DOE Patents title logo U.S. Department of Energy
Office of Scientific and Technical Information

Title: Catalytic distillation process

Abstract

A method is described for conducting chemical reactions and fractionation of the reaction mixture comprising feeding reactants to a distillation column reactor into a feed zone and concurrently contacting the reactants with a fixed bed catalytic packing to concurrently carry out the reaction and fractionate the reaction mixture. For example, a method for preparing methyl tertiary butyl ether in high purity from a mixed feed stream of isobutene and normal butene comprising feeding the mixed feed stream to a distillation column reactor into a feed zone at the lower end of a distillation reaction zone, and methanol into the upper end of said distillation reaction zone, which is packed with a properly supported cationic ion exchange resin, contacting the C[sub 4] feed and methanol with the catalytic distillation packing to react methanol and isobutene, and concurrently fractionating the ether from the column below the catalytic zone and removing normal butene overhead above the catalytic zone.

Inventors:
Issue Date:
OSTI Identifier:
7261843
Patent Number(s):
4336407
Application Number:
PPN: US 6-234653
Assignee:
Chemical Research Licensing Co., Houston, TX (United States)
DOE Contract Number:  
FC07-80CS40454
Resource Type:
Patent
Resource Relation:
Patent File Date: 17 Feb 1981
Country of Publication:
United States
Language:
English
Subject:
10 SYNTHETIC FUELS; DISTILLATION EQUIPMENT; CATALYSTS; ETHERS; SYNTHESIS; 2-METHYLPROPENE; BUTENES; CHEMICAL REACTIONS; FRACTIONATION; METHANOL; ALCOHOLS; ALKENES; EQUIPMENT; HYDROCARBONS; HYDROXY COMPOUNDS; ORGANIC COMPOUNDS; ORGANIC OXYGEN COMPOUNDS; SEPARATION PROCESSES; 100200* - Synthetic Fuels- Production- (1990-)

Citation Formats

Smith, Jr, L A. Catalytic distillation process. United States: N. p., 1982. Web.
Smith, Jr, L A. Catalytic distillation process. United States.
Smith, Jr, L A. Tue . "Catalytic distillation process". United States.
@article{osti_7261843,
title = {Catalytic distillation process},
author = {Smith, Jr, L A},
abstractNote = {A method is described for conducting chemical reactions and fractionation of the reaction mixture comprising feeding reactants to a distillation column reactor into a feed zone and concurrently contacting the reactants with a fixed bed catalytic packing to concurrently carry out the reaction and fractionate the reaction mixture. For example, a method for preparing methyl tertiary butyl ether in high purity from a mixed feed stream of isobutene and normal butene comprising feeding the mixed feed stream to a distillation column reactor into a feed zone at the lower end of a distillation reaction zone, and methanol into the upper end of said distillation reaction zone, which is packed with a properly supported cationic ion exchange resin, contacting the C[sub 4] feed and methanol with the catalytic distillation packing to react methanol and isobutene, and concurrently fractionating the ether from the column below the catalytic zone and removing normal butene overhead above the catalytic zone.},
doi = {},
journal = {},
number = ,
volume = ,
place = {United States},
year = {1982},
month = {6}
}

Patent:
Search for the full text at the U.S. Patent and Trademark Office Note: You will be redirected to the USPTO site, which may require a pop-up blocker to be deactivated to view the patent. If so, you will need to manually turn off your browser's pop-up blocker, typically found within the browser settings. (See DOE Patents FAQs for more information.)

Save / Share: