Check patentability & draft patents in minutes with Patsnap Eureka AI!

Polycrystalline silicon cold hydrogenation method adopting gas-solid parallel flow downer reactor

A reactor and polysilicon technology, applied in chemical instruments and methods, silicon compounds, silicon halide compounds, etc., can solve problems such as gas short circuit, economic loss, environmental pollution, etc., and achieve single-pass yield improvement, sufficient and uniform reaction, and reaction efficiency high effect

Active Publication Date: 2021-02-19
TIANJIN UNIV
View PDF1 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The gas-solid fluidized bed reaction is easy to produce a ring nucleus structure, which is easy to form a gas short circuit, which reduces the conversion rate of SiCl4 and affects the single-pass yield of SiHCl3
In addition, the fluidized silicon powder and catalyst are easily carried out of the reactor, resulting in a large amount of slurry
The loss of a large amount of slurry not only pollutes the environment, but also brings serious economic losses

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Polycrystalline silicon cold hydrogenation method adopting gas-solid parallel flow downer reactor
  • Polycrystalline silicon cold hydrogenation method adopting gas-solid parallel flow downer reactor

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] A single-stage gas-solid co-flow down-flow reactor (see figure 1 and figure 2 (a) The cold hydrogenation method of polysilicon comprises the following steps: silicon powder and solid catalyst CuCl are mixed with preheated H 2 and preheated vaporized SiCl 4 The gas is fed from the upper part of the single-stage gas-solid co-current down-flowing bed reactor 1, and reacted at a reaction temperature of 400°C and a reaction pressure of 1.5MPa to obtain SiHCl-containing 3 The gas-solid mixture is extracted from the bottom of the reactor and enters the gas-solid separator (cyclone separator) 2 for separation; respectively obtain SiHCl carrying a small amount of impurities 3 The gas is sent to the downstream separation and refining section, and the separated silicon powder and solid catalyst CuCl mixture is re-introduced from the upper part of the reactor to realize the recycling of silicon powder and solid catalyst.

[0023] h 2 , silicon powder, solid catalyst CuCl and S...

Embodiment 2

[0026] Adopt multistage (3 stage) gas-solid co-flow down-bed reactor (see figure 1 and figure 2 (b)) the polysilicon cold hydrogenation method, comprises the steps: silicon powder and solid catalyst Ni and the H of preheating (preheating to 600 ℃) 2 and preheated vaporized SiCl 4 The gas is added from the upper part of the reactor 1, and the reaction temperature is 600° C., and the reaction pressure is 3.5 MPa to react to obtain SiHCl-containing 3 The gas-solid mixture is extracted from the bottom of the reactor and enters the gas-solid separator (cyclone separator) 2 for separation; respectively obtain SiHCl carrying a small amount of impurities 3 The gas is sent to the downstream separation and refining section, and the mixture of the separated silicon powder and solid catalyst Ni is re-introduced from the upper part of the reactor to realize the recycling of silicon powder and solid catalyst Ni.

[0027] h 2 , silicon powder, solid catalyst CuCl and SiCl 4 The gas mas...

Embodiment 3

[0031] Adopt the polysilicon cold hydrogenation method of multi-stage (2 stages) gas-solid co-current down-flow bed reactor (see figure 1 ), comprising the steps of: silicon powder and solid catalyst (mass ratio is 1:1 of CuCl and CuCl 2 mixture) with preheated (preheated to 550°C) H 2 and preheated vaporized SiCl 4 The gas is added from the upper part of the reactor 1, and the reaction temperature is 550° C., and the reaction pressure is 3 MPa to react to obtain SiHCl-containing 3 The gas-solid mixture is extracted from the bottom of the reactor and enters the gas-solid separator (membrane separator) 2 for separation; respectively obtain SiHCl carrying a small amount of impurities 3 The gas is sent to the downstream separation and refining section, and the separated silicon powder and solid catalyst mixture is re-introduced from the upper part of the reactor to realize the recycling of silicon powder and solid catalyst.

[0032] The H 2 , silicon powder, solid catalyst an...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention discloses a polycrystalline silicon cold hydrogenation method adopting a gas-solid parallel flow downer reactor. The method comprises the following steps: adding silicon powder, a solidcatalyst, preheated H2 and preheated and vaporized SiCl4 gas from the upper portion of a reactor, reacting to obtain a gas-solid mixture containing SiHCl3, extracting the gas-solid mixture from the bottom of the reactor, and separating in a gas-solid separator; and obtaining SiHCl3 gas carrying impurities, and sending to a downstream separation and refining section, and introducing a mixture of silicon powder obtained through separation and the solid catalyst into the reactor again from the upper portion of the reactor. According to the invention, the gas-solid ring core structure of the ascending fluidized bed reactor is eliminated, the reaction is sufficient and uniform, and the efficiency is high; the silicon powder and the catalyst are taken out less during reaction and are recycled, so that the utilization rate of the silicon powder is high, and the yield of the slurry is greatly reduced; the single-pass yield of SiHCl3 is increased to 30% or above; and the method has the advantages of simple operation, high efficiency, energy saving, economy and environmental protection.

Description

technical field [0001] The invention belongs to the technical field of polysilicon manufacture, and specifically relates to a polysilicon cold hydrogenation method using a gas-solid co-current down-bed reactor. Background technique [0002] With the increasing consumption of traditional fossil energy, today's energy is becoming increasingly tense, and environmental pressure is increasing. It is increasingly urgent and important to find a new type of alternative energy. Due to its advantages of safety, cleanliness, richness and high efficiency, solar energy has gradually received more and more attention from people. Polysilicon is the basic raw material of crystalline silicon photovoltaic materials, and its price has a great influence on the cost of crystalline silicon photovoltaic materials. The traditional polysilicon production process is mainly the improved Siemens method. For every ton of polysilicon produced, the by-products produced are about 15 tons of SiCl 4 , by-p...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
IPC IPC(8): C01B33/107
CPCC01B33/10763
Inventor 张金利李豪杰李韡刘玉东郭俊恒彭茂
Owner TIANJIN UNIV
Features
  • R&D
  • Intellectual Property
  • Life Sciences
  • Materials
  • Tech Scout
Why Patsnap Eureka
  • Unparalleled Data Quality
  • Higher Quality Content
  • 60% Fewer Hallucinations
Social media
Patsnap Eureka Blog
Learn More