Electrocatalytic process for carbon dioxide conversion
An electrocatalytic process for carbon dioxide conversion includes combining a Catalytically Active Element and a Helper Polymer in the presence of carbon dioxide, allowing a reaction to proceed to produce a reaction product, and applying electrical energy to said reaction to achieve electrochemical conversion of said carbon dioxide reactant to said reaction product. The Catalytically Active Element can be a metal in the form of supported or unsupported particles or flakes with an average size between 0.6 nm and 100 nm. The reaction products comprise at least one of CO, HCO − , H 2 CO, (HCO 2 ) − , H 2 CO 2 , CH 3 OH, CH 4 , C 2 H 4 , CH 3 CH 2 OH, CH 3 COO − , CH 3 COOH, C 2 H 6 , (COOH) 2 , (COO − ) 2 , and CF 3 COOH.
1. A process for making a chemical reaction product, comprising:
(a) combining a Catalytically Active Element and Helper Polymer in the presence of CO 2 , wherein the Catalytically Active Element is a metal in the form of supported or unsupported particles or flakes with an average size between 0.6 nm and 100 nm;
(b) allowing a reaction to proceed to produce a reaction product; and
(c) applying electrical energy to said reaction to achieve electrochemical conversion of at least a portion of said CO 2 to said reaction product;
wherein a polymer P is identifiable as a Helper Polymer for an electrochemical reaction R that is catalyzed by a Catalytically Active Element M by applying a test comprising:
(i) preparing two different membrane electrode assemblies with 5 cm 2 of active area: i) one having the polymer P in the cathode catalyst layer; and ii) one otherwise identical but without the polymer P in the cathode catalyst layer, wherein the weight of the polymer in the catalyst layer is 4% of the weight of the catalytically active element M in the catalyst layer;
(ii) mounting both membrane electrode assemblies in a Fuel Cell Technologies 5 cm 2 fuel cell hardware assembly with serpentine flow fields;
(iii) providing CO 2 humidified at 50° C. to the cathode of both cells at a rate of 5 sccm with the cell at room temperature and pressure, with the anode side left open to the atmosphere at room temperature and pressure;
(iv) applying a voltage of 1 V to the cell without the polymer P, and then raising the cell voltage to a voltage V such that the output current is as least 20 mA/cm 2 , then recording the current output of the cell after running for 30 minutes;
(v) applying the same voltage V to the cell with the polymer P and recording the current output of the cell after running for 30 minutes; and
(vi) designating the polymer P as a Helper Polymer if the current is at least 20% higher in the cell with the polymer P in the catalyst layer than the cell without the polymer P in the catalyst layer.
2. The process of claim 1 wherein said Catalytically Active Element is selected from the group consisting of V, Cr, Mn, Fe, Co, Ni, Cu, Sn, Zr, Nb, Mo, Ru, Rh, Pd, Ag, Cd, Hf, Ta, W, Re, Ir, Pt, Au, Hg, Al, Si, In, Tl, Pb, Bi, Sb, Te, U, Sm, Tb, La, Ce, and Nd.
3. The process of claim 2 wherein said Catalytically Active Element is selected from the group consisting of Pt, Pd, Au, Ag, Cu, Ni, Fe, Co, Ru and Rh.
4. The process of claim 1 wherein said Helper Polymer is selected from the group consisting of polymers containing positively charged cyclic amines, phosphines, imidazoliums, pyridiniums, pyrrolidiniums, phosphoniums, sulfoniums, prolinates, methioninates, and cholines.
5. The process of claim 1 wherein the reaction products comprise at least one of CO, HCO − , H 2 CO, (HCO 2 ) − , H 2 CO 2 , CH 3 OH, CH 4 , C 2 H 4 , CH 3 CH 2 OH, CH 3 COO − , CH 3 COOH, C 2 H 6 , (COOH) 2 , (COO − ) 2 , and CF 3 COOH.
6. The process of claim 5 wherein said reaction product is one of formic acid (H 2 CO 2 ) and carbon monoxide (CO).
7. The process of claim 1 , wherein the Catalytically Active Element is electrically connected to an electrode of an electrochemical device.