西安交通大学能源与动力工程学院,西安,710049
网络首发:2008-01-10,
纸质出版:2008
移动端阅览
翟小伟, 杨伯伦, 邱鹏, 等. 萃取精馏分离甲醇和碳酸二甲酯二元共沸物[J]. 西安交通大学学报, 2008,42(1):91-95.
翟小伟, 杨伯伦, 邱鹏, et al. Separation of Azeotropic DMC-MEOH Mixture by Extractive Distillation[J]. 2008, 42(1): 91-95.
在对三塔萃取精馏分析的基础上
提出了以邻二甲苯为萃取剂
两塔分离甲醇和碳酸二甲酯共沸物的萃取精馏新流程.考察了进料配比、回流比等操作参数对萃取精馏性能的影响
并采用共沸和非共沸两种进料方式
考察了三塔体系和两塔体系在操作条件和分离性能上的差异.利用ASPEN软件对两种流程进行了优化分析和模拟放大研究.实验和模拟结果表明:两种分离流程均可实现甲醇与碳酸二甲酯的有效分离.两塔体系省去了一个塔
降低了设备费用
简化了操作
能量的消耗略有增加.考虑到低品位的能量容易取得以及萃取剂可以回收利用等因素
两塔体系具有较高的工业利用价值.
Analyzing the three-column system of extractive distillation
two-column system adopting o-xylene as an extraction agent for separation of azeotropic methanol-dimethyl carbonate mixture is developed. The influence of the operation parameters
such as the feed conditions
the reflux ratio and the extractant to feed ratio on the extractive distillation efficiency is investigated. The difference of separation capability between three-column system and two-column system is also investigated under the conditions of azeotropic feed and non-azeotropic feed. The simulation and optimization are carried out with ASPEN plus software. The results show that these two routes enable to realize separation of azeotropic DMC-MEOH mixture. Compared with three-column system
the device cost is reduced and the operation gets simplified
while the consumption of extractant and energy is slightly increased in the two-column system. Since the lower grade heat can be obtained easily and the extractant can be recycled
the two-column system shows a wider industrial foreground.
SUN Jianjun, YANG Bolun, LIN Hongye. A semicontinuous process for the synthesis of methyl carbamate from urea and methanol[J]. Chemical Engineering & Technology, 2004, 27(4): 435-439.
WANG Xiaoping, YANG Blun, WANG Dongpeng, et al. Reactive rectifying for producing dimethyl carbonate[J]. Chemical Engineering Journal, 2006,122(12): 15-20.
DIANCE D, KANNE B. Air pollution reduction: US Patent, 5004480 [P]. 1991-04-02.
ONO Y. Dimethy carbonate for environmentally benign reactions [J]. Catalysis Today, 1997, 11(35):15-25.
SHIAO H C, CHUA D, LIN H P, et al. Low temperature electrolytes for Li-ion PVDF cells[J]. Power Sources, 2000, 12(87):167-173.
ISAACS N S, O'SULLIVAN B. High pressure routes to dimethyl carbonate from supercritical carbon dioxide[J]. Tetrahedron, 1999, 40(55):11949-11956.
BUYSCH H J, KRIMM H. Process for the preparation of dimethyl carbonate: US Patent, 4335051[P]. 1982-06-15.
SAKAKURA T, CHOI J, SAITO Y, et al. Synthesis of dimethyl carbonate from carbon dioxide[J]. Catalysis and mechanism, 2000, 5(19):573-576.
ROMANO U, RIVETTI F, MUZIO N D. Process for producing dimethyl carbonate:US Patent, 4318862[P]. 1982-03-09.
RAMZI Y, ROBERT C, ELENA N, et al. Process for manufacturing dialkyl carbonate from urea and alcohol:US Patent, 5565603[P]. 1996-10-15.
RYU Y, ABRAHAM P. Process for making dialkyl carbonates:US Patent, 7074951 [P].2006-07-11.
DOYA M, KIMIZUKA K I, KANBARA Y. Process for the production of dialkyl carbonate:US Patent, 5489702 [P]. 1996-02-06.
熊国玺,李光兴. 碳酸二甲酯-甲醇二元共沸物的分离方法[J]. 化工进展,2002, 5(1):26-28.
XIONG Guoxi, LI Guangxing. Separation of binary methanol-dimethyl carbonate azeotrope[J]. Chemical Industry and Engineering Progress, 2002, 5(1):26-28.
黄凤林, 杨伯伦. 甲醇四塔精馏模拟过程分析[J]. 现代化工, 2006, 26(S2):324-329.
HUANG Fenglin, YANG Bolun. Simulation analysis of four towers flow in methanol distillation process[J]. Modern Chemical Industry, 2006, 26(S2):324-329.
0
浏览量
5
下载量
5
CSCD
关联资源
相关文章
相关作者
相关机构
京公网安备11010802024621