IP Library Granted Patent US 8,845,878
Granted Patent B2
US 8,845,878 · App. 13/787,304 · Granted Sep 30, 2014

Reducing carbon dioxide to products

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Quick Facts
Patent No.
US 8,845,878
App. No.
13/787,304
Granted
Sep 30, 2014
Kind
B2
Abstract

A method reducing carbon dioxide to one or more products may include steps (A) to (C). Step (A) may bubble said carbon dioxide into a solution of an electrolyte and a catalyst in a divided electrochemical cell. The divided electrochemical cell may include an anode in a first cell compartment and a cathode in a second cell compartment. The cathode may reduce said carbon dioxide into said products. Step (B) may adjust one or more of (a) a cathode material, (b) a surface morphology of said cathode, (c) said electrolyte, (d) a manner in which said carbon dioxide is bubbled, (e), a pH level of said solution, and (f) an electrical potential of said divided electrochemical cell, to vary at least one of (i) which of said products is produced and (ii) a faradaic yield of said products. Step (C) may separate said products from said solution.

Claims (20)

1. A method for reducing carbon dioxide to one or more products, comprising:

(A) bubbling said carbon dioxide into a solution of an electrolyte and a catalyst in a divided electrochemical cell, wherein (i) said divided electrochemical cell comprises an anode in a first cell compartment and a cathode in a second cell compartment, (ii) said cathode reducing said carbon dioxide into carbon monoxide, and (iii) said catalyst is a homogeneous heterocyclic amine catalyst and said cathode is selected from the group consisting of Al, Au, Ag, Bi, C, Cd, Co, Cr, Cu, a Cu alloy, Ga, Hg, In, Mo, Nb, Ni, NiCo2O4, a Ni alloy, a Ni—Fe alloy, Pb, Rh, Sn, a Sn alloy, Ti, V, W, Zn, elgiloy, Nichrome, austenitic steel, duplex steel, ferritic steel, martensitic steel, stainless steel, degenerately doped p-Si, degenerately doped p-Si:As, degenerately doped p-Si:B, degenerately doped n-Si, degenerately doped n-Si:As, degenerately doped n-Si:B, and mixtures thereof;

(B) separating said carbon monoxide from said solution.

2. The method according to claim 1 , wherein said homogeneous heterocyclic amine catalyst is one or more of adenine, an amine containing sulfur, an amine containing oxygen, an azole, benzimidazole, a bipyridine, furan, an imidazole, an imidazole-related species with at least one five-member ring, an indole, methylimidazole, an oxazole, phenanthroline, pterin, pteridine, a pyridine, a pyridine-related species with at least one six-member ring, pyrrole, quinoline, and a thiazole.

3. The method according to claim 1 , wherein said electrolyte is at least one of Na2SO4, KHCO3, KCl, NaNO 3 , NaCl, NaF, NaClO 4 , KClO 4 , K 2 SiO 3 , CaCl 2 , a guanidinium cation, a H cation, an alkali metal cation, an ammonium cation, an alkylammonium cation, a halide ion, an alkyl amine, a borate, a carbonate, a guanidinium derivative, a nitrite, a nitrate, a phosphate, a polyphosphate, a perchlorate, a silicate, a sulfate, and a tetraalkyl ammonium salt.

4. The method according to claim 3 , further comprising:

introducing to said solution of said electrolyte at least one of a divalent cation including at least one of calcium, magnesium, or zinc.

5. The method according to claim 1 , wherein said manner in which said carbon dioxide is bubbled comprises:

bubbling said carbon dioxide to contact said cathode.

6. The method according to claim 1 , wherein said manner in which said carbon dioxide is bubbled comprises:

bubbling said carbon dioxide to avoid contact with said cathode.

7. The method according to claim 1 , wherein said solution has a pH between approximately 1 and approximately 8.

8. The method according to claim 1 , wherein said stainless steel includes at least one of SS 2205, SS 304, SS 316, and SS 321; and wherein said Sn alloy includes at least one of SnAg, SnPb, SnSb.

9. The method according to claim 1 , wherein said cathode is selected from the group consisting of Sn, SnAg, SnPb, SnSb and mixtures thereof.

10. The method according to claim 1 , wherein said catalyst includes quinoline.

11. The method according to claim 10 , wherein the catalyst has a concentration of 10 to 100 mM.

12. The method according to claim 1 , wherein the electrolyte includes KCl.

13. The method according to claim 12 , wherein the electrolyte has a concentration of 0.25 to 1M.

14. The method according to claim 1 , wherein the cathode has a potential of −1 to −1.4 volts vs SCE.

15. The method according to claim 1 , wherein the solution has a pH of 5 to 7.

Assignments (5)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 27, 2017
From: AVANTIUM HOLDING B.V.
To: AVANTIUM KNOWLEDGE CENTRE B.V.
Reel/Frame 041214/0698 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 13, 2017
From: ARES CAPITAL CORPORATION
To: AVANTIUM HOLDING B.V.
Reel/Frame 041033/0406 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 7, 2016
From: LIQUID LIGHT, INC.
To: ARES CAPITAL CORPORATION
Reel/Frame 040644/0921 →
CONFIRMATORY LICENSE Recorded Dec 30, 2014
From: LIQUID LIGHT, INC.
To: ENERGY, UNITED STATES DEPARTMENT OF
Reel/Frame 034752/0660 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 23, 2013
From: COLE, EMILY BARTON; SIVASANKAR, NARAYANAPPA; PARAJULI, RISHI; KEETS, KATE A.
To: LIQUID LIGHT, INC.
Reel/Frame 030488/0289 →