Mixed butene oligomerizing process at supercritical state

The present invention uses solid acid as catalyst, under the conditions of reaction temp. of 160-240 deg.C and pressure of 3.0-6.0 MPa makes mixed butene implement oligomerization reaction, controls reaction pressure and critical pressure, and makes their ratio values be greater than or equal to 1,...

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Bibliographic Details
Main Authors YAPING YAO, GUOQIN LIAO, LING WANG
Format Patent
LanguageEnglish
Published 05.12.2001
Edition7
Subjects
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Summary:The present invention uses solid acid as catalyst, under the conditions of reaction temp. of 160-240 deg.C and pressure of 3.0-6.0 MPa makes mixed butene implement oligomerization reaction, controls reaction pressure and critical pressure, and makes their ratio values be greater than or equal to 1, and makes reaction mixture implement oligomerization reaction in supercritical and near-critical state from inlet or reactor along catalyst bed layer in turn, under the condition of retaining high conversion rate and high selectivity, the said invented method features long service life of catalyst,and can be extensively used in industrial production.
Bibliography:Application Number: CN2000115799