Acetylene hydrogenation slurry bed reaction as well as catalyst separation device and method

A technology of acetylene hydrogenation and separation device, which is applied in the field of acetylene hydrogenation to ethylene, which can solve the problems of unfavorable development, decreased catalyst activity, low filtration accuracy, etc., to improve the uniformity of radial distribution, promote the smooth progress of the reaction, and uniform materials stable effect

Pending Publication Date: 2018-03-09
河北美邦工程科技股份有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0002] Ethylene is an important chemical raw material, mainly used in the field of PVC production. China is a big consumer of ethylene, and the annual ethylene consumption is increasing year by year. However, 70% of the world's ethylene is currently produced using crude oil as raw material. The development of this "oil-poor and coal-rich" region in China is extremely unfavorable; the production of acetylene from coal and hydrogenation of acetylene to ethylene are not only in line with China's basic national conditions, but also can solve the problem of excess acetylene in some areas. Good economic development model, but the acetylene hydrogenation process has the characteristics of large heat release and difficult control of the reaction. The traditional fixed bed hydrogenation reactor is difficult to meet the existing process requirements, while the slurry bed reactor can Under certain conditions, the temperature in the reactor is kept uniform, and the solid catalyst is uniformly dispersed in the reactor, and the inner surface of the catalyst is utilized to a greater extent, thereby increasing the conversion rate of acetylene and the yield of ethylene. Therefore, the ethylene hydrogenation slurry bed production process It is widely used in the process of hydrogenation of acetylene to ethylene; however, in the industrialization process of hydrogenation of acetylene in a slurry bed to ethylene, there are often problems due to uneven gas distribution, which affects the conversion rate of acetylene and the yield of ethylene, or conventional plate and frame filtration Poor airtightness of operation, high risk index, low filtration precision, poor separation effect and other problems make the working flui

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  • Acetylene hydrogenation slurry bed reaction as well as catalyst separation device and method
  • Acetylene hydrogenation slurry bed reaction as well as catalyst separation device and method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0053] Acetylene and hydrogen enter the acetylene hydrogenation reactor 1 through the external raw material gas delivery pipeline 4, the raw material gas inlet 13, and the gas distributor 5, and the working fluid whose component is acetone enters the acetylene hydrogenation reactor 1 from the mixed liquid inlet 14 In the process, the catalyst loaded with the active component palladium enters the acetylene hydrogenation reactor 1 from the inlet 17 of the concentrated solution, and the water at about 25°C enters from the heat exchange medium inlet 12 of the built-in heat exchanger 2, and becomes 110°C through heat exchange. Left and right water vapor is discharged through the heat exchange medium outlet 17 of the built-in heat exchanger 2, so that the temperature in the acetylene hydrogenation reactor 1 is controlled at 130°C, and the pressure in the acetylene hydrogenation reactor 1 is controlled at about 3MPaG. 1. Hydrogenation reaction occurs on the surface of the catalyst who...

Embodiment 2

[0057] Acetylene and hydrogen enter the acetylene hydrogenation reactor 1 through the external raw material gas delivery pipeline 4, raw material gas inlet 13, and gas distributor 5, and the working fluid whose component is cyclohexanone enters the acetylene hydrogenation reaction from the mixed liquid inlet 14 In the reactor 1, the catalyst loaded with the active component palladium enters the acetylene hydrogenation reactor 1 from the concentrated solution inlet 17, and the water at about 20°C enters from the heat exchange medium inlet 12 of the built-in heat exchanger 2, and becomes The water vapor at about 120°C is discharged through the heat exchange medium outlet 17 of the built-in heat exchanger 2, so that the temperature in the acetylene hydrogenation reactor 1 is controlled at 140°C, and the pressure in the acetylene hydrogenation reactor 1 is controlled at about 4MPaG , the hydrogenation reaction of acetylene and hydrogen occurs on the surface of the catalyst whose ac...

Embodiment 3

[0061]Acetylene and hydrogen enter the acetylene hydrogenation reactor 1 through the external raw material gas delivery pipeline 4, raw material gas inlet 13, and gas distributor 5, and the working fluid whose component is N-methyl-2-pyrrolidone is from the mixed liquid inlet 14 Entering the acetylene hydrogenation reactor 1, the catalyst loaded with the active component palladium enters the acetylene hydrogenation reactor 1 from the concentrated solution inlet 17, and the water at about 25°C enters from the heat exchange medium inlet 12 of the built-in heat exchanger 2, After heat exchange, it becomes water vapor at about 130°C, and then it is discharged through the heat exchange medium outlet 17 of the built-in heat exchanger 2, so that the temperature in the acetylene hydrogenation reactor 1 is controlled at 150°C, and the acetylene hydrogenation reactor 1 is controlled The internal pressure is about 3.5MPaG, and the hydrogenation reaction of acetylene and hydrogen occurs on...

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Abstract

The invention belongs to the field of preparing ethylene through acetylene hydrogenation, and relates to acetylene hydrogenation slurry bed reaction as well as a catalyst separation device and method.The method comprises the following steps of enabling acetylene and hydrogen gas to be subjected to hydrogenation reaction in a hydrogenation reactor which contains a catalyst and a working solution,discharging crude ethylene after reaction, separating a working slurry solution with a membrane separator to obtain a concentrated solution and a clear solution, conveying the concentrated solution directly to the hydrogenation reactor to be recycled, enabling the obtained clear solution to be subjected to gas-liquid separation, and then enabling gas and a fresh working solution to return into thehydrogenation reactor to be continuously used. The hydrogenation reactor is internally provided with an angle gear-shaped gas redistribution device, the gas volume fraction in the working solution can be improved, the radial distribution uniformity of the gas in the reactor is improved, the conversion rate of acetylene and ethylene yield are improved; an airtight membrane separator is adopted toperform solid-liquid separation on the working slurry liquid, the separation process can be guaranteed to be safe and stable, a by-product 'green oil' can be timely extracted, the activity of the catalyst is guaranteed, and the reaction can be promoted to be successfully performed.

Description

technical field [0001] The invention belongs to the field of hydrogenation of acetylene to produce ethylene, and relates to a slurry bed reaction and catalyst separation device and method for hydrogenation of acetylene. Background technique [0002] Ethylene is an important chemical raw material, mainly used in the field of PVC production. China is a big consumer of ethylene, and the annual ethylene consumption is increasing year by year. However, 70% of the world's ethylene is currently produced using crude oil as raw material. The development of this "oil-poor and coal-rich" region in China is extremely unfavorable; the production of acetylene from coal and hydrogenation of acetylene to ethylene are not only in line with China's basic national conditions, but also can solve the problem of excess acetylene in some areas. Good economic development model, but the acetylene hydrogenation process has the characteristics of large heat release and difficult control of the reactio...

Claims

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Application Information

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IPC IPC(8): B01J8/18C07C5/09C07C11/04
CPCB01J8/006B01J8/009B01J8/1827B01J8/1836C07C5/09B01J2208/00132C07C11/04Y02P20/52
Inventor 刘常青王富民赵风云刘正贤赵途李华北赵少博刘硕磊高文杲张玉新
Owner 河北美邦工程科技股份有限公司
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