Research Article
Glycerin as a Renewable Feedstock for Epichlorohydrin Production. The GTE Process
Article first published online: 5 AUG 2008
DOI: 10.1002/clen.200800067
Copyright © 2008 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim
Issue
1863-0669/asset/cover.gif?v=1&s=48bc1c9783c553a33358fbf925ebc83203745831)
CLEAN – Soil, Air, Water
Special Issue: Feedstocks for the Future: Renewables in Green Chemistry
Volume 36, Issue 8, pages 657–661, August 2008
Additional Information
How to Cite
Bell, B. M., Briggs, J. R., Campbell, R. M., Chambers, S. M., Gaarenstroom, P. D., Hippler, J. G., Hook, B. D., Kearns, K., Kenney, J. M., Kruper, W. J., Schreck, D. J., Theriault, C. N. and Wolfe, C. P. (2008), Glycerin as a Renewable Feedstock for Epichlorohydrin Production. The GTE Process. Clean Soil Air Water, 36: 657–661. doi: 10.1002/clen.200800067
Publication History
- Issue published online: 5 AUG 2008
- Article first published online: 5 AUG 2008
- Manuscript Revised: 9 APR 2008
- Manuscript Received: 12 MAR 2008
- Abstract
- References
- Cited By
Keywords:
- Glycerin;
- Renewable;
- Feedstock;
- Green Chmistry;
- Epichlorohydrin Production
Abstract
A significant improvement in a process to produce epichlorohydrin through the use of glycerin as renewable feedstock is presented. The glycerin to epichlorohydrin (GTE) process proceeds in two chemical steps. In the first step, glycerin is hydrochlorinated with hydrogen chloride gas at elevated temperature and pressure to a mixture of 1,3-DCH (1,3-dichlorohydrin, 1,3-dichloropropan-2-ol) and 2,3-DCH (2,3-dichlorohydrin, 2,3-dichloropropan-1-ol), using a carboxylic acid catalyst. In the second step, the mixture of dichlorohydrins is converted to epichlorohydrin with a base. This solventless process represents an economically and environmentally advantageous, atom-efficient process to an existing commodity chemical that can employ a renewable resource for its primary feedstock.

1863-0669/asset/olbannerright.jpg?v=1&s=0865801c8a6f80aa02594522e888cfa6de5a816a)