GB283163A - - Google Patents
Info
- Publication number
- GB283163A GB283163A GB283163DA GB283163A GB 283163 A GB283163 A GB 283163A GB 283163D A GB283163D A GB 283163DA GB 283163 A GB283163 A GB 283163A
- Authority
- GB
- United Kingdom
- Prior art keywords
- ammonia
- litres
- acetylene
- per cent
- bases
- 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.)
- Active
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Pyridine Compounds (AREA)
Abstract
283,163. I. G. Farbenindustrie Akt.- Ges. Jan. 5, 1927, [Convention date]. Ethylamines; heterocyclic bases; hydrocarbons. -Organic bases are obtained by passing a mixture of acetylene and ammonia over a catalyst consisting of an inorganic salt which is capable of forming an addition compound with ammonia and is not reduced by acetylene, such as a metal chloride. The formation of acetonitrile is negligible. Preferably, the catalyst is a halide which forms an additional compound with ammonia which is stable at the reaction temperature. Suitable catalysts may be prepared by soaking a carrier such as pumice, asbestos, or coke, dried at 500-600‹ C., in a solution of an anhydrous halide in absolute alcohol or methanol, evaporating the solvent, and, if desired, treating the mass with ammonia at ordinary or raised temperature. The catalysts mentioned are obtained from zinc chloride, an equi-molecular mixture of zinc and ferric chlorides, and an equi-molecular mixture of cadmium and cupric chlorides. The reaction is effected at 280-350‹ C., but as the reaction is exothermic it is preferred to use a diluent gas which is constantly returned to the catalytic apparatus. In an example, 400 litres of ammonia per hour are circulated over a zinc chloride catalyst and 10 litres of ammonia and 10-20 litres of acetylene are added to the stream while 10 litres are withdrawn after passing the catalytic apparatus. The gas withdrawn is cooled to separate liquid products, and the uncondensed gas contains, besides ammonia, some hydrogen and heavy hydrocarbons. The liquid products comprise 15-20 per cent, chiefly diethylamine, 5-6 per cent tri-ethylamine and cyclic bases rich in hydrogen, 60-65 per cent a- and gamma-methyl-pyridine, and 10-12 per cent higher methyl pyridines and polynuclear bases. i The Specification as open to inspection under Sect. 91 (3) (a) describes the catalysts as preferably capable of forming addition compounds with pyridine, and does not limit them to those which are not reduced by acetylene. This subject-matter does not appear in the Specification as accepted.
Publications (1)
Publication Number | Publication Date |
---|---|
GB283163A true GB283163A (en) |
Family
ID=1741035
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB283163D Active GB283163A (en) |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB283163A (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
-
0
- GB GB283163D patent/GB283163A/en active Active
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
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 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB283163A (en) | ||
Li et al. | Catalytic properties of sprayed Ru/Al2O3 and promoter effects of alkali metals in CO2 hydrogenation | |
Weigert | Synthesis of aryl isocyanates from nitro compounds and carbon monoxide | |
Tsuda et al. | Preparation and characterization of copper (I) amides | |
Obuchi et al. | Reactivity of nitrogen containing organic intermediates in the selective catalytic reduction of NOx with organic compounds: a model study with tert-butyl substituted nitrogen compounds | |
Goswami et al. | Efficient Activation of 2‐Iminomethylpyridine/Cobalt‐Based Alkyne [2+ 2+ 2] Cycloaddition Catalyst by Addition of a Silver Salt | |
Ahmed et al. | A K-arylacetylide complex for catalytic terminal alkyne functionalization using KO t Bu as a precatalyst | |
Stroek et al. | Discovery of a simple iron catalyst reveals the intimate steps of C–H amination to form C–N bonds | |
Darensbourg et al. | Arene-transition metal complexes. 1. Site exchange and chemical characteristics of. eta. 6-C6 (CH3) 6Ru-. eta. 4-C6 (CH3) 6 | |
L’Argentière et al. | A palladium tetra-coordinated complex as catalyst in the selective hydrogenation of 1-heptyne | |
JPS63287732A (en) | Reduction dehalogenation for organic halogen compound | |
Heinsohn et al. | Stereochemistry of reduction of substituted cyclohexanones with triisobutylaluminum and diisobutylaluminum hydride | |
Rani et al. | Amino cyclization of terminal (α, ω)-diols over modified ZSM-5 catalysts | |
EP0006999A1 (en) | A process for the production of 2-chlorobenzonitrile derivatives | |
Captain et al. | On the mechanism of the NO reduction by propylene over supported Pt catalysts | |
Davis et al. | Infrared spectra and ab initio SCF calculations for alkane-hydrogen fluoride complexes | |
Aime et al. | Reactions of Solid H2Os3 (CO) 10 with Gaseous CO, NH3, and H2S | |
Janz et al. | The Reaction of Cyanogen and Related Nitriles with 1, 3-Dienes. V. Acrylonitrile and Butadiene1 | |
Bushkov et al. | Ti-catalyzed heterometathetical condensation of N-sulfinylamines into sulfurdiimines | |
Murata et al. | Lithium-doped sulfated-zirconia catalysts for oxidative coupling of methane to give ethylene and ethane | |
US1811959A (en) | Vinyl derivatives of acetylene and method of preparing the same | |
JPS60169471A (en) | Preparation of piperidine | |
US2425267A (en) | Process of manufacturing acrylonitrile from acetylene and hcn | |
CA2056075C (en) | Preparation of ortho-phenylenediamine | |
US11518685B2 (en) | Conversion of ammonium nitrate into useful products |