GB426741A - Improvements in and relating to the preparation and purification of nickel carbonyl - Google Patents
Improvements in and relating to the preparation and purification of nickel carbonylInfo
- Publication number
- GB426741A GB426741A GB3145233A GB3145233A GB426741A GB 426741 A GB426741 A GB 426741A GB 3145233 A GB3145233 A GB 3145233A GB 3145233 A GB3145233 A GB 3145233A GB 426741 A GB426741 A GB 426741A
- Authority
- GB
- United Kingdom
- Prior art keywords
- pressure
- carbonyl
- atm
- condensation
- nickel
- 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
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G53/00—Compounds of nickel
- C01G53/02—Carbonyls
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
Nickel carbonyl is separated in the liquid phase from a mixture of gases or vapours including carbon monoxide and nickel carbonyl by condensation at such a partial pressure of carbon monoxide in the condensation vessel that the vapour pressure of the nickel carbonyl is in the neighbourhood of the minimum for the condensation temperature. The concentration of carbon monoxide may be varied to give the desired partial pressure, or the pressure at which the carbonyl is formed may be raised or lowered to the optimum value and condensation effected at this pressure. Where the carbonyl has been formed at this optimum pressure, no adjustment will be necessary. For condensation temperatures of 0-40 DEG C., a partial pressure of 10--150 atm. gives good results. Preferably, the carbonyl vapour pressure is not greater than corresponds to 50 g. Ni per cubic metre of gas at N.T.P. above the minimum. Between 0--80 DEG C. the partial pressure of CO should be between 45 atm. less and 75 atm. more than corresponds to the minimum carbonyl vapour pressure. According to examples: (1) Gases from an atmospheric pressure nickel extraction plant containing nickel carbonyl equivalent to 420 g. Ni per c.m., are compressed at 0 DEG C. to 55 atm. and separation then effected. (2) Gases from a high pressure plant containing carbonyl equivalent to 450 g. Ni per c.m. at 250 atm. and 80 DEG C. are expanded to 70 atm. at atmospheric temperature and separation then effected.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3145233A GB426741A (en) | 1933-11-11 | 1933-11-11 | Improvements in and relating to the preparation and purification of nickel carbonyl |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3145233A GB426741A (en) | 1933-11-11 | 1933-11-11 | Improvements in and relating to the preparation and purification of nickel carbonyl |
Publications (1)
Publication Number | Publication Date |
---|---|
GB426741A true GB426741A (en) | 1935-04-09 |
Family
ID=10323285
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3145233A Expired GB426741A (en) | 1933-11-11 | 1933-11-11 | Improvements in and relating to the preparation and purification of nickel carbonyl |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB426741A (en) |
-
1933
- 1933-11-11 GB GB3145233A patent/GB426741A/en not_active Expired
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2060940A (en) | Process for obtaining krypton and xenon | |
GB426741A (en) | Improvements in and relating to the preparation and purification of nickel carbonyl | |
US2399142A (en) | Thermal dissociation of monoethanolamine salts | |
GB353704A (en) | Improvements in and relating to the liquifaction of chlorine | |
GB129989A (en) | ||
US2167112A (en) | Preparation of nickel carbonyl | |
US1523314A (en) | Natural-gas gasoline | |
ES313064A1 (en) | A procedure for the purification of gaseous hydrogen contaminated with methane. (Machine-translation by Google Translate, not legally binding) | |
GB355861A (en) | Process for the separation of carbon monoxide from mixed gases containing hydrogen | |
GB434193A (en) | Process for obtaining constituents of the atmosphere with a higher boiling point than oxygen | |
GB479265A (en) | Improvements in or relating to a method of making sponge rubber | |
US1879497A (en) | Preparation of ketene | |
US2064359A (en) | Microbiological preparation of 2.3-butylene glycol | |
GB495464A (en) | Improvements in or relating to method of manufacture of smokeless powder | |
US1315544A (en) | Ration | |
GB495463A (en) | Improvements in or relating to method of manufacture of smokeless powder | |
GB495516A (en) | Process for the separation of trimethylamine from mixtures with monomethylamine and dimethylamine | |
US2061523A (en) | Sulphur | |
GB355832A (en) | Improvements in the collection of sulphur | |
GB511848A (en) | Process for recovering acetylene from acetylene-containing gases | |
GB365092A (en) | Improvements in or relating to the treatment of gaseous mixtures for the purpose of separating them into their components or enriching them with respect to one or more of their components | |
GB410848A (en) | Improvements in processes of removing and recovering acidic gases from gas mixtures containing said acidic gases | |
US496047A (en) | Franxois gustave dosmond and jean ferdinand rozxs | |
GB456836A (en) | Improvements in or relating to a method of, and apparatus for determining variations in the physical or chemical characteristics or properties of a fluid | |
US1565345A (en) | Process of producing methyl alcohol and methylene chloride from methane |