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: 2008-04-09
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The method of recovering and reusing the post-reaction catalyst (carbon-containing sample or sample after

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] It is 30wt% to calculate by oxide dry base solid content in feed liquid, the silica sol (content 30wt%) of metering, aluminum sol (content 20%), calcium nitrate (content 23%), kaolin (content 85wt%) and SAPO The former powder of -34 molecular sieve was added into a certain amount of deionized water in sequence, and stirred for 30 minutes (the oxide dry basis mass content of each raw material was respectively 25%, 10%, 5%, 30%, and 30%) in sequence, and finally added Squash powder (soaked with a small amount of ethanol) equivalent to 0.5% of the dry weight of the total oxides, stirred for 30 minutes. The feed liquid is passed through a colloid mill for colloid milling, so that 70% of the particle diameters in the finally obtained slurry are less than 5 μm. After the slurry was left at room temperature for 2 hours, it was subjected to centrifugal spray drying, the atomizer rotated at 30 Hz, the inlet temperature was 400°C, and the outlet temperature was not lower than 120...

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) in an industrial test to carry out methanol conversion to olefins reaction. After 30 days of stable operation of the device, the collected catalyst powder was taken out from the sampling port of the cyclone separator, and recorded as XM. A small amount of catalyst sample was taken from the sampling port of the reactor, denoted as FM.

Embodiment 3

[0025] Some samples of XM and FM were taken and calcined in air at 650°C to remove the moisture and reaction carbon residue contained therein, and the obtained samples were 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 contained in 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 used in a fluidized bed and the catalytic application of the recovered catalyst in the reaction of converting oxygen-containing compounds into olefins. Background technique [0002] Ethylene and propylene are important basic chemical raw materials. At present, my country mainly adopts light oil cracking method to prepare them. With the shortage of petroleum resources and rising prices, the technology of producing low-carbon olefins through non-petroleum routes is becoming increasingly urgent. The research and development of ethylene and propylene has become a hot spot for domestic and foreign research institutions and major international companies to invest in technology. The single-series and large-scale industrialization technology for producing methanol from natural gas or coal is very mature, so the research on producing olefins (MTO) from methanol has become a key technology ...

Claims

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Application Information

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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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