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Olefin disproportionation catalyst and method of use thereof

An olefin disproportionation and catalyst technology, applied in the direction of carbon compound catalysts, catalysts, physical/chemical process catalysts, etc., can solve the problems of single product structure, inflexible disproportionation technology, failure to produce ethylene, etc., to prolong stability and slow down coking. process, the effect of inhibiting cracking polymerization

Active Publication Date: 2021-03-30
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0011] One of the technical problems to be solved by the present invention is to provide a new disproportionation reaction process for the problems that the disproportionation technology in the prior art is not flexible enough, the product structure is single, ethylene cannot be produced, and the selectivity of the target product is low; the method When used in the reaction of propylene disproportionation to ethylene and butene, it has the advantages of rich product structure, high ethylene content of the product, and high selectivity of the target product.

Method used

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  • Olefin disproportionation catalyst and method of use thereof
  • Olefin disproportionation catalyst and method of use thereof
  • Olefin disproportionation catalyst and method of use thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] Weigh 50 grams of commercial MgO, add 500 grams of deionized water, heat and stir in a water bath at 90°C for 2 hours, filter the water in the solution with suction, dry the product at 80°C for 15 hours, and roast at 450°C for 8 hours to obtain the finished catalyst II.

[0046] will load tungsten oxide 10% SiO 2 Calcined at 450°C for 8 hours, mixed with Catalyst II at a ratio of 1:6 (mass ratio), installed in a Φ25mm fixed-bed reactor, using propylene as raw material, at a weight space velocity of 10 hours -1 , the reaction temperature was 300°C, and the reaction pressure was 3MPa to evaluate the performance of the catalyst. The results are shown in Table 1.

Embodiment 2

[0048] Weigh 50 grams of commercial MgO, add 500 grams of deionized water, heat and stir in a water bath at 90°C for 2 hours, filter the water in the solution with suction, dry the product at 80°C for 15 hours, and roast at 450°C for 8 hours to obtain the finished catalyst II.

[0049] will load tungsten oxide 15% SiO 2 Calcined at 450°C for 8 hours, mixed with Catalyst II at a ratio of 1:6 (mass ratio), installed in a Φ25mm fixed-bed reactor, using propylene as raw material, at a weight space velocity of 10 hours -1 , the reaction temperature was 300°C, and the reaction pressure was 3MPa to evaluate the performance of the catalyst. The results are shown in Table 1.

Embodiment 3

[0051] Weigh 50 grams of commercial MgO, add 500 grams of deionized water, heat and stir in a water bath at 90°C for 2 hours, filter the water in the solution with suction, dry the product at 80°C for 15 hours, and roast at 450°C for 8 hours to obtain the finished catalyst II.

[0052] The loaded tungsten oxide 5% SiO 2 Calcined at 450°C for 8 hours, mixed with Catalyst II at a ratio of 1:6 (mass ratio), installed in a Φ25mm fixed-bed reactor, using propylene as raw material, at a weight space velocity of 10 hours -1 , the reaction temperature was 300°C, and the reaction pressure was 3MPa to evaluate the performance of the catalyst. The results are shown in Table 1.

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Abstract

The invention relates to an olefin disproportionation catalyst and its use method. It mainly solves the problem that the previous technology is relatively single and only focuses on the disproportionation of ethylene and butene to prepare propylene, which cannot be flexibly adjusted with the fluctuation of product prices in the market, and the catalyst is easy to lose during the propylene disproportionation reaction. living problem. The invention adopts an olefin disproportionation catalyst, which includes catalyst I and catalyst II in parts by weight; catalyst I is a tungsten-based or molybdenum-based or rhenium-based catalyst, and catalyst II is an alkali metal and / or alkaline earth metal oxide; its characteristics The technical solution in which the weight ratio of catalyst I to catalyst II is (1:20) to (10:1) better solves this problem. This method can flexibly modulate the product structure according to the fluctuation of product prices in the market. During the modulation process, the device, catalyst and process flow remain unchanged, and the cost is economical. It can be used for the industrial production of ethylene by olefin disproportionation.

Description

technical field [0001] The invention relates to an olefin disproportionation catalyst and a method for using the same; in particular, it relates to a catalyst for preparing ethylene by disproportionation of propylene and a method thereof. Background technique [0002] Olefin disproportionation is a process in which the C=C double bond in the olefin is broken and re-formed under the action of a transition metal compound catalyst to obtain a new olefin product. [0003] Olefin disproportionation technology is one of the effective technical means to adjust product structure. Using propylene as a raw material, the production of ethylene and butene by disproportionation of propylene can expand the selection of lower olefins production, and is an effective process to provide olefins with higher utilization value. Conversely, propylene can also be produced from ethylene and butene. [0004] At present, there are many patents on the production of propylene with ethylene and butene...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/30B01J23/31B01J23/36B01J23/888B01J29/03C07C6/04C07C11/04
CPCC07C6/04B01J23/002B01J23/30B01J23/31B01J23/36B01J23/888B01J29/0341C07C2529/03C07C2523/888C07C2521/10C07C2521/08C07C2523/36C07C2523/30C07C2523/31B01J23/04B01J23/02B01J2229/20B01J2523/00B01J35/19B01J2523/22B01J2523/41B01J2523/69B01J2523/32B01J2523/54B01J2523/43B01J2523/72B01J2523/74B01J2523/68B01J2523/31B01J2523/13B01J2523/14B01J2523/11B01J2523/17B01J2523/28B01J2523/27C07C11/04Y02P20/52
Inventor 董静宋庆英刘苏王仰东宣东
Owner CHINA PETROLEUM & CHEM CORP