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Aromatization method

An aromatization and structural formula technology, applied in the field of aromatization, can solve problems such as the inevitable generation of olefin species and catalyst deactivation

Active Publication Date: 2018-01-16
CHINA PETROLEUM & CHEM CORP +1
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  • 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 olefin species are inevitably produced during the aromatization process of levulinic acid compounds, thereby generating carbon deposits and causing catalyst deactivation, and providing a new aromatization method

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0049] Weigh 35 grams of ZSM-5 with a silicon-aluminum ratio of 25 and mix them with 35 grams of γ-alumina, 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, calcined at 500°C for 2 hours, and impregnated with Zn(NO 3 ) 2 , the added amount of Zn is 1%, and the molecular sieve catalyst is obtained by roasting after drying.

[0050] 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 200°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...

Embodiment 2

[0053] 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, calcined at 500°C for 2 hours, and impregnated with Cu(NO 3 ) 2 , the amount of Cu added is 2%, and the molecular sieve catalyst C2 is obtained by roasting after drying.

[0054] Catalyst activity evaluation is carried out on a fixed bed, the reaction conditions catalyst mass is 3 grams, the reaction substrate is levulinic acid+water (50 / 50), and the weight space velocity is 1.0 hours -1 , hydrogen pressure 1.0MPa, flow 50ml min -1 , temperature 420°C. After completion of the reaction, the conversion rate of levulinic acid was 99%, and T60 was 1372 hours.

Embodiment 3

[0056]Weigh 30 grams of wood, put it in an autoclave and add 300 grams of ethanol, then add a 5mol / L sulfuric acid solution with 7% water quality, heat up to 200°C and react for 30 minutes, then cool, and filter the cooled reaction solution , to obtain a filter cake and a filtrate, the filtrate is a 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 10.5 grams.

[0057] 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. Adding nitric acid mass percentage content afterwards is 48 grams of nitric acid aqueous solution of 5.5%, kneading molding, adding Ga(NO 3 ) 2 , the amount of Ga added is 1% by molecular sieve mass, extruded. The obtained catalyst precursor was dried at 120° C. for 8 hours, and calcined at 500° C. for 2 hours to obtain molecular siev...

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Abstract

The invention relates to an aromatization method. 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), R is optionally substituted C1-8 straight chain or branched alkyl, optionally substituted C2-8 straight chain or branched alkenyl; R2 is hydrogen, optionally substituted C1-10 straight chain or branched alkyl, and n is a positive integer of 1-6. The catalyst is a molecular sieve composition, which comprises the following components: a) 20-80 parts by weight of a molecular sieve, which is at least one of a ZSM type molecular sieve, a Y type molecular sieve, a Beta type molecular sieve, an L type molecular sieve or MCM type molecular sieve; b) 20-80 parts by weight of a binder; and c) 0.01-10 parts by weight of an assistant.

Description

technical field [0001] The invention relates to an aromatization method, 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 / phenol, and more. Par...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C1/207C07C15/04C07C15/06C07C15/08B01J29/40B01J29/46B01J29/48B01J29/70B01J29/14B01J29/12B01J29/08B01J29/78B01J29/04C07C51/16C07C63/26
CPCY02P20/52
Inventor 宋奇孔德金郑均林
Owner CHINA PETROLEUM & CHEM CORP