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Copper catalyst, preparation method and application thereof

A copper catalyst and catalyst technology, applied in catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems affecting the stability and economy of the device, the lack of pertinence of reaction conditions, and the difficulty of fluidized state. control and other issues, to achieve the effect of easy control of fluidization state, good reaction conditions, and good thermal stability

Inactive Publication Date: 2018-06-22
HENAN NORMAL UNIV
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Problems solved by technology

However, the existing catalysts have the following disadvantages during use: 1. The supported catalyst needs to be reduced in advance, and the catalyst residue may burn during the unloading process, which is inconvenient to use; 2. The alloy catalyst reacts in a fluidized bed Its fluidized state in the device is not easy to control; 3. CuCl or CuCl 2 It is a general-purpose catalyst in the industry, lacks the pertinence of the reaction conditions, and its particle size and density are poorly matched with Si. It is difficult to control the fluidized state in the fluidized bed reactor, and after being lost, it enters the follow-up system as an impurity, affecting the overall performance of the device. stability and economy

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  • Copper catalyst, preparation method and application thereof

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preparation example Construction

[0020] The present invention also provides the catalyst prepared according to the preparation method of the present invention in SiCl 4 Conversion to prepare SiHCl 3 in the application. During implementation, the above application conditions are: reaction temperature 450-580°C, reaction pressure 1.5-4.0Mpa, H 2 : SiCl 4 (Molar ratio) is (1-5): 1. Gas hourly space velocity 500-100000h ‐1 . The reactor used in the above reaction is a fixed bed reactor or a fluidized bed reactor. In actual production, in order to make SiCl 4 All converted to SiHCl 3 , for the reaction H 2 and Si relative to SiCl 4 Large excess, therefore, the field usually uses SiCl 4 Convert to SiHCl 3 Expressed by the calculated conversion rate, that is, the conversion rate (%) = SiHCl generated 3 moles / SiCl 4 The total moles of raw materials and the conversion rate in this specification are calculated by this method. In the present invention, gas hourly space velocity refers to hydrogen and SiCl ...

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Abstract

The invention relates to a copper catalyst, a preparation method and application thereof. The catalyst comprises 1-50wt% of CuCl or CuCl2, 10-90wt% of Cu and 1-50wt% of Si. The preparation method comprises the following steps: firstly, heating and melting components of the contents, rapidly cooling and curing the molten mixture, further crushing, and screening, thereby obtaining the copper catalyst. Compared with a common catalyst, the catalyst provided by the invention has the advantages of being convenient to use, relatively good in reaction working condition and Si granule matching property, relatively easy in fluidized state control in a fluidized bed reactor, having relatively good thermal stability, and having an relatively good activity.

Description

technical field [0001] The invention relates to a copper catalyst, a preparation method and application thereof. Background technique [0002] In recent years, solar energy has developed rapidly because of its cleanness, safety and abundant resources. Demand for high-purity polysilicon as a raw material for solar cells is increasing. In the mainstream process of polysilicon production, about 20t of SiCl is produced in the production of 1t of polysilicon 4 . In order to reduce the material consumption of polysilicon production, thereby reducing production costs and avoiding environmental pollution, the most effective and economical method is to use SiCl 4 Convert to SiHCl 3 , SiHCl 3 As a raw material, it returns to the polysilicon production system, thus forming a "closed-loop" production. [0003] At present, the industrial SiCl 4 Conversion to produce SiHCl 3 The mainstream technical route is SiCl 4 Cold hydrogenation, that is, under the action of certain temperat...

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/122B01J27/128B01J27/13B01J37/08C01B33/107
CPCB01J27/122B01J27/128B01J27/13B01J37/08C01B33/10757
Inventor 杨宗献路战胜任延涛耿振铎王天兴周忠坡杨新伟
Owner HENAN NORMAL UNIV
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