Method for preparing carbonyl iron through medium pressure continuous gasification
A carbonyl iron, medium-pressure technology, which is applied in the field of medium-pressure continuous gasification to prepare carbonyl iron, can solve the problems of low production efficiency and long auxiliary time.
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Embodiment 1
[0014] The ferroalloy powder is controlled to enter the bottom of the synthesis kettle at a feed rate of 50kg / h, and the 7MPa CO gas is heated to 150°C at a feed rate of 1000NM3 / h and then passed into the bottom of the synthesis kettle. The primary copper-iron alloy powder flows upward from the bottom driven by the CO gas flow. The mixed gas obtained at the top of the continuous synthesis kettle is passed through the dust collector, and the primary ferroalloy reaction residue is obtained at the bottom of the dust collector. The mixed gas drawn from the top of the dust collector passes through the gas heat exchanger and condenser to obtain carbonyl iron liquid and CO gas containing a small amount of carbonyl iron. After the mixed gas passes through the pyrolysis device, a small amount of carbonyl iron powder and pure CO gas are obtained. CO gas is sent into the synthesis kettle through a gas compressor to re-participate in the continuous carbonyl carbonylation reaction of iron c...
Embodiment 2
[0016] The ferroalloy powder is controlled to enter the bottom of the synthesis kettle at a feeding rate of 80kg / h. 8MPa CO gas is heated to 180°C at a feeding rate of 1500NM3 / h and then passed into the bottom of the synthesis kettle. The ferroalloy powder flows upward from the bottom driven by the CO gas flow. The mixed gas obtained from the top of the continuous synthesis kettle is passed through the dust collector, and the ferroalloy reaction residue is obtained at the bottom of the dust collector. The mixed gas drawn from the top of the dust collector passes through the gas heat exchanger and condenser to obtain carbonyl iron liquid and CO gas containing a small amount of carbonyl iron. After the mixed gas passes through the pyrolysis device, a small amount of carbonyl iron powder and pure CO gas are obtained. CO gas is sent into the synthesis kettle through a gas compressor to re-participate in the continuous carbonylation reaction of carbonyl iron, and the reaction ends a...
Embodiment 3
[0018] The ferroalloy powder is controlled to enter the bottom of the synthesis kettle at a feeding rate of 120kg / h. 8Mpa CO gas is heated to 180°C at a feeding rate of 1500NM3 / h and then passed into the bottom of the synthesis kettle. The ferroalloy powder flows upward from the bottom driven by the CO gas flow. The mixed gas obtained from the top of the continuous synthesis kettle is passed through the dust collector, and the ferroalloy reaction residue is obtained at the bottom of the dust collector. The mixed gas drawn from the top of the dust collector passes through the gas heat exchanger and condenser to obtain carbonyl iron liquid and CO gas containing a small amount of carbonyl iron. After the mixed gas passes through the pyrolysis device, a small amount of carbonyl iron powder and pure CO gas are obtained. CO gas is sent into the synthesis kettle through a gas compressor to re-participate in the continuous carbonyl carbonylation reaction of iron carbonyl, and the react...
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