Richard John Martin
Engineers in Manhattan Beach, CA
License number
Colorado 44184
Issued Date
May 14, 2010
Renew Date
Nov 1, 2013
Expiration Date
Oct 31, 2015
Type
Professional Engineer
Address
Address
PO Box 873, Manhattan Beach, CA 90267
Professional information
Gradual Oxidation With Adiabatic Temperature Above Flameout Temperature
US Patent:
2013023, Sep 12, 2013
Filed:
Mar 9, 2012
Appl. No.:
13/417094
Inventors:
Jeffrey ARMSTRONG - Exeter NH, US
Richard MARTIN - Manhattan Beach CA, US
Douglas HAMRIN - Laguna Niguel CA, US
Richard MARTIN - Manhattan Beach CA, US
Douglas HAMRIN - Laguna Niguel CA, US
Assignee:
FlexEnergy, Inc. - Irvine CA
International Classification:
F02C 7/22, F02B 45/06, B01J 19/00
US Classification:
60 3923, 422198, 123 2
Abstract:
Described herein are embodiments of systems and methods for oxidizing gases. In some embodiments, a reaction chamber is configured to receive a fuel gas and maintain the gas at a temperature within the reaction chamber that is above an autoignition temperature of the gas. The reaction chamber may also be configured to maintain a reaction temperature within the reaction chamber below a flameout temperature. In some embodiments, heat and product gases from the oxidation process can be used, for example, to drive a turbine, reciprocating engine, and injected back into the reaction chamber.
Staged Gradual Oxidation
US Patent:
2013023, Sep 12, 2013
Filed:
Mar 9, 2012
Appl. No.:
13/417162
Inventors:
Jeffrey ARMSTRONG - Exeter NH, US
Richard MARTIN - Manhattan Beach CA, US
Douglas HAMRIN - Laguna Niguel CA, US
Joe PERRY - Mission Viejo CA, US
Richard MARTIN - Manhattan Beach CA, US
Douglas HAMRIN - Laguna Niguel CA, US
Joe PERRY - Mission Viejo CA, US
Assignee:
FLEXENERGY, INC. - Irvine CA
International Classification:
F23N 1/08, F23C 9/00, F23C 6/00
US Classification:
431 12
Abstract:
Described herein are embodiments of systems and methods for oxidizing gases. In some embodiments, a reaction chamber is configured to receive a fuel gas and maintain the gas at a temperature within the reaction chamber that is above an autoignition temperature of the gas. The reaction chamber may also be configured to maintain a reaction temperature within the reaction chamber below a flameout temperature. In some embodiments, heat and product gases from the oxidation process can be used, for example, to drive a turbine, reciprocating engine, and injected back into the reaction chamber.
Hybrid Gradual Oxidation
US Patent:
2013023, Sep 12, 2013
Filed:
Mar 9, 2012
Appl. No.:
13/417165
Inventors:
Richard MARTIN - Manhattan Beach CA, US
Jeffrey ARMSTRONG - Exeter NH, US
Douglas HAMRIN - Laguna Niguel CA, US
Jeffrey ARMSTRONG - Exeter NH, US
Douglas HAMRIN - Laguna Niguel CA, US
Assignee:
FLEXENERGY, INC. - Irvine CA
International Classification:
F23L 7/00, F23C 99/00, F23J 15/00
US Classification:
110348, 110297, 110203, 110234
Abstract:
Described herein are embodiments of systems and methods for oxidizing gases. In some embodiments, a reaction chamber is configured to receive a fuel gas and maintain the gas at a temperature within the reaction chamber that is above an autoignition temperature of the gas. The reaction chamber may also be configured to maintain a reaction temperature within the reaction chamber below a flameout temperature. In some embodiments, heat and product gases from the oxidation process can be used, for example, to drive a turbine, reciprocating engine, and injected back into the reaction chamber.
Gradual Oxidation With Heat Transfer
US Patent:
2013023, Sep 12, 2013
Filed:
Mar 9, 2012
Appl. No.:
13/417140
Inventors:
Douglas HAMRIN - Laguna Niguel CA, US
Richard MARTIN - Manhattan Beach CA, US
Jeffrey ARMSTRONG - Exeter NH, US
Richard MARTIN - Manhattan Beach CA, US
Jeffrey ARMSTRONG - Exeter NH, US
Assignee:
FLEXENERGY, INC. - Irvine CA
International Classification:
F02C 3/22, F23N 5/00, F23N 1/02
US Classification:
60772, 431 2
Abstract:
Described herein are embodiments of systems and methods for oxidizing gases. In some embodiments, a reaction chamber is configured to receive a fuel gas and maintain the gas at a temperature within the reaction chamber that is above an autoignition temperature of the gas. The reaction chamber may also be configured to maintain a reaction temperature within the reaction chamber below a flameout temperature. In some embodiments, heat and product gases from the oxidation process can be used, for example, to drive a turbine, reciprocating engine, and injected back into the reaction chamber.
Staged Gradual Oxidation
US Patent:
2013023, Sep 12, 2013
Filed:
Mar 9, 2012
Appl. No.:
13/417164
Inventors:
Jeffrey ARMSTRONG - Exeter NH, US
Richard MARTIN - Manhattan Beach CA, US
Douglas HAMRIN - Laguna Niguel CA, US
Richard MARTIN - Manhattan Beach CA, US
Douglas HAMRIN - Laguna Niguel CA, US
Assignee:
FLEXENERGY, INC. - Irvine CA
International Classification:
F02C 3/22, F23D 14/66, F23N 5/00, F23C 6/00, F23C 9/00
US Classification:
60 39465, 110208, 110211, 110234, 110185, 431 36
Abstract:
Described herein are embodiments of systems and methods for oxidizing gases. In some embodiments, a reaction chamber is configured to receive a fuel gas and maintain the gas at a temperature within the reaction chamber that is above an autoignition temperature of the gas. The reaction chamber may also be configured to maintain a reaction temperature within the reaction chamber below a flameout temperature. In some embodiments, heat and product gases from the oxidation process can be used, for example, to drive a turbine, reciprocating engine, and injected back into the reaction chamber.
Gradual Oxidation With Heat Transfer
US Patent:
2013023, Sep 12, 2013
Filed:
Mar 9, 2012
Appl. No.:
13/417129
Inventors:
Jeffrey ARMSTRONG - Exeter NH, US
Richard MARTIN - Manhattan Beach CA, US
Douglas HAMRIN - Laguna Niguel CA, US
Richard MARTIN - Manhattan Beach CA, US
Douglas HAMRIN - Laguna Niguel CA, US
Assