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
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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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