Method for simultaneously synthesizing 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate andhexadecanedioic diester
A technology of dodecyl alcohol ester and carbon diester, which is applied in the field of simultaneous synthesis of dodecyl alcohol ester and hexadecyl diester, can solve the problems such as difficult separation of by-products, lack of much economic benefits, etc., and achieves improved activity and Longevity, improved reactivity, and improved pore volume
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2021-12-03
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Abstract
Description
technical field
[0001] The invention relates to the technical field of fine chemicals, in particular to a method for simultaneously synthesizing dodecyl alcohol ester and hexadecanyl diester. Background technique
[0002] 2,2,4-Trimethyl-1,3-pentanediol monoisobutyrate (dodecyl alcohol ester) and 2,2,4-trimethyl-1,3-pentanediol diisobutyrate Ester (hexadecyl diester) is a commonly used coalescent for water-based coatings. Coalescing aids soften the latex polymer particles, allowing them to coalesce and fuse together to better form films. In addition to reducing the minimum film forming temperature (MFT) of latex paint, film-forming additives can also improve the film properties of latex paint such as weather resistance, scrubability, and color development of the coating.
[0003] At present, the most important method for synthesizing dodecyl alcohol esters is the isobutyraldehyde basic catalytic method, that is, isobutyraldehyde is used as a raw material, carried out under...
Examples
Embodiment 1
[0035] A method for simultaneously synthesizing dodecyl alcohol ester and hexadecyl diester, wherein: comprising the following steps:
[0036] S1. Under the action of an acidic catalyst, 2,2,4-trimethyl-1,3-pentanediol is transesterified with isobutyl isobutyrate to generate dodecyl alcohol ester and hexadecyl diester, The acidic catalyst is p-toluenesulfonic acid, and the acidic catalyst consumption is 0.3% of the total mass of the feed;
[0037]S2. in the transesterification reaction process, the isobutanol generated by the reaction is distilled out, and the impurities are removed by distillation in a rectification tower, and finally the product dodecyl alcohol ester and hexadecyl diester are obtained, and the dodecyl alcohol ester of generation is and hexadecyl diester to remove the acidic catalyst, and separate through ordinary rectification to obtain 2,2,4-trimethyl-1,3-pentanediol diisobutyrate and 2,2,4-trimethyl -1,3-pentanediol monoisobutyrate; the temperature of the...
Embodiment 2
[0039] A method for simultaneously synthesizing dodecyl alcohol ester and hexadecyl diester, wherein: comprising the following steps:
[0040] S1. Under the action of an acidic catalyst, 2,2,4-trimethyl-1,3-pentanediol is transesterified with isobutyl isobutyrate to generate dodecyl alcohol ester and hexadecanyl diester, The temperature of the transesterification reaction is 170°C, and the reaction time is 8h;
[0041] S2. in the transesterification reaction process, the isobutanol generated by the reaction is distilled out, and the impurities are removed by distillation in a rectification tower, and finally the product dodecyl alcohol ester and hexadecyl diester are obtained, and the dodecyl alcohol ester of generation is and hexadecyl diester to remove the acidic catalyst, and separate through ordinary rectification to obtain 2,2,4-trimethyl-1,3-pentanediol diisobutyrate and 2,2,4-trimethyl -1,3-pentanediol monoisobutyrate; the normal distillation temperature is 160°C and t...
Embodiment 3
[0049] A method for simultaneously synthesizing dodecyl alcohol ester and hexadecyl diester, wherein: comprising the following steps:
[0050] S1. Under the action of an acidic catalyst, 2,2,4-trimethyl-1,3-pentanediol is transesterified with isobutyl isobutyrate to generate dodecyl alcohol ester and hexadecanyl diester, The temperature of the transesterification reaction is 190°C, and the reaction time is 3h;
[0051] S2. in the transesterification reaction process, the isobutanol generated by the reaction is distilled out, and the impurities are removed by distillation in a rectification tower, and finally the product dodecyl alcohol ester and hexadecyl diester are obtained, and the dodecyl alcohol ester of generation is and hexadecyl diester without removing the acidic catalyst, directly carry out reactive distillation to obtain dodecyl alcohol ester and hexadecyl diester, the temperature of the reaction rectification is 185° C., and the pressure is -0.099 MPa.
[0052] Th...