GB258887A - Method of effecting catalytic reactions for the production of ammonia - Google Patents

Method of effecting catalytic reactions for the production of ammonia

Info

Publication number
GB258887A
GB258887A GB23529/26A GB2352926A GB258887A GB 258887 A GB258887 A GB 258887A GB 23529/26 A GB23529/26 A GB 23529/26A GB 2352926 A GB2352926 A GB 2352926A GB 258887 A GB258887 A GB 258887A
Authority
GB
United Kingdom
Prior art keywords
zinc
carbon monoxide
hydrogen
gases
catalyst
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
Application number
GB23529/26A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
LAZOTE Inc
Original Assignee
LAZOTE Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by LAZOTE Inc filed Critical LAZOTE Inc
Publication of GB258887A publication Critical patent/GB258887A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00Ammonia; Compounds thereof
    • C01C1/02Preparation, purification or separation of ammonia
    • C01C1/04Preparation of ammonia by synthesis in the gas phase
    • C01C1/0405Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Abstract

258,887. Lazote, Inc., (Assignees of Williams, R.). Sept. 24, 1925, [Convention date]. Methyl alcohol; oxygenated organic compounds.- Carbon monoxide is removed from hydrogen - containing gases by passage under pressure over a catalyst capable of forming oxygenated organic compounds such as methyl alcohol and then removing the latter by condensation while the gases are still under pressure. Preferably the pressure employed is that under which the resulting hydrogen-containing gas is to react. Catalytic substances mentioned comprise zinc, zinc and chromium, and zinc and copper; iron may also be employed if the formation of some methane is not deleterious. In condensing out the methyl alcohol &c., impurities such as water, methane and sulphur compounds are simultaneously removed. Any carbon monoxide remaining in the gases is eliminated by passage under pressure over a methaneforming catalyst or through one of the known absorbents. In this manner, up to 10 per cent of carbon monoxide present in hydrogen-containing gases can be removed, whilst carbon dioxide and hydrocarbons such as methane may also be transformed into condensable products by the same process. Oily products and higher alcohols are produced when the gas speed is reduced, the temperature increased, or alkali oxides added to the catalyst. According to the example, a purified mixture of nitrogen and hydrogen in the volume proportions of 1 3 and containing 2 per cent of carbon monoxide is compressed by pump 2 to 900 atmospheres and conducted through a catalytic apparatus 3 containing a heated catalyst comprising zinc oxide prepared by igniting precipitated zinc carbonate, or a mixture of zinc and chromium oxides obtained by adding ammonia to a solution of zinc and chromium nitrates. The products pass through a water-cooled condenser 4, where the oxygenated compounds in which the impurities are dissolved separate out and are collected in the receiver 5. The Specification as open to inspection under Sect. 91 (3) (a) includes also an example according to which hydrogen containing 2 per cent of carbon monoxide and free from sulphur compounds is compressed by the pump 2 to 150 atmospheres and then passed as before through the catalytic apparatus 3 and condenser 4. This subject-matter does not appear in the Specification as accepted.
GB23529/26A 1925-09-24 1926-09-23 Method of effecting catalytic reactions for the production of ammonia Expired GB258887A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US258887XA 1925-09-24 1925-09-24

Publications (1)

Publication Number Publication Date
GB258887A true GB258887A (en) 1928-01-23

Family

ID=21828594

Family Applications (1)

Application Number Title Priority Date Filing Date
GB23529/26A Expired GB258887A (en) 1925-09-24 1926-09-23 Method of effecting catalytic reactions for the production of ammonia

Country Status (1)

Country Link
GB (1) GB258887A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3365268A (en) * 1964-08-19 1968-01-23 Pulp Paper Res Inst Production of ammonia from the organic materials present in spent pulping liquors with the simultaneous recovery of the pulping base and sulphur values present in said liquors
US4367206A (en) 1978-11-10 1983-01-04 Imperial Chemical Industries Limited Method for producing methanol and ammonia

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3365268A (en) * 1964-08-19 1968-01-23 Pulp Paper Res Inst Production of ammonia from the organic materials present in spent pulping liquors with the simultaneous recovery of the pulping base and sulphur values present in said liquors
US4367206A (en) 1978-11-10 1983-01-04 Imperial Chemical Industries Limited Method for producing methanol and ammonia

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