Gas generator and enhanced energy conversion systems

• US 3,975,913 A
• Filed: 12/20/1973
• Issued: 08/24/1976
• Est. Priority Date: 12/20/1973
• Status: Expired due to Term

• Current Assignee: Donald C. Erickson
• Original Assignee: Donald C. Erickson
• Inventors: Erickson, Donald C.
• Primary Examiner(s): Ostrager, Allen M.
• Application Number:
  US05/426,524
• Time in Patent Office: 978 Days
• Field of Search: 204/DIG. 3, 204/DIG. 4, 204/DIG. 6, 204/274, 60/645, 60/673, 60/648, 60/670, 60/671, 60/682, 122/21, 126/263
• US Class Current: 60/645
• CPC Class Codes: F01K 25/005 the working fluid being steam, created by combustion of hydrogen with oxygen
• CPC Class Codes: F02G 1/043 the engine being operated by expansion and contraction of a mass of working gas which is heated and cooled in one of a plurality of constantly communicating expansible chambers, e.g. Stirling cycle type engines
• CPC Class Codes: F02G 2250/03 Brayton cycles
• CPC Class Codes: H01M 8/0606 with means for production of gaseous reactants
• CPC Class Codes: Y02E 60/50 Fuel cells
• CPC Class Codes: Y10S 204/04 Electrolysis cell combined with fuel cell
• CPC Class Codes: Y10S 204/06 Unusual non-204 uses of electrolysis

Abstract

A gas generator is disclosed which will simply and reliably effect a gas producing reaction between a gaseous and a liquid reactant. The generator can operate at elevated temperatures and has heat exchange means incorporated. The gas generator is applied as a hydrogen generator to an energy conversion system in which hydrogen from the hydrogen-producing reaction powers a fuel cell and the reaction heat from the hydrogen producing reaction powers a thermal engine, thereby enhancing the energy conversion system relative to one in which the hydrogen generator is merely cooled and its heat is rejected as waste heat. Other possible energy conversion systems based on this gas generator are disclosed.

Claims

1. An energy conversion system comprised of:

hydrogen gas generator of the type in which a gas is produced by an exothermic chemical reaction between a gaseous substance and a liquid substance which is present in excess, and in which heat exchange means is incorporated;

a conduit to remove the gas produced in the gas generator;

a fuel cell which receives the gas produced by the gas generator through the conduit and uses that gas as one of its reactants;

a thermal engine which is powered by the heat from the exothermic reaction in the gas generator, the heat being transferred to the thermal engine by the heat exchange means.

2. A system as recited in claim 1 wherein the operating temperature of the gas generator is a temperature selected from the range 400°

to 2400°

F.

3. A system as recited in claim 2 wherein the gas produced is comprised of hydrogen.

4. A system as recited in claim 3 wherein the reacting gaseous substance is comprised of H₂ O and the reacting liquid substance is comprised of constituents selected from the list Al, Na, Li, LiH, K, Ca, Mg, and Si.

5. A system as recited in claim 4 wherein the fuel cell is a hydrogen oxygen fuel cell, and further comprised of a H₂ O conduit which is used to recycle the product H₂ O from the fuel cell to the gas generator where it comprises the reacting gaseous substance.

6. A system as recited in claim 5 further comprised of a hydrogen surge tank connected to and communicating with the hydrogen conduit.

7. A method of producing useful energy comprising the steps of:

a generating hydrogen from an exothermic reaction between a gaseous substance and a liquid substance which react to produce hydrogen said liquid substance being present in excess;

converting the thermal energy from the exothermic reaction to useful energy in a thermal engine;

converting the hydrogen to useful energy by reacting it with an oxidant in an energy conversion device.

8. A method as recited in claim 7 wherein the energy conversion device employs an electrochemical reaction.

9. A method as recited in claim 7 wherein the energy conversion device is a second thermal engine.

10. A method as recited in claim 7 wherein the energy conversion device is the thermal engine.

11. A method as recited in claim 7 wherein the generated gas comprises part of the working fluid of the thermal engine.