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Title: Alkylation of organic aromatic compounds

Abstract

Aromatic compounds are alkylated in a catalytic distillation, wherein the catalyst structure also serves as a distillation component by contacting the aromatic compound with a C[sub 2] to C[sub 10] olefin in the catalyst bed under 0.25 to 50 atmospheres of pressure and at temperatures in the range of 80 C to 500 C, using as the catalyst a mole sieve characterized as acidic or an acidic cation exchange resin. For example, ethyl benzene is produced by feeding ethylene below the catalyst bed while benzene is conveniently added through the reflux in molar excess to that required to react with ethylene, thereby reacting substantially all of the ethylene and recovering benzene as the principal overhead and ethyl benzene in the bottoms. 1 fig.

Inventors:
Issue Date:
OSTI Identifier:
7169859
Patent Number(s):
4849569
Application Number:
PPN: US 7-258892
Assignee:
Chemical Research Licensing Co., Houston, TX (United States)
DOE Contract Number:  
FC07-80CS40454
Resource Type:
Patent
Resource Relation:
Patent File Date: 17 Oct 1988
Country of Publication:
United States
Language:
English
Subject:
10 SYNTHETIC FUELS; 02 PETROLEUM; ALKYLATED AROMATICS; SYNTHESIS; AROMATICS; ALKYLATION; ALKENES; CATALYSTS; CHEMICAL REACTORS; MOLECULAR SIEVES; OPERATION; ADSORBENTS; CHEMICAL REACTIONS; HYDROCARBONS; ORGANIC COMPOUNDS; 100200* - Synthetic Fuels- Production- (1990-); 020500 - Petroleum- Products & By-Products

Citation Formats

Smith, Jr, L A. Alkylation of organic aromatic compounds. United States: N. p., 1989. Web.
Smith, Jr, L A. Alkylation of organic aromatic compounds. United States.
Smith, Jr, L A. Tue . "Alkylation of organic aromatic compounds". United States.
@article{osti_7169859,
title = {Alkylation of organic aromatic compounds},
author = {Smith, Jr, L A},
abstractNote = {Aromatic compounds are alkylated in a catalytic distillation, wherein the catalyst structure also serves as a distillation component by contacting the aromatic compound with a C[sub 2] to C[sub 10] olefin in the catalyst bed under 0.25 to 50 atmospheres of pressure and at temperatures in the range of 80 C to 500 C, using as the catalyst a mole sieve characterized as acidic or an acidic cation exchange resin. For example, ethyl benzene is produced by feeding ethylene below the catalyst bed while benzene is conveniently added through the reflux in molar excess to that required to react with ethylene, thereby reacting substantially all of the ethylene and recovering benzene as the principal overhead and ethyl benzene in the bottoms. 1 fig.},
doi = {},
journal = {},
number = ,
volume = ,
place = {United States},
year = {Tue Jul 18 00:00:00 EDT 1989},
month = {Tue Jul 18 00:00:00 EDT 1989}
}

Patent:
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