GB998771A - Improvements in or relating to the purification of gaseous helium - Google Patents
Improvements in or relating to the purification of gaseous heliumInfo
- Publication number
- GB998771A GB998771A GB2370262A GB2370262A GB998771A GB 998771 A GB998771 A GB 998771A GB 2370262 A GB2370262 A GB 2370262A GB 2370262 A GB2370262 A GB 2370262A GB 998771 A GB998771 A GB 998771A
- Authority
- GB
- United Kingdom
- Prior art keywords
- molecular sieve
- remove
- gas
- vapour
- residual
- 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
- C01B23/00—Noble gases; Compounds thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Drying Of Gases (AREA)
- Gas Separation By Absorption (AREA)
Abstract
<PICT:0998771/C1/1> Gaseous helium is purified by effecting a catalytic combination of gaseous oxygen and hydrogen present, passing the gas through a molecular sieve to remove H2O vapour formed; passing the resultant gas through an oxidation stage to oxidize residual H2 to H2O and CO to CO2, then through a second molecular sieve, a getterer to remove residual oxygen and nitrogen, and then possibly through a third molecular sieve. In Fig. 1, helium is introduced through control valve 2 into catalytic chamber 3 where O2 and H2 impurities combine, and the gas mixture is passed into molecular sieve 6 which contains molecular sieve material type 5a (calcium aluminosilicate) at, e.g. 20 DEG C. to remove water vapour. The gas then passes through a two-stage oxidation means which consists of (a) silica tube 67 containing copper oxide heated to 630 DEG C. by furnace 8, and then (b) a silica tube 9 containing "Hopcalite" (MnO2 + CnO) at 240 DEG C. Thus residual H2 is oxidized to water vapour and CO to CO2, which are removed in the second molecular sieves 10 and 11, which contain Linde type 5a. Unit 10 is at room temperature, unit 11 is at - 196 DEG C. The emergent gases now pass through metal gettering means 13 which contains lithium vapour to remove the last traces of O2 and N2, and finally molecular sieve 15 (identical with 11). The apparatus may be operated at a pressure of 5-10 p.s.i.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DENDAT1252187D DE1252187B (en) | 1962-06-20 | Process for purifying helium | |
GB2370262A GB998771A (en) | 1962-06-20 | 1962-06-20 | Improvements in or relating to the purification of gaseous helium |
FR938684A FR83874E (en) | 1962-06-20 | 1963-06-19 | Helium purification |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2370262A GB998771A (en) | 1962-06-20 | 1962-06-20 | Improvements in or relating to the purification of gaseous helium |
Publications (1)
Publication Number | Publication Date |
---|---|
GB998771A true GB998771A (en) | 1965-07-21 |
Family
ID=10199902
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2370262A Expired GB998771A (en) | 1962-06-20 | 1962-06-20 | Improvements in or relating to the purification of gaseous helium |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE1252187B (en) |
GB (1) | GB998771A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102311102A (en) * | 2010-07-07 | 2012-01-11 | 住友精化株式会社 | The purification process of helium and purification devices |
EP2404656A2 (en) | 2010-07-08 | 2012-01-11 | Air Products And Chemicals, Inc. | Treatment of flue gas from an oxyfuel combustion process |
CN102602899A (en) * | 2011-01-21 | 2012-07-25 | 住友精化株式会社 | Helium purification method and device |
CN113697785A (en) * | 2020-05-22 | 2021-11-26 | 中国石油化工股份有限公司 | Method for preparing helium by combining oxidation method with membrane separation |
CN114229810A (en) * | 2021-12-15 | 2022-03-25 | 华能核能技术研究院有限公司 | Helium purification system and method for high-temperature gas-cooled reactor internals thermal aging test |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3137569A1 (en) * | 1981-09-22 | 1983-04-21 | Leybold-Heraeus GmbH, 5000 Köln | METHOD AND DEVICE FOR PRODUCING HIGH PURITY NITROGEN |
US6517791B1 (en) * | 2000-12-04 | 2003-02-11 | Praxair Technology, Inc. | System and process for gas recovery |
-
0
- DE DENDAT1252187D patent/DE1252187B/en active Pending
-
1962
- 1962-06-20 GB GB2370262A patent/GB998771A/en not_active Expired
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102311102A (en) * | 2010-07-07 | 2012-01-11 | 住友精化株式会社 | The purification process of helium and purification devices |
EP2404656A2 (en) | 2010-07-08 | 2012-01-11 | Air Products And Chemicals, Inc. | Treatment of flue gas from an oxyfuel combustion process |
CN102602899A (en) * | 2011-01-21 | 2012-07-25 | 住友精化株式会社 | Helium purification method and device |
CN102602899B (en) * | 2011-01-21 | 2015-04-01 | 住友精化株式会社 | Helium purification method and device |
CN113697785A (en) * | 2020-05-22 | 2021-11-26 | 中国石油化工股份有限公司 | Method for preparing helium by combining oxidation method with membrane separation |
CN114229810A (en) * | 2021-12-15 | 2022-03-25 | 华能核能技术研究院有限公司 | Helium purification system and method for high-temperature gas-cooled reactor internals thermal aging test |
CN114229810B (en) * | 2021-12-15 | 2023-11-03 | 华能核能技术研究院有限公司 | Helium purification system and method for thermal aging test of high-temperature gas cooled reactor internals |
Also Published As
Publication number | Publication date |
---|---|
DE1252187B (en) | 1967-10-19 |
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