Study on a New Reactive Dividing-Wall Column for the Reaction of Vinyl Carbonate and Methanol Ester Exchange to Produce Dimethyl Carbonate

被引:2
作者
Ben, Guoxun [1 ]
Guo, Dong [1 ]
Tang, Zhigang [1 ]
Zhou, Mengyue [1 ]
Liu, Yubing [1 ]
Wu, Tianzhong [2 ]
Zhang, Shouming [2 ]
Zhao, Gang [2 ]
Guo, Zhengang [2 ]
Li, Hongwei [4 ]
Guo, Dongfang [3 ]
Wang, Huanjun [3 ]
Liu, Lianbo [3 ]
机构
[1] Tsinghua Univ, Dept Chem Engn, State Key Lab Chem Engn, Beijing 100084, Peoples R China
[2] Zhejiang Petrochem Co LTD, Zhoushan 316000, Peoples R China
[3] Huaneng Clean Energy Res Inst, Natl Key Lab High Efficiency Flexible Coal Power G, Beijing 102209, Peoples R China
[4] Res Inst Petr Proc, Beijing 100083, Peoples R China
关键词
ETHYLENE CARBONATE; CATALYST; TRANSESTERIFICATION; DISTILLATION; PERFORMANCE; SEPARATION;
D O I
10.1021/acs.iecr.3c03727
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Dimethyl carbonate (DMC) is a promising green chemical that plays a significant role in the sustainable chemical industry, clean energy technologies, and environmental protection. In response to the challenges of high equipment investment and energy consumption in the existing process for producing dimethyl carbonate through an ester exchange reaction using vinyl carbonate and methanol, a new reactive dividing-wall column (RDWC) process was developed. A new RDWC model was established by using Aspen Plus. The impact factors of reaction conditions such as reactant molar ratio, theoretical number of reaction stages, reaction pressure, and separation conditions such as theoretical number of common rectifying section, theoretical number of common stripping section, liquid phase distribution on both sides of the dividing wall, and side draw location were analyzed. A laboratory-scale new RDWC was designed and built referenced to the simulation results. The experimental research investigated key parameters affecting the reaction distillation column, such as the reaction zone height, reactant molar ratio, liquid phase distribution, reflux ratio, and vapor phase distribution on both sides of the dividing wall. This research laid the foundation for the scale-up designing of process parameters for the new RDWC. Under optimized conditions, the conversion rate of reactant EC (ethylene carbonate) exceeded 99.9%, the purity of methanol in the side draw was at least 99 wt %, and the purity of methanol ethylene glycol in the distillation column achieved a concentration greater than 99% (excluding the catalyst). The new method can greatly shorten the transesterification process (integrate the three towers in the original process into one) to produce dimethyl carbonate, save investment, and reduce energy consumption.
引用
收藏
页码:13637 / 13649
页数:13
相关论文
共 38 条
[1]   Direct synthesis of dimethyl carbonate with supercritical carbon dioxide: Characterization of a key organotin oxide intermediate [J].
Ballivet-Tkatchenko, Danielle ;
Chambrey, Stephane ;
Keiski, Riitta ;
Ligabue, Rosane ;
Plasseraud, Laurent ;
Richard, Philippe ;
Turunen, Helka .
CATALYSIS TODAY, 2006, 115 (1-4) :80-87
[2]   Concurrent synthesis of dimethyl carbonate and ethylene glycol via transesterification of ethylene carbonate and methanol using smectite catalysts containing Mg and/or Ni [J].
Bhanage, BM ;
Fujita, S ;
He, YF ;
Ikushima, Y ;
Shirai, M ;
Torii, K ;
Arai, M .
CATALYSIS LETTERS, 2002, 83 (3-4) :137-141
[3]   Coating with mesoporous silica remarkably enhances the stability of the highly active yet fragile flower-like MgO catalyst for dimethyl carbonate synthesis [J].
Cui, Zhi-Min ;
Chen, Zhe ;
Cao, Chang-Yan ;
Song, Wei-Guo ;
Jiang, Lei .
CHEMICAL COMMUNICATIONS, 2013, 49 (54) :6093-6095
[4]   From simulation studies to experimental tests in a reactive dividing wall distillation column [J].
Delgado-Delgado, Raul ;
Hernandez, Salvador ;
Omar Barroso-Munoz, Fabricio ;
Gabriel Segovia-Hernandez, Juan ;
Jaime Castro-Montoya, Agustin .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2012, 90 (07) :855-862
[5]   Developments in the production and application of dimethylcarbonate [J].
Delledonne, D ;
Rivetti, F ;
Romano, U .
APPLIED CATALYSIS A-GENERAL, 2001, 221 (1-2) :241-251
[6]   Studies in transesterification of ethylene carbonate to dimethyl carbonate over Amberlyst A-21 catalyst [J].
Dhuri, SM ;
Mahajani, VV .
JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2006, 81 (01) :62-69
[7]   Production of Methyl Oleate in Reactive-Separation Systems [J].
Dolores Lopez-Ramirez, Maria ;
Miguel Garcia-Ventura, Ulises ;
Omar Barroso-Munoz, Fabricio ;
Gabriel Segovia-Hernandez, Juan ;
Hernandez, Salvador .
CHEMICAL ENGINEERING & TECHNOLOGY, 2016, 39 (02) :271-275
[8]   Experimental operation of a reactive dividing wall column and comparison with simulation results [J].
Ehlers, Christoph ;
Egger, Torben ;
Fieg, Georg .
AICHE JOURNAL, 2017, 63 (03) :1036-1050
[9]   A reactive distiflation process for an azeotrople reaction system: Transesteirification of ethylene carbonate with methanol [J].
Fang, Yun-Jin ;
Liu, Dao-Jun .
CHEMICAL ENGINEERING COMMUNICATIONS, 2007, 194 (10-12) :1608-1622
[10]   Kinetics of dimethyl carbonate synthesis from ethylene carbonate and methanol using alkalimetal compounds as catalysts [J].
Han, MS ;
Lee, BG ;
Ahn, BS ;
Park, KY ;
Hong, SI .
REACTION KINETICS AND CATALYSIS LETTERS, 2001, 73 (01) :33-38