GB736111A - Process for the production of acrylonitrile - Google Patents
Process for the production of acrylonitrileInfo
- Publication number
- GB736111A GB736111A GB2216/53A GB221653A GB736111A GB 736111 A GB736111 A GB 736111A GB 2216/53 A GB2216/53 A GB 2216/53A GB 221653 A GB221653 A GB 221653A GB 736111 A GB736111 A GB 736111A
- Authority
- GB
- United Kingdom
- Prior art keywords
- reaction
- catalyst
- reaction chamber
- chamber
- alkali metal
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C253/00—Preparation of carboxylic acid nitriles
- C07C253/08—Preparation of carboxylic acid nitriles by addition of hydrogen cyanide or salts thereof to unsaturated compounds
- C07C253/12—Preparation of carboxylic acid nitriles by addition of hydrogen cyanide or salts thereof to unsaturated compounds to compounds containing carbon-to-carbon triple bonds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
- B01J8/12—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow
Abstract
In a continuous process for the production of acrylonitrile by passing acetylene and hydrocyanic acid together in the gas phase at elevated temperature through a reaction chamber in the presence of a solid known to be capable of catalysing the reaction of acetylene with hydrocyanic acid in the gas phase to form acrylonitrile, the catalyst is continuously introduced into, and withdrawn from, the reaction chamber, and moves continuously through the reaction chamber in countercurrent to the reaction gases throughout the period of the reaction. It is preferred to operate with the catalyst moving downwardly through the reaction chamber, the speed of the reaction gases in the reaction chamber being preferably 200 to 1500 times the speed of migration of the catalyst through the reaction chamber. The reacting gases are expediently heated to temperatures up to a maximum of 200-220 DEG C. and may be diluted with an inert gas, e.g. nitrogen, which is preferably preheated and supplied to the reaction chamber entirely or partially separate from the reacting gases. The diluent gas can be preheated by heat exchange with the hot gaseous reaction products or by allowing it to flow through the spent catalyst before the latter is withdrawn from the reaction chamber. To avoid overheating in the reaction zone a cold inert flushing gas, preferably nitrogen, may be supplied intermittently to the reaction zone and the supply of the reacting gases may also be shut off or reduced. The supply of the flushing gas and of the reacting gases may be automatically controlled by temperature sensers arranged in the reaction zone. The acetylene and hydrocyanic acid may be employed in the form of a synthesis gas mixture obtained by reaction of hydrocarbons, especially methane, with excess nitrogen in the electric arc. This synthesis gas mixture is preferably cooled to below 650 DEG C. before use and may be supplied to the reaction zone without previous purification. The catalyst should enter the reaction zone at 450-580 DEG C. and separate heating means may be necessary to attain this temperature. Preferred catalysts are active carbons, e.g. activated charcoals such as wood charcoal. Active carbons which have been formed by steam activation and particularly those which have been activated in the presence of alkali metal compounds, especially potassium compounds, are particularly suitable. The catalyst may also comprise an active carbon, e.g. wood charcoal, which has been moulded with an alkali metal compound as binding agent and tar before activation in the presence of an alkali metal compound, said carbon still containing 10 per cent or more of an alkali metal compound after activation and being used without previous washing. A suitable active carbon can be obtained by pressing wood charcoal dust into shaped elements with alkali lye and tar and activating with hydrogen at 800-1000 DEG C. after low temperature carbonization at 400 DEG to 600 DEG C. The active carbons may also be impregnated before use with an alkali metal compound, especially an alkali metal hydroxide, and if desired additionally treated with an alkaline earth metal compound, e.g. a barium salt. Mercury vanadate is also stated to have a good catalytic action. When active carbons are used they are first deaerated by subjecting to a reduced pressure treatment, if desired at elevated temperature, and then introduced into the reaction chamber in an atmosphere of inert gas, preferably being conveyed pneumatically. The apparatus used should preferably be constructed of a low-alloy steel containing up to 0.2 per cent carbon, 1.5 to 9 per cent chromium and 0.5 to 1.5 per cent aluminium. These alloys may also contain silicon and/or titanium in an amount of 0.3 to 1.5 per cent in each case. Two types of apparatus for carrying out the process are described and illustrated. They comprise essentially a reaction chamber provided with heating means and gas supply means. The chamber is connected at one end with a hopper for continuously charging the catalyst to the chamber and is provided at the other end with a bucket wheel or a horizontally rotating perforated base-plate for the continuous discharge of the catalyst in regulated quantities. In each case the catalyst migrates downwardly through the chamber which in one embodiment is divided into a plurality of reaction tubes from which the catalyst is discharged through the horizontally rotating perforated base-plate.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE736111X | 1952-01-25 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB736111A true GB736111A (en) | 1955-08-31 |
Family
ID=6642270
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2216/53A Expired GB736111A (en) | 1952-01-25 | 1953-01-26 | Process for the production of acrylonitrile |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB736111A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102895920A (en) * | 2012-10-31 | 2013-01-30 | 重庆鹏越科技发展有限公司 | Feeding device for dry acetylene generator |
-
1953
- 1953-01-26 GB GB2216/53A patent/GB736111A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102895920A (en) * | 2012-10-31 | 2013-01-30 | 重庆鹏越科技发展有限公司 | Feeding device for dry acetylene generator |
CN102895920B (en) * | 2012-10-31 | 2015-09-23 | 重庆鹏越科技发展有限公司 | A kind of feed arrangement of dry acetylene generators |
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