Electrochemical system for the selective reduction of carbon monoxide into methanol
View Patent ↗The present invention describes an electrochemical system ( 1 ) to electrochemically reduce carbon monoxide (CO) into liquid methanol and gaseous H 2 , comprising an electrochemical cell with an anodic compartment with an anode ( 2 ) with a current collector ( 2 A), at least a catalyst to electrochemically oxidize H 2 O, and a cathodic compartment with a cathodic electrolyte solution comprising the solvent ( 3 ), and a cathodic supporting electrolyte, the solvent ( 3 ) being water at basic pH of between 10.5 and 13.5, the reagent CO; a cathode ( 4 ) which comprises, on a current collector ( 4 A) which is electrochemically inert, at least a cobalt molecular catalyst ( 4 B) to electrochemically reduce CO into liquid methanol and the gas H 2 , a power supply ( 5 ) providing the energy necessary to trigger the electrochemical reactions involving the reagent.
1. Electrochemical system to electrochemically reduce CO into liquid methanol and deliver by-product gaseous H 2 , comprising an electrochemical cell with:
an anodic compartment with:
an anode with an anode current collector, and on the anode current collector, at least a catalyst to electrochemically oxidize H 2 O to O 2 ,
an anodic electrolyte solution comprising a solvent, and an anodic supporting electrolyte, the solvent being water at a pH between 10.5 and 13.5;
a cathodic compartment with:
a cathodic electrolyte solution comprising the solvent, and a cathodic supporting electrolyte;
the reagent CO;
a cathode which comprises, on a cathode current collector which is electrochemically inert, at least a molecular catalyst to electrochemically reduce CO into liquid methanol and to deliver the by-product gaseous H 2 , the molecular catalyst comprising a cobalt phthalocyanine or substituted form thereof is selected from:
compounds having formula I:
wherein:
R 1 to R 16 are independently selected from the groups consisting of H, F, +N(C 1 -C 4 alkyl) 3 groups, or
one or several of the following specific groups R 1 , R 4 , R 5 , R 8 , R 9 , R 12 , R 13 and R 16 being a phenyl group bearing +N(C 1 -C 4 alkyl) 3 substituent in ortho position, the others of those specific groups being H;
Or the compound of formula:
a power supply providing energy necessary to trigger electrochemical reactions involving a gas reagent comprising said CO.
2. The electrochemical system according to claim 1 , wherein at least 1 and at most 8 groups among R 1 to R 16 are independently +N(C 1 -C 4 alkyl) 3 , and the other groups among R 1 to R 16 are H.
3. The electrochemical system according to claim 1 , wherein at least 1 to 16 groups among R 1 to R 16 are independently F, and the other groups among R 1 to R 16 are H.
4. The electrochemical system according to claim 1 , wherein at least 1 and at most 8 groups among R 1 , R 4 , R 5 , R 8 , R 9 , R 12 , R 13 and R 16 being are independently a phenyl group bearing a +N(C 1 -C 4 alkyl) 3 group in ortho position, and the other groups among R 1 to R 16 are H.
5. The electrochemical system according to claim 1 , wherein the molecular catalyst is a cobalt phthalocyanine CoPc of formula:
6. The electrochemical system according to claim 1 , wherein the molecular catalyst is a cobalt phthalocyanine CoPc of formula:
7. The electrochemical system according to claim 1 , wherein the solvent has a pH between 12 and 13.
8. The electrochemical system according to claim 1 , wherein the cathode comprises on the cathode current collector, an electrode film deposit which contains: the molecular catalyst, at least a binder, and optionally conductive materials as additives.
9. The electrochemical system according to claim 8 , wherein the molecular catalyst in the electrode film deposit is in a concentration of between 1 nmol·cm −2 and 100 μmol·cm −2 .
10. The electrochemical system according to claim 8 , wherein the cathode current collector is carbon paper, the binder is Nafion@ resin, the conductive materials are made of carbon nanotubes, or carbon powder, or reduced graphene oxide or graphite powder.
11. Electrochemical device to electrochemically reduce CO 2 into methanol and deliver by-product gaseous H 2 , comprising:
a first electrochemical system adapted to electrochemically reduce CO 2 into CO with a first-system molecular catalyst, and
a second electrochemical system adapted to electrochemically reduce CO into methanol and gaseous H 2 , comprising the electrochemical system according to claim 1 .
12. The electrochemical device according to claim 11 , wherein the first electrochemical system to electrochemically reduce CO 2 into CO comprises an electrochemical cell with:
a further anodic compartment with:
an anode with a further anode current collector, and on the further current collector, at least a further catalyst to electrochemically oxidize H 2 O,
a further anodic electrolyte solution comprising said solvent, and a further anodic supporting electrolyte;
a further cathodic compartment with:
a further cathodic electrolyte solution comprising the solvent, and a further cathodic supporting electrolyte;
the reagent CO 2 ;
a further cathode which comprises, on a further cathode current collector, at least a further molecular catalyst to electrochemically reduce CO 2 into CO, the further molecular catalyst being of formula I;
a further power supply providing energy necessary to trigger electrochemical reactions involving the gas reagent.
13. The electrochemical device according to claim 12 , wherein the first-system molecular catalyst is the same as the further molecular catalyst.
14. An electrochemical system comprising a flow cell adapted to electrochemically reduce a gas reactant comprising CO, passing through a gas diffusion electrode, into methanol, comprising:
an anodic compartment comprising:
an anode with an anode current collector, and on the anode current collector, a first catalyst to electrochemically oxidize H 2 O to O 2 ,
an anodic electrolyte solution, flowable at a controlled flow rate Q a , comprising: a solvent, and an anodic electrolyte, the solvent being water at a pH between 10.5 and 13.5,
an anodic electrolyte solution inlet and an anodic electrolyte solution outlet connected to the anodic compartment, adapted to circulate the anodic electrolyte solution;
a cathodic compartment comprising:
a cathodic electrolyte solution, flowable at a controlled flow rate Q c , comprising: said solvent,
a cathodic electrolyte solution inlet and a cathodic electrolyte solution outlet connected to the cathodic compartment, adapted to circulate the cathodic electrolyte solution, and remaining reagent gaseous CO and methanol by the cathodic electrolyte solution outlet;
a gas diffusion electrode comprising on an electrochemically inert gas diffusion porous current collector of surface S, a second molecular catalyst adapted to electrochemically reduce the gas reactant comprising CO into methanol in the cathodic electrolyte solution, with by-production of gaseous H2, said second molecular catalyst comprising a cobalt phthalocyanine or substituted form thereof that is selected from:
compounds having formula I:
wherein:
R 1 to R 16 are independently selected from the groups consisting of H, F, +N(C 1 -C 4 alkyl) 3 groups, or
one or several of the following specific groups R 1 , R 4 , R 5 , R 8 , R 9 , R 12 , R 13 and R 16 being a phenyl group bearing +N(C 1 -C 4 alkyl) 3 substituent in ortho position, the others of those specific groups being H;
Or the compound of formula:
an anion exchange membrane, impermeable to CO, H 2 and O 2 , between the anodic compartment and the cathodic compartment;
a channel adapted to pass the reagent gaseous CO, at a controlled flow rate Q g , through the porous surface S of the gas diffusion electrode, while the cathodic electrolyte solution circulates in between the gas diffusion electrode and the anion exchange membrane;
pumping means adapted to:
Circulate by pumping the anodic electrolyte solution in the anodic compartment and the cathodic electrolyte solution in the cathodic compartment between their respective inlets and the outlets,
Control flow by pumping gaseous CO in the channel, passing through the gas diffusion porous cathode.