초록 ▼

Systems and methods for initiating startup of PSA assemblies in hydrogen-processing assemblies, which may include a hydrogen-generation assembly and/or a fuel cell stack. The systems and methods include startup procedures that provide for pressurization of the adsorbent beds of the PSA assembly with

Systems and methods for initiating startup of PSA assemblies in hydrogen-processing assemblies, which may include a hydrogen-generation assembly and/or a fuel cell stack. The systems and methods include startup procedures that provide for pressurization of the adsorbent beds of the PSA assembly without the need for a stored quantity or other supply of purified hydrogen gas. The systems and methods additionally or alternatively include startup procedures that restrict or even prevent contamination of portions of the PSA assembly, hydrogen storage devices and/or accumulator tanks with an impure gas stream and/or decrease accumulation of the impure gas stream therein. This impure gas stream may be the mixed gas, reformate, or other gas stream that is intended to be purified by the PSA assembly when the PSA assembly is in its hydrogen-purifying operating state.

대표청구항 ▼

1. A method for controlling the startup of a pressure swing adsorption (PSA) assembly that is configured to receive a mixed gas stream and to produce a product hydrogen stream and a byproduct stream therefrom, the method comprising: supplying the mixed gas stream to the PSA assembly;controlling a pr

1. A method for controlling the startup of a pressure swing adsorption (PSA) assembly that is configured to receive a mixed gas stream and to produce a product hydrogen stream and a byproduct stream therefrom, the method comprising: supplying the mixed gas stream to the PSA assembly;controlling a pressure associated with a portion of the PSA assembly to a setpoint pressure using a flow regulating assembly, wherein the flow regulating assembly is configured to receive the product hydrogen stream from the PSA assembly and to selectively discharge the product hydrogen stream to maintain the pressure associated with the portion of the PSA assembly at the setpoint pressure, and further wherein the flow regulating assembly is in fluid communication with and upstream from an accumulator tank;detecting the pressure associated with the portion of the PSA assembly;performing PSA startup cycling, wherein the PSA startup cycling is initiated responsive to detecting that the pressure associated with the portion of the PSA assembly is at least a threshold PSA assembly pressure;accumulating at least a portion of the product hydrogen stream in the accumulator tank, wherein the accumulating is initiated after the PSA startup cycling is initiated;detecting a pressure associated with the accumulator tank; andceasing controlling the pressure associated with the portion of the PSA assembly responsive to detecting that the pressure associated with the accumulator tank is at least a threshold accumulator tank pressure. 2. The method of claim 1, wherein the method further comprises determining that the PSA startup cycling has completed, and further wherein the accumulating is initiated responsive to determining that the PSA startup cycling has completed. 3. The method of claim 1, wherein the method further includes providing the product hydrogen stream discharged from the flow regulating assembly to a hydrogen disposal device. 4. The method of claim 3, wherein the method further includes ceasing the providing the product hydrogen stream discharged from the flow regulating assembly to the hydrogen disposal device, wherein the ceasing the providing is subsequent to the determining that the PSA startup cycling has completed. 5. The method of claim 1, wherein the flow regulating assembly includes a back pressure regulator and the method includes controlling the pressure associated with the portion of the PSA assembly with the back pressure regulator. 6. The method of claim 5, wherein the flow regulating assembly includes a fixed orifice valve in parallel with the back pressure regulator, and further wherein ceasing the controlling the pressure associated with the portion of the PSA assembly includes opening the fixed orifice valve to bypass the back pressure regulator. 7. The method of claim 1, wherein the flow regulating assembly includes a variable orifice valve and the method includes controlling the pressure associated with the portion of the PSA assembly by controlling the variable orifice valve. 8. The method of claim 1, wherein the threshold PSA assembly pressure is at least one of less than the setpoint pressure and equal to the setpoint pressure. 9. The method of claim 1, wherein controlling the pressure associated with the portion of the PSA assembly includes selectively discharging the product hydrogen stream from the flow regulating assembly as a pressure control stream when the pressure associated with the portion of the PSA assembly is above the setpoint pressure. 10. The method of claim 9, wherein the selectively discharging includes flowing the pressure control stream through the accumulator tank. 11. The method of claim 9, wherein the selectively discharging includes bypassing the accumulator tank with at least a portion of the pressure control stream. 12. The method of claim 1, wherein performing the PSA startup cycling includes performing at least one reduced-duration PSA cycle. 13. The method of claim 1, wherein the method further includes producing the mixed gas stream. 14. The method of claim 13, wherein producing the mixed gas stream includes supplying at least one feedstock stream to a hydrogen-producing region and producing the mixed gas stream in the hydrogen-producing region, wherein the method further includes controlling a flow rate of the at least one feedstock stream to the hydrogen-producing region, wherein the method further includes detecting a flow rate of the mixed gas stream, and further wherein controlling the flow rate of the at least one feedstock stream includes controlling the flow rate of the at least one feedstock stream responsive to the flow rate of the mixed gas stream. 15. The method of claim 14, wherein the method further includes detecting a pressure associated with the product hydrogen stream, and further wherein, subsequent to determining that the PSA startup cycling has completed, the method includes controlling the flow rate of the at least one feedstock stream responsive to the pressure associated with the product hydrogen stream. 16. The method of claim 1, wherein the PSA assembly includes a plurality of adsorbent beds, and further wherein the portion of PSA assembly includes at least a portion of the plurality of adsorbent beds.