GB334193A - Improvements in the manufacture and production of valuable products from gaseous acetylene hydrocarbons or aldehydes - Google Patents

Improvements in the manufacture and production of valuable products from gaseous acetylene hydrocarbons or aldehydes

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Publication number
GB334193A
GB334193A GB601829A GB601829A GB334193A GB 334193 A GB334193 A GB 334193A GB 601829 A GB601829 A GB 601829A GB 601829 A GB601829 A GB 601829A GB 334193 A GB334193 A GB 334193A
Authority
GB
United Kingdom
Prior art keywords
over
hydrogen
acetylene
silica gel
mixture
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
GB601829A
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.)
IG Farbenindustrie AG
Original Assignee
IG Farbenindustrie AG
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 IG Farbenindustrie AG filed Critical IG Farbenindustrie AG
Priority to GB601829A priority Critical patent/GB334193A/en
Publication of GB334193A publication Critical patent/GB334193A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C209/00Preparation of compounds containing amino groups bound to a carbon skeleton
    • C07C209/60Preparation of compounds containing amino groups bound to a carbon skeleton by condensation or addition reactions, e.g. Mannich reaction, addition of ammonia or amines to alkenes or to alkynes or addition of compounds containing an active hydrogen atom to Schiff's bases, quinone imines, or aziranes

Abstract

334,193. Johnson, J. Y., (I. G. Farbenindustrie Akt.-Ges.). Feb. 23, 1929. Amines; nitriles; heterocyclic nitrogen compounds.-Nitrogenous products are obtained by passing acetylene, or mixtures thereof with its homologues, together with ammonia and/or amines, and if desired with steam, over heated condensation catalysts, and then conducting the products, without isolation, together with hydrogen over metallic hydrogenating catalysts. Instead of acetylene, aliphtic aldehydes may be employed, or mixtures thereof with the acetylene hydrocarbons. The condensation and hydrogenation may be effected simultaneously by mixing the two catalysts and introducing the hydrogen at the beginning of the operation. The condensation catalysts comprise compounds of aluminium or of metals, except arsenic, having a specific gravity above 4.4 and belonging to the second to the seventh periodic groups; hydrogenating catalysts mentioned are metals of the iron group, copper and platinum. Industrial gas mixtures containing hydrogen and acetylenic hydrocarbons may be employed, e.g. coke-oven gas or gas mixtures obtained by passing coke-oven gas or a mixture of methane and hydrogen through a high tension electric arc. The condensation is effected at a temperature of 250‹- 500‹ C., whilst the hydrogenation preferably takes place at a lower temperature, e.g. 150- 250‹ C. When producing hydrogenated heterocyclic bases from mixtures of acetylene with ammonia and/or an amine in the presence of steam, the gas mixture is preferably passed over the catalyst at a speed of at least 10 litres of the hydrocarbon per hour per litre of the catalyst. According to the examples, (1) acetylene, ammonia and hydrogen are passed at 350‹ C. over a mixture of equal parts by weight of zinc oxide and thorium oxide precipitated on silica gel and then over finely-divided nickel on silica gel at 150‹ C. ; the condensate consists mainly of piperidine and monoethylamine; the addition of steam increases the proportion of the piperidine; (2) ammonia and acetaldehyde vapour mixed with hydrogen are led at 350‹ C. over zinc oxide mounted on silica gel incorporated with thorium oxide and then at 150‹ C. over nickel on silica gel; the product mainly comprises piperidine and a small quantity of amines; (3) ammonia, acetylene, hydrogen and the vapours of acetaldehyde and ethylamine are passed at 400‹ C. over a mixture of zinc oxide, thorium oxide and metallic cadmium on silica gel and then at 120‹ C. over nickel on silica gel; the condensate consists chiefly of ethylamine and piperidines, together with small quantities of acetonitrile, propionitrile, pyridine bases and pyrrol derivatives; (4) aniline vapour, acetylene and hydrogen are conducted at 300‹ C. over a mixture of chromic oxide, aluminium oxide and zinc oxide on silica gel and then at 200‹ C. over nickel on silica gel; the condensate mainly comprises hydrogenated quinolines, chiefly tetrahydroquinoline; (5) acety. lene, hydrogen, methane and nitrogen (obtained by treating a mixture of methane and hydrogen in the electric arc and containing a small amount of allylene and diacetylene) is mixed with ammonia and passed at 380‹ C. over a mixture of zinc and chromic oxides and then at 150‹ C. over activated nickel; on cooling, a product consisting of primary ethylamine and acetonitrile is obtained. Specifications 109,983, 265,960, 321,177 and 332,623 are referred to. The Provisional Specification describes the use of any acetylene hydrocarbon.
GB601829A 1929-02-23 1929-02-23 Improvements in the manufacture and production of valuable products from gaseous acetylene hydrocarbons or aldehydes Expired GB334193A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB601829A GB334193A (en) 1929-02-23 1929-02-23 Improvements in the manufacture and production of valuable products from gaseous acetylene hydrocarbons or aldehydes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB601829A GB334193A (en) 1929-02-23 1929-02-23 Improvements in the manufacture and production of valuable products from gaseous acetylene hydrocarbons or aldehydes

Publications (1)

Publication Number Publication Date
GB334193A true GB334193A (en) 1930-08-25

Family

ID=9806931

Family Applications (1)

