Catalyst for producing propylene, ethane through catalytic cracking olefin

A catalytic cracking and catalyst technology, applied in the field of ethylene catalyst and olefin catalytic cracking to produce propylene, can solve the problems of easy coking and deactivation of the catalyst, poor hydrothermal stability of the catalyst at high temperature, etc., to reduce the hydrogen transfer reaction, improve the conversion rate of raw materials, The effect of increasing the reaction temperature
CN1915515AActive Publication Date: 2007-02-21CHINA PETROLEUM & CHEM CORP +1

Patent Information

Authority / Receiving Office
CN · China
Current Assignee / Owner
CHINA PETROLEUM & CHEM CORP
Publication Date
2007-02-21
Patent Text Reader

Abstract

A catalyst for preparing propene or ethene from olefin by catalytic cracking with high high-temp hydrothermal stability and no coking is proportionally prepared from the ZSM-5 molecular sieve whose mole ratio of SiO2 to Al2O3 is 20-800, RE oxide, and phosphorus oxide as modifier.
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Description

technical field

[0001] The invention relates to a catalyst for producing propylene and ethylene by catalytic cracking of olefins, in particular to a catalyst for producing propylene and ethylene by catalytic cracking of olefins with carbon four or more. Background technique

[0002] The demand for basic chemical raw materials such as propylene and ethylene continues to grow, while crude oil raw materials are deteriorating day by day, which has brought about increasingly prominent contradictions in the production of propylene and ethylene. On the other hand, mixed carbon four and above olefins and alkanes are by-products of ethylene plants, refinery FCC units, methanol to olefins, and gasoline units, and usually can only be used as low value-added products such as liquefied gas fuels. It is of great significance to use these olefins and alkanes raw materials for further deep processing to produce high value-added products propylene and ethylene,...

Claims

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