Systems and methods for hydrate management
US-2017335833-A1 · Nov 23, 2017 · US
US11440796B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11440796-B2 |
| Application number | US-201816956742-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 16, 2018 |
| Priority date | Dec 22, 2017 |
| Publication date | Sep 13, 2022 |
| Grant date | Sep 13, 2022 |
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The present relates to a Metal hydride compressor control method for generating a variable output pressure P_desired_outPut, comprising a first step of inflowing gaseous hydrogen into a metal hydride compartment at a constant temperature and then stopping the gaseous hydrogen inflow, a second step of heating the metal hydride to a predetermined temperature which corresponds to a temperature which passes through the α+β phase at the desired output pressure P_desired_output, a third step of opening the output connection of the compressor and keeping it at a constant pressure by regulating the temperature to keep a constant output pressure P_desired_outPut until the system completely leaves the α+β phase.
Opening claim text (preview).
The invention claimed is: 1. Metal hydride compressor control method for generating a variable output pressure P _desired_output , comprising a first step of inflowing gaseous hydrogen into a metal hydride compartment at a constant temperature and then stopping the gaseous hydrogen inflow, a second step of heating the metal hydride to a predetermined temperature, which corresponds to a temperature, which passes through an α+β phase and leaves the α+β phase at the desired output pressure P _desired_output a third step of opening an output connection of the compressor and keeping it at a constant pressure by regulating the temperature to keep a constant output pressure P _desired_output until the system completely leaves the α+β phase. 2. Metal hydride compressor control method according to claim 1 , characterized in that the first step also comprises cooling the metal hydride to keep its temperature constant. 3. Metal hydride compressor control method to claim 1 characterized in that the first step is continued until the border of the α+β phase is reached. 4. Metal hydride compressor control method according to claim 1 characterized in that the temperature regulation is done with a control approach chosen in the group including PID control, MIMO control or control with any number of inputs and outputs and different sensing devices. 5. Metal hydride compressor control method according to claim 1 to characterized in that a connection to a gaseous hydrogen source is closed using a closing means. 6. Metal hydride compressor control method according to claim 1 characterized in that the output connection of the compressor is opened with a opening/closing means. 7. Metal hydride compressor control method according to claim 1 characterized in that at the end of step three, when the H 2 has been completely outputted, the output connection is closed and the system is cooled down. 8. Metal hydride compressor control method according to claim 1 characterized in that at the end of the cooling a further cycle starts again, to generate a different pressure than in the previous cycle by choosing a different temperature T 3 in the second step.
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