Application Number Title Priority Date Filing Date
GB601829A Expired GB334193A (en) 1929-02-23 1929-02-23 Improvements in the manufacture and production of valuable products from gaseous acetylene hydrocarbons or aldehydes

Country Status (1)

Country Link
GB (1) GB334193A (en)

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2443420A (en) * 1946-02-21 1948-06-15 Du Pont Synthesis of nitriles
US2452187A (en) * 1946-02-21 1948-10-26 Du Pont Synthesis of nitriles
US2468363A (en) * 1942-02-19 1949-04-26 Alais & Froges & Camarque Cie Methods for preparing acetonitrile
US2523580A (en) * 1944-12-11 1950-09-26 Phillips Petroleum Co Production of alkyl pyridines
US2525818A (en) * 1946-06-24 1950-10-17 Phillips Petroleum Co Production of nitriles
US2605264A (en) * 1944-02-25 1952-07-29 Shell Dev Process for the production of pyridines
US2762813A (en) * 1952-04-03 1956-09-11 Distillers Co Yeast Ltd Process of producing piperidine compounds
US2995558A (en) * 1957-11-05 1961-08-08 Phillips Petroleum Co Production of pyridine homologs
WO2014031226A1 (en) * 2012-08-21 2014-02-27 Uop Llc The production of nitrogen compounds from a methane conversion process
US8927769B2 (en) 2012-08-21 2015-01-06 Uop Llc Production of acrylic acid from a methane conversion process
US8933275B2 (en) 2012-08-21 2015-01-13 Uop Llc Production of oxygenates from a methane conversion process
US8937186B2 (en) 2012-08-21 2015-01-20 Uop Llc Acids removal and methane conversion process using a supersonic flow reactor
US9205398B2 (en) 2012-08-21 2015-12-08 Uop Llc Production of butanediol from a methane conversion process
US9308513B2 (en) 2012-08-21 2016-04-12 Uop Llc Production of vinyl chloride from a methane conversion process
US9327265B2 (en) 2012-08-21 2016-05-03 Uop Llc Production of aromatics from a methane conversion process
US9370757B2 (en) 2012-08-21 2016-06-21 Uop Llc Pyrolytic reactor
US9434663B2 (en) 2012-08-21 2016-09-06 Uop Llc Glycols removal and methane conversion process using a supersonic flow reactor
US9656229B2 (en) 2012-08-21 2017-05-23 Uop Llc Methane conversion apparatus and process using a supersonic flow reactor
US9689615B2 (en) 2012-08-21 2017-06-27 Uop Llc Steady state high temperature reactor
US9707530B2 (en) 2012-08-21 2017-07-18 Uop Llc Methane conversion apparatus and process using a supersonic flow reactor

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2468363A (en) * 1942-02-19 1949-04-26 Alais & Froges & Camarque Cie Methods for preparing acetonitrile
US2605264A (en) * 1944-02-25 1952-07-29 Shell Dev Process for the production of pyridines
US2523580A (en) * 1944-12-11 1950-09-26 Phillips Petroleum Co Production of alkyl pyridines
US2443420A (en) * 1946-02-21 1948-06-15 Du Pont Synthesis of nitriles
US2452187A (en) * 1946-02-21 1948-10-26 Du Pont Synthesis of nitriles
US2525818A (en) * 1946-06-24 1950-10-17 Phillips Petroleum Co Production of nitriles
US2762813A (en) * 1952-04-03 1956-09-11 Distillers Co Yeast Ltd Process of producing piperidine compounds
US2995558A (en) * 1957-11-05 1961-08-08 Phillips Petroleum Co Production of pyridine homologs
US8933275B2 (en) 2012-08-21 2015-01-13 Uop Llc Production of oxygenates from a methane conversion process
US8927769B2 (en) 2012-08-21 2015-01-06 Uop Llc Production of acrylic acid from a methane conversion process
WO2014031226A1 (en) * 2012-08-21 2014-02-27 Uop Llc The production of nitrogen compounds from a methane conversion process
US8937186B2 (en) 2012-08-21 2015-01-20 Uop Llc Acids removal and methane conversion process using a supersonic flow reactor
US9023255B2 (en) 2012-08-21 2015-05-05 Uop Llc Production of nitrogen compounds from a methane conversion process
US9205398B2 (en) 2012-08-21 2015-12-08 Uop Llc Production of butanediol from a methane conversion process
US9308513B2 (en) 2012-08-21 2016-04-12 Uop Llc Production of vinyl chloride from a methane conversion process
US9327265B2 (en) 2012-08-21 2016-05-03 Uop Llc Production of aromatics from a methane conversion process
US9370757B2 (en) 2012-08-21 2016-06-21 Uop Llc Pyrolytic reactor
US9434663B2 (en) 2012-08-21 2016-09-06 Uop Llc Glycols removal and methane conversion process using a supersonic flow reactor
US9656229B2 (en) 2012-08-21 2017-05-23 Uop Llc Methane conversion apparatus and process using a supersonic flow reactor
US9689615B2 (en) 2012-08-21 2017-06-27 Uop Llc Steady state high temperature reactor
US9707530B2 (en) 2012-08-21 2017-07-18 Uop Llc Methane conversion apparatus and process using a supersonic flow reactor

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