System and process for the production of renewable fuels and chemicals
A renewable fuel production system includes a carbon dioxide capture unit for extracting carbon dioxide from atmospheric air, a carbon dioxide electrolyzer for converting carbon dioxide to carbon monoxide, a water electrolyzer for converting water to hydrogen, a synfuels generator for converting carbon monoxide produced by the carbon dioxide electrolyzer and hydrogen produced by the water electrolyzer to a fuel. The fuel produced can be synthetic gasoline and/or synthetic diesel. A renewable fuel production process includes the steps of extracting carbon dioxide from atmospheric air via a carbon dioxide capture unit, converting carbon dioxide to carbon monoxide via a carbon dioxide electrolyzer, converting water to hydrogen via a water electrolyzer, and converting carbon monoxide produced via the carbon dioxide electrolyzer and H 2 produced via the water electrolyzer to a fuel. The system is also capable of simultaneously or alternatively producing a separate industrial chemical.
1. A system for the manufacture of renewable fuels and/or renewable chemicals comprising:
(a) a CO 2 electrolyzer for converting CO 2 to CO and O 2 , wherein said CO 2 electrolyzer has a CO selectivity of at least 90%;
(b) a separate water electrolyzer for converting H 2 O to H 2 and O 2 ;
(c) a control unit for directing signals to each of said electrolyzers to vary the ratio of CO to H 2 produced by said electrolyzers; and
(d) a series of reactors to convert a CO/H 2 mixture to fuels and/or chemicals,
wherein said CO 2 electrolyzer operates in the temperature range of 40° C. to 120° C.
2. A system for the manufacture of renewable fuels and/or renewable chemicals comprising:
(a) a CO 2 electrolyzer for converting CO 2 to CO;
(b) a water electrolyzer for converting H 2 O to H 2 ;
(c) a mixer for mixing the CO with the H 2 ;
(d) a control unit to vary the ratio of CO to H 2 according to which product is being produced; and
(e) a series of reactors to convert the CO/H 2 mixture to fuels and/or chemicals,
wherein said CO 2 electrolyzer operates in the temperature range of 40° C. to 120° C.,
wherein said CO 2 electrolyzer comprises an anion-conducting polymeric membrane comprising a terpolymer of styrene, vinylbenzyl-Rs and vinylbenzyl-Rx,
wherein Rs is a positively charged cyclic amine group,
wherein Rx is at least one constituent selected from the group consisting of Cl, OH and a reaction product between an OH or Cl and a species other than a simple amine or a cyclic amine,
wherein the total weight of the vinylbenzyl-Rx groups is 1-25% of the total weight of the terpolymer, and
wherein the total weight of the vinylbenzyl-Rs groups is at least 30% of the total weight of the terpolymer.
3. The system of claim 2 , wherein Rs is tetra-methyl-imidazolium.
4. The system in claim 1 , wherein the system is capable of produce at least one fuel and at least one chemical.
5. The system of claim 4 , wherein said fuel is at least one of synthetic gasoline, synthetic diesel, synthetic avgas, and a blend-stock therefor.
6. The system of claim 4 , wherein the chemical is at least one of methanol, dimethylether, ethanol and propylene.
7. The system of claim 1 , wherein said series of reactors comprises at least 3 reactors.
8. The system of claim 7 , wherein a first reactor of said series of reactors converts the CO and H 2 to methanol, wherein a second reactor coverts methanol to dimethyl ether, and wherein a third reactor converts dimethyl ether to at least one of a synthetic fuel and a chemical.
9. The system of claim 8 , wherein the reactor that converts dimethyl ether to a synthetic fuel or chemical comprises a zeolite catalyst.
10. The system of claim 9 , wherein said zeolite catalyst is a micropore zeolite catalyst.
11. The system of claim 10 , wherein the zeolite catalyst has an SiO 2 /Al 2 O 3 weight ratio of 2 to 9, a BET surface of 250 to 500 m 2 /g, and an Na content under 200 ppm.
12. The system of claim 1 , wherein said CO 2 electrolyzer comprises:
(a) a cathode prepared as follows: Silver ink is made by mixing 2 mg carbon black, 0.2 ml of a 1% solution of the membrane polymer and 0.5 ml ethanol is sonicated for 5 minutes; 100 mg of silver nanoparticles (20-40 nm) with 1.5 ml ethanol is added and then sonicated for 5 more minutes; the silver ink is then hand-painted onto a gas diffusion layer covering an area of 5 cm×5 cm; the gas diffusion layer is sintered at 80° C. for 15 min followed by 120° C. for 15 minutes; the gas diffusion layer is then soaked in a 1 M KOH bath for 1 hour with the painted side face down; and
(b) an anode prepared as follows: IrO 2 ink is made by mixing 100 mg of IrO 2 with 1 ml deionized water, 2 ml isopropanol and 0.101 ml of 5% NAFION solution; the IrO 2 ink is then hand-painted onto a 5% wet proofed carbon fiber paper covering an area of 6 cm×6 cm; then, it is sintered at 80° C. for 30 minutes;
(c) an anion-conducting polymeric membrane interposed between the inked sides of said cathode and said anode to form a membrane electrode assembly, said membrane electrode assembly mounted in a fuel cell hardware assembly with serpentine reactant flow field channels, said membrane meeting the following test:
when (i) CO 2 humidified at 65° C. is fed into the cathode at a rate of 20 sccm and 10 mM KHCO 3 is fed into the anode flow field at a flow rate of 3 ml/min, (ii) the cell is heated to 50° C., (iii) a power supply interconnects said cathode and said anode, (iv) the cell is maintained at 3 V for 2 hours, and then switched to constant current mode at 200 mA/cm 2 ; (v) the cell is maintained in constant current mode for at least 100 hours, (vi) selectivity is calculated as follows:
Selectivity
=
(
CO
production
rate
)
(
CO
production
rate
+
H
2
production
rate
)
and (vii) CO and H 2 production rates are measured in standard cubic centimeters per minute exiting the cell, selectivity is greater than 90%, and the voltage to maintain 200 mA/cm 2 is less than 3 V.