Systems and methods for local generation and/or consumption of hydrogen gas
Systems for producing hydrogen gas for local distribution, consumption, and/or storage, and related devices and methods are disclosed herein. A representative system includes a pyrolysis reactor system that can be coupled to a supply of reaction material that includes a hydrocarbon. The pyrolysis reactor system includes one or more combustion components positioned to transfer heat to the reaction material to convert the hydrocarbon into an output that includes hydrogen gas and carbon particulates. The pyrolysis reactor system also includes a carbon separation system positioned to separate the hydrogen gas the carbon particulates in the output. In various embodiments, the system also includes components to locally consume the filtered hydrogen gas, such as a power generator, heating appliance, and/or a combined heat and power device.
1 . A pyrolysis reactor system for generating hydrogen gas for local distribution, consumption, and/or storage, the pyrolysis reactor system comprising:
an autothermal pyrolysis reactor having a heating region, wherein a reactant is directed through the heating region, wherein the heating region is in thermal communication with a combustion component, and wherein the reactant includes a hydrocarbon;
a combustion component thermally coupleable to a supply of a combustion fuel and configured to combust, in the combustion component, the combustion fuel to indirectly heat the reactant in the heating region of the autothermal pyrolysis reactor above a reaction temperature, wherein, at the reaction temperature, at least a portion of the hydrocarbon in the reactant converts into an output that includes hydrogen gas and carbon particulates; and
a carbon separation component configured to separate at least a portion of the carbon particulates from the hydrogen gas in the output.
2 . The pyrolysis reactor system of claim 1 wherein the combustion component comprises a downfired burner system.
3 . The pyrolysis reactor system of claim 1 , further comprising an air supply fluidly coupled to the combustion component to control a supply of oxygen to the combustion of the combustion fuel.
4 . The pyrolysis reactor system of claim 1 wherein the output further includes one or more byproduct gases, and wherein the pyrolysis reactor system further comprises a gas separator fluidly coupled to the carbon separation system to receive the output downstream of the carbon separation system to remove at least a portion the byproduct gases from the hydrogen gas in the output.
5 . The pyrolysis reactor system of claim 1 wherein the combustion fuel includes hydrogen gas from a previous pyrolysis reaction in the autothermal pyrolysis reactor.
6 . A method for generating hydrogen gas for local distribution, consumption, and/or storage, the method comprising:
directing a reactant through a heating region of an autothermal pyrolysis reactor, wherein the heating region is in thermal communication with a combustion component, wherein reactant includes a hydrocarbon;
combusting, in the combustion component, a combustion fuel to indirectly heat the reactant in the heating region of the autothermal pyrolysis reactor above a reaction temperature, wherein, at the reaction temperature, at least a portion of the hydrocarbon in the reactant converts into an output that includes hydrogen gas and carbon particulates; and
separating at least a portion of the carbon particulates from the hydrogen gas in the output.
7 . The method of claim 6 , further comprising directing at least a portion of the hydrogen gas in the output to at least one of:
a power generation component to generate electricity from a combustion of the at least a portion of the hydrogen gas; and
the combustion component to direct heat from a combustion of the at least a portion of the hydrogen gas into the heating region of the autothermal pyrolysis reactor.
8 . The method of claim 6 wherein the output further includes one or more byproduct gases, and wherein the method further comprises removing at least a portion of the one or more byproduct gases from the hydrogen gas in the output.
9 . The method of claim 6 wherein the reactant is natural gas, and wherein the method further comprises receiving the natural gas through a gas meter.
10 . The method of claim 6 , further comprising directing at least a portion of the hydrogen gas in the output to a residential and/or commercial heating unit.
11 . The method of claim 6 , further comprising directing at least a portion of the hydrogen gas in the output to a residential and/or commercial boiler.
12 . The method of claim 6 wherein separating at least a portion of the carbon particulates from the hydrogen gas in the output includes removing the carbon particulates from the output through a mechanical carbon separation device.
13 . The method of claim 6 wherein separating at least a portion of the carbon particulates from the hydrogen gas in the output includes removing the carbon particulates from the output through a fluidic carbon separation device.
14 . The method of claim 6 , further comprising directing, through a point-to-point connection, at least a portion of the hydrogen gas in the output to a power generation component.
15 . The method of claim 6 wherein the combustion fuel comprises hydrogen gas, and wherein the method further comprises directing a portion of the hydrogen gas in the output to the combustion component.
16 . The method of claim 15 wherein the portion of the hydrogen gas fully fuels the combustion component.
17 . The method of claim 6 , further comprising recuperating heat from the output to preheat oxygen upstream from the combustion component.
18 . The method of claim 6 , wherein the combustion component comprises a downfired burner system.
19 . The method of claim 6 , further comprising actuating a carbon removal component within the autothermal pyrolysis reactor to remove a portion of the carbon particulates from the output.
20 . The method of claim 6 , further comprising driving a rotatable body within the autothermal pyrolysis reactor to remove a portion of the carbon particulates from the output.
21 . The method of claim 6 , wherein the reactant is directed at a flow rate of from 500 to 165,000,000 standard cubic centimeters per minute.