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Preparation method and application of a molecular sieve catalyst containing aluminum phosphate binder

A molecular sieve and binder technology, which is applied in the field of preparation of molecular sieve catalysts, can solve problems such as researches that have not yet been published, and achieve the effect of improving conversion rate and good anti-carbon deposition performance

Active Publication Date: 2016-08-24
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

[0018] The above-mentioned aluminum phosphate binder has many advantages, but it is limited to the ZSM-5 molecular sieve system, and the research on adding aluminum phosphate binder to the ZSM-11 molecular sieve system has not yet been reported.

Method used

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  • Preparation method and application of a molecular sieve catalyst containing aluminum phosphate binder

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Experimental program
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Effect test

Embodiment 1

[0030] A certain amount of rare earth ZSM-11 molecular sieve with a particle size of 350nm (the rare earth content accounts for 1.2wt% of the rare earth ZSM-11 molecular sieve) is calcined at 550°C for 4h to remove the stencil agent, and 0.8mol / L ammonium nitrate is used at 80°C Solution exchange 3 times, water wash 2 times, 120°C drying, 540°C roasting for 3 hours to obtain H-type molecular sieve, then conventionally impregnated loaded zinc metal, using zinc nitrate solution, drying at 85°C for 2 hours, 550°C roasting for 4 hours, the resulting catalyst The Zn loading is 5wt%; the phosphoric acid solution and the boehmite are in accordance with the P / Al molar ratio (the molar ratio of P element in the phosphoric acid solution to the Al element in the boehmite, the same below), stir evenly, and add to the previous preparation For a good molecular sieve catalyst, the weight ratio of molecular sieve dry basis to boehmite dry basis is 4, stirred uniformly, dried at 125°C and calcin...

Embodiment 2

[0032] A certain amount of 500nm rare earth ZSM-11 molecular sieve (the rare earth content accounts for 2.3wt% of the rare earth ZSM-11 molecular sieve) is calcined at 500℃ for 3h to remove the stencil agent, and 0.6mol / L ammonium nitrate is used at 70℃ Solution exchange 3 times, water wash 2 times, 120°C drying, 500°C roasting for 4h to obtain H-type molecular sieve, and then conventionally dipping the loaded zinc metal, using zinc acetate solution, drying at 90°C for 1.5h, 500°C roasting for 5h, the resulting The Zn loading of the catalyst is 1.2wt%; the phosphoric acid solution and the boehmite are stirred evenly according to the P / Al molar ratio of 0.5, and the molecular sieve catalyst prepared in the previous step is added. The weight ratio of the molecular sieve dry basis to the boehmite dry basis is 3, and the stirring is uniform , Dried at 145°C and calcined at 500°C for 7h, the resulting catalyst is denoted as C.

Embodiment 3

[0034] A certain amount of 900nm rare earth ZSM-11 molecular sieve (the rare earth content accounts for 2.5wt% of the rare earth ZSM-11 molecular sieve) is calcined at 550°C for 4 hours to remove the stencil agent, then 0.7mol / L nitric acid is used at 60°C Exchange 3 times with ammonium solution, wash 2 times with water, dry at 120°C, roast at 550°C for 4h to obtain H-type molecular sieve, then conventionally impregnate the loaded zinc metal, use zinc nitrate solution, dry at 80°C for 3h, and roast at 550°C for 6h. The Zn loading of the catalyst is 4wt%; the phosphoric acid solution and the boehmite are stirred evenly according to the P / Al molar ratio of 0.2, and the molecular sieve catalyst prepared in the previous step is added, and the weight ratio of the molecular sieve dry basis to the boehmite dry basis is 5, and the stirring is uniform. After drying at 150°C, it was calcined at 650°C for 6 hours. The resulting catalyst was marked as D.

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Abstract

A preparation method and an application of a molecular sieve catalyst containing an aluminum phosphate binder particularly comprises following steps: (1) exchanging a prepared ultrafine rare earth ZSM-11 molecular sieve with an ammonium nitrate solution, drying the molecular sieve and roasting the molecular sieve to prepare an H-rare earth ZSM-11 molecular sieve; (2) supporting zinc on the H-rare earth ZSM-11 molecular sieve by a zinc salt through a conventional impregnation method, drying the molecular sieve and roasting the molecular sieve; and (3) mixing a phosphoric acid solution and boehmite to generate colloidal aluminium phosphate and uniformly mixing the colloidal aluminium phosphate with the zinc-type molecular sieve prepared in the last step according to a certain weight ratio, drying the molecular sieve and roasting the molecular sieve to obtain the molecular sieve catalyst. When the molecular sieve catalyst is used in an alkylation reaction between dimethyl ether and benzene, aromatic hydrocarbon with carbon number being 7-9 can be prepared at a high yield. The molecular sieve catalyst, compared with a molecular sieve catalyst which only contains an aluminum oxide binder, is increased in conversion rate of benzene and can promote generation of alkylation products of benzene (methyl benzene, dimethyl benzene and trimethyl benzene) and meanwhile inhibit generation of ethylation products of benzene (ethyl benzene and diethyl benzene). In addition, the molecular sieve catalyst is significantly improved in anti-carbon deposition performance.

Description

Technical field [0001] The invention belongs to the technical field of production of petrochemical products, and specifically relates to a preparation method and application of a molecular sieve catalyst containing an aluminum phosphate binder. Background technique [0002] Aromatics are an important basic raw material for petrochemicals. Among the total of about 8 million known organic compounds, aromatics account for about 30%. The use of natural gas (main component methane) or petroleum refinery dry gas (mainly containing methane, ethane, ethylene) and liquefied petroleum gas or methanol (dimethyl ether) for anaerobic aromatization to prepare aromatic hydrocarbons is currently academia and industry More popular research topics. [0003] Aromatics obtained from methanol and dimethyl ether were first seen in the MTG (Methanol to Gasoline) technology developed by Mobil Corporation in the United States. In the 1970s, Mobil Corporation developed the ZSM-5 zeolite catalyst to convert...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/40C07C2/88C07C15/06C07C15/08C07C15/02
CPCY02P20/52
Inventor 徐龙伢刘惠辛文杰刘盛林谢素娟
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI