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Preparation method of microporous ceramic gas distribution plate for high temperature fluidized bed reaction

A technology of gas distribution plate and high-temperature fluidized bed, which is applied in the field of ceramics, can solve the problems of poor distribution of reaction materials, influence on polysilicon yield, and uneven distribution of pores, and achieve high purity and yield, good suspension state, and gas good distribution effect

Inactive Publication Date: 2012-02-22
铁生年
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Traditional gas distribution plates are mainly used in catalytic or non-catalytic processes in the chemical industry, coal gasification or coal combustion processes. At this stage, fluidized bed technology is used to produce solar-grade polysilicon. Due to the requirements of polysilicon purity and yield, The above-mentioned gas distribution plate is not suitable for the production of solar-grade polysilicon particles. Generally, quartz powder is used to make the gas distribution plate. The distribution of pores is uneven, the resistance is large, and the distribution of reaction materials is poor, which affects the yield of polysilicon.

Method used

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  • Preparation method of microporous ceramic gas distribution plate for high temperature fluidized bed reaction
  • Preparation method of microporous ceramic gas distribution plate for high temperature fluidized bed reaction
  • Preparation method of microporous ceramic gas distribution plate for high temperature fluidized bed reaction

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preparation example Construction

[0017] A method for preparing a microporous ceramic gas distribution plate for high-temperature fluidized bed reaction of the present invention, the method is based on inorganic ceramic silicon carbide as the main material and is equipped with a certain auxiliary raw material to make a microporous ceramic gas distribution plate, and adopts the following steps :

[0018] a. Preparation of mixed slurry

[0019] SiC particles with a particle size of 250-350 microns are 30-50% by weight, 1000-mesh SiC powder is 3-5% by weight, Al 2 o 3 The weight percentage is 3.0~5.0%, SiO 2 The weight percentage is 1.0~2.0%, CaCO 3 The weight percentage is 2.0~5.0% and Mg(OH) 2 The weight percentage is 2.0-5.0%, the potato flour is 1.0-5.0% by weight and the rest is ion-exchanged water to make a slurry, and ball milled at 20-30°C for 10-24 hours;

[0020] b. Pouring

[0021] Pour the slurry obtained in the above step a into a plaster mold with a sawtooth cone at one end and a plane at the ...

Embodiment approach 1

[0027] The preparation method of microporous ceramic gas distribution plate for high-temperature fluidized bed reaction, the SiC particle weight percentage content of 250 microns is 30%, the SiC powder weight percentage content of 1000 mesh is 3.0%, Al 2 o 3 3.0% by weight, SiO 2 1.0% by weight, CaCO 3 The weight percentage is 2.0% and Mg(OH) 2 The percentage by weight is 2.0%, the percentage by weight of potato flour is 1.0%, and the balance is ion-exchanged water to make a slurry, ball mill for 10-24 hours at 20°C, and pour the slurry into one end of the sawtooth Conical, the other end is a flat plaster mold and dried to produce a microporous ceramic with a diameter of 2 cm, a thickness of 0.5 cm, a sawtooth conical height of 0.2 cm, a cone angle of 40 degrees, and a distance of 0.2 cm between the cones. distribution plate. Demoulding and drying the gypsum mold, the microporous ceramic multi-cloth plate with one side as a sawtooth cone and the other end as a plane is pla...

Embodiment approach 2

[0029] The preparation method of the microporous ceramic gas distribution plate for high-temperature fluidized bed reaction, the SiC particles with a particle size of 350 microns are 50% by weight, the SiC powder of 1000 mesh is 5% by weight, Al 2 o 3 5.0% by weight, SiO 2 2.0% by weight, CaCO 3 The weight percentage is 5.0% and Mg(OH) 2 The percentage by weight is 5.0%, the percentage by weight of potato flour is 5.0%, and the balance is mixed with ion-exchanged water to make a slurry. Ball mill it for 24 hours at 30°C, and pour the slurry into a sawtooth conical shape at one end. , the other end is a flat plaster mold and dried to produce a microporous ceramic distribution plate with a diameter of 10 cm, a thickness of 0.8 cm, a sawtooth cone-shaped height of 0.5 cm, a cone angle of 70 degrees, and a distance of 0.3 cm between the cones. . The plaster mold is demolded and dried, and the one side is a sawtooth cone-shaped cone, and the other end is a flat microporous cera...

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Abstract

The invention discloses a method for preparing a microporous ceramic gas distribution plate for high-temperature fluidized bed reaction. The slurry composition for preparing the microporous ceramic gas distribution plate is as follows: 30 to 50 SiC particles with a particle diameter of 250 to 350 microns %, 1000 mesh SiC powder is 3-5%, Al2O3 is 3.0-5.0%, SiO2 is 1.0-2.0%, CaCO3 is 2.0-5.0% and Mg(OH)2 is 2.0-5.0%, potato flour is 1.0-5.0% % and the rest are mixed with ion-exchanged water to make a slurry, ball milled for 10-24 hours at 20-30°C, pour the obtained slurry into a plaster mold with sawtooth conical shape at one end and a flat surface at the other end, and then dry. The microporous ceramic gas distribution plate waste material obtained by demoulding and drying the plaster mold is a sawtooth cone-shaped cone on one side and a plane on the other end. It is sintered at 1350° C. to 1500° C. for 4-6 hours, and then cooled naturally to obtain a microporous ceramic gas distribution plate for high-temperature fluidized bed reaction with an overall porosity of 50-70%.

Description

technical field [0001] The invention relates to the field of ceramics, and provides a method for preparing a microporous ceramic gas distribution plate for high-temperature fluidized bed reaction. Background technique [0002] The gas distribution plate is an important component in the fluidized bed. In order to distribute the gas evenly through the distribution plate and stabilize the operation of the fluidized bed, the distribution plate must have a certain resistance. The design and manufacture of the gas distribution plate are directly related to whether the fluidized bed can operate normally. A good gas distribution plate needs to meet the requirements of good gas distribution state, small resistance, no material leakage, no clogging, simple structure, and convenient manufacturing and maintenance. For the multi-layer fluidized bed with overflow pipe and the gas distribution plate of the fluidized catalytic cracking unit, in addition to meeting the above requirements, i...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C04B38/06C04B35/565C04B35/622B01J8/44
Inventor 铁生年李昀珺李星
Owner 铁生年