GB812134A - Process for removal of carbon dioxide and (where necessary) hydrogen sulphide from gases containing these constituents - Google Patents
Process for removal of carbon dioxide and (where necessary) hydrogen sulphide from gases containing these constituentsInfo
- Publication number
- GB812134A GB812134A GB10280/55A GB1028055A GB812134A GB 812134 A GB812134 A GB 812134A GB 10280/55 A GB10280/55 A GB 10280/55A GB 1028055 A GB1028055 A GB 1028055A GB 812134 A GB812134 A GB 812134A
- Authority
- GB
- United Kingdom
- Prior art keywords
- salt
- ammonia
- solution
- carbon dioxide
- synthesis gas
- 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
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/025—Preparation or purification of gas mixtures for ammonia synthesis
-
- 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
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/52—Hydrogen sulfide
- B01D53/526—Mixtures of hydrogen sulfide and carbon dioxide
-
- 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
- C10K1/124—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 containing metal compounds other than alkali- or earth-alkali carbonates, hydroxides- or oxides- or salts of inorganic acids derived from 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
- Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- Industrial Gases (AREA)
Abstract
A process for separating carbon dioxide or hydrogen sulphide from a synthesis gas comprising hydrogen and carbon monoxide and utilizing the separated gases, comprises purifying the synthesis gas by contacting with an aqueous solution of an inorganic salt rendered alkaline with ammonia, which solution reacts with the carbon dioxide or hydrogen sulphide to form an aqueous solution of a crystallizable salt and a precipitate of a salt less soluble than the crystallizable salt, removing the precipitated less soluble salt, subsequently crystallizing and removing the more soluble crystallizable salt, converting all or a portion of the purified synthesis gas to ammonia, dissolving fresh inorganic salt, and all or a portion of the synthesized ammonia, in the residual solution after the removal of the less soluble salt and before or after the more soluble crystallizable salt, and recycling the solution remaining remainkng after the removal of the more soluble salt, and after dissolution of the fresh inorganic salt and synthesized ammonia, to the synthesis gas-purifying step. Hydrogen sulphide and carbon dioxide may be separately removed in succession by the above method. The remaining purified gas, if any, may be used in a fuel or alcohol synthesis process. Crystallization of the more soluble salt may be effected by cooling with water and/or liquid synthesized ammonia, gaseous ammonia evolved from said liquid ammonia being dissolved in said residual solution. The synthesis gas may be washed before purification in one or more towers with a circulating solution containing carbon dioxide and ammonia in a ratio of not less than 1.29 and may be washed after purification in one or more towers with a circulating solution containing carbon dioxide and ammonia in a ratio of not more than 1.29. Inorganic salts specified for the separation of carbon dioxide are sodium nitrate, chloride, sulphate, and phosphate, calcium chloride, sulphate and phosphate, and barium nitrate, and chloride. Inorganic salts specified for the separation of hydrogen sulphide are the sulphate of iron, zinc, nickel and copper. The synthesis gas may pass up a tower in countercurrent to the ammoniacal solution (Fig. 1, not shown), or may be bubbled into a vessel which contains the ammoniacal solution (Figs. 2, 3 and 4, not shown). According to Fig. 3, the gas is further purified by countercurrent tower washing first with aqueous ammonia or an ammoniacal salt solution, then with acid, and finally with water. According to Fig. 4, the gas may in addition be prepurified by countercurrent tower washing with aqueous ammonia or ammoniacal salt solution.
Publications (1)
Publication Number | Publication Date |
---|---|
GB812134A true GB812134A (en) | 1959-04-22 |
Family
ID=1697750
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB10280/55A Expired GB812134A (en) | 1955-04-07 | Process for removal of carbon dioxide and (where necessary) hydrogen sulphide from gases containing these constituents |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB812134A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2200621A (en) * | 1987-02-06 | 1988-08-10 | Coal Ind | Treatment of gases |
CN112920835A (en) * | 2019-12-05 | 2021-06-08 | 中国石油化工股份有限公司 | System and method for dredging S Zorb recycle hydrogen control valve salt deposition on line and S Zorb adsorption desulfurization mechanism |
-
1955
- 1955-04-07 GB GB10280/55A patent/GB812134A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2200621A (en) * | 1987-02-06 | 1988-08-10 | Coal Ind | Treatment of gases |
CN112920835A (en) * | 2019-12-05 | 2021-06-08 | 中国石油化工股份有限公司 | System and method for dredging S Zorb recycle hydrogen control valve salt deposition on line and S Zorb adsorption desulfurization mechanism |
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