Method for preparing carbonyl iron
A carbonyl iron and preparation process technology, applied in the direction of carbonyl iron, etc., can solve the problems of reduced reaction rate in the carbonylation process, low activity of sponge iron, increased production costs, etc., and achieve the goal of increasing carbonylation rate, simple operation, and easy realization Effect
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Embodiment 1
[0012] Put 4 tons of sponge iron with an iron content of 96.8% in the reactor, and after compression and heating by a heater, pure carbon monoxide gas at 8.5MPa and 200°C enters the reactor to react with the sponge iron, and continuously feeds carbon monoxide Gas, the reaction period is 3 days, and finally produces carbonyl iron liquid 5.82m 3 , The carbonylation rate of sponge iron is 61%.
Embodiment 2
[0014] Put iron content at 96.8%, 4 tons of the same batch of sponge iron in the reactor, use a high-pressure compressor to 3 The 3% decomposition gas is pressurized to 8.5MPa, and the mixed gas is compressed and heated by a heater, so that the mixed gas at 8.5MPa and 200°C enters the reactor to react with the sponge iron. The reaction period is 3 days, and finally produces carbonyl iron liquid 6.68m 3 , The carbonylation rate of sponge iron is 70%.
Embodiment 3
[0016] Put iron content at 96.8%, 4 tons of the same batch of sponge iron in the reactor, use a high-pressure compressor to 3 The decomposed gas after 5% decarburization is pressurized to 8.5MPa, and the mixed gas is compressed and heated by a heater, so that the mixed gas at 8.5MPa and 200°C enters the reactor to react with the sponge iron. The reaction period is 3 days, and finally produces carbonyl iron liquid 7.16m 3 , The carbonylation rate of sponge iron is 75%.
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