Aromatization catalyst and applications thereof

A catalyst and aromatization technology, applied in physical/chemical process catalysts, molecular sieve catalysts, organic compounds/hydrides/coordination complex catalysts, etc., can solve the problem of low yield of mixed xylenes, benzene and mixed xylenes Low yield and other problems, to achieve the effect of low reaction temperature, increased yield, and high yield

Active Publication Date: 2011-10-19
CHINA PETROCHEMICAL CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0015] The purpose of the present invention is to provide an aromatization catalyst to solve the problems in the prior art that the yield of benzene and mixed xylenes in the aromatization product is low, especially the low yield of mixed xylenes, etc.

Method used

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  • Aromatization catalyst and applications thereof
  • Aromatization catalyst and applications thereof
  • Aromatization catalyst and applications thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Take SiO 2 / Al 2 o 3 500 grams of HZSM-5 molecular sieve with a molar ratio of 38, gradually poured into 500 milliliters of zinc nitrate solution containing 15% zinc in batches, mixed and stirred for one hour, dried at 120 degrees for 4 hours, and roasted at 550 degrees for 6 hours , cooled and ground to obtain catalyst active component A1 for use.

Embodiment 2

[0036] Take SiO 2 / Al 2 o 3 500 grams of HZSM-5 molecular sieve with a molar ratio of 38, gradually poured into 500 milliliters of zinc nitrate solution containing 10% zinc in batches, mixed and stirred for one hour, dried at 120 degrees for 4 hours, and roasted at 550 degrees for 6 hours , cooled and ground to obtain catalyst active component A2 for use.

Embodiment 3

[0038] Take SiO 2 / Al 2 o 3 500 grams of HZSM-5 molecular sieve with a molar ratio of 38, gradually poured into 500 milliliters of zinc nitrate solution containing 5% zinc in batches, mixed and stirred for one hour, dried at 120 degrees for 4 hours, and roasted at 550 degrees for 6 hours , cooled and ground to obtain catalyst active component A3 for use.

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PUM

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Abstract

The invention discloses an aromatization catalyst and applications thereof, and aims at solving the problems such as low yield of benzene and mixed xylene in the liquid outcomes and the like during the existing hydrocarbon aromatization reaction. The catalyst comprises the following components by weight percentage of 30-90wt% of molecular sieves, 0-60wt% of carriers and 10-20 wt% of adhesives, wherein the molecular sieves are mixtures of a molecular sieve I, a molecular sieve II, a molecular sieve III and a molecular sieve IV; the molecular sieve I is at least one modified HZSM-5 molecular sieve out of modified elements zinc, gallium and lanthanum; the molecular sieve II is at least one modified HZSM-5 molecular sieve out of modified elements bismuth, molybdenum, silver, copper, zirconiumand rhenium; the molecular sieve III is the HZSM-5 molecular sieve formed by modifying polysiloxane; and the molecular sieve IV is a modified hydrogenated mercerization type molecular sieve, a modified hydrogenated Beta-type molecular sieve, a hydrogenated ZSM-11 molecular sieve and a hydrogenated MCM-22 molecular or mixtures thereof.

Description

technical field [0001] The invention relates to a catalyst for the production of high-quality aromatic products by aromatization of hydrocarbons, especially suitable for C in liquefied gas 3 ~C 5 The process of aromatizing olefins at a lower temperature to produce high-quality aromatics and high-octane gasoline rich in non-benzene aromatics. [0002] The invention also relates to the application of the above-mentioned catalyst in producing aromatic hydrocarbons and high-octane gasoline by aromatization of hydrocarbons. Background technique [0003] With the implementation of my country's "West-to-East Gas Transmission" plan and civil natural gas pipeline projects, the already surplus liquefied gas LPG in refineries has been further backlogged, especially the amount of carbon tetraolefins contained in it is less than 50%, and refineries The existence of high content of olefins in liquefied gas affects the production of liquefied gas for vehicles (the QJ / DSH712-1999 standard ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J31/06B01J29/80C10G35/095
Inventor 郝代军刘丹禾魏小波韩海波沈方峡任潇航俞安平李昕朱伟王贵云张国良
Owner CHINA PETROCHEMICAL CORP
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