US2014221684A1PendingUtilityA1
Electrochemical Co-Production of Chemicals Utilizing a Halide Salt
Est. expiryJul 26, 2032(~6 yrs left)· nominal 20-yr term from priority
C25B 9/19C25B 3/25C25B 3/23C25B 9/23C25B 3/27C25B 3/29Y02P20/129C25B 1/24Y02P20/582C25B 15/08Y02P20/10C07C 1/26Y02P20/133C07C 51/15C25B 3/00C07C 67/08C07C 29/149C07C 29/58C25B 1/00C07C 51/367C25B 15/00C25B 13/08C07C 51/02C25B 3/04
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Claims
Abstract
The present disclosure includes a system and method for co-producing a first product and a second product. The system may include a first electrochemical cell, at least one second reactor, and an acidification chamber. The method and system for co-producing a first product and a second product may include co-producing a carboxylic acid and at least one of an alkene, alkyne, aldehyde, ketone, or an alcohol while employing a recycled halide salt.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A method for co-producing M-carboxylate and a halogen, the method comprising the steps of:
contacting a first region of an electrochemical cell having a cathode with a catholyte comprising carbon dioxide; contacting a second region of the electrochemical cell having an anode with an anolyte comprising an MX where M is at least one cation and X is selected from the group consisting of F, Cl, Br, I and mixtures thereof; applying an electrical potential between the anode and the cathode of the electrochemical cell sufficient to produce the M-carboxylate recoverable from the first region of the electrochemical cell and the halogen recoverable from the second region of the electrochemical cell; reacting the halogen from the second region of the electrochemical cell with one of an alkane, an alkene, or an aromatic to produce a halogenated compound and HX.
2 . The method according to claim 1 , further comprising:
recycling the HX back to an acidification chamber.
3 . The method according to claim 2 , further comprising:
reacting the M-carboxylate with the HX via the acidification chamber to produce a carboxylic acid and MX, the MX being recycled to an input of the second region of the electrochemical cell.
4 . The method according to claim 3 , further comprising:
reacting the halogenated compound via a third reactor to produce a second product and HX, the HX being recycled to the acidification chamber.
5 . The method according to claim 1 , wherein the halogen includes at least one of F 2 , Cl 2 , Br 2 or I 2 .
6 . The method according to claim 1 , wherein the halogenated compound includes at least one of a brominated compound, benzyl bromide, (1-bromethyl)benzene, perhalocarbon, bromoethane, vinyl chloride, dichloroethane, allyl chloride, chlorophenol, bromobenzene, vinyl bromide, vinyl fluoride, vinylidene fluoride, tetrafluoroethylene, hexafluoropropylene, difluoromethane, or pentafluoroethane.
7 . The method according to claim 4 , wherein the second product is at least one of an alkane, an alkene, an alkyne, an alcohol, an aldehyde, or a ketone.
8 . The method according to claim 4 , wherein the third reactor includes water.
9 . The method according to claim 8 , wherein the second product is an alcohol.
10 . The method according to claim 4 , wherein the carboxylic acid is oxalic acid.
11 . The method according to claim 4 , further comprising:
feeding the carboxylic acid to a thermal hydrogenation chamber, the thermal hydrogenation chamber comprising H 2 ; and forming a third product in the thermal hydrogenation chamber.
12 . The method according to claim 11 , wherein the third product includes at least one of glyoxylic acid, glycolic acid, glyoxal, glycolaldeyde, ethylene glycol, ethanol, acetic acid, acetaldehyde, ethane, or ethylene.
13 . The method according to claim 1 , wherein the cathode and the anode of the first electrochemical cell and the second electrochemical cell are separated by an ion permeable barrier that operates at a temperature less than 600 degrees C.
14 . The method according to claim 13 , wherein the ion permeable barrier includes one of a polymeric or inorganic ceramic-based ion permeable barrier.
15 . The method according to claim 1 , wherein the catholyte is a liquid and the anolyte is a gas.
16 . A method for co-producing M-carboxylate and bromine, the method comprising the steps of:
contacting a first region of an electrochemical cell having a cathode with a catholyte comprising carbon dioxide; contacting a second region of the electrochemical cell having an anode with an anolyte comprising an MBr where M is at least one cation; applying an electrical potential between the anode and the cathode of the electrochemical cell sufficient to produce the M-carboxylate recoverable from the first region of the electrochemical cell and the bromine recoverable from the second region of the electrochemical cell; reacting the bromine from the second region of the electrochemical cell with an alkane to produce a halogenated compound and HBr.
17 . The method according to claim 16 , further comprising:
recycling the HBr back to an acidification chamber.
18 . The method according to claim 17 , further comprising:
reacting the M-carboxylate with the HBr via the acidification chamber to produce a carboxylic acid and MBr, the MBr being recycled to an input of the second region of the electrochemical cell.
19 . The method according to claim 18 , wherein the alkane is ethane.
20 . The method according to claim 19 , wherein the halogenated compound is bromoethane.
21 . The method according to claim 20 , wherein M is tetrabutylammonium.Cited by (0)
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