Methyl acetate hydrolysis process and its equipment

A technology of methyl acetate and process, applied in the field of methyl acetate hydrolysis process and equipment, can solve the problems of catalyst particles falling off, inconvenient catalyst replacement and activation, and troublesome catalyst package manufacturing.

Inactive Publication Date: 2002-11-20
FUZHOU UNIV
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  • Abstract
  • Description
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  • Application Information

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Problems solved by technology

The Chinese patent (ZL97101306.3) adopts the method of "bundling bag", puts the cation exchange resin into the corrosion-resistant cloth bag to make the catalyst packing, and then puts it into the tower for reaction, which solves the problem of catalyst particles falling off and losing, However, the manufacture of the catalyst package is still troublesome, and the replacement and activation of the catalyst is still inconvenient

Method used

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  • Methyl acetate hydrolysis process and its equipment
  • Methyl acetate hydrolysis process and its equipment
  • Methyl acetate hydrolysis process and its equipment

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Embodiment

[0012] The specific operation process of the methyl acetate hydrolysis process is: the methyl acetate or the mixture of methyl acetate and methanol measured according to the ratio is continuously transported to the second preheater 6 through the second metering pump 5 and heated to a predetermined temperature from the top of the hydrolysis tower or The bottom of the reaction rectification section of the hydrolysis tower or the middle part of the stripping section of the hydrolysis tower is sent into the hydrolysis tower, and the metered water is continuously sent to the first preheater 2 by the first metering pump 3 to be heated to a predetermined temperature and enters the hydrolysis from the top of the tower Tower, the hydrolysis reaction is carried out in the reaction zone. The reaction product is separated by rectification in the tower, and the volatile components (mainly methyl acetate) are condensed by the condenser 1 at the top of the tower, and the condensate is mixed w...

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Abstract

The present invention discloses a hydrolysis process of methyl acetate by using cation exchange resin as catalyst and its equipment. Said hydrolysis equipment is a cylindrical tower, its interior contains reactive rectification section and stripping section, the hydrolysis reaction is implemented in reactive rectification section, and the reactive rectification structure unit being in reaction zone organically combines the catalyst loading, liquid distributor, overflow pipe and vapour-liquid contact equipment together, its structure is compact and its equipment efficiency is high. Its hydrolysis process is as follows; making water and methyl acetate product hydrolysis in the reaction zone according to a certain proportion, and making non-reacted reactant pass through the condenser and condensed, then returning it back into reaction zone to further react. Its ester hydrolysis rate is 40%-99.8%.

Description

Technical field: [0001] The present invention relates to the reaction rectification technology of methyl acetate hydrolysis and used equipment, exactly, a kind of hydrolysis technology that uses cationic exchange resin as the methyl acetate of catalyst, and the equipment used for this technology. Background technique: [0002] In the production of polyvinyl alcohol (PVA), a large amount of methyl acetate is produced as a by-product. At present, most PVA manufacturers use cationic fixed bed hydrolysis process to decompose methyl acetate into methanol and acetic acid for recycling. The main disadvantage of fixed bed hydrolysis process is acetic acid The hydrolysis rate of methyl ester is low, and a large amount of unhydrolyzed methyl acetate needs to be recycled, resulting in huge equipment and high energy consumption. When the water-to-ester molar ratio of the reactants is 0.95-1.0, the general hydrolysis rate can only reach 23%-25%. At present, there are patents and literat...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C27/02C07C31/04C07C51/09C07C53/08
CPCY02P20/10
Inventor 吴燕翔苏文瑞王良恩唐金海赵之山王碧玉王莹淑赵素英邱挺
Owner FUZHOU UNIV
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