Process for producing carbonyl iron
A production method, carbonyl iron technology, applied in the direction of carbonyl iron, etc., can solve the problems of difficult preparation, poor chemical stability, easy decomposition, etc., and achieve the effect of simple operation, short process and high metal recovery rate
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Embodiment 1
[0012] Put 1000Kg of pig iron into the synthesis reactor, control the temperature of the synthesis reactor at 105°C and the pressure of 23.5Mpa, and feed CO gas with a flow rate of 5000L / h into the synthesis reactor. The CO content in the CO gas is ≥70%, O 2 <0.4%. After the reaction starts, pass the carbonyl compound gas drawn out into a condenser, control the condensation temperature at 25°C, and obtain 2302L of carbonyl iron liquid, pass the carbonyl iron liquid and CO gas through a three-stage separator, and the pressures are 23.5MPa, 10MPa, and At normal pressure, all the CO gas dissolved in the liquid is released to obtain the carbonyl iron product.
Embodiment 2
[0014] Put 1000Kg of pig iron into the synthesis reactor, control the temperature of the synthesis reactor at 155°C and the pressure of 17.5Mpa, and feed CO gas with a flow rate of 5000L / h into the synthesis reactor. The CO content in the CO gas is ≥70%, O 2 <0.4%. After the reaction starts, pass the carbonyl compound gas drawn out into a condenser, control the condensation temperature to 25°C, and obtain 2313L of carbonyl iron liquid, pass the carbonyl iron liquid and CO gas through a three-stage separator, and the pressures are 17.5MPa, 10MPa, and At normal pressure, all the CO gas dissolved in the liquid is released to obtain the carbonyl iron product.
Embodiment 3
[0016] Put 1000Kg of pig iron into the synthesis reactor, control the temperature of the synthesis reactor at 215°C and the pressure of 12.5Mpa, and feed CO gas with a flow rate of 5000L / h into the synthesis reactor. The CO content in the CO gas is ≥70%, O 2 <0.4%. After the reaction starts, pass the carbonyl compound gas drawn out into a condenser, control the condensation temperature at 25°C, and obtain 2309L of carbonyl iron liquid, pass the carbonyl iron liquid and CO gas through a three-stage separator, and the pressures are 12.5MPa, 5MPa, and At normal pressure, all the CO gas dissolved in the liquid is released to obtain the carbonyl iron product.
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