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Recovery method of microspherical catalyst of fluid bed

A technology of catalyst and fluidized bed, which is applied in the recovery field of microsphere catalyst for fluidized bed

Active Publication Date: 2010-12-15
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

The method of recovering and reusing the post-reaction catalyst (carbon-containing sample or sample after roasting) to prepare microsphere catalyst for fluidized bed has not been reported in the literature so far.

Method used

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  • Recovery method of microspherical catalyst of fluid bed
  • Recovery method of microspherical catalyst of fluid bed

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] According to the solid content of oxide dry basis in the material solution of 30wt%, the measured silica sol (content 30wt%), aluminum sol (content 20%), calcium nitrate (content 23%), kaolin (content 85wt%) and SAPO -34 molecular sieve raw powder was added to a certain amount of deionized water in sequence, stirred for 30 minutes (the oxide dry basis mass content of each raw material was 25%, 10%, 5%, 30%, 30% in sequence), and finally added Sesbania powder (soaked with a small amount of ethanol) equivalent to 0.5% of the total oxide dry basis mass, stirred for 30 min. The material liquid is passed through the colloid mill for colloid grinding, so that 70% of the particle diameter in the final slurry is less than 5 μm. After the slurry is placed at room temperature for 2 hours, it is subjected to centrifugal spray drying. The rotating speed of the atomizer is 30 Hz, the inlet temperature is 400°C, and the outlet temperature is not less than 120°C. The spray-dried produ...

Embodiment 2

[0023] The MC sample obtained in Example 1 was used in a circulating fluidized bed (catalyst loading capacity of 4 tons, methanol processing capacity of 50 tons / day) for an industrial test to perform methanol conversion to olefin reaction. Device level

[0024] After 30 days of stable operation, take out the collected catalyst powder from the sampling port of the cyclone separator and record it as XM. Take a small amount of catalyst sample from the sampling port of the reactor and record it as FM.

Embodiment 3

[0026] Take part of XM and FM samples, and roast them in air at 650°C to remove the moisture and reaction residual carbon contained in them. The samples obtained are denoted as XMC and FMC, respectively.

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Abstract

The invention relates to a recovery method of microspherical catalyst for a fluidized bed. The invention provides the method that catalyst to be recovered is mixed with each raw material preparing the fresh microspherical catalyst in certain proportion, the spray drying and the high temperature roasting are performed after the colloid milling of feed pulp, and the microspherical catalyst having the low abrasion index and the suitable particle size distribution can be obtained. The invention has the preparation processes that: firstly, according to the stoichiometric ratio of oxide dry basis, the catalyst to be recovered, molecular sieve initial powder, binding agent, auxiliary agent, pore forming agent, and deionized water are mixed and pulped, and the weight content of the oxide dry basis of recovered catalyst is not more than 80 percent in total blending; secondly, the colloid milling of the feed pulp through a colloid mill is performed, thereby the solid particle diameter containedin the feed pulp is smaller than 20 micron, 90 percent of the particle diameter is small than 10 micron, and 70 percent of the particle diameter is small than 5 micron; thirdly, the spray drying is performed, thereby producing a microspherical sample; fourthly, the microspherical sample is roasted in oxygen-containing atmosphere at 500 to 800 DEG C, thereby obtaining the microspherical catalyst for the fluidized bed. The recovered and prepared microspherical catalyst can be used for the reaction of producing alkene by converting an oxygen compound.

Description

Technical field [0001] The invention relates to a method for recovering a microsphere catalyst for a fluidized bed and the catalytic application of the recovered catalyst in the conversion of oxygenated compounds to olefins. Background technique [0002] Ethylene and propylene are important basic chemical raw materials. At present, our country mainly adopts light oil cracking method to prepare. With the shortage of petroleum resources and rising prices, the technology of producing low-carbon olefins from non-petroleum routes has become increasingly urgent. The research and development of ethylene and propylene has become a hot spot of technology investment by domestic and foreign research institutions and major international companies. The single-series, large-scale industrialization technology of methanol production from natural gas or coal has been very mature, so the research of methanol production of olefins (MTO) has become a key technology for the production of low-carbon ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/90B01J29/85C07C1/20C07C11/02
CPCB01J29/90B01J37/0018B01J37/0036C07C1/20B01J35/023B01J29/85B01J29/83B01J2229/42B01J37/0045Y02P20/584
Inventor 田鹏刘中民许磊杨立新袁翠峪吕志辉孟霜鹤齐越何长青魏迎旭王贤高
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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