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Method for producing aromatic hydrocarbons

A manufacturing method and technology of aromatic hydrocarbons, applied in chemical instruments and methods, physical/chemical process catalysts, bulk chemical production, etc., can solve the problems of inevitable production of olefin species, catalyst deactivation, etc., and restore aromatization activity , reduce the frequency of regeneration and prolong the service life

Active Publication Date: 2020-03-27
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The technical problem to be solved by the present invention is the inevitable generation of olefin species during the aromatization process of lactone compounds, thereby generating carbon deposition, leading to the problem of catalyst deactivation, and providing a new method for producing aromatic hydrocarbons

Method used

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  • Method for producing aromatic hydrocarbons
  • Method for producing aromatic hydrocarbons
  • Method for producing aromatic hydrocarbons

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0044] Weigh 35 grams of ZSM-5 with a silicon-aluminum ratio of 25 and mix it with 35 grams of γ-alumina additive, add 2.7 grams of scallop powder, and mix well. Then add 48 grams of nitric acid aqueous solution with a mass percentage of nitric acid of 5.5%, knead and shape, and extrude. The obtained catalyst precursor was dried at 120° C. for 8 hours and calcined at 500° C. for 2 hours to obtain molecular sieve catalyst C1.

[0045] Catalyst activity evaluation is carried out on a fixed bed, reaction conditions: catalyst mass is 3 grams, reaction substrate is 50% propiolactone+50% water, weight space velocity 1.0 hour -1 , hydrogen pressure 1.0MPa, flow 50ml min -1 , the temperature is 450°C, the conversion rate of propiolactone is 86%, and the T60 is 970 hours.

Embodiment 2

[0047] Weigh 35 grams of ZSM-5 with a silicon-aluminum ratio of 50 and mix them with 35 grams of pseudo-boehmite, add 2.7 grams of celadon powder, and mix well. Then add 48 grams of nitric acid aqueous solution with a mass percentage of nitric acid of 5.5%, knead and shape, and extrude. The obtained catalyst precursor was dried at 120° C. for 8 hours and calcined at 500° C. for 2 hours to obtain molecular sieve catalyst C2.

[0048] Catalyst activity evaluation is carried out on a fixed bed, the reaction conditions catalyst mass is 3 grams, the reaction substrate is 30% butyrolactone + 70% water, and the weight space velocity is 2.0 hours -1 , hydrogen pressure 1.0MPa, flow 50ml min -1 , the temperature is 400°C, the conversion rate of butyrolactone is 82%, and the T60 is 960 hours.

Embodiment 3

[0050] Weigh 35 grams of ZSM-5 with a silicon-aluminum ratio of 150 and mix them with 35 grams of pseudo-boehmite, add 2.7 grams of safflower powder, and mix well. Then add 48 grams of nitric acid aqueous solution with a mass percentage of nitric acid of 5.5%, knead and shape, and extrude. The obtained catalyst precursor was dried at 120° C. for 8 hours and calcined at 500° C. for 2 hours to obtain molecular sieve catalyst C3.

[0051] Weigh 60 grams of corn stalks, place in an autoclave and add 700 grams of water, then add a 5mol / L sulfuric acid solution with 7% water quality, heat up to 180°C and react for 45 minutes, then cool, and the cooled reaction solution Filtrate to obtain filter cake and filtrate, the filtrate is the hydrolyzate of cellulose, after the reaction, the mass spectrometry is used to identify the reaction result. The main product is levulinic acid, and its production amount is 18 grams. Levulinic acid was obtained in a fixed bed at 20% metal loading on Cu...

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Abstract

The invention relates to a manufacturing method of aromatic hydrocarbon. The method includes the step of contacting a raw material with a catalyst in the presence of water under an aromatization reaction condition to manufacture aromatic hydrocarbon, wherein the raw material has a structural formula shown as (I), in the formula (I), R1 is selected from optionally substituted C1-20 straight chain or branched alkylidene, optionally substituted C2-20 straight chain or branched enylene, optionally substituted C2-20 straight chain or branched alkynylene, optionally substituted C3-20 cycloalkylene and optionally substituted C6-20 arylene; and R2 is selected from hydrogen, optionally substituted C1-20 straight chain or branched alkyl and carboxyl.

Description

technical field [0001] The invention relates to a method for producing aromatic hydrocarbons, in particular to a method for producing BTX aromatic hydrocarbons. The present invention further relates to a method for producing p-xylene and terephthalic acid based on the method for producing aromatic hydrocarbons. Background technique [0002] Aromatic products are widely used in many fields such as polyester, chemical fiber, rubber, medicine, and fine chemicals. The domestic consumption is considerable, which has an important impact on the development of the national economy. At the same time, it is an important basic organic chemical raw material for social development. Benzene, toluene, and xylene are three aromatic bulk chemicals widely used in aromatics, collectively referred to as light aromatics or BTX aromatics. Benzene is a versatile basic petrochemical raw material that can be used to produce numerous products derived from it, including ethylbenzene / styrene, cumene / p...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C1/207C07C15/04C07C15/06C07C15/08B01J29/40B01J29/65B01J29/70B01J29/08B01J29/04
CPCY02P20/52
Inventor 宋奇孔德金祁晓岚郑均林姜向东王晓晨
Owner CHINA PETROLEUM & CHEM CORP