Advanced aromatic amine heterocyclic catalysts for carbon dioxide reduction
US-9090976-B2 · Jul 28, 2015 · US
US10287696B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10287696-B2 |
| Application number | US-201414471152-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 28, 2014 |
| Priority date | Jul 26, 2012 |
| Publication date | May 14, 2019 |
| Grant date | May 14, 2019 |
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Methods and systems for electrochemical conversion of carbon dioxide to organic products including formate and formic acid are provided. A method may include, but is not limited to, steps (A) to (C). Step (A) may introduce an acidic anolyte to a first compartment of an electrochemical cell. The first compartment may include an anode. Step (B) may introduce a bicarbonate-based catholyte saturated with carbon dioxide to a second compartment of the electrochemical cell. The second compartment may include a high surface area cathode including indium and having a void volume of between about 30% to 98%. At least a portion of the bicarbonate-based catholyte is recycled. Step (C) may apply an electrical potential between the anode and the cathode sufficient to reduce the carbon dioxide to at least one of a single-carbon based product or a multi-carbon based product.
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What is claimed is: 1. A method for electrochemical reduction of carbon dioxide into products, comprising: (A) introducing an acidic anolyte to a first compartment of a first electrochemical cell, the first compartment including an anode; (B) introducing a catholyte including an alkali metal bicarbonate to a second compartment of the first electrochemical cell, the catholyte saturated with carbon dioxide, the second compartment including a high surface area cathode, the high surface area cathode including a coating containing indium and having a void volume of between about 30% to 98%, at least a portion of the catholyte including the alkali metal bicarbonate being recycled; (C) applying an electrical potential between the anode and the cathode sufficient to reduce the carbon dioxide to an alkali metal formate; (D) introducing the alkali metal formate to an ion exchange compartment of a second electrochemical cell; (E) applying an electrical potential between an anode of the second electrochemical cell and a cathode of the second electrochemical cell sufficient to produce at least formic acid and an alkali metal hydroxide; (F) introducing the alkali metal hydroxide with carbon dioxide to generate at least a portion of the alkali metal bicarbonate introduced to the second compartment of the first electrochemical cell; and (G) separating the alkali metal formate from the alkali metal bicarbonate of the catholyte of the first electrochemical cell with a nano-filtration system, wherein the nano-filtration system separates monovalent anions from divalent anions. 2. The method of claim 1 , wherein separating the alkali metal formate from the alkali metal bicarbonate of the catholyte of the first electrochemical cell with a nano-filtration system comprises: introducing the alkali metal bicarbonate of the catholyte to an alkali metal hydroxide to convert at least a portion of the alkali metal bicarbonate to an alkali metal carbonate; and separating the alkali metal carbonate from the alkali metal formate with a nano-filtration unit. 3. The method of claim 2 , further comprising: introducing the alkali metal carbonate with the alkali metal hydroxide and with carbon dioxide to generate at least a portion of the alkali metal bicarbonate introduced to the second compartment of the first electrochemical cell. 4. The method of claim 1 , wherein at least a portion of the alkali metal hydroxide is generated by one or more of the first electrochemical cell and the second electrochemical cell. 5. The method of claim 1 , wherein the formic acid is generated in the ion exchange compartment of the second electrochemical cell. 6. The method of claim 1 , wherein the alkali metal hydroxide is generated in a cathode compartment of the second electrochemical cell. 7. The method of claim 1 , wherein the high surface area cathode has a specific surface area of greater than 2 cm 2 /cm 3 . 8. The method of claim 1 , wherein the acidic anolyte includes sulfuric acid. 9. The method of claim 1 , further comprising: generating a halogen selected from the group consisting of F 2 , Cl 2 , Br 2 , and I 2 in at least one of the first compartment of the first electrochemical cell and the first compartment of the second electrochemical cell. 10. The method of claim 9 , further comprising: reacting the halogen with an organic compound to produce a halogenated product. 11. The method of claim 10 , wherein the halogen is bromine. 12. The method of claim 9 , wherein the halogen is bromine. 13. The method of claim 1 , wherein the high surface area cathode includes from 5% to 99% as indium in alloy with bismuth.
Operating or servicing cells · CPC title
Chemistry & Metallurgy · mapped topic
Chemistry & Metallurgy · mapped topic
Supplying or removing reactants or electrolytes; Regeneration of electrolytes · CPC title
Chemistry & Metallurgy · mapped topic
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