Production of petrochemical feedstocks and products using a fuel cell
View Patent ↗A method of producing petrochemicals using a hydrocarbon fuel cell includes the steps of operating the fuel cell to produce electricity, thermal energy, and one or more exhaust stream, the one or more exhaust stream comprising at least a carbon-containing gas and water, reacting at least a portion of the exhaust stream with the reactant stream of natural gas to produce one or more petrochemical streams in a reactor, and heating one or more reactants using at least a portion of at least one of the electricity and the thermal energy.
1. A method of producing petrochemicals using a hydrocarbon fuel cell, comprising the steps of:
operating the fuel cell to produce electricity, thermal energy, and an exhaust stream, the exhaust stream comprising at least a carbon-containing gas and water, the fuel cell receiving a fuel stream of natural gas and a stream of atmospheric air as inputs;
heating a reactant stream of natural gas using some or all of the electricity, some or all of the thermal energy, or a combination thereof to produce a heated reactant stream of natural gas; and
combining at least a portion of the exhaust stream with the heated reactant stream of natural gas into a reactor input stream, and reacting the reactor input stream in a reactor to produce one or more petrochemical streams.
2. The method of claim 1 , wherein the carbon-containing gas and the water are produced from an anode of the fuel cell.
3. The method of claim 1 , wherein the exhaust stream further comprises a nitrogen-containing gas produced from a cathode of the fuel cell.
4. The method of claim 1 , wherein at least a portion of the thermal energy is carried by the exhaust stream.
5. The method of claim 4 , wherein the thermal energy is used to preheat the reactant stream of natural gas.
6. The method of claim 1 , wherein the one or more petrochemical streams comprises one or more petrochemicals selected from a group consisting of: synthesis gas, methanol, ammonia, urea, polymers, prepolymers, hydrocarbon fuels, acetic acid, and glycol.
7. The method of claim 1 , further comprising the step of separating the carbon-containing gas and the water into separate streams using heat exchangers and phase separators.
8. The method of claim 1 , wherein the reactant stream of natural gas and the at least a portion of the exhaust stream is preconditioned in heat exchangers using the thermal energy produced by the fuel cell.
9. The method of claim 1 , further comprising the step of powering at least one of material handling equipment and heating equipment of the reactor using electricity produced by the fuel cell.
10. The method of claim 1 , wherein the reactant stream of natural gas comprises a slipstream of the fuel stream of natural gas.
11. The method of claim 1 , wherein substantially all of the carbon in the carbon-containing gas is consumed in the reactor.
12. The method of claim 1 , wherein the reactor conducts two or more reactions in parallel or in series.
13. The method of claim 1 , wherein the at least a portion of the exhaust stream is mixed with the reactant stream of natural gas upstream of the reactor, the exhaust stream comprising a heated stream of carbon-containing gas and water vapor.
14. The method of claim 13 , wherein the reactor is a tri-reform reactor (TRM) that produces methanol.
15. The method of claim 14 , wherein the TRM is cooled by an expanded stream of natural gas, the reactant stream of natural gas being derived from the expanded stream of natural gas.