Microwave processing multi-phase fluidized bed reactor and process for treating phosphogypsum

A multi-phase fluidized bed and microwave treatment technology, applied in the field of reactors, can solve the problems such as the inability of gas to form a standard flow field, the inability to achieve local control of gas, and the inability to achieve local heating, so as to improve the chemical reaction rate and improve chemical Effect of reaction rate, enhanced two-phase flow and heat and mass transfer efficiency

Active Publication Date: 2018-07-24
SICHUAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the microwave fluidized bed high-pressure reactor solves the problem of fluidized bed high-pressure reaction, the control of local heating cannot be realized in the fluidized bed high-pressure reactor, and the gas cannot form a standardized flow field in the reactor.
At the same time, the waveguide is connected to the inner cavity of the reactor, so the waveguide will affect the reaction environment in the reactor. In order to avoid the influence of the waveguide on the reaction environment in the inner cavity of the reactor, an isolation mechanism is set up, which makes the structure more complicated.
Finally, the microwave is directly introduced into the reactor, so the heating of the reactor by the microwave is the overall heating, and it is impossible to realize local control and control the flow field of the gas by controlling the heating temperature

Method used

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  • Microwave processing multi-phase fluidized bed reactor and process for treating phosphogypsum
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  • Microwave processing multi-phase fluidized bed reactor and process for treating phosphogypsum

Examples

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Effect test

Embodiment 1

[0087] Industrial reaction of phosphogypsum by microwave treatment in a multiphase fluidized bed reactor: S 2 (g)+CaSO 4 →CaS+2SO 2 (g) process, including the following steps:

[0088] A, liquid sulfur and solid calcium sulfate particles are injected into the reactor 2 along the feed port 5; the molar ratio of the solid calcium sulfate particles and liquid sulfur is 1:10;

[0089] B. The bottom of the reactor 2 is heated by the microwave generator 3 corresponding to the gasification deposition chamber 23 on the microwave reflecting shell 1, and the inside of the reactor 2 is heated by the microwave generator 3 corresponding to the fluidization reaction chamber 24 on the microwave reflecting shell 1. The material is heated; so that the temperature of sulfur reaches 200 ° C;

[0090] C, control the pressure in the reactor 2, so that the pressure in the reactor 2 is less than 1Mpa;

[0091] D, the gas obtained by the reaction of sulfur and calcium sulfate is discharged throug...

Embodiment 2

[0093] Industrial reaction of phosphogypsum by microwave treatment in a multiphase fluidized bed reactor: S 2 (g)+CaSO 4 →CaS+2SO 2 (g) process, including the following steps:

[0094] A, liquid sulfur and solid calcium sulfate particles are injected into the reactor 2 along the feed port 5; the molar ratio of the solid calcium sulfate particles and liquid sulfur is 1:5;

[0095] B. The bottom of the reactor 2 is heated by the microwave generator 3 corresponding to the gasification deposition chamber 23 on the microwave reflecting shell 1, and the inside of the reactor 2 is heated by the microwave generator 3 corresponding to the fluidization reaction chamber 24 on the microwave reflecting shell 1. The material is heated; so that the temperature of sulfur reaches 400 ° C;

[0096] C, control the pressure in the reactor 2, so that the pressure in the reactor 2 is less than 1Mpa;

[0097] D, the gas obtained by the reaction of sulfur and calcium sulfate is discharged through...

Embodiment 3

[0099] Industrial reaction of phosphogypsum by microwave treatment in a multiphase fluidized bed reactor: S 2 (g)+CaSO 4 →CaS+2SO 2 (g) process, including the following steps:

[0100] A, liquid sulfur and solid calcium sulfate particles are injected into the reactor 2 along the feed port 5; the molar ratio of the solid calcium sulfate particles and liquid sulfur is 1:3;

[0101] B. The bottom of the reactor 2 is heated by the microwave generator 3 corresponding to the gasification deposition chamber 23 on the microwave reflecting shell 1, and the inside of the reactor 2 is heated by the microwave generator 3 corresponding to the fluidization reaction chamber 24 on the microwave reflecting shell 1. The material is heated; the temperature of sulfur reaches 600°C;

[0102] C, control the pressure in the reactor 2, so that the pressure in the reactor 2 is less than 1Mpa;

[0103] D, the gas obtained by the reaction of sulfur and calcium sulfate is discharged through the exhau...

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Abstract

The invention discloses a microwave processing multi-phase fluidized bed reactor and a process for treating phosphogypsum, in the microwave processing multi-phase fluidized bed reactor, a reactor canbe heated divisionally, material flow fields in the reactor can be controlled, the reactor and microwave generators are separately arranged, the microwave processing multi-phase fluidized bed reactorcomprises the microwave-penetrable reactor and a microwave-reflecting shell sleeving the lower portion of the reactor, and the microwave generators, which are distributed from bottom to top and transmit microwave to a microwave-reflecting chamber, are arranged on the microwave-reflecting shell. The process for treating the phosphogypsum comprises the following steps: placing solid calcium sulfateparticles and liquid sulfur in a molar ratio of 1:1 to 1:10 in the reactor; heating the reactor through the microwave generators, controlling the pressure inside of the reactor to less than 1Mpa; andafter the reaction is completed, discharging a material. The microwave processing multi-phase fluidized bed reactor and the process for treating the phosphogypsum can enhance the heat and mass transfer efficiency among gas, liquid and solid three phases, reduce subsequent separation cost, save the process, and increase the chemical reaction rate.

Description

technical field [0001] The invention relates to a microwave-heated reactor and its application, in particular to a microwave-treated multiphase fluidized-bed reactor and a process for treating phosphogypsum with a microwave-treated multiphase fluidized-bed reactor. Background technique [0002] As we all know, chemical reactions often require heating or high temperature and high pressure. Traditional heating methods are based on heat conduction and heat convection. This method makes the reaction speed slower, and the selectivity and yield are not up to standard. Therefore, we are committed to speeding up the reaction rate, enhancing the yield, improving the selectivity, simplifying the post-treatment process, and improving the production efficiency of chemical reactions as a whole. [0003] Phosphogypsum, as an important renewable gypsum resource, is a solid waste discharged from the production of wet-process phosphoric acid. At present, the process of producing sulfuric ac...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J8/24B01J8/42C01F11/08C01B17/50
CPCB01J8/24B01J8/42B01J2208/00442C01B17/503C01F11/08
Inventor 孔行健杨秀山张萍娱王辛龙张志业
Owner SICHUAN UNIV
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