Environmentally friendly system and method for manufacturing iron powder
A low-temperature process of producing high-purity iron powder by feeding hematite and a reducing agent into a rotary reactor under pressure to form a mechanical fluid bed. The fluid bed is rotated at a particular speed within a rotary reactor. The fluid bed is simultaneously heated to a reaction temperature, and the pressure is then reduced within the rotary reactor to a pressure in a range of 0.01 bars to 2.0 bars, as a result reducing the reaction temperature to a temperature in a range of 600° C. to 850° C. Maintaining the pressure and the rotation results in the formation of a high-purity iron oxide without the requirement for post-grinding process steps because sintering is prevented by using a combination of pressure reduction and a rotary set at an optimum rotation speed, resulting in useful additives produced by a more environmentally-friendly process.
1. A process of producing high-purity iron powder, comprising the steps of:
feeding hematite and a reducing agent into a rotary reactor to form a mechanical fluid bed;
rotating said mechanical fluid bed with a rotation speed in the range of 6 to 100 rpm;
heating said mechanical fluid bed to a reaction temperature of up to 1100° C.;
reducing pressure within said rotary reactor to a pressure in a range of 0.01 bars to 2.0 bars, as a result reducing said reaction temperature to a temperature in a range of 600° C. to 850° C.; and,
maintaining said pressure and said rotation to form said high-purity iron powder.
2. The process of claim 1 , wherein prior to the step of feeding, said hematite is discharged to a grinding mill such that said hematite is milled to reduce agglomerates.
3. The process of claim 1 , wherein said reducing agent is selected from the group consisting of coal, hydrogen, natural gas, ammonia, and carbon powder.
4. The process of claim 1 , further comprising the step of cooling said high-purity iron powder to below 60° C.
5. The process of claim 1 , wherein each said particle of said high-purity iron powder has a particle size in a range of 0.5 μm to 40 μm.
6. The process of claim 5 , wherein 95% of said high-purity iron powder has a particle size of under 5 μm.
7. The process of claim 1 , wherein said high-purity iron powder has a purity of up to 99.7%.
8. The process of claim 1 , further comprising the step of injecting a process gas into said mechanical fluid bed to form an off-gas.
9. The process of claim 8 , further comprising the step of processing said off-gas through a thermal oxidizer.
10. The process of claim 8 , wherein said process gas is selected from the group consisting of ammonia, hydrogen, and natural gas.
11. The process of claim 8 , further comprising the step of treating said off-gas to retain CO 2 and H 2 O, leaving in a stream only N 2 , a small amount of H 2 , and traces of CO, as a result producing an inert gas blanket.
12. The process of claim 11 , further comprising the step of injecting said inert gas blanket into said mechanical fluid bed to prevent re-oxidation of said high-purity iron powder.