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In relation to this article, we declare that there is no conflict of interest.
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Received July 29, 2009
Accepted February 14, 2010
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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A comparative study on the recovery of 1,2-dichloroethane and the removal of benzene contained in the byproducts of VCM process

Department of Materials Science and Engineering, Hongik University, 300, Shian, Yongi, Chungnam 339-701, Korea 1Department of Automotive Engineering, Hoseo University, 268, Anseo, Asan, Chungnam 330-713, Korea 2Department of Chemical Engineering, Kongju National University, 275, Budae-dong, Cheonan, Chungnam 331-240, Korea
jhcho@kongju.ac.kr
Korean Journal of Chemical Engineering, March 2010, 27(3), 970-976(7), 10.1007/s11814-010-0206-7
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Abstract

A comparative study has been performed to compare initial investment costs and operation costs for two different process configurations. The two processes were used to recover 1,2-dichloroethane (EDC) and to remove benzene contained in the byproducts of the vinyl chloride monomer (VCM) process. The objectives of this process were to recover 70% of EDC contained in the byproducts and to reduce the benzene content below 0.7 wt%. The first process configuration for comparison is a conventional distillation column that consists of upper and lower columns. The other process configuration is an extractive distillation process that uses Normal Formyl Morpholine (NFM) as a solvent to remove benzene. The conventional distillation process which consists of upper and lower distillation columns was superior to the extractive distillation process, which used a solvent, in the aspects of the initial investment and annual operating cost.

References

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