Hydrogen generator
US-9005572-B2 · Apr 14, 2015 · US
US11837764B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11837764-B2 |
| Application number | US-202016809178-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 4, 2020 |
| Priority date | Sep 5, 2017 |
| Publication date | Dec 5, 2023 |
| Grant date | Dec 5, 2023 |
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Methods and devices and aspects thereof for generating power using PEM fuel cell power systems comprising a rotary bed (or rotatable) reactor for hydrogen generation are disclosed. Hydrogen is generated by the hydrolysis of fuels such as lithium aluminum hydride and mixtures thereof. Water required for hydrolysis may be captured from the fuel cell exhaust. Water is preferably fed to the reactor in the form of a mist generated by an atomizer. An exemplary 750 We-h, 400 We PEM fuel cell power system may be characterized by a specific energy of about 550 We-h/kg and a specific power of about 290 We/kg. Turbidity fixtures within the reactor increase turbidity of fuel pellets within the reactor and improve the energy density of the system.
Opening claim text (preview).
We claim: 1. A method of generating electrical power, the method comprising: providing fuel pellets ( 600 ) in a rotatable reactor ( 509 ) containment insert ( 1000 ); controlling an addition of pressurized liquid into the containment insert; rotating at least the reactor during the pressurized liquid feed addition; generating hydrogen by the hydrolysis of fuel pellets in the reactor; providing hydrogen via fluid communication to the anode side of an open cathode PEM fuel cell stack; and, whereby said fuel cell stack generates electricity. 2. The method of claim 1 wherein the liquid contains between 100%, and about 80%, water by volume. 3. The method of claim 1 wherein the pressurized liquid addition step comprises feeding liquid from a fluid container ( 506 ) at a first flow rate during start-up of the fuel cell stack and reducing the flow rate of the liquid from the fluid container to a rate that is below the first flow rate during normal operation of the fuel cell stack. 4. The method of claim 1 further comprising atomizing, with an atomizer, at least a portion of the pressurized liquid before it reaches the fuel pellets. 5. The method of claim 1 wherein the fuel pellets comprise lithium aluminum hydride. 6. The method of claim 1 wherein the fuel pellets comprise an admixture of lithium aluminum hydride and an additive comprising at least one of AlCl 3 , MgCl 2 , BeCl 2 , CuCl 2 , LiCl, NaCl, and KCl. 7. The method of claim 6 wherein the amount of additive in the admixture is <65 wt.-%. 8. The method of claim 4 wherein the atomizer is an ultrasonic mist generator. 9. The method of claim 1 further comprising turbidity fixtures ( 602 ) on an interior surface ( 510 ) of the reactor; and whereby turbidity of the fuel pellets is increased during rotation of the containment insert as opposed to what occurs with a smooth interior. 10. The method of claim 1 further comprising at least one stirring element ( 604 ) on at least one of a distal end ( 530 ) and proximal end ( 520 ) an interior surface ( 510 ) of the reactor; and whereby turbidity of the fuel pellets is increased during movement or rotation of the containment insert as opposed to what occurs with a smooth interior. 11. The method of claim 10 wherein the rotation of the containment insert is via motor and ( 514 ). 12. The method of claim 1 wherein the fuel pellets are between about 4 mm and about 15 mm in diameter. 13. The method of claim 1 further comprising routing the hydrogen to the anode side of the fuel cell stack at a rate that is excess of that required by the fuel cell stack for producing power yielding a recirculation hydrogen stream; enriching the recirculation hydrogen exiting the anode with water; and routing the water-enriched recirculation stream to the rotatable reactor. 14. The method of claim 13 wherein the enriching further step comprises: condensing water from a cathode air exhaust; converting the condensed water to a mist comprising a plurality of water droplets using an atomizer; and entraining the water mist in the recirculation hydrogen stream. 15. The method of claim 13 wherein the enriching step comprises splitting the recirculation hydrogen stream into a first recirculation stream and a second recirculation stream using a 3-way valve and routing the first recirculation stream to a humidifier and the second recirculation stream directly to the reactor bypassing a humidifier. 16. The method of claim 1 wherein the fuel cell stack is a dosed cathode PEM fuel cell stack comprising a plurality of fuel cells, each cell having an anode side and a cathode side that enables operation of the cathode side at a pressure above ambient pressure. 17. The method of claim 16 wherein reactant air to the cathode side of the fuel cell stack is separately provided from coolant air to the fuel cell stack.
Reactor construction specially adapted for combination reactor/fuel cell (hydrogen C01B3/00; reactors for physicochemical processes B01J19/00) · CPC title
Moving reactors, e.g. rotary drums (B01J19/08 takes precedence) · CPC title
by reaction of inorganic compounds with hydrides · CPC title
by reaction of inorganic compounds with metals · CPC title
of gaseous reactants · CPC title
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