Integrated process for producing carboxylic acids from carbon dioxide

• US 9,085,827 B2
• Filed: 07/03/2013
• Issued: 07/21/2015
• Est. Priority Date: 07/26/2012
• Status: Active Grant

• Current Assignee: Avantium Knowledge Centre B.V. (Avantium NV)
• Original Assignee: Liquid Light, Inc. (Avantium NV)
• Inventors: Kaczur, Jerry J., Teamey, Kyle
• Primary Examiner(s): Wilkins, III, Harry D
• Application Number:
  US13/934,500
• Publication Number:
  US 20130292257A1
• Time in Patent Office: 748 Days
• Field of Search: None
• US Class Current: 1/1
• CPC Class Codes: C07C 51/02 from salts of carboxylic acids
• CPC Class Codes: C07C 51/10 by reaction with carbon monoxide
• CPC Class Codes: C07C 51/41 Preparation of salts of carboxylic acids C07C51/093 - C07C51/34 take precedence preparation of soap C11D
• CPC Class Codes: C07C 53/06 Salts thereof
• CPC Class Codes: C07C 55/07 Salts thereof
• CPC Class Codes: C25B 1/22 Inorganic acids
• CPC Class Codes: C25B 3/23 Oxidation halogenation C25B3/27
• CPC Class Codes: C25B 3/25 Reduction
• CPC Class Codes: C25B 3/27 Halogenation
• CPC Class Codes: C25B 9/19 with diaphragms
• CPC Class Codes: Y02P 20/10 Process efficiency
• CPC Class Codes: Y02P 20/133 Renewable energy sources, e.g. sunlight
• CPC Class Codes: Y02P 20/582 Recycling of unreacted starting or intermediate materials

Abstract

The present disclosure is a method and system for production of carboxylic based chemicals, including carboxylic acids and salts. A method for producing at oxalic acid may include receiving an anolyte feed at an anolyte region of an electrochemical cell including an anode and receiving a catholyte feed including carbon dioxide and an alkali metal hydroxide at a catholyte region of the electrochemical cell including a cathode. Method may include applying an electrical potential between the anode and cathode sufficient to reduce the carbon dioxide to at least one reduction product and converting the at least one reduction product and the alkali metal hydroxide to an alkali metal oxalate via a thermal reactor. The method may further include receiving the alkali metal oxalate at an electrochemical acidification electrolyzer and converting the alkali metal oxalate to oxalic acid at the electrochemical acidification electrolyzer.

Claims

1. A method for producing oxalic acid comprising:

receiving an anolyte feed including a hydrogen halide and at least one of a alkane, haloalkane, alkene, haloalkene, aromatic compound, haloaromatic compound, heteroaromatic compound or halo-heteroaromatic compound at an anolyte region of an electrochemical cell including an anode;

receiving a catholyte feed including carbon dioxide and an alkali metal hydroxide at a catholyte region of the electrochemical cell including a cathode;

applying an electrical potential between the anode and the cathode sufficient to reduce the carbon dioxide to at least one reduction product and an anolyte product;

converting the at least one reduction product and the alkali metal hydroxide to an alkali metal oxalate via at least one thermal reactor;

receiving the alkali metal oxalate at an electrochemical acidification electrolyzer; and

converting the alkali metal oxalate to oxalic acid at an electrochemical acidification electrolyzer while co-generating an alkali metal hydroxide and a halogen.

2. The method of claim 1, wherein the hydrogen halide includes hydrogen bromide.

3. The method of claim 1, wherein the alkali metal hydroxide includes potassium hydroxide.

4. The method of claim 1, wherein the at least one reduction product includes carbon monoxide.

5. The method of claim 1, wherein converting the at least one reduction product and the alkali metal hydroxide to an alkali metal oxalate at least one thermal reactor comprises:

generating an alkali metal formate intermediate product.

6. The method of claim 5, wherein the alkali metal formate intermediate is potassium formate.

7. The method of claim 1, wherein converting the alkali metal oxalate to oxalic acid at the electrochemical acidification electrolyzer comprises:

passing the alkali metal oxalate through an ion exchange region of the electrochemical acidification electrolyzer bounded by one or more cation ion exchange membranes.

8. The method of claim 1, wherein the electrochemical acidification electrolyzer includes three compartments.

9. The method of claim 1, wherein the electrochemical acidification electrolyzer includes at least two cation exchange membranes.

10. The method of claim 1, further comprising recycling the alkali metal hydroxide co-generated at the electrochemical acidification electrolyzer to at least one of the catholyte feed.

11. The method of claim 1, further comprising recycling the alkali metal hydroxide co-generated at the electrochemical acidification electrolyzer to the at least one thermal reactor.

12. The method of claim 1, wherein the anolyte product is a halogenated compound.

13. The method of claim 12, further comprising:

removing the halogenated compound from the anolyte region; and

converting the halogenated compound to a different compound.

14. A method for producing oxalic acid comprising:

receiving an anolyte feed including a hydrogen halide and at least one of a alkane, haloalkane, alkene, haloalkene, aromatic compound, haloaromatic compound, heteroaromatic compound or halo-heteroaromatic compound at an anolyte region of an electrochemical cell including an anode;

receiving a catholyte feed including carbon dioxide and potassium hydroxide at a catholyte region of the electrochemical cell including a cathode;

applying an electrical potential between the anode and the cathode sufficient to reduce the carbon dioxide to carbon monoxide and an anolyte product;

converting the carbon monoxide and the potassium hydroxide to a potassium formate via a first thermal reactor;

converting the potassium formate to potassium oxalate via a second thermal reactor;

receiving the potassium oxalate at an electrochemical acidification electrolyzer; and

converting the potassium oxalate to oxalic acid at an electrochemical acidification electrolyzer.

15. The method of claim 14, further comprising receiving a feed of potassium hydroxide at the second thermal reactor.

16. The method of claim 14, wherein converting the potassium oxalate to oxalic acid at the electrochemical acidification electrolyzer comprises:

passing the potassium oxalate through an ion exchange region of the electrochemical acidification electrolyzer bounded by one or more cation ion exchange membranes.

17. The method of claim 14, wherein the anolyte product is a halogenated compound.

18. The method of claim 17, further comprising:

removing the halogenated compound from the anolyte region; and

converting the halogenated compound to a different compound.