Kinetics Study of the Peroxidation of tert-Butyl Alcohol to tert-Butyl Hydrogen Peroxide in a Microreactor

被引:6
作者
Zhu, Hongwei [1 ,2 ]
Yan, Junjie [3 ]
Zhang, Zhichen [2 ]
Ren, Junpeng [1 ]
Zhu, Yunfeng [2 ]
Zhao, Hui [3 ]
Xu, Wei [1 ,2 ]
Sun, Bing [1 ,2 ]
Yang, Chaohe [3 ]
机构
[1] State Key Lab Chem Safety, Qingdao 266071, Peoples R China
[2] SINOPEC Res Inst Safety Engn, Qingdao 266071, Peoples R China
[3] China Univ Petr East China, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R China
基金
中国国家自然科学基金;
关键词
microchannel reactor; tert-butyl alcohol; tert-butylhydrogen peroxide; hydrogenperoxide; kinetic model; di-tert-butyl peroxide; THERMAL-DECOMPOSITION; FLOW CHEMISTRY; TECHNOLOGY; GREEN;
D O I
10.1021/acs.oprd.3c00079
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
tert-Butyl hydroperoxide (TBHP), an organic peroxide, is mainly used as a polymer initiator and is typically synthesized by the thermal reaction of tert-butyl alcohol (TBA) with hydrogen peroxide (H2O2). In this study, we adopted sulfuric acid (H2SO4) as the homogeneous catalyst to promote the peroxidation reaction of TBA in a microchannel reactor. The reaction conditions for the synthesis of TBHP were optimized, and the kinetic model of the synthesis was subsequently established. The results show that byproducts exist during the reaction as well, such as di-tert-butyl peroxide (DTBP). The reaction temperature was 50 degrees C, the optimum molar ratio of TBA to H2O2 was determined to be 1:1, and the optimum molar ratio of H2SO4 to TBA was determined to be 0.95. Kinetics studies showed that the pre-exponential factors for producing TBHP and DTBP were 1 x 10(19) and 3.12 x 10(25), respectively, while the activation energies of the corresponding reactions were 131.72 and 179.33 kJ/mol, respectively. The calculation results of the kinetic model fit well with the concentration of the products measured during the microreactor experiments.
引用
收藏
页码:1486 / 1493
页数:8
相关论文
共 28 条
[1]  
Boodhoo K., 2013, PROCESS INTENSIFICAT, P11
[2]   Development of a microreactor for chemical production [J].
Burns, JR ;
Ramshaw, C .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 1999, 77 (A3) :206-211
[3]   Chemical kinetics on thermal decompositions of di-tert-butyl peroxide studied by calorimetry [J].
Duh, Yih-Shing ;
Kao, Chen-San ;
Lee, Wen-Lian William .
JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2017, 127 (01) :1071-1087
[4]   Safety analysis of intensified processes [J].
Ebrahimi, F. ;
Virkki-Hatakka, T. ;
Turunen, I. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2012, 52 :28-33
[5]   Safety Advantages of On-Site Microprocesses [J].
Ebrahimi, Fatemeh ;
Kolehmainen, Eero ;
Turunen, Ilkka .
ORGANIC PROCESS RESEARCH & DEVELOPMENT, 2009, 13 (05) :965-969
[6]   Contribution of microreactor technology and flow chemistry to the development of green and sustainable synthesis [J].
Fanelli, Flavio ;
Parisi, Giovanna ;
Degennaro, Leonardo ;
Luisi, Renzo .
BEILSTEIN JOURNAL OF ORGANIC CHEMISTRY, 2017, 13 :520-542
[7]  
Fuaraji M. K., 1996, ZEOLITES, V17, P320, DOI [10.1016/0144-2449(96)80726-3, DOI 10.1016/0144-2449(96)80726-3]
[8]   Liquid phase oxidation chemistry in continuous-flow microreactors [J].
Gemoets, Hannes P. L. ;
Su, Yuanhai ;
Shang, Minjing ;
Hessel, Volker ;
Luque, Rafael ;
Noel, Timothy .
CHEMICAL SOCIETY REVIEWS, 2016, 45 (01) :83-117
[9]   Microchemical systems for continuous-flow synthesis [J].
Hartman, Ryan L. ;
Jensen, Klavs F. .
LAB ON A CHIP, 2009, 9 (17) :2495-2507
[10]   HOMOLYTIC DECOMPOSITIONS OF HYDROPEROXIDES .4. METAL-CATALYZED DECOMPOSITIONS [J].
HIATT, R ;
IRWIN, KC ;
GOULD, CW .
JOURNAL OF ORGANIC CHEMISTRY, 1968, 33 (04) :1430-&