Unlock instant, AI-driven research and patent intelligence for your innovation.

Method for liquid-phase transalkylation of polyethylbenzene and benzene

A polyethylbenzene, transalkylation technology, applied in chemical instruments and methods, hydrocarbons, molecular sieve catalysts, etc., can solve the problems of poor catalyst stability, low ethylbenzene selectivity, and short regeneration cycle, and achieve stability. Good, high selectivity, and the effect of improving stability

Active Publication Date: 2016-06-08
CHINA PETROLEUM & CHEM CORP +1
View PDF13 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The technical problem to be solved by the present invention is that the prior art has the problems of low ethylbenzene selectivity, poor catalyst stability and short regeneration cycle, and provides a new method for liquid-phase transalkylation of polyethylbenzene and benzene

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Method for liquid-phase transalkylation of polyethylbenzene and benzene

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Weigh 50 grams of β-type molecular sieve powder (SiO 2 / Al 2 o 3 than 25, the grain size is between 0.01 and 0.05 microns). Molecular sieve / alumina (dry base ratio) is 80 / 20, extruded, dried at 110°C, and calcined at 550°C for 3 hours. Then it was added to the prepared ammonium nitrate aqueous solution with a weight concentration of 10%, stirred at a temperature of 90° C. for 1 hour, then centrifugally filtered, and washed twice with deionized water. Repeat the above ammonium ion exchange process 2 times. Dry at 110°C and bake at 550°C for 3 hours. Then at 550°C, under normal pressure, the weight ratio of ammonia to catalyst is 0.1h -1 treated under an ammonia atmosphere for 4 hours. Then stop feeding the ammonia gas, lower it to room temperature, then use a citric acid solution with a weight concentration of 5%, stir at 90°C for 2 hours, wash with deionized water twice, dry at 110°C, and roast at 550°C for 3 hours. That is, the finished catalyst is obtained.

Embodiment 2~9

[0031] With [embodiment 1], only the conditions of ammonia treatment are different. See Table 1 for details.

[0032] Table 1

[0033]

Embodiment 10

[0035] The initial activity of the catalyst was investigated in a fixed-bed reactor from bottom to top, and the reactor was a stainless steel tube with an inner diameter of 28 mm and a length of 800 mm. The catalyst load was 3 grams and diluted with glass beads. The catalyst was calcined at 550°C for 3 hours before use.

[0036]After loading the catalysts of [Example 1~9] into the reactor, test the leak of the system under the pressure greater than the reaction pressure, and then raise the temperature of the catalyst under the protection of nitrogen. After the temperature reaches the set temperature, the nitrogen pressure is increased to the set pressure, and the pre-mixed benzene and polyethylbenzene transalkylation materials are quickly pumped in. After some liquid materials come out of the sampling port, the feed is changed to the set flow rate.

[0037] The reaction conditions are: temperature 240°C, pressure 4.0MPa, liquid phase weight space velocity 2 hours -1 , The we...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention relates to a method for liquid-phase transalkylation of polyethylbenzene and benzene, which mainly solves the problems of low ethylbenzene selectivity, poor catalyst stability and short regeneration period in the prior art. The present invention uses polyethylbenzene and benzene as reaction raw materials, at a reaction temperature of 200-280°C, a reaction pressure of 2.0-4.5MPa, and a liquid phase weight space velocity of 1-10 hours -1 , under the condition that the weight ratio of benzene / polyethylbenzene is 1-10, the reaction raw material and the catalyst contact and react to form ethylbenzene; the catalyst includes the following components in parts by weight: a) 30-90 parts of β-type molecular sieve ; b) 10-70 parts of binder; wherein, the β-type molecular sieve is a technical solution obtained by passing the original powder of the β-type molecular sieve through at least one step of ammonia treatment, which solves this problem well and can be used in In the industrial production of polyethylbenzene and benzene liquid-phase transalkylation to produce ethylbenzene.

Description

technical field [0001] The invention relates to a method for liquid-phase transalkylation of polyethylbenzene and benzene. Background technique [0002] Ethylbenzene is an important organic chemical raw material, and it is mainly used as a raw material for the production of styrene in industry. Ethylbenzene is mainly produced by the alkylation reaction of benzene and ethylene, and the alkylation process is generally divided into gas-phase molecular sieve method and liquid-phase molecular sieve method. Regardless of the alkylation process of the gas-phase molecular sieve method or the liquid-phase molecular sieve method, since the reaction product ethylbenzene can continue to undergo alkylation reaction with ethylene like the raw material benzene to form polyethylbenzenes such as diethylbenzene, triethylbenzene, tetraethylbenzene, etc. Generally, the amount of polyethylbenzene produced should account for 10% to 15% of the amount of ethylbenzene. In order to obtain a high yie...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): C07C15/073C07C6/12B01J29/70
CPCY02P20/52Y02P20/584
Inventor 宦明耀孙洪敏杨为民张斌沈震浩
Owner CHINA PETROLEUM & CHEM CORP