GB931469A - Process for the production of inert gas mixtures - Google Patents
Process for the production of inert gas mixturesInfo
- Publication number
- GB931469A GB931469A GB20915/61A GB2091561A GB931469A GB 931469 A GB931469 A GB 931469A GB 20915/61 A GB20915/61 A GB 20915/61A GB 2091561 A GB2091561 A GB 2091561A GB 931469 A GB931469 A GB 931469A
- Authority
- GB
- United Kingdom
- Prior art keywords
- tank
- hydrogen
- pressure
- air
- valves
- 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
- B01D53/46—Removing components of defined structure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/14—Production of inert gas mixtures; Use of inert gases in general
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/02—Preparation of nitrogen
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/04—Purification or separation of nitrogen
- C01B21/0405—Purification or separation processes
- C01B21/0411—Chemical processing only
- C01B21/0422—Chemical processing only by reduction
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B23/00—Noble gases; Compounds thereof
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0043—Impurity removed
- C01B2210/0045—Oxygen
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Biomedical Technology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Catalysts (AREA)
- Drying Of Gases (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Oxygen free gas mixtures are prepared by adding to recycled oxygen free mixture of nitrogen and noble gases, in a proportion of less than 1 part air to 10 parts mixture, adding hydrogen in sufficient amount to react with all the oxygen present as in the parent Specification, passing resulting mixture over a catalyst for the reaction between hydrogen and oxygen at a pressure higher than that at which the product is to be collected, removing the water formed, separating a major portion of the oxygen free mixture for recycling, expanding the remainder in a tank, and starting or stopping the feed of air and hydrogen in response to pressure variations in the tank. Air and hydrogen pass through valves 3,4 from compressors 2,1, into recycle stream from pump G, and the resulting mixture is fed to catalyst furnace K. The proportion of hydrogen to air is controlled in response to <PICT:0931469/III/1> analyser A. Water is separated in condenser W and withdrawn through two float operated valves, S1,S2 the former being of smaller section than the latter. A major part of the effluent is recycled through pump G and the remainder passed through drying tank T1 which operates or is regenerated alternately with drying tank T2. Dry gas is withdrawn through valve U operating at a certain pressure to tank V at a lower pressure. The feed valves 3,4 are operated by pressure controller D. The drying tanks are regenerated by hot gases circulated by pump P or by cooling in tank W2 under reduced pressure, condensate being removed by float operated valves S3,S4.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEZ0007798 | 1960-02-04 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB931469A true GB931469A (en) | 1963-07-17 |
Family
ID=7620266
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3968/61A Expired GB913148A (en) | 1960-02-04 | 1961-02-02 | Process for the production of inert gas mixtures |
GB20915/61A Expired GB931469A (en) | 1960-02-04 | 1961-06-09 | Process for the production of inert gas mixtures |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3968/61A Expired GB913148A (en) | 1960-02-04 | 1961-02-02 | Process for the production of inert gas mixtures |
Country Status (3)
Country | Link |
---|---|
DE (1) | DE1417743A1 (en) |
FR (1) | FR80157E (en) |
GB (2) | GB913148A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2640159A1 (en) * | 1988-12-09 | 1990-06-15 | Commissariat Energie Atomique | Process and device for purifying a neutral gas containing oxygen and/or hydrogen as impurities |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4057510A (en) * | 1975-09-29 | 1977-11-08 | Texaco Inc. | Production of nitrogen rich gas mixtures |
DE3137569A1 (en) * | 1981-09-22 | 1983-04-21 | Leybold-Heraeus GmbH, 5000 Köln | METHOD AND DEVICE FOR PRODUCING HIGH PURITY NITROGEN |
US4579723A (en) * | 1985-03-28 | 1986-04-01 | The Boc Group, Inc. | Methods for purifying inert gas streams |
-
1960
- 1960-02-04 DE DE19601417743 patent/DE1417743A1/en active Pending
-
1961
- 1961-02-02 GB GB3968/61A patent/GB913148A/en not_active Expired
- 1961-05-12 FR FR861849A patent/FR80157E/en not_active Expired
- 1961-06-09 GB GB20915/61A patent/GB931469A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2640159A1 (en) * | 1988-12-09 | 1990-06-15 | Commissariat Energie Atomique | Process and device for purifying a neutral gas containing oxygen and/or hydrogen as impurities |
Also Published As
Publication number | Publication date |
---|---|
GB913148A (en) | 1962-12-19 |
DE1417743A1 (en) | 1969-01-02 |
FR80157E (en) | 1963-03-22 |
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