APPARATUS, SYSTEM, AND METHOD FOR PROCESSING HYDROGEN GAS

• US 20090025293A1
• Filed: 07/24/2008
• Published: 01/29/2009
• Est. Priority Date: 07/25/2007
• Status: Abandoned Application

• Current Assignee: Trulife Incorporated (Trulife)
• Original Assignee: Trulife Incorporated (Trulife)
• Inventors: Brydon, Chris, Patton, John, Pearson, Ken
• Application Number:
  US12/179,578
• Publication Number:
  US 20090025293A1
• Time in Patent Office: Days
• US Class Current: 48/199.FM
• CPC Class Codes: C01B 2203/0415 Purification by absorption in liquids
• CPC Class Codes: C01B 2203/0465 Composition of the impurity
• CPC Class Codes: C01B 2203/048 the impurity being an organic compound
• CPC Class Codes: C01B 2203/0485 the impurity being a sulfur compound
• CPC Class Codes: C01B 2203/0495 the impurity being water
• CPC Class Codes: C01B 2203/066 with fuel cells
• CPC Class Codes: C01B 3/065 from a hydride
• CPC Class Codes: C01B 3/52 by contacting with liquids; Regeneration of used liquids C01B3/508 takes precedence
• CPC Class Codes: C01B 3/56 by contacting with solids; Regeneration of used solids C01B3/508 takes precedence
• CPC Class Codes: H01M 16/006 of fuel cells with rechargeable batteries
• CPC Class Codes: H01M 8/04007 related to heat exchange
• CPC Class Codes: H01M 8/04126 Humidifying
• CPC Class Codes: H01M 8/04231 Purging of the reactants
• CPC Class Codes: H01M 8/065 by dissolution of metals or alloys; by dehydriding metallic substances
• CPC Class Codes: Y02E 60/10 Energy storage using batteries
• CPC Class Codes: Y02E 60/36 Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

An apparatus, system, and method are disclosed for processing a hydrogen gas stream comprising a housing, a condensing media, a mechanical filtration element, a coalescer element, and an outlet port. The housing comprises a heat- and pressure-resistant material and has an internal chamber configured to receive a hydrogen gas stream. A condenser may cool the hydrogen gas stream to promote water condensation. The condensing media removes entrained liquid water from the hydrogen gas stream. The mechanical filtration element receives the hydrogen gas stream as the hydrogen gas stream exits the condensing media. The mechanical filtration element collects particulate matter from the hydrogen gas stream. The coalescer element receives the hydrogen gas stream as the hydrogen gas stream exits the mechanical filtration element. The coalescer element removes substantially all of the liquid water formed in the hydrogen gas stream. The outlet port delivers the hydrogen gas stream outside the housing.

Claims

1. An apparatus for processing a hydrogen gas stream generated from a chemical:

hydride comprising;

a housing comprising a heat- and pressure-resistant material, the housing having an internal chamber configured to receive a hydrogen gas stream;

a condensing media disposed within the internal chamber, the condensing media having a plurality of condensing passages sized to engage liquid water entrained in the hydrogen gas stream to remove the entrained liquid water from the hydrogen gas stream, the liquid water forming as the hydrogen gas stream cools;

a coalescer element disposed within the internal chamber to receive the hydrogen gas stream as the hydrogen gas stream exits the condensing media, the coalescer element removing liquid water formed in the hydrogen gas stream as the hydrogen gas stream cools; and

an outlet port disposed in the housing in fluid communication with the internal chamber, the outlet port configured to receive the hydrogen gas stream as the hydrogen gas stream exits the coalescer element and to deliver the hydrogen gas stream outside the housing.

2. The apparatus of claim 1, further comprising a condenser, the condenser comprising a channel defined by at least one wall, the wall absorbing heat from the hydrogen gas stream, the channel delivering the hydrogen gas stream to the internal chamber upstream of the condensing media.

3. The apparatus of claim 2, wherein the condenser comprises a corrosion-resistant material with a thermal conductivity greater than about 5 W/m K.

4. The apparatus of claim 2, further comprising a cooling module that conducts heat from the condenser to a surrounding environment, the cooling module comprising a fluid circulation device that circulates a fluid in contact with the at least one wall.

5. The apparatus of claim 1, further comprising a mechanical filtration element disposed within the internal chamber to receive the hydrogen gas stream as the hydrogen gas stream exits the condensing media and deliver the hydrogen gas stream to the coalescer element, the mechanical filtration element having a plurality of filtration passages sized to collect particulate matter larger than a selected diameter from the hydrogen gas stream.

6. The apparatus of claim 1, further comprising a pre-filter that receives the hydrogen gas stream before the hydrogen gas stream enters the condensing media, the pre-filter having a plurality of filtration passages comprising a material that collects contaminants from the hydrogen gas stream.

7. The apparatus of claim 6, wherein one or more of the condensing media, the mechanical filtration element, the pre-filter, and the coalescer element are located within a chemical hydride fuel cartridge.

8. The apparatus of claim 1, further comprising a pre-filter that receives the hydrogen gas stream before the hydrogen gas stream enters the condensing media, the pre-filter having a plurality of filtration passages comprising a material that collects one or more of solid contaminants and gaseous contaminants from the hydrogen gas stream.

9. The apparatus of claim 8, wherein the pre-filter comprises one or more materials, each material configured specifically to remove one or more specific contaminants from the hydrogen gas stream.

10. The apparatus of claim 1, wherein the apparatus is configured such that the hydrogen gas stream exiting the outlet port has,

a temperature within an operating temperature threshold of a fuel cell configured to consume the hydrogen gas stream and

a relative humidity less than or equal to 100 percent.

11. The apparatus of claim 1, further comprising an organic filter that receives the hydrogen gas stream from the coalescer element and captures one or more of organic vapor contamination and inorganic vapor contamination from the hydrogen gas stream.

12. The apparatus of claim 1, further comprising a hydrogen-selective membrane that receives the hydrogen gas stream upstream from the outlet port.

13. An apparatus for processing a hydrogen gas stream generated from a chemical hydride comprising:

a housing comprising a heat- and pressure-resistant material, the housing having a condensing chamber and a coalescing chamber, the housing configured to receive a hydrogen gas stream;

an inlet port disposed in the housing in fluid communication with a condenser, the inlet port configured to deliver the hydrogen gas stream to the condenser;

the condenser comprising a channel defined by at least one wall, the wall absorbing heat from the hydrogen gas stream, the channel delivering the hydrogen gas stream to a bypass tube disposed between the condenser and the condensing chamber;

a condensing media disposed within the condensing chamber, the condensing media having a plurality of condensing passages sized to engage liquid water entrained in the hydrogen gas stream to remove the entrained liquid water from the hydrogen gas stream, the liquid water forming as the hydrogen gas stream cools;

a mechanical filtration element disposed between the condensing chamber and the coalescing chamber to receive the hydrogen gas stream as the hydrogen gas stream exits the condensing media, the mechanical filtration element having a plurality of filtration passages sized to collect particulate matter larger than a selected diameter from the hydrogen gas stream;

a coalescer element disposed within the coalescing chamber to receive the hydrogen gas stream as the hydrogen gas stream exits the mechanical filtration element, the coalescer element removing substantially all of the liquid water formed in the hydrogen gas stream as the hydrogen gas stream cools; and

an outlet port disposed in the housing in fluid communication with the coalescing chamber, the outlet port configured to

receive the hydrogen gas stream as the hydrogen gas stream exits the coalescer element, and

deliver the hydrogen gas stream outside the housing.

14. The apparatus of claim 13, wherein the apparatus is configured such that the hydrogen gas stream exiting the outlet port has:

a temperature within an operating temperature threshold of a fuel cell configured to consume the hydrogen gas stream, and

a relative humidity less than or equal to 100 percent.

15. The apparatus of claim 13, wherein the condenser further comprises a cooling module that conducts heat from the condenser to a surrounding environment, the cooling module comprising a fluid circulation device that circulates a fluid in contact with the at least one wall.

16. The apparatus of claim 13, further comprising a pre-filter that receives the hydrogen gas stream before the hydrogen gas stream enters the condenser, the pre-filter having a plurality of filtration passages comprising a material that collects one or more of solid contaminants and gaseous contaminants from the hydrogen gas stream.

17. The apparatus of claim 16, wherein the pre-filter comprises one or more materials, each material configured specifically to remove one or more specific contaminants from the hydrogen gas stream.

18. A method for processing a hydrogen gas stream generated from a chemical hydride comprising:

cooling a hydrogen gas stream in a condenser, the hydrogen gas stream generated from a chemical hydride, the condenser comprising a channel defined by at least one wall, the wall absorbing heat from the hydrogen gas stream, the channel delivering the hydrogen gas stream to a single housing, the housing having an internal chamber configured to receive the hydrogen gas stream

engaging liquid water in the hydrogen gas stream within a plurality of condensing passages of a condensing media disposed within the internal chamber, the liquid water forming as the hydrogen gas stream cools;

collecting particulate matter larger than a selected diameter from the hydrogen gas stream in a plurality of filtration passages of a mechanical filtration element disposed within the internal chamber to receive the hydrogen gas stream as the hydrogen gas stream exits the condensing media;

removing in a coalescer element substantially all of the liquid water from the hydrogen gas stream, the coalescer element disposed within the internal chamber to receive the hydrogen gas stream as the hydrogen gas stream exits the mechanical filtration element, the liquid water forming in the hydrogen gas stream as the hydrogen gas stream cools; and

delivering the hydrogen gas stream from the housing, the hydrogen gas stream having a temperature within an operating temperature threshold of a fuel cell configured to consume the hydrogen gas stream, and a relative humidity less than or equal to 100 percent.

19. The method of claim 18, further comprising pre-filtering the hydrogen gas stream in a pre-filter before the hydrogen gas stream enters the condenser, the pre-filter having a plurality of filtration passages comprising a material that collects solid and gaseous contaminants from the hydrogen gas stream.

20. The method of claim 18, wherein the apparatus is configured such that the hydrogen gas stream exiting the housing has less than 0.5 percent contaminants.

21. The method of claim 18, further comprising collecting water recovered from the hydrogen gas stream and delivering the collected water to a chemical hydride water supply reservoir.

22. A system to generate electric power from a chemical hydride, the system comprising:

a removable fuel cartridge configured to produce a hydrogen gas stream by reacting water with a chemical hydride;

a condenser that receives the hydrogen gas stream, the condenser having a condensing media having a plurality of condensing passages sized to engage liquid water entrained in the hydrogen gas stream to remove the entrained liquid water from the hydrogen gas stream, the liquid water forming as the hydrogen gas stream cools;

a coalescer that receives the hydrogen gas stream from the condenser, the coalescer having a coalescer element that receives the hydrogen gas stream as the hydrogen gas stream exits the condenser, the coalescer element removing substantially all of the liquid water formed in the hydrogen gas stream as the hydrogen gas stream cools;

a fuel cell stack configured to receive the hydrogen gas stream and to generate electric power using air and the hydrogen gas stream;

an electric power storage device coupled with the fuel cell stack, the electric power storage device configured to store and supply electric power;

one or more water pumps configured to inject water from a water supply into the fuel cartridge at a variable rate; and

a controller configured to manage a water injection rate for each of the one or more water pumps based on power demands of an electric load coupled to the system.

23. The system of claim 22, wherein the fuel cartridge is replaceable and comprises a pre-filter configured to collect solid and gaseous contaminants from the produced hydrogen.

24. The system of claim 22, wherein the condenser comprises a channel defined by at least one wall, the wall absorbing heat from the hydrogen gas stream prior to the hydrogen gas stream contacting the condensing media.