Articles & Issues
- Language
- English
- Conflict of Interest
- In relation to this article, we declare that there is no conflict of interest.
- Publication history
-
Received July 29, 2009
Accepted February 14, 2010
- 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.
Copyright © KIChE. All rights reserved.
All issues
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
Download PDF
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.
Keywords
References
1,2-Dichloroethane, Geneva: World Health Organization, Environ. Health Criter., 176 (1995)
Bruzzi V, Colaianni M, Zanderighi L, Energy Conv. Manag., 39(16-18), 1853 (1998)
Holland CD, Fundamentals of multicomponent distillation, 1st Ed., McGraw-Hill (1981)
Cho JH, Park JK, Lee TJ, The Sixth International Symposium on Separation Technology, 203 (2002)
Ko MS, Na S, Cho J, Kim H, Korean J. Chem. Eng., 19(6), 996 (2002)
Renon H, Prausnitz JM, AIChE J., 14, 135 (1968)
Nelder JA, Mead RA, Comput. J., 7, 303 (1965)
PRO/II Input Manual, Simulation Science Inc., South Lake Forest (2005)
Bruzzi V, Colaianni M, Zanderighi L, Energy Conv. Manag., 39(16-18), 1853 (1998)
Holland CD, Fundamentals of multicomponent distillation, 1st Ed., McGraw-Hill (1981)
Cho JH, Park JK, Lee TJ, The Sixth International Symposium on Separation Technology, 203 (2002)
Ko MS, Na S, Cho J, Kim H, Korean J. Chem. Eng., 19(6), 996 (2002)
Renon H, Prausnitz JM, AIChE J., 14, 135 (1968)
Nelder JA, Mead RA, Comput. J., 7, 303 (1965)
PRO/II Input Manual, Simulation Science Inc., South Lake Forest (2005)