GB1516202A - Suppression of cos formation in molecular sieve purification of hydrocarbon streams - Google Patents
Suppression of cos formation in molecular sieve purification of hydrocarbon streamsInfo
- Publication number
- GB1516202A GB1516202A GB28489/75A GB2848975A GB1516202A GB 1516202 A GB1516202 A GB 1516202A GB 28489/75 A GB28489/75 A GB 28489/75A GB 2848975 A GB2848975 A GB 2848975A GB 1516202 A GB1516202 A GB 1516202A
- Authority
- GB
- United Kingdom
- Prior art keywords
- per cent
- bed
- water
- adsorption
- zeolite
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/12—Purification; Separation; Use of additives by adsorption, i.e. purification or separation of hydrocarbons with the aid of solids, e.g. with ion-exchangers
- C07C7/13—Purification; Separation; Use of additives by adsorption, i.e. purification or separation of hydrocarbons with the aid of solids, e.g. with ion-exchangers by molecular-sieve technique
-
- 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
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Water Supply & Treatment (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Separation Of Gases By Adsorption (AREA)
Abstract
1516202 Purifying hydrocarbons by adsorption UNION CARBIDE CORP 7 July 1975 [8 July 1974] 28489/75 Heading C5E Formation of carbonyl sulphide during the selective adsorption of H 2 S from a hydrocarbon stream containing H 2 S and CO 2 is suppressed by carrying out the adsorption in the vapour phase at 60-120‹F and 200-1200 psia using a crystalline zeolite adsorbent having a pore diameter of at least 5 Angstroms, containing 0À7-3 weight per cent adsorbed water and having at least 45% of the framework aluminium atoms associated with at least one cation of Be, Mg, Ca and Sr. The zeolite can be the calcium forms of zeolite A, X or Y, mordenite, chabazite, faujasite or zeolite Y, L or #. Natural gas 10, containing up to 5 mole percent H 2 S, 0À5-55 mole per cent CO 2 , up to 25 mole per cent of hydrocarbons having more than one carbon atom and a water content of up to saturation is passed through the adsorbent bed 12. A portion 16 of the purified product is used to cool the bed 18 which has been regenerated and is then heated to 550‹F in a furnace 22 and used to desorb the bed 26. Water injected through line 28 raises the water vapour content of the gas 24 to 0À185 mole per cent and ensures that the bed, when used for the adsorption, contains 0À7-3 weight per cent water.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US48663874A | 1974-07-08 | 1974-07-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1516202A true GB1516202A (en) | 1978-06-28 |
Family
ID=23932674
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB28489/75A Expired GB1516202A (en) | 1974-07-08 | 1975-07-07 | Suppression of cos formation in molecular sieve purification of hydrocarbon streams |
Country Status (7)
Country | Link |
---|---|
AU (1) | AU498733B2 (en) |
CA (1) | CA1070249A (en) |
DE (1) | DE2530091B2 (en) |
FR (1) | FR2277798A1 (en) |
GB (1) | GB1516202A (en) |
IT (1) | IT1036464B (en) |
NL (1) | NL7508072A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2882941A1 (en) * | 2005-03-08 | 2006-09-15 | Inst Francais Du Petrole | PROCESS FOR PURIFYING NATURAL GAS BY ADSORPTING MERCAPTANS |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2654599C2 (en) * | 1976-12-02 | 1984-11-15 | Union Carbide Corp., New York, N.Y. | Process for purifying natural gas |
DE3029187C2 (en) * | 1980-08-01 | 1986-04-17 | Bergwerksverband Gmbh, 4300 Essen | Process for removing hydrogen sulfide from oxygen-free or oxygen-containing gas mixtures |
DE3306371A1 (en) * | 1983-02-24 | 1984-08-30 | Bergwerksverband Gmbh, 4300 Essen | METHOD FOR PRODUCING A METHANE-RICH GAS MIXTURE, ESPECIALLY FROM MINE GAS |
US4830733A (en) * | 1987-10-05 | 1989-05-16 | Uop | Integrated process for the removal of sulfur compounds from fluid streams |
GB8803767D0 (en) * | 1988-02-18 | 1988-03-16 | Ici Plc | Desulphurisation |
US9144765B2 (en) | 2007-05-18 | 2015-09-29 | Shell Oil Company | Reactor system, an absorbent and a process for reacting a feed |
CA2723988A1 (en) | 2008-05-15 | 2009-11-19 | Shell Internationale Research Maatschappij B.V. | Process for the preparation of alkylene carbonate and/or alkylene glycol |
US8273912B2 (en) | 2008-05-15 | 2012-09-25 | Shell Oil Company | Process for the preparation of an alkylene carbonate and an alkylene glycol |
CN104291275A (en) * | 2013-07-15 | 2015-01-21 | 北京丰汉工程技术有限公司 | Method and system for recovering sulfur from acid gas in coal gasification process |
-
1975
- 1975-06-13 CA CA229,314A patent/CA1070249A/en not_active Expired
- 1975-07-05 DE DE2530091A patent/DE2530091B2/en not_active Withdrawn
- 1975-07-07 AU AU82799/75A patent/AU498733B2/en not_active Expired
- 1975-07-07 NL NL7508072A patent/NL7508072A/en unknown
- 1975-07-07 IT IT68764/75A patent/IT1036464B/en active
- 1975-07-07 FR FR7521239A patent/FR2277798A1/en active Granted
- 1975-07-07 GB GB28489/75A patent/GB1516202A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2882941A1 (en) * | 2005-03-08 | 2006-09-15 | Inst Francais Du Petrole | PROCESS FOR PURIFYING NATURAL GAS BY ADSORPTING MERCAPTANS |
Also Published As
Publication number | Publication date |
---|---|
AU8279975A (en) | 1977-01-13 |
CA1070249A (en) | 1980-01-22 |
FR2277798A1 (en) | 1976-02-06 |
IT1036464B (en) | 1979-10-30 |
FR2277798B1 (en) | 1979-05-11 |
DE2530091A1 (en) | 1976-01-29 |
NL7508072A (en) | 1976-01-12 |
AU498733B2 (en) | 1979-03-22 |
DE2530091B2 (en) | 1978-03-23 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |