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In-situ preparation method of a catalyst for co-producing p-xylene and light olefins from benzene and methanol to toluene

A technology of p-xylene and low-carbon olefins, applied in the field of chemical engineering, can solve the problems of huge investment, complex catalyst preparation process, and unmentioned content content, etc., to simplify the process, save preparation and transfer steps, and overcome technical prejudice Effect

Active Publication Date: 2020-08-07
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the technology reported above has also obtained higher PX selectivity, the preparation process of the catalyst is complex, requiring multiple modification and roasting processes, and a series of catalyst production devices need to be built, which requires a huge investment; in addition, this technology does not provide And the content of chain hydrocarbons in the product, the content of ethylene and propylene in the chain hydrocarbons, the content of toluene in aromatic products and the content of ethylbenzene in C 8 Content in aromatics

Method used

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  • In-situ preparation method of a catalyst for co-producing p-xylene and light olefins from benzene and methanol to toluene
  • In-situ preparation method of a catalyst for co-producing p-xylene and light olefins from benzene and methanol to toluene
  • In-situ preparation method of a catalyst for co-producing p-xylene and light olefins from benzene and methanol to toluene

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0074] Example 1 Preparation of HZSM-5 shaped molecular sieve sample for fixed bed

[0075] 100g HZSM-5 zeolite molecular sieve raw powder (Nankai University Catalyst Factory, Si / Al=30) was calcined in air atmosphere at 550°C for 4 hours, then pressed into tablets, crushed, and sieved to obtain 40-60 mesh particles. Molecular sieve particles, denoted as FXHZSM-5-A.

[0076] 100g HZSM-5 zeolite molecular sieve raw powder (Nankai University Catalyst Factory, Si / Al=5) was calcined in an air atmosphere at 550°C for 4 hours, then pressed into tablets, crushed, and sieved to obtain 40-60 mesh particles. Molecular sieve particles, denoted as FXHZSM-5-B.

[0077]100g HZSM-5 zeolite molecular sieve raw powder (Nankai University Catalyst Factory, Si / Al=10) was calcined in air atmosphere at 550°C for 4 hours, then pressed into tablets, crushed, and sieved to obtain 40-60 mesh particles. Molecular sieve particles, denoted as FXHZSM-5-C.

Embodiment 2

[0078] Example 2 Preparation of HZSM-11 shaped molecular sieve sample for fixed bed

[0079] 100g HZSM-11 zeolite molecular sieve raw powder (Nankai University Catalyst Factory, Si / Al=35) was calcined in air atmosphere at 550°C for 4 hours, pressed into tablets, crushed, and sieved to obtain 40-60 mesh particles. Molecular sieve particles, denoted as FXHZSM-11-A.

[0080] 100g HZSM-11 zeolite molecular sieve raw powder (Nankai University Catalyst Factory, Si / Al=12) was calcined in air atmosphere at 550°C for 4 hours, pressed into tablets, crushed, and sieved to obtain 40-60 mesh particles. Molecular sieve particles, denoted as FXHZSM-11-B.

[0081] Example 3 Preparation of HZSM-5 shaped molecular sieve sample for fluidized bed

[0082] 100g of HZSM-5 zeolite molecular sieve former powder (Nankai University Catalyst Factory, Si / Al=30) is mixed with aluminum or silicon-containing amorphous binder and spray-dried to form. The specific steps are:

[0083] Mix the original powde...

Embodiment 4

[0086] Example 4 Preparation of HZSM-5 shaped molecular sieve sample for fluidized bed

[0087] The specific preparation conditions and steps are the same as those in Example 3, except that the raw material HZSM-5 zeolite molecular sieve raw powder is used in an amount of 10 kg, and the particle size distribution of the obtained microsphere particle sample is 20-120 μm, and the abrasion index is 1.2, which is recorded as FLHZSM -5-B.

[0088] The specific preparation conditions and steps are the same as in Example 3, the difference is that the raw material HZSM-5 zeolite molecular sieve powder has a silicon-aluminum ratio of Si / Al=10, the obtained microsphere particle sample particle size distribution is 20-100 μm, and the wear index is 1.2, denoted as FLHZSM-5-C.

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Abstract

The present application discloses a method for in-situ preparation of a catalyst for the co-production of p-xylene and light olefins from benzene and methanol to toluene. The catalyst for the in-situ preparation of the benzene and methanol-toluene co-production of p-xylene and low-carbon olefins; the reactor is a reactor for benzene and methanol-toluene co-production of p-xylene and low-carbon olefins. The method simplifies the entire chemical production process by directly preparing the catalyst in the reaction system, saves catalyst preparation and transfer steps, and is easy to operate.

Description

technical field [0001] The application relates to an in-situ preparation method of a catalyst for the co-production of p-xylene and light olefins from benzene and methanol to toluene, which belongs to the field of chemical engineering. Background technique [0002] Ethylene and propylene are the cornerstones of the huge petrochemical industry, and most organic chemical products are derived from ethylene and propylene. Paraxylene (PX) is a raw material for the production of polyesters such as PET (polyethylene terephthalate), PBT (polybutylene terephthalate) and PTT (polytrimethylene terephthalate). In recent years, a large number of applications of polyester in textiles, clothing, beverage packaging and other fields have driven the rapid growth of the production and consumption of PTA (purified terephthalic acid) and upstream products PX. At present, the source of PX is mainly produced from toluene, C9 aromatics and mixed xylene obtained from naphtha reforming through dispr...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/40C07C1/20C07C2/86C07C11/04C07C11/06C07C15/08
CPCB01J29/40B01J2229/32B01J2229/34C07C1/20C07C2/864C07C2/865C07C2529/40C07C11/04C07C11/06C07C15/08C07C15/06Y02P20/52Y02P30/20Y02P30/40
Inventor 于政锡刘中民朱书魁杨越
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI