Continuous Synthesis of 1,3,2-Dioxathiolane 2,2-Dioxide (DTD) by Hydrogen Peroxide with Titanium Silicalite-1 Catalyst Using a Fixed-Bed Reactor

被引:0
|
作者
Liu, Zunchao [1 ]
Wang, Tianlai [1 ]
Li, Jianing [1 ]
Tian, Xiangmin [1 ]
Ma, Cunfei [1 ]
Zhao, Jingnan [1 ]
Meng, Qingwei [1 ,2 ]
机构
[1] Dalian Univ Technol, Frontiers Sci Ctr Smart Mat Oriented Chem Engn, Sch Chem Engn, State Key Lab Fine Chem, Dalian 116024, Peoples R China
[2] Dalian Univ Technol, Ningbo Inst, Ningbo 315000, Peoples R China
基金
中国国家自然科学基金;
关键词
1,3,2-dioxathiolane 2; 2-dioxide (DTD); continuousprocess; titanium silicalite-1; oxidation; fixed-bed reactor; CYCLIC SULFATES; EFFICIENT EPOXIDATION; CHEMISTRY; ESTERS; GREEN; ACID;
D O I
10.1021/acs.oprd.4c00482
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
1,3,2-Dioxathiolane 2,2-dioxide (DTD) plays a significant role as an electrolyte additive in lithium-ion batteries. It can enhance battery performance, stability, and safety. Additionally, it is a commonly used hydroxylation reagent in organic chemistry. This paper presents a highly efficient, safe preparation, and environmentally friendly continuous DTD synthesis process that does not require catalyst separation. A fixed-bed reactor was constructed with spherical TS-1 as the catalyst and H2O2 as the oxidizer. Under optimized reaction conditions, efficient oxidation of ethylene sulfite (ES) was achieved using dimethyl carbonate as a solvent. The process involved controlling the reaction temperatures at gradients of 10 and 5 degrees C, respectively, maintaining a molar ratio of H2O2 to substrate of 1.05:1, a liquid hourly space velocity of 0.6 h-1, and using a 30 wt % concentration of H2O2 at a substrate concentration of 1 mol/L. The conversion rate was up to 99.5%, and the selectivity of DTD was 99.1%. To prevent hydrolysis of DTD, a continuous separation operation was initiated immediately after the completion of the reaction, and the yield of DTD reached 96%. The successful application of this process not only improves the production efficiency of DTD and reduces the production cost but also establishes the foundation for the industrialized continuous production of DTD.
引用
收藏
页码:490 / 496
页数:7
相关论文
共 26 条
  • [21] Continuous-flow synthesis of N,N′-bis(2,2,6,6-tetramethyl-4-piperidinyl)-1,6-hexanediamine (DTMPA) in a Micro fixed-bed reactor
    Gao, Liang
    Lai, Liangchuan
    Ye, Baijun
    Liu, Minjie
    Cheng, Dang
    Jiang, Meifen
    Chen, Fener
    JOURNAL OF FLOW CHEMISTRY, 2022, 12 (04) : 419 - 427
  • [22] Continuous-flow synthesis of N,N′-bis(2,2,6,6-tetramethyl-4-piperidinyl)-1,6-hexanediamine (DTMPA) in a Micro fixed-bed reactor
    Liang Gao
    Liangchuan Lai
    Baijun Ye
    Minjie Liu
    Dang Cheng
    Meifen Jiang
    Fener Chen
    Journal of Flow Chemistry, 2022, 12 : 419 - 427
  • [23] Solid-Phase Synthesis of 1,3,6-Trisubstituted-1H-thiazolo[4,5-c][1,2]thiazin-4(3H)one-2,2-dioxide Derivatives using Traceless Linker
    Lee, Taeho
    Park, Ji-Hoon
    Jeon, Moon-Kook
    Gong, Young-Dae
    JOURNAL OF COMBINATORIAL CHEMISTRY, 2009, 11 (02): : 288 - 293
  • [24] A green one-pot process for the synthesis of 1,2,4-triazole-fused heterocycles using FeBr3 catalyst and hydrogen peroxide
    Pan, Yuliang
    Tian, Ruotong
    Chen, Yini
    Wang, Linyang
    Qin, Huilin
    Wang, Jian
    TETRAHEDRON, 2023, 148
  • [25] Metal-free and green synthesis of a series of new bis(2-alkylsulfanyl-[1,3,4] thiadiazolyl)-5,5′-disulfides and 2,2′-Dibenzothiazyl disulfide via oxidative self-coupling using hydrogen peroxide
    Ong, Chiu Ling
    Heidelberg, Thorsten
    Juan, Joon Ching
    Khaligh, Nader Ghaffari
    POLYHEDRON, 2022, 213
  • [26] Solid Catalyst Alkylation of C2-C3 Olefins with Isobutane in the Presence of Hydrogen Using a Slurry Transport Reactor-Hydrocyclone-Regenerator System and PtSO4TiZr/SiO2 Catalyst: Part 1. Alkylation in Continuous Pilot Plant Operation and Simulation of a Slurry Transport Reactor-Hydrocyclone Settler System
    Galiasso Tailleur, Roberto
    Rodriguez, Sergio
    Farina, Carlos
    Derjani-Bayeh, Sylvana
    ENERGY & FUELS, 2018, 32 (02) : 2527 - 2548