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Synthesis method of tert-butyl (meth) acrylate

A technology for the synthesis of tert-butyl acrylate, which is applied in the preparation of carboxylic acid esters, chemical instruments and methods, and the preparation of organic compounds, and can solve the problem of high 78%, selectivity not mentioned, catalyst and by-product water treatment difficulties , did not mention the problem of polymerization inhibitor system, etc., to achieve the effect of improving conversion rate and selectivity, inhibiting side reactions of polymerization, and reducing steam energy consumption

Pending Publication Date: 2022-05-17
华谊合丰特种化学淄博有限公司
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  • Application Information

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Problems solved by technology

[0005] Chinese patent CN101155771A discloses a method for synthesizing tert-butyl (meth)acrylate. Solid acids such as sulfuric acid or solid phosphoric acid are used as catalysts, and tert-butanol is decomposed into isobutylene, which is dissolved in an organic solvent containing acrylic acid and reacted to obtain the product. The disadvantage is that the process is complicated, and the catalyst and by-product water are difficult to treat.
[0006] Chinese patent CN103073426A discloses a method for producing tert-butyl acrylate with an acidic cation exchange resin as a catalyst. A kettle reaction is adopted. In a reaction kettle equipped with acrylic acid, cationic resin and polymerization inhibitor, liquid isobutylene is added dropwise for 1.5 to 4 hours. The reaction is carried out at -20-40°C, and the product is obtained by keeping it warm for 6-8 hours. The disadvantage is that it is a batch reaction process, and the reaction time is long and the efficiency is too low.
The process adds a relatively high content of olefin polymerization inhibitor tert-butanol, which increases the complexity of the recovery process; no polymerization inhibitor system is mentioned, and the process is more cumbersome; the highest conversion rate is 83.76% in terms of isobutylene
[0008] Chinese patent CN 104276948 A discloses a process for preparing tert-butyl (meth)acrylate, which uses a strong acidic ion exchange resin catalyst and is packed in a tubular reactor connected in series with multiple fixed-bed reactors. , 1.0~5.0MPa, volume space velocity 0.5~5.0h-1, acid-ene molar ratio 1.0~5.0:1, isobutene reacts with acrylic acid to form ester, the conversion rate is up to 78% based on isobutene, selectivity not mentioned
There are common problems such as low esterification yield, complicated process, polymerization risk, and high energy consumption.

Method used

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  • Synthesis method of tert-butyl (meth) acrylate
  • Synthesis method of tert-butyl (meth) acrylate
  • Synthesis method of tert-butyl (meth) acrylate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] Use resin catalyst QRE-02 (particle size is 0.3-1.1mm, cross-linking degree is about 10-20%, exchange capacity is greater than 4.0mmolH + / g (干) above. ) is the catalyst 232 of the esterification reaction, selects HQ and MEHQ as polymerization inhibitor, wherein the molar ratio of HQ and MEHQ is 2:1; Adopt fixed bed reactor 1 as the first reactor, adopt as Figure 2-3 The shown reactive distillation tower 2 is used as the second reactor, and the vacuum distillation tower is used as the light removal tower 5 and the weight removal tower 6; the catalyst module 23 of the reactive distillation tower 2 is equipped with a catalyst 232, and the amount of the catalyst 232 is 100ml. The structural parameters of the reactive distillation tower 2 are that the rectification section is 2 to 5 theoretical trays, the reaction section is 6-10 theoretical trays, the stripping section is 11 to 20 theoretical trays, and the catalyst The number of modules 23 is 4 to 10. A liquid distrib...

Embodiment 2

[0047] Use modified resin Amberlyst A35 (particle size is 0.3-1.1mm, cross-linking degree is about 10-20%, exchange capacity is greater than 4.0mmolH + / g (干) above. ) is the catalyst 232 for the esterification reaction, and HQ and 4-hydroxyl-2,2,6,6-tetramethylpiperidine-1-oxyl radical are selected as polymerization inhibitors, wherein HQ and 4-hydroxyl-2,2 , the molar ratio of 6,6-tetramethylpiperidine-1-oxyl radical is 1:1; adopt fixed bed reactor 1 as the first reactor, adopt as Figure 2-3 The shown reactive distillation tower 2 is used as the second reactor, and the vacuum distillation tower is used as the light removal tower 5 and the weight removal tower 6; the catalyst module 23 of the reactive distillation tower 2 is equipped with a catalyst 232, and the amount of the catalyst 232 is 100ml. The structural parameters of the reactive distillation tower 2 are that the rectification section is 2 to 5 theoretical trays, the reaction section is 6-10 theoretical trays, th...

Embodiment 3

[0055] In the first reactor: pressure 0.1~0.5MPa, temperature 10~40℃, liquid space velocity 0.5~5.0h -1 , the acid-ene ratio is 1.0-5.0 mol / mol;

[0056] Inside the reactive distillation tower 2: pressure -0.02~0.1MPa, reaction section temperature 20~45°C, acid-ene ratio 2.0~6.0: 1mol / mol;

[0057] Light removal tower 5: pressure -0.01~-0.09MPa, tower top temperature 45~78℃, reflux ratio 5~20;

[0058] Weight removal tower 6: pressure -0.07~-0.10MPa, tower top temperature 48~73℃, reflux ratio 5~15;

[0059] The parameters involved in the first reactor, reactive distillation tower 2, light removal tower 5 and weight removal tower 6 are arbitrarily selected and combined within the above range; other operations are the same as in embodiment 1 or embodiment 2. The isobutene reacts completely.

[0060] The product extracted from the top of the weight-removing tower 6 is detected by a chromatograph:

[0061] The content of tert-butyl acrylate is 99.3-99.7%, and the selectivity o...

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Abstract

The invention discloses a synthesis method of tert-butyl (meth) acrylate. Belongs to the technical field of fine chemical engineering. The method comprises the following steps: (methyl) acrylic acid and isobutene react in a first reactor in the presence of a polymerization inhibitor and a catalyst, and a mixture from the first reactor enters a stripping section; a mixture of (methyl) acrylic acid and a polymerization inhibitor enters a rectifying section; (methyl) acrylic acid flowing down from the rectifying section reacts with isobutene evaporated from the stripping section in the reaction section, the reacted mixture is discharged from the bottom of the reaction rectifying tower, and unreacted isobutene is discharged from the top of the reaction rectifying tower; and separating the reacted mixture discharged from the bottom of the reactive distillation tower to obtain the tert-butyl (meth) acrylate. The synthesis method provided by the invention has the characteristics of high conversion rate and good selectivity, and can prolong the operation cycle of the esterification catalyst.

Description

technical field [0001] The invention relates to a method for synthesizing tert-butyl (meth)acrylate, which belongs to the technical field of fine chemicals. Background technique [0002] Tert-butyl acrylate (tBA) and tert-butylmethacrylate (tBMA) are important organic acid esters, which are colorless and transparent liquids at room temperature. Since tBA / tBMA has a highly reactive unsaturated double bond and a tert-butyl ester (-COOR) structure that is easily hydrolyzed into a carboxylic acid, it can be self-polymerized or copolymerized with other vinyl monomers to prepare a variety of copolymers and homopolymers. things. Its copolymer has excellent physical and chemical properties such as light resistance, water resistance, and oil resistance. The finished product has the advantages of strong adhesion, good transparency, and clear film formation. be more and more widely used. [0003] The traditional preparation methods of acrylate include: vinyl chloride potassium cyani...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C67/04C07C69/54C07C67/54
CPCC07C67/04C07C67/54C07C69/54
Inventor 彭光辉顾晓烨范风智
Owner 华谊合丰特种化学淄博有限公司
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