Process for extracting and recovering tantalum present in an acid aqueous phase by means of an ionic liquid, and use of such an ionic liquid for extracting the tantalum from an acid aqueous phase
US-2018230572-A1 · Aug 16, 2018 · US
US2024410069A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024410069-A1 |
| Application number | US-202118717023-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 20, 2021 |
| Priority date | Dec 20, 2021 |
| Publication date | Dec 12, 2024 |
| Grant date | — |
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A method for manufacturing iron metal in an apparatus through reduction of iron ore by an electrolysis reaction, the electrolysis reaction generating a gas, the apparatus including at least one casing including a gas permeable anode plate, a cathode plate, both facing each other and being separated by an electrolyte chamber, the cathode and the anode being connected to an electric power supply, the casing being provided with a circulator for circulating an electrolyte within the chamber and with a inlet to supply iron ore to the chamber, the pressure P of the electrolyte within the casing being maintained at a value of at least Plimit and the voltage V applied between the cathode and said anode being maintained at a value of at least Vlimit, the voltage V being always kept at a value strictly below the reduction curve of the electrolyte for the pressure P.
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What is claimed is: 1 - 8 . (canceled) 9 : A method for manufacturing iron metal in an apparatus through reduction of iron ore by an electrolysis reaction, the electrolysis reaction generating a gas, the apparatus comprising at least one casing including a gas permeable anode plate, a cathode plate, both facing each other and being separated by an electrolyte chamber, the cathode plate and the anode plate being connected to an electric power supply, the casing permitting circulation of an electrolyte within the chamber and with a supply inlet to supply iron ore to the chamber, the method comprising: maintaining a pressure P of the electrolyte within the casing at a value of at least P limit and maintaining a voltage V applied between the cathode plate and the anode plate at a value of at least V limit , such P limit and V limit values being previously determined as the voltage and pressure values at an intersection of respective reduction curves showing the voltage at which the electrolysis of the electrolyte and of the iron ore occurs as a function of the pressure, the voltage V being always kept at a value strictly below the reduction curve of the electrolyte for the pressure P. 10 : The method as recited in claim 9 wherein both electrolyte and gases generated during the electrolysis reaction and flowing through the anode plate are recovered and recirculated towards the electrolyte chamber, the recirculated electrolyte being continuously degassed before re-entering the electrolyte chamber and the gases resulting from the continuous degassing step being evacuated from the casing. 11 : The method as recited in claim 10 wherein the casing of the apparatus further includes a degassing unit including an electrolyte recirculation part extending continuously from anode plate end up to a gas outlet and being in fluidic connection with the electrolyte chamber, the recirculation part including a gas-liquid partition in contact with the anode plate and extending along the recirculation part. 12 : The method as recited in claim 9 wherein the electrolyte is based on water. 13 : The method as recited in claim 12 wherein the casing is maintained at a temperature of 100 to 120° C. 14 : The method as recited in claim 13 wherein the pressure P limit is at least 24 bars. 15 : The method as recited in claim 13 wherein the pressure P limit is at least 40 bars. 16 : The method as recited in claim 9 wherein the electric power supply is fed with renewable energy.
or iron group metals, refractory metals or manganese · CPC title
Operating or servicing · CPC title
by avoiding CO2, e.g. using hydrogen · CPC title
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