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Method for increasing yield of propylene and ethylene

A technology of ethylene and propylene, which is applied in chemical instruments and methods, bulk chemical production, molecular sieve catalysts, etc. It can solve the problems of low economic value and achieve the effect of increasing economic benefits and increasing production

Active Publication Date: 2013-02-27
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For this part of carbon tetraolefin and alkane mixture, it is often used as urban civil fuel liquefied petroleum gas, and its economic value is relatively low

Method used

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  • Method for increasing yield of propylene and ethylene

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] On the basis of Comparative Example 1, add a catalytic cracking system that uses carbon tetraolefins and alkane mixtures in the steam cracking process as raw materials. The catalytic cracking system is mainly composed of olefin catalytic cracking reactors, mixed olefins and alkane catalytic cracking reactors ,details as follows:

[0041] (1) At first the butane and butene mixture in Comparative Example 1 are passed in the catalytic cracking reactor 1 (olefin catalytic cracking reactor), the carbon tetraolefins in the raw material contact with the olefin catalyst and react at a reaction temperature of 550° C. Pressure (gauge pressure) 0.15Mpa, space velocity is 3 hours -1 The catalytic cracking reaction is carried out under the conditions, and the catalyst catalytically cracks 70% carbon tetraolefins in the feed into stream 1 rich in propylene and ethylene, wherein the content of propylene in stream 1 is 30.72%, and the content of ethylene is 9.6%. The olefin catalytic ...

Embodiment 2

[0060] On the basis of comparative example 1, increase a catalytic cracking system with catalytic cracking gasoline as raw material (raw material composition is shown in Table 2), the processing capacity of the cracked gasoline of this catalytic cracking system is 50,000 tons / year, this catalytic cracking system consists of Two catalytic cracking reactors constitute, specifically as follows:

[0061] Table 2. Composition of FCC gasoline

[0062]

[0063] (1) First pass the catalytic cracking gasoline into the catalytic cracking reactor 1, the olefins of the catalytic cracking gasoline are contacted with a specific catalyst 1, and the olefin catalytic cracking catalyst is a small grain modified with phosphorus and / or alkaline earth metal (particle diameter is less than 800 nanometers) ZSM-5 molecular sieve type catalyst, the composition of catalyst is: 5wt%P, 1wt%La, 64wt%ZSM-5 molecular sieve (silicon-aluminum ratio is 100, and particle diameter is 500 nanometers), 30wt% ox...

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Abstract

The invention relates to a method for increasing yield of propylene and ethylene in the steam cracking process. The steam cracking process is performed through a cracking furnace and a separation system; and on the basis, a catalytic cracking system which takes C4 fraction produced in an oil refining process, C4 fraction produced in the steam cracking process and / or catalytic cracking gasoline produced in the oil refining process as a raw material is increased; the mixture of C4 olefine and alkane and / or the catalytic cracking gasoline are / is completely or partially converted into the cracked gas containing rich propylene and ethylene through the catalytic cracking system; and the separation and purification of an objective product are mainly finished by the separation system in the steam cracking process. The method is characterized by making the most of the potential of the separation (recovery) system in the steam cracking; only the catalytic cracking system consisting of a catalytic cracking reactor and a simple separation device is increased; and the method increases the yield of low carbon olefins such as propylene, ethylene and the like and contributes to improving the economic benefit of enterprises.

Description

technical field [0001] The invention relates to a method for increasing the production of propylene and ethylene, more specifically, the invention relates to a method for increasing the output of propylene and ethylene by utilizing the existing steam cracking ethylene production device and separation device. Background technique [0002] At present, the main production method of low-carbon olefins such as ethylene and propylene in the world is steam cracking / thermal cracking. The steam cracking process consists of two parts: a cracking furnace and a separation (recovery) system. In the steam cracking process, the mixture of cracking raw materials and steam is heated to a high temperature in the cracking furnace for thermal cracking reaction to generate cracked gas rich in ethylene and propylene, and then the cracked gas is sent to the separation (recovery) system for Separation and purification to obtain cracking products such as ethylene and propylene. [0003] In recent y...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C11/06C07C11/04C07C4/06B01J29/85B01J29/40B01J29/18B01J29/70
CPCY02P20/52
Inventor 王国清白杰杜志国张利军张兆斌陈硕
Owner CHINA PETROLEUM & CHEM CORP