight distillation isopropylacetylene, dimethylacetylene, methylethylacetylene and pentadiene-1,4 are separated overhead, the bottoms are extractively distilled to separate C5 mono-olefins and the extract is extractively distilled in the presence of further solvent to separate isoprene as overhead from methylethylacetylene, cyclopentadiene, propylacetylene, piperylene and allylacetylene in the extract. The solvent may be acetone or acetonitrile and may contain water. The extract is preferably removed near the bottom of extractive distillation columns, the solvent separated and returned to the bottom of the extraction column and bottoms then recycled from the bottom to the top to supply the solvent.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB4404165A GB1113279A (en) | 1965-10-18 | 1965-10-18 | Isoprene purification process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB4404165A GB1113279A (en) | 1965-10-18 | 1965-10-18 | Isoprene purification process |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1113279A true GB1113279A (en) | 1968-05-08 |
Family
ID=10431482
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4404165A Expired GB1113279A (en) | 1965-10-18 | 1965-10-18 | Isoprene purification process |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1113279A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1055281C (en) * | 1996-03-20 | 2000-08-09 | 中国石油化工总公司 | Method for separation of petroleum cracking C5 fraction by liquid phase feeding extraction rectification |
CN1331830C (en) * | 2004-12-24 | 2007-08-15 | 中国石化上海石油化工股份有限公司 | Refining separation method for coarse piperyene |
CN110498726A (en) * | 2018-05-18 | 2019-11-26 | 抚顺伊科思新材料有限公司 | The extractant modified technique of acetonitrile method light dydrocarbon separation |
-
1965
- 1965-10-18 GB GB4404165A patent/GB1113279A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1055281C (en) * | 1996-03-20 | 2000-08-09 | 中国石油化工总公司 | Method for separation of petroleum cracking C5 fraction by liquid phase feeding extraction rectification |
CN1331830C (en) * | 2004-12-24 | 2007-08-15 | 中国石化上海石油化工股份有限公司 | Refining separation method for coarse piperyene |
CN110498726A (en) * | 2018-05-18 | 2019-11-26 | 抚顺伊科思新材料有限公司 | The extractant modified technique of acetonitrile method light dydrocarbon separation |
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