详细信息

Continuous Addition Terpolymerization of Maleic Anhydride, Octadecyl Acrylate, and Docosyl Acrylate: Experimenting the Terpolymers as Pour Point Depressants for Waxy Crude Oils  ( SCI-EXPANDED收录 EI收录)  

文献类型:期刊文献

英文题名:Continuous Addition Terpolymerization of Maleic Anhydride, Octadecyl Acrylate, and Docosyl Acrylate: Experimenting the Terpolymers as Pour Point Depressants for Waxy Crude Oils

作者:Hu, Jiawen[2];Pu, Xin[2];Fang, Saifei[2];Qian, Jiayu[2];Zhao, Kexin[2];Han, Xin[2];Ye, Lei[2];Liu, Pengpeng[1];Liu, Zhenxue[1];Liu, Jichang[2,3]

机构:[1]Shandong Chambroad Holding Grp Co Ltd, Binzhou 256500, Shandong, Peoples R China;[2]East China Univ Sci & Technol, Sch Chem Engn, State Key Lab Chem Engn, Shanghai 200237, Peoples R China;[3]Shihezi Univ, Sch Chem & Chem Engn, State Key Lab Incubat Base Green Proc Chem Engn, Shihezi 832003, Peoples R China

年份:2023

卷号:62

期号:19

起止页码:7352

外文期刊名:INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH

收录:;EI(收录号:20232114114082);WOS:【SCI-EXPANDED(收录号:WOS:000985837500001)】;

基金:This work was supported financially by the National Natural Science Foundation of China (NO. 22008070, U22B20141) .

语种:英文

外文关键词:Chemical industry - Heat transfer - Maleic anhydride - Mass transfer - Molecular weight distribution - Polydispersity - Polymerization - Terpolymers

摘要:Owing to their large specific surface areas and excellent heat and mass transfer compared with those of conventional batch reactors, microreactors have been widely used in chemical industries. In this study, a strategy is proposed for precisely controlling the synthesis of comb-type terpolymers in a microreactor. Poly(octadecyl acrylate- docosyl acrylate-maleic anhydride) was investigated as a pour point depressant (PPD) for waxy crude oils. A terpolymer showing a high weight-average molecular weight (Mw) and low polydispersity index (PDI) was synthesized within 5 min compared with a conventional time-consuming batch reaction. Under the optimal conditions, the Mw of the terpolymer reached 3.7 x 104, and the PDI was 1.42. Notably, the pour point of the crude oil was reduced by 8 K at a PPD dosage of 1300 ppm. The polymerization kinetics revealed that the microreactor accelerated the polymerization. In contrast to the batch reactor, the microreactor exhibited better heat transfer, which avoided the generation of hot spots. Furthermore, the calculated Bodenstein number (Bo) revealed that the degrees of plug-flow deviation and backmixing are negatively correlated with the molecular weight distribution.

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