GB1131989A - Process for the removal of gas or liquid residues from solvents used to treat gases or liquids - Google Patents
Process for the removal of gas or liquid residues from solvents used to treat gases or liquidsInfo
- Publication number
- GB1131989A GB1131989A GB5739466A GB5739466A GB1131989A GB 1131989 A GB1131989 A GB 1131989A GB 5739466 A GB5739466 A GB 5739466A GB 5739466 A GB5739466 A GB 5739466A GB 1131989 A GB1131989 A GB 1131989A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gas
- solvent
- vapour
- stream
- scrubbing
- 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
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
- C10K1/10—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
- C10K1/12—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids alkaline-reacting including the revival of the used wash liquors
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/10—Purification; Separation; Use of additives by extraction, i.e. purification or separation of liquid 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
- C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Analytical Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Gas Separation By Absorption (AREA)
- Industrial Gases (AREA)
Abstract
1,131,989. Separating gases. SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ N.V. 22 Dec., 1966 [24 Dec., 1965], No. 57394/66. Heading B1L [Also in Division C5] Impurities, such as H 2 S, SO 2 , CO 2 , COS, NH 3 or amines, present in scrubbing solvents which have been contracted with such gases or vapours as air, natural gas, combustion products of coal or oil, refinery gas, town gas, coke oven gas, water gas, H 2 , CO, N 2 , O 2 , water vapour and light hydrocarbons such as propane and propylene, are separated from gas or liquid residues of the gas or vapour being treated which are present in the solvent by treating the impurity-containing solvent at a pressure lower than that obtaining in the scrubbing zone with a second quantity of solvent in the presence of more of a gas or liquid which is to be similarly processed. As shown, gas or vapour stream 1 flows in countercurrent to solvent stream 3 in column 2 maintained at 7-70 kg./cm<SP>2</SP>, scrubbed gas or vapour leaving at 4. Solvent rich in impurities and containing residues of the gas or vapour leaves by line 5 and passes to column 18, which is at a lower pressure than column 2, where it encounters a rising stream 19 of a gas or liquid to be scrubbed and a falling stream 16 of fresh scrubbing solvent. Impurity-free gas or liquid leaves at 20, while laden solvent passes by line 21 to stripper 13, the impurities leaving at 15. Commonly, the principal impurity is H 2 S, in which case stream 15 is desirably treated with an oxygencontaining gas so as partially to oxidise the H 2 S to elementary sulphur. In both scrubbing zones, the temperature is suitably maintained at 25-135‹C, preferably 30-80‹C. A number of conventional solvents are listed as suitable scrubbing media for particular purposes; an especially suitable one comprises by weight 1-15% water, 15-35% diisopropanolamine and 50-84 % sulpholane (cyclotetrahydromethylene sulphone).
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL6516902A NL146061B (en) | 1965-12-24 | 1965-12-24 | PROCEDURE FOR THE REMOVAL OF RESIDUAL GASES OR LIQUIDS FROM SOLVENTS. |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1131989A true GB1131989A (en) | 1968-10-30 |
Family
ID=19795026
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5739466A Expired GB1131989A (en) | 1965-12-24 | 1966-12-22 | Process for the removal of gas or liquid residues from solvents used to treat gases or liquids |
Country Status (4)
Country | Link |
---|---|
DE (1) | DE1544141B2 (en) |
FR (1) | FR1505994A (en) |
GB (1) | GB1131989A (en) |
NL (1) | NL146061B (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7250450B2 (en) | 2002-06-05 | 2007-07-31 | Shell Oil Company | Process for the production of hydrocarbons from gaseous hydrocarbonaceous feed |
WO2011048066A1 (en) | 2009-10-21 | 2011-04-28 | Shell Internationale Research Maatschappij B.V. | Method & apparatus for processing fischer-tropsch off-gas |
WO2012078218A1 (en) | 2010-12-07 | 2012-06-14 | Exxonmobil Chemical Patents Inc. | Processes utilizing solvent extraction |
WO2013017700A1 (en) | 2011-08-04 | 2013-02-07 | Shell Internationale Research Maatschappij B.V. | Process for producing hydrocarbons from syngas |
US9505674B2 (en) | 2012-11-29 | 2016-11-29 | Exxonmobil Chemical Patents Inc. | Processes for treating olefin feedstreams and related oligomerization processes |
CN111321017A (en) * | 2018-12-14 | 2020-06-23 | 乔治洛德方法研究和开发液化空气有限公司 | Method and apparatus for regenerating loaded scrubbing media from gas scrubbing |
-
1965
- 1965-12-24 NL NL6516902A patent/NL146061B/en not_active IP Right Cessation
-
1966
- 1966-12-22 FR FR88541A patent/FR1505994A/en not_active Expired
- 1966-12-22 GB GB5739466A patent/GB1131989A/en not_active Expired
- 1966-12-22 DE DE19661544141 patent/DE1544141B2/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7250450B2 (en) | 2002-06-05 | 2007-07-31 | Shell Oil Company | Process for the production of hydrocarbons from gaseous hydrocarbonaceous feed |
WO2011048066A1 (en) | 2009-10-21 | 2011-04-28 | Shell Internationale Research Maatschappij B.V. | Method & apparatus for processing fischer-tropsch off-gas |
WO2012078218A1 (en) | 2010-12-07 | 2012-06-14 | Exxonmobil Chemical Patents Inc. | Processes utilizing solvent extraction |
US9643902B2 (en) | 2010-12-07 | 2017-05-09 | Exxonmobil Chemical Patents Inc. | Processes utilizing solvent extraction |
WO2013017700A1 (en) | 2011-08-04 | 2013-02-07 | Shell Internationale Research Maatschappij B.V. | Process for producing hydrocarbons from syngas |
US9505674B2 (en) | 2012-11-29 | 2016-11-29 | Exxonmobil Chemical Patents Inc. | Processes for treating olefin feedstreams and related oligomerization processes |
CN111321017A (en) * | 2018-12-14 | 2020-06-23 | 乔治洛德方法研究和开发液化空气有限公司 | Method and apparatus for regenerating loaded scrubbing media from gas scrubbing |
Also Published As
Publication number | Publication date |
---|---|
DE1544141A1 (en) | 1970-06-04 |
DE1544141B2 (en) | 1976-01-08 |
NL146061B (en) | 1975-06-16 |
NL6516902A (en) | 1967-06-26 |
FR1505994A (en) | 1967-12-15 |
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