System and methods for separation of electrolytic iron from iron-containing feedstock
AssigneeForm Energy, Inc.
InventorsJanna Rathert, Alex Luyima, Joseph Stephen Manser
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AssigneeForm Energy, Inc.
InventorsJanna Rathert, Alex Luyima, Joseph Stephen Manser
Estimating the term…
An electrochemical reactor system includes: an electrochemical cell, having: an anode; a cathode; an electrolyte stream including an electrolyte and an iron-containing feedstock containing feedstock particles; and a channel that contains the electrolyte stream; and a magnetic field source positioned to provide a magnetic field at the surface of the cathode. The electrochemical cell electrochemically reduces the iron-containing feedstock to form iron particles at a surface of the cathode and in the magnetic field. The feedstock particles have an average particle size in at least one dimension of 10 micrometers or less, and the iron particles have an average particle size in at least one dimension of 50 to 1,000 micrometers, or the feedstock particles have an average particle size in at least one dimension of 25 micrometers or greater, and the iron particles have an average particle size in at least one dimension of 0.1 to 20 micrometers.
An electrochemical reactor system, comprising:
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The electrochemical reactor system of any one of the preceding claims, wherein the electrolyte stream contained within the electrochemical cell comprises from 0.1 to 30 wt % of the iron-containing feedstock, based on a total weight of the electrolyte stream contained within the electrochemical cell, wherein the iron-containing feedstock comprises hematite, maghemite, magnetite, goethite, limonite, or a combination thereof, wherein the iron particles comprise greater than 90 wt % of iron metal, or a combination thereof.
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The electrochemical reactor system of any one of the preceding claims, wherein a current density at the cathode for the reduction of the iron-containing feedstock is from 40 to 5,000 milliamperes per square centimeter, wherein the at least a portion of the iron-containing feedstock is electrochemically reduced to form the iron particles at a current efficiency of at least 0.6, wherein the current efficiency is a ratio of charge used for the reduction of the iron-containing feedstock to a total charge provided to the cathode, or a combination thereof.
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Dependencies are inferred from the claim text.