GB910087A - A method for the vapour phase synthesis of vinyl acetate - Google Patents
A method for the vapour phase synthesis of vinyl acetateInfo
- Publication number
- GB910087A GB910087A GB2083060A GB2083060A GB910087A GB 910087 A GB910087 A GB 910087A GB 2083060 A GB2083060 A GB 2083060A GB 2083060 A GB2083060 A GB 2083060A GB 910087 A GB910087 A GB 910087A
- Authority
- GB
- United Kingdom
- Prior art keywords
- temperature
- reactor
- reaction temperature
- reaction
- starting material
- 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
-
- 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
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1836—Heating and cooling the reactor
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B13/00—Conditioning or physical treatment of the material to be shaped
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00026—Controlling or regulating the heat exchange system
- B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
- B01J2208/00044—Temperature measurement
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00176—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles outside the reactor
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- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00054—Controlling or regulating the heat exchange system
- B01J2219/00056—Controlling or regulating the heat exchange system involving measured parameters
- B01J2219/00058—Temperature measurement
- B01J2219/00063—Temperature measurement of the reactants
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- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00094—Jackets
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- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00159—Controlling the temperature controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00164—Controlling or regulating processes controlling the flow
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
<PICT:0910087/III/1> Vinyl acetate is synthesized by the vapour phase reaction of acetylene and acetic acid in a fluidized catalytic reaction apparatus 1 wherein the reaction temperature is controlled by regulating the temperature of the starting material entering the reactor in response to the variation of the reaction temperature so as to maintain the reaction temperature substantially constant. In one method of operation, the starting material mixture 3, comprising acetylene gas from a blower and acetic acid vapour from an evaporator, is passed through a cooler or preheater 4 and a by-pass 5 in parallel and the proportion which passes through either path is regulated by valves 6 and 61 controlled in response to variations in the reaction temperature whereby the temperature of the starting material mixture entering the reactor is adjusted so as to maintain the reaction temperature substantially constant. In the apparatus shown, in which the reactor is large, two instruments 7 and 8 form a compound controlling system in which 7 measures the internal temperature (a) of the reactor 1 and will give a command to 8 corresponding to the variation of temperature whilst 8 will measure the temperature (b) and operate the valves 6 and 61 to make temperature (b) vary by an amount equal to the command given by 7. In a smaller apparatus, the instrument 7 can be used to control 6 and 61 directly. The catalyst may be powdered active carbon impregnated with zinc acetate and dried.ALSO:<PICT:0910087/IV (b)/1> Vinyl acetate is synthesized by this vapour phase reaction of acetylene and acetic acid in fluidized catalytic reaction apparatus 1 wherein the reaction temperature is controlled by regulating the temperature of the starting material entering the reactor in response to the variation of the reaction temperature so as to maintain the reaction temperature substantially constant. In one method operation, the starting material mixture 3, comprising acetylene gas from a blower and acetic acid vapour from an evaporator, is passed through a cooler or preheater 4 and a bypass 5 in parallel and the proportion which passes through either path is regulated by valves 6 and 61 controlled in response to variations in the reaction temperature whereby the temperature of the starting material mixture entering the reactor is adjusted so as to maintain the reaction temperature substantially constant. In the apparatus shown, in which the reactor is large, two instruments 7 and 8 form a compound controlling system in which 7 measures the internal temperature (a) of the reactor 1 and will give a command to 8 corresponding to the variation of the temperature, whilst 8 will measure the temperature (b) and operate the valves 6 and 61 to make the temperature (b) vary by an amount equal to the command given by 7. In smaller apparatus, the instrument 7 can be used to control 6 and 61 directly. The catalyst may be powdered active carbon impregnated with zinc acetate and dried.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2815359 | 1959-09-04 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB910087A true GB910087A (en) | 1962-11-07 |
Family
ID=12240800
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2083060A Expired GB910087A (en) | 1959-09-04 | 1960-06-14 | A method for the vapour phase synthesis of vinyl acetate |
Country Status (3)
Country | Link |
---|---|
DE (1) | DE1230013B (en) |
FR (1) | FR1262344A (en) |
GB (1) | GB910087A (en) |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT162578B (en) * | 1940-12-27 | 1949-03-10 | Lonza Ag | Process for the production of vinyl esters |
-
1960
- 1960-06-14 GB GB2083060A patent/GB910087A/en not_active Expired
- 1960-07-11 FR FR832653A patent/FR1262344A/en not_active Expired
- 1960-08-30 DE DE1960K0041580 patent/DE1230013B/en active Pending
Also Published As
Publication number | Publication date |
---|---|
DE1230013B (en) | 1966-12-08 |
FR1262344A (en) | 1961-05-26 |
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