Apparatuses and methods for hydrogen production
The present disclosure provides systems and methods for hydrogen production as well as apparatuses useful in such systems and methods. Hydrogen is produced by steam reforming of a hydrocarbon in a gas heated reformer that is heated using one or more streams comprising combustion products of a fuel in an oxidant, preferably in the presence of a carbon dioxide circulating stream.
1. A hydrogen production system comprising:
a reactor comprising a pressure containment vessel and at least one set of reaction tubes positioned within the pressure containment vessel and arranged to receive reactants for an endothermic reaction that forms a synthesis gas stream comprising at least hydrogen and carbon monoxide, the pressure containment vessel being configured to receive a stream of heated carbon dioxide as a source of convective heating of the endothermic reaction carried out within the at least one set of reaction tubes;
at least one component effective to process the synthesis gas and deliver a stream of substantially pure hydrogen product;
at least one shift reactor configured to convert at least a portion of the carbon monoxide in the synthesis gas from the reactor to carbon dioxide and output a shift stream comprising at least hydrogen, carbon dioxide, and waste gas, the at least one shift reactor being arranged between the reactor and the at least one component effective to process the synthesis gas and deliver a stream of substantially pure hydrogen; and
at least one component effective to provide the stream of heated carbon dioxide;
wherein the at least one set of reaction tubes comprises: an outer catalyst tube; an inner reaction product gas tube; and catalyst material positioned within a space defined between an inside surface of the outer catalyst tube and an outside surface of the inner reaction product gas tube;
wherein the at least one set of reaction tubes is arranged vertically so that an upper end of the at least one set of reaction tubes defines a hot end where the reactor operates with a higher temperature, and a lower end of the at least one set of reaction tubes defines a cold end where the reactor operates with a lower temperature relative to the hot end; and
wherein the reactor comprises an inlet arranged so that the stream of heated carbon dioxide enters the reactor, contacts the hot end of the at least one set of reaction tubes, and flows downwardly around an outer surface of the outer catalyst tube toward a second outlet through which the stream of heated carbon dioxide leaves the reactor.
2. The hydrogen production system of claim 1 , wherein the reactor further comprises an upper tube sheet that is arranged to functionally align with the outer catalyst tube, and a lower tube sheet that is arranged to functionally align with the inner reaction product gas tube.
3. The hydrogen production system of claim 2 , wherein the reactor comprises an opening into a space defined between the upper tube sheet and the lower tube sheet, the opening being arranged to receive the reactants so that the reactants pass upwardly, from the cold end toward the hot end, through the space within which the catalyst material is positioned.
4. The hydrogen production system of claim 2 , wherein the reactor comprises synthesis gas outlet that is positioned below the lower tube sheet.
5. The hydrogen production system of claim 1 , wherein the at least one component effective to provide the stream of heated carbon dioxide is a combustor configured to combust a fuel with oxygen in the presence of a stream comprising predominately carbon dioxide and form a combustion product stream that defines the stream of heated carbon dioxide.
6. The hydrogen production system of claim 5 , further comprising one or more components configured to direct at least a portion of the stream of heated carbon dioxide leaving the reactor to the combustor in the stream comprising predominately carbon dioxide.
7. The hydrogen production system of claim 1 , wherein the at least one component effective to process the synthesis gas and deliver a stream of substantially pure hydrogen product comprises a hydrogen isolation unit.
8. The hydrogen production system of claim 7 , wherein the hydrogen isolation unit comprises a hydrogen multi-bed pressure swing adsorber (PSA) configured to output a pressurized stream of substantially pure hydrogen and output a stream comprising a waste gas.
9. The hydrogen production system of claim 1 , wherein the upper end of the at least one set of reaction tubes defines a filling tube with a removable plug.
10. The hydrogen production system of claim 1 , further comprising a steam generator arranged between the reactor and the at least one shift reactor.
11. The hydrogen production system of claim 1 , further comprising a recuperative heat exchanger arranged between the at least one shift reactor and the at least one component effective to process the synthesis gas and deliver a stream of substantially pure hydrogen product.
12. A hydrogen production system comprising:
a reactor comprising an outer vessel and at least one set of reaction tubes positioned within the outer vessel, the at least one set of reaction tubes being arranged to receive reactants for an endothermic reaction that forms a synthesis gas stream comprising at least hydrogen and carbon monoxide, and the at least one set of reaction tubes being arranged vertically within the outer vessel to define a hot end where the reactor operates with a higher temperature, and a cold end where the reactor operates with a lower temperature, relative to the hot end;
at least one component effective to process the synthesis gas and deliver a stream of substantially pure hydrogen product;
at least one shift reactor configured to convert at least a portion of the carbon monoxide in the synthesis gas from the reactor to carbon dioxide and output a shift stream comprising at least hydrogen, carbon dioxide, and waste gas, the at least one shift reactor being arranged between the reactor and the at least one component effective to process the synthesis gas and deliver a stream of substantially pure hydrogen;
at least one component effective to provide the stream of heated carbon dioxide;
a reactor inlet that is configured to receive a stream of heated carbon dioxide as a source of convective heating of the endothermic reaction carried out within the at least one set of reaction tubes, the reactor inlet being arranged so that the stream of heated carbon dioxide received in the reactor contacts the hot end of the at least one set of reaction tubes and flows around an outer surface of the at least one set of reaction tubes; and
a reactor outlet through which the stream of heated carbon dioxide passes from the reactor.
13. The hydrogen production system of claim 12 , wherein the at least one set of reaction tubes comprises: an outer catalyst tube; an inner reaction product gas tube; and
catalyst material positioned within a space defined between an inside surface of the outer catalyst tube and an outside surface of the inner reaction product gas tube.
14. The hydrogen production system of claim 13 , wherein the reactor further comprises an upper tube sheet that is arranged to functionally align with one of the outer catalyst tube and the inner reaction product gas tube, and a lower tube sheet that is arranged to functionally align with an other of the outer catalyst tube and the inner reaction product gas tube.
15. The hydrogen production system of claim 14 , wherein the reactor comprises an opening into a space defined between the upper tube sheet and the lower tube sheet, the opening being arranged to receive the reactants so that the reactants pass from the cold end toward the hot end through the space within which the catalyst material is positioned.
16. The hydrogen production system of claim 12 , wherein the at least one component effective to provide the stream of heated carbon dioxide is a combustor configured to combust a fuel with oxygen in the presence of a stream comprising predominately carbon dioxide and form a combustion product stream that defines the stream of heated carbon dioxide.
17. The hydrogen production system of claim 16 , further comprising one or more components configured to direct at least a portion of the stream of heated carbon dioxide from the reactor outlet to the combustor in the stream comprising predominately carbon dioxide.
18. The hydrogen production system of claim 12 , wherein the reactor comprises a synthesis gas outlet.
19. The hydrogen production system of claim 12 , wherein an upper end of the at least one set of reaction tubes defines the hot end, and a lower end of the at least one set of reaction tubes defines the cold end.
20. The hydrogen production system of claim 12 , wherein the at least one set of reaction tubes includes a filling tube.
21. The hydrogen production system of claim 12 , wherein the at least one component effective to process the synthesis gas and deliver a stream of substantially pure hydrogen product comprises a hydrogen multi-bed pressure swing adsorber (PSA) configured to output a pressurized stream of substantially pure hydrogen and output a stream comprising a waste gas.
22. The hydrogen production system of claim 12 , further comprising a steam generator arranged between the reactor and the at least one shift reactor.
23. The hydrogen production system of claim 12 , further comprising a recuperative heat exchanger arranged between the at least one shift reactor and the at least one component effective to process the synthesis gas and deliver a stream of substantially pure hydrogen product.