ES2001293A6 - Selective processing of gases containing olefins by the mehra process. - Google Patents
Selective processing of gases containing olefins by the mehra process.Info
- Publication number
- ES2001293A6 ES2001293A6 ES8601671A ES8601671A ES2001293A6 ES 2001293 A6 ES2001293 A6 ES 2001293A6 ES 8601671 A ES8601671 A ES 8601671A ES 8601671 A ES8601671 A ES 8601671A ES 2001293 A6 ES2001293 A6 ES 2001293A6
- Authority
- ES
- Spain
- Prior art keywords
- stream
- extractive
- stripping
- gases containing
- containing olefins
- 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
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/11—Purification; Separation; Use of additives by absorption, i.e. purification or separation of gaseous hydrocarbons with the aid of liquids
-
- 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
- C10G5/00—Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas
- C10G5/04—Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas with liquid absorbents
-
- 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
- C10G2300/1025—Natural gas
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (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)
Abstract
A gas-liquid extractive stripping process which uses at least one preferential physical solvent in at least one solvent loop, each loop passing through at least two unit operations: extractive-stripping and distillation. At least the first extractive-stripping operation may additionally comprise a rectification section on top of the extraction section. Three products are made from streams of thermally cracked gases or refinery gases: a hydrogen-rich gas stream, a methane-rich gas stream, and a C2=+ hydrocarbons stream which is the feed stream for the conventional fractionation train of an olefins manufacturing facility. Ethylene can be economically produced from the C2=+ hydrocarbons product stream at a recovery of at least 99.5% and a purity of at least 99.9%.
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US06/784,566 US4617038A (en) | 1985-07-26 | 1985-10-04 | Process for using preferential physical solvents for selective processing of hydrocarbon gas streams |
US06/808,463 US4692179A (en) | 1982-05-03 | 1985-12-13 | Process for using alkyl substituted C8-C10 aromatic hydrocarbons as preferential physical solvents for selective processing of hydrocarbon gas streams |
US06/828,996 US4696688A (en) | 1985-12-13 | 1986-02-13 | Conversion of lean oil absorption process to extraction process for conditioning natural gas |
US06/828,988 US4680042A (en) | 1985-12-13 | 1986-02-13 | Extractive stripping of inert-rich hydrocarbon gases with a preferential physical solvent |
US06/854,383 US4743282A (en) | 1982-05-03 | 1986-04-21 | Selective processing of gases containing olefins by the mehra process |
Publications (1)
Publication Number | Publication Date |
---|---|
ES2001293A6 true ES2001293A6 (en) | 1988-05-01 |
Family
ID=27542205
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES8601671A Expired ES2001293A6 (en) | 1985-10-04 | 1986-09-05 | Selective processing of gases containing olefins by the mehra process. |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP0241485A1 (en) |
AU (1) | AU6284086A (en) |
BR (1) | BR8606899A (en) |
ES (1) | ES2001293A6 (en) |
GB (1) | GB2189805A (en) |
WO (1) | WO1987002031A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110981684B (en) * | 2019-12-18 | 2022-09-13 | 宁波同润和海科技有限公司 | Method for recovering various effective components in tail gas of hydrogenation device of refinery plant |
CN110963881B (en) * | 2019-12-18 | 2022-08-23 | 宁波同润和海科技有限公司 | Method for recovering various effective components in refinery catalytic unit dry gas |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2780580A (en) * | 1953-03-04 | 1957-02-05 | Lummus Co | Production of ethylene |
US2804488A (en) * | 1954-12-27 | 1957-08-27 | Phillips Petroleum Co | Separation and recovery of ethylene |
CA1215217A (en) * | 1983-06-24 | 1986-12-16 | Yuv R. Mehra | Process for extracting natural gas streams with physical solvents |
-
1986
- 1986-08-15 GB GB08712199A patent/GB2189805A/en not_active Withdrawn
- 1986-08-15 BR BR8606899A patent/BR8606899A/en unknown
- 1986-08-15 WO PCT/US1986/001674 patent/WO1987002031A1/en not_active Application Discontinuation
- 1986-08-15 AU AU62840/86A patent/AU6284086A/en not_active Abandoned
- 1986-08-15 EP EP19860905507 patent/EP0241485A1/en not_active Withdrawn
- 1986-09-05 ES ES8601671A patent/ES2001293A6/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
GB8712199D0 (en) | 1987-06-24 |
GB2189805A (en) | 1987-11-04 |
EP0241485A1 (en) | 1987-10-21 |
AU6284086A (en) | 1987-04-24 |
BR8606899A (en) | 1987-11-03 |
WO1987002031A1 (en) | 1987-04-09 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FD1A | Patent lapsed |
Effective date: 20000208 |