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Reforming catalyst and application in high selectivity production of para-xylene of the same

A reforming catalyst and catalyst technology, applied in molecular sieve catalysts, physical/chemical process catalysts, organic chemistry, etc., can solve the problems of molecular sieve crystallization destruction, molecular sieve modification, reduction, etc., to reduce investment and operating costs, strong resistance to sulfur and nitrogen Poisoning ability, the effect of improving operation efficiency

Active Publication Date: 2008-05-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the preparation process of the catalyst of the present invention, in order to reduce the carbon deposition in the use process of the catalyst and improve the stability of the catalyst, it is necessary to steam the catalyst (carrier) at 400°C to 650°C, which may lead to two deficiencies : First, due to high temperature water vapor treatment may lead to the destruction of some molecular sieve crystallization, which reduces the concentration of molecular sieve pore size distribution, thereby reducing the selectivity of the reaction; in addition, due to high temperature water vapor treatment leads to partial crystallization destruction and dealumination, The amount of acid on the surface of the molecular sieve (inner surface and outer surface) is greatly reduced, and the aromatization reaction requires a strong acid center, which leads to a significant reduction in the aromatization activity of the catalyst
However, since the purpose of this patent is to improve the aromatization activity, the acidity and pore structure of the molecular sieve are not modified, and the selectivity of p-xylene is not involved.

Method used

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  • Reforming catalyst and application in high selectivity production of para-xylene of the same
  • Reforming catalyst and application in high selectivity production of para-xylene of the same

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] The preparation method of catalyst (E-1) of the present invention is as follows:

[0038] (1) Preparation of phosphorus-containing molecular sieves

[0039] a. Ammonium dihydrogen phosphate and water are used to prepare 1000 grams of phosphorus pentoxide concentration into a solution of 5 wt%, and the above solution is added to 950 grams of HZSM-5 (the molar ratio of silicon to aluminum is 65, and the specific surface area is 187m 2 / g, pore volume 0.18ml / g, provided by Nankai University), the mixture was dried for 8 hours, then in the air atmosphere at 550 ° C, roasted for 6 hours to obtain the ZSM-5 molecular sieve with a phosphorus pentoxide content of 5wt%, which is denoted as ZSM-5a.

[0040] B. same as step a, its difference is that the phosphorus-containing compound used is phosphoric acid, and the concentration of preparing phosphorus pentoxide is 9.5wt%, obtains the ZSM-5 molecular sieve that phosphorus pentoxide content is 9.5wt%, is denoted as ZSM here -5b....

Embodiment 2

[0047] The preparation method of catalyst (E-2) of the present invention is as follows:

[0048] Catalyst preparation method is the same as embodiment 1, and difference is that molecular sieve used is ZSM-5b, and its content in catalyst carrier is 80wt%, Sb 2 o 3 The content of rhenium is 5wt%; the content of rhenium and zinc in the catalyst is different, and the catalyst number is E-2, its composition is shown in Table 1, and the evaluation results are shown in Table 2.

Embodiment 3

[0050] The preparation method of catalyst (E-3) of the present invention is as follows:

[0051] Catalyst preparation method is the same as embodiment 1, and difference is that molecular sieve used is ZSM-5c, and its content in catalyst carrier is 60wt%, Sb 2 o 3 The content of the catalyst is 10wt%; the active metals are rhenium and gallium, the compounds used are perrhenic acid and gallium nitrate respectively, and the obtained catalyst number is E-3, its composition is shown in Table 1, and the evaluation results are shown in Table 2.

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Abstract

The invention discloses reforming catalyst and the application in the preparation of para xylene reforming high selectivity and taking saturated hydrocarbon, cycloparaffinic hydrocarbon and naphtha as the raw material. The carrier of the catalyst includes mesoporous molecular sieve, antimony oxide and inorganic melt-resistant oxide, wherein, the mesoporous molecular sieve includes 0.5 wt percent to 10.0 wt percent of phosphorus pentoxide. The surfaces of the antimony oxide and the molecular sieve included in the catalyst are contacted to facilitate the strong acid position on the surface of the molecular sieve to be intoxicated, so as to lower the reaction activity center with poor selectivity, and to maintain a passage reaction site with high selectivity; meanwhile the invention adopts phosphorus pentoxide modified molecular sieve to adjust the internal surface of the molecular sieve, particularly to adjust the size of the passage of the molecular sieve, so as to further contract the size of the passage to restrain the generation of the nonideal products of ortho xylene and meta xylene, and to improve the selectivity of the ideal product para xylene.

Description

technical field [0001] The invention relates to a reforming catalyst and its application in high-selectivity preparation of p-xylene by reforming saturated hydrocarbons, naphthenes, olefins, naphtha and the like as raw materials. Background technique [0002] P-xylene is an important organic chemical raw material, a by-product of naphtha reforming process, mainly used in the synthesis of terephthalic acid or dimethyl terephthalate, dimethyl terephthalate and ethylene glycol The polyester obtained by the reaction has excellent properties and is widely used as a raw material for fibers and plastics. With the sharp increase of the global demand for polyester, the production of p-xylene will increase rapidly. According to the forecast results of the British TECNON consulting company in December 1999, the absolute growth value of the global demand for p-xylene during the period from 2001 to 2007 It is 7.042 million tons, and the annual growth rate is expected to be around 5.6%. ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/85C07C15/08C07C6/00
CPCY02P20/52
Inventor 刘全杰徐会青贾立明王伟
Owner CHINA PETROLEUM & CHEM CORP
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