Carbon to liquids system and method of operation
A carbon to liquids system comprising: a source of syngas; a first reactor coupled in flow communication with said syngas source and configured to receive a flow of syngas therein, said first reactor comprising a polymeric material, wherein said first reactor reacts the syngas and a catalyst in a Fischer-Tropsch reaction that produces a product comprising steam, wherein the polymeric material is configured to permit the permeation of the steam therethrough; and a recycle path coupled in flow communication with said first reactor, wherein said recycle path is configured to channel the permeated steam to a vessel positioned upstream from said first reactor. A method of operating a carbon to liquids system includes receiving a flow of syngas and reacting the syngas and a catalyst to produce a product including steam. The method also includes recycling the permeated steam to a vessel positioned upstream from the reactor.
1. A carbon to liquids reactor comprising:
a reactor configured to receive a flow of cooling fluid therein,
the reactor having a passage that circumscribes at least one reactor tube present in the reactor in which syngas can be reacted in the presence of a catalyst in a Fischer-Tropsch reaction that produces a product comprising hydrocarbons and steam,
wherein the reactor tube comprises a polymeric material permeable to steam thereby enabling steam to permeate through the polymeric material into the passage, and
wherein the passage is configured to enable flow of the cooling fluid therethrough to enable contact of the cooling fluid with the permeated steam in the passage.
2. The carbon to liquids reactor of claim 1 , wherein the cooling fluid comprises natural gas.
3. The carbon to liquids reactor of claim 1 , wherein the passage is configured to channel a flow of cooling fluid therethrough to reduce the temperature of reactants in said at least one reactor tube.
4. The carbon to liquids reactor of claim 1 wherein the polymeric material is any one or more of polyamide, polyaramide, polycarbonate, aliphatic polyamides, polyesters, polycarbonates, copolycarbonate esters, polyethers, polyetherketones, polyetherimides, polyethersulfones, polyetheresters, polysulfones, polyvinylidene fluoride, polybenzimidazoles, polybenzoxazoles, polyaerylonitrile, polyazoaromatics, poly(2,6-dimethylphenylene oxide), polyphenylene oxides, polyureas, polyurethanes, polyhydrazides, polyazomethines, polyacetals, cellulosic derivatives, cellulose acetates, cellulose nitrate, ethyl cellulose, styrene-acrylonitrile copolymers, brominated poly(xylene oxide), sulfonated poly(xylylene oxide), polyquinoxaline, polyamideimides, polyamideesters, polysiloxanes, polyacetylenes, polyphosphazenes, polyolefines, polyethylene, polypropylene, polyphenylenes, poly(4-methylpentene), poly(trimethylsilylpropyne), polyesters, blends thereof, copolymers thereof, and substituted polymers thereof.
5. The carbon to liquids reactor of claim 1 , wherein the polymeric material can withstand temperatures of up to about 350° C.
6. The carbon to liquids reactor of claim 1 , wherein the polymeric material resists permeation of hydrogen and carbon monoxide therethrough.
7. The carbon to liquids reactor of claim 6 , wherein the polymeric material comprises a water-to-hydrogen separation factor of up to about 15 and a water-to-carbon monoxide separation factor of up to about 500.
8. The carbon to liquids reactor of claim 1 , wherein said at least one reactor tube is constructed at least partially of metal having the polymeric material thereon.
9. A carbon to liquids system comprising,
a source of syngas;
a cooling fluid source,
a reactor in flow communication with the syngas source and with the cooling fluid source and configured to receive a flow of syngas and a flow of cooling fluid therein,
the reactor comprising at least one reactor tube in which the syngas can be reacted in the presence of a catalyst in a Fischer-Tropsch reaction that produces a product comprising hydrocarbons and steam wherein the reactor tube comprises a polymeric material permeable to steam,
the reactor having a passage that circumscribes the at least one reactor tube comprising a polymeric material permeable to steam thereby enabling steam to flow into the passage,
wherein the passage is configured to enable flow of the cooling fluid therethrough, and
wherein passage is in flow communication with syngas source to enable recycle of a mixture of steam and the cooling fluid to the syngas source.
10. The carbon to liquids system of claim 9 wherein the cooling fluid comprises natural gas.
11. The carbon to liquids system of claim 9 wherein the syngas source comprises a catalytic partial oxidation reactor.
12. The carbon to liquids system of claim 9 wherein the syngas source comprises a steam reformer.
13. The carbon to liquids system in accordance with claim 9 wherein the polymeric material is any one or more of polyimide, polysulfone, polyamide, polyaramide, polycarbonate, aliphatic polyamides, polyesters, polycarbonates, copolycarbonate esters, polyethers, polyetherketones, polyetherimides, polyethersulfones, polyetheresters, polysulfones, polyvinylidene fluoride, polybenzimidazoles, polybenzoxazoles, polyaerylonitrile, polyazoaromatics, poly(2,6-dimethylphenylene oxide), polyphenylene oxides, polyureas, polyurethanes, polyhydrazides, polyazomethines, polyacetals, cellulosic derivatives, cellulose acetates, cellulose nitrate, ethyl cellulose, styrene-acrylonitrile copolymers, brominated poly(xylene oxide), sulfonated poly(xylylene oxide), polyquinoxaline, polyamideimides, polyamideesters, polysiloxanes, polyacetylenes, polyphosphazenes, polyolefines, polyethylene, polypropylene, polyphenylenes, poly(4-methylpentene), poly(trimethylsilylpropyne), polyesters, blends thereof, copolymers thereof, and substituted polymers thereof.
14. The carbon to liquids system in accordance with claim 9 wherein the polymeric material comprises a water-to-hydrogen separation factor of up to about 15 and a water-to-carbon monoxide separation factor of up to about 500.