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A catalyst for non-hydrogenation deolefination of aromatic hydrocarbons and its preparation method

A catalyst and non-hydrogen-facing technology, applied in the direction of molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of wastewater discharge, waste gas, complex catalyst preparation process, high cost, etc., and achieve low loss of aromatics and low cost low cost, simple preparation

Inactive Publication Date: 2017-11-17
BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Compared with activated clay catalysts, these research results have certain advantages, but the catalyst preparation process is complicated, the cost is high, and pollutants such as waste water and waste gas will be discharged to the environment during the catalyst preparation process.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] The metal content is weighed to 4600μg / g, the composition of the waste catalytic cracking catalyst is 80g of 60% USY molecular sieve and kaolin, and 20g of alumina dry rubber powder is mixed and extruded to have a diameter of 2*4mm, and then calcined at 540℃. Hours, catalyst A was obtained.

Embodiment 2

[0022] The metal content is weighed to 3800μg / g, the composition of the waste catalytic cracking catalyst is 80g of the composition of 65% ReY molecular sieve and kaolin, and 20g of alumina dry rubber powder is mixed and kneaded with a diameter of 2*4mm, and then calcined at 540℃. Hours, catalyst B was obtained.

Embodiment 3

[0024] The metal content is weighed to 4600μg / g, the composition of the waste catalytic cracking catalyst is 70g of a composition of 60% USY molecular sieve and kaolin, and 30g of alumina dry rubber powder is mixed and kneaded with a diameter of 2*4mm, and then calcined at 540℃. Hours, catalyst C was obtained.

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PUM

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Abstract

The invention uses waste catalytic cracking catalysts as raw materials to prepare aromatic hydrocarbon non-hydrogenation deolefin catalysts. The waste catalytic cracking catalyst with a metal content of less than 5000 μg / g is mixed with alumina dry rubber powder and extruded into a rod, and roasted at 540°C for 4 hours to obtain an aromatic hydrocarbon non-hydrogenated deolefin catalyst. Wherein the mass content of the waste catalytic cracking catalyst is 60-80%, and the alumina content is 20-40%; the acid content of the catalyst is 0.3-0.5mmol / g, the specific surface area is 290-320m2 / g, and the average pore diameter is 8.5-10nm; The catalyst catalyzes the non-hydrogenation deolefination of aromatics, and can generally reduce the bromine value of raw materials from 3000mg / 100g to below 20mg / 100g, and the loss of aromatics is less than 0.01%.

Description

Technical field [0001] The invention relates to a catalyst for removing olefins, more specifically a catalyst for removing trace olefin impurities from aromatic hydrocarbon mixtures without hydrogen and a preparation method thereof. Background technique [0002] At present, in the petrochemical industry, the production of aromatics mainly adopts catalytic reforming and steam cracking processes. While using these processes to convert petroleum fractions such as naphtha, light diesel oil and hydrogenated tail oil into BTX (benzene, toluene, xylene), a small amount of olefins will be produced, and the general content of the product composition is less than the mass fraction 1%. This part of a small amount of olefins is chemically active due to the presence of carbon-carbon double bonds in the molecular structure. Since the subsequent processing of aromatic hydrocarbons, such as xylene isomerization, toluene disproportionation, xylene adsorption separation, and benzene alkylation, ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/08C07C7/148C07C15/04C07C15/06C07C15/08
CPCY02P20/52
Inventor 姚志龙毛进池李季伟刘文飞孙培永高永林
Owner BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY