GB1211033A - Treatment of waste gases - Google Patents
Treatment of waste gasesInfo
- Publication number
- GB1211033A GB1211033A GB0741/68A GB174168A GB1211033A GB 1211033 A GB1211033 A GB 1211033A GB 0741/68 A GB0741/68 A GB 0741/68A GB 174168 A GB174168 A GB 174168A GB 1211033 A GB1211033 A GB 1211033A
- Authority
- GB
- United Kingdom
- Prior art keywords
- sulphur
- catalyst
- produced
- reaction
- sufficient
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8603—Removing sulfur compounds
- B01D53/8609—Sulfur oxides
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/02—Preparation of sulfur; Purification
- C01B17/04—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides
- C01B17/0404—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process
- C01B17/0426—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process characterised by the catalytic conversion
- C01B17/0439—Preparation of sulfur; Purification from gaseous sulfur compounds including gaseous sulfides by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process characterised by the catalytic conversion at least one catalyst bed operating below the dew-point of sulfur
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
Abstract
1,211,033. Removing SO 2 from waste gases. ONTARIO RESEARCH FOUNDATION. 10 Jan., 1969 [11 Jan., 1968], No. 1741/68. Heading C1A. Sulphur dioxide containing effluent gas is contacted with a reducing gas comprising H 2 S in the presence of a catalyst at a temperature of 50- 150‹ C. whereby the SO 2 is at least partially reduced to sulphur in accordance with the equation: and the sulphur is deposited on the catalyst, and removing the sulphur from the catalyst at least partially by reaction with carbon monoxide at a temperature of from 250-500‹ C. in order to provide regenerated, substantially sulphur free catalyst. The reaction with carbon monoxide preferably occurs at 300-450‹ C. The carbonyl sulphide produced may in turn be hydrolysed to CO 2 and H 2 S which is recycled, further H 2 S being produced if a mixture of CO and H 2 is used for removing the sulphur, steam (removing the necessity for subsequent hydrolysis) and an inert gas, such as N 2 , may also be present. Sufficient H 2 S is used in order to react with all the SO 2 , sufficient CO with or without H 2 is used to react with 2/3 of the sulphur produced, the rest being removed as sulphur vapour in the COS and subsequently removed; sufficient steam is used to hydrolyse all the COS produced. A continuous process for the removal of the catalyst from the sulphur depositing zone to the sulphur removing zone and: thereafter recycling the catalyst, is described. Catalysts disclosed for the sulphur producing stage are Pd, Pt, Rh, promoted iron oxide but preferably activated alumina or bauxite is used. This stage may be broken up into 2 parts: (a) reaction with H 2 S at 250-400‹ C. (b) completion of the reaction at 50-150‹ C. Some CS 2 may be produced especially if hydrocarbons are present in the CO or H 2 . This need not be hydrolysed since CS 2 will reduce SO 2 to S if recycled.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0741/68A GB1211033A (en) | 1968-01-11 | 1968-01-11 | Treatment of waste gases |
FR6900325A FR2000167A1 (en) | 1968-01-11 | 1969-01-10 | |
DE19691901171 DE1901171B2 (en) | 1968-01-11 | 1969-01-10 | METHOD OF REMOVING SULFUR DIOXIDE FROM EXHAUST GASES, IN PARTICULAR SMOKE GASES |
BE726756D BE726756A (en) | 1968-01-11 | 1969-01-10 | |
JP44002297A JPS4814305B1 (en) | 1968-01-11 | 1969-01-11 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0741/68A GB1211033A (en) | 1968-01-11 | 1968-01-11 | Treatment of waste gases |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1211033A true GB1211033A (en) | 1970-11-04 |
Family
ID=9727187
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB0741/68A Expired GB1211033A (en) | 1968-01-11 | 1968-01-11 | Treatment of waste gases |
Country Status (5)
Country | Link |
---|---|
JP (1) | JPS4814305B1 (en) |
BE (1) | BE726756A (en) |
DE (1) | DE1901171B2 (en) |
FR (1) | FR2000167A1 (en) |
GB (1) | GB1211033A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3961035A (en) | 1974-03-27 | 1976-06-01 | Stauffer Chemical Company | Process for preparing hydrogen sulfide |
US4094961A (en) | 1974-11-07 | 1978-06-13 | Ralph M. Parsons Company | Hydrogen sulfide production |
US4894216A (en) * | 1985-10-25 | 1990-01-16 | Societe Nationale Elf Aquitaine (Production) | Catalytic process for producing sulphur from H2 S containing sour gas |
US4980146A (en) * | 1985-10-25 | 1990-12-25 | Societe Nationale Elf Aquitaine (Production) | Process for removing sulphur compounds contained in a residual gas |
DE3690569C2 (en) * | 1985-10-25 | 1998-10-01 | Elf Aquitaine | Removing sulphur cpds. from residual gas |
CN106621796A (en) * | 2016-10-31 | 2017-05-10 | 昆明理工大学 | Method and device for simultaneously removing carbonyl sulfide and carbon disulfide |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2122407A1 (en) * | 1971-01-18 | 1972-09-01 | Parsons Co Ralph M | Carbon-sulphur cpds conversion to hydrogen sulphide - over cobalt/molybdenum catalyst in claus sulphur process |
FR2190517B1 (en) * | 1972-06-29 | 1975-08-29 | Rhone Progil | |
DE3929227A1 (en) * | 1989-09-02 | 1991-03-07 | Koenig & Bauer Ag | PAPER RAIL SEPARATION AND HOLDING DEVICE |
-
1968
- 1968-01-11 GB GB0741/68A patent/GB1211033A/en not_active Expired
-
1969
- 1969-01-10 FR FR6900325A patent/FR2000167A1/fr not_active Withdrawn
- 1969-01-10 DE DE19691901171 patent/DE1901171B2/en active Pending
- 1969-01-10 BE BE726756D patent/BE726756A/xx unknown
- 1969-01-11 JP JP44002297A patent/JPS4814305B1/ja active Pending
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3961035A (en) | 1974-03-27 | 1976-06-01 | Stauffer Chemical Company | Process for preparing hydrogen sulfide |
US4094961A (en) | 1974-11-07 | 1978-06-13 | Ralph M. Parsons Company | Hydrogen sulfide production |
US4894216A (en) * | 1985-10-25 | 1990-01-16 | Societe Nationale Elf Aquitaine (Production) | Catalytic process for producing sulphur from H2 S containing sour gas |
US4980146A (en) * | 1985-10-25 | 1990-12-25 | Societe Nationale Elf Aquitaine (Production) | Process for removing sulphur compounds contained in a residual gas |
US5077031A (en) * | 1985-10-25 | 1991-12-31 | Societe Nationale Elf Aquitaine | Catalytic process for producing sulphur from H2 S containing sour gas |
DE3690568C2 (en) * | 1985-10-25 | 1998-08-27 | Elf Aquitaine | Removing sulphur cpds. from residual gas |
DE3690569C2 (en) * | 1985-10-25 | 1998-10-01 | Elf Aquitaine | Removing sulphur cpds. from residual gas |
DE3690570C2 (en) * | 1985-10-25 | 1998-10-15 | Elf Aquitaine | Removing sulphur cpds. from residual gas |
CN106621796A (en) * | 2016-10-31 | 2017-05-10 | 昆明理工大学 | Method and device for simultaneously removing carbonyl sulfide and carbon disulfide |
CN106621796B (en) * | 2016-10-31 | 2023-06-13 | 昆明理工大学 | Method and device for simultaneously removing carbonyl sulfide and carbon disulfide |
Also Published As
Publication number | Publication date |
---|---|
DE1901171B2 (en) | 1972-03-16 |
FR2000167A1 (en) | 1969-08-29 |
JPS4814305B1 (en) | 1973-05-07 |
DE1901171A1 (en) | 1969-09-04 |
BE726756A (en) | 1969-06-16 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PLNP | Patent lapsed through nonpayment of renewal fees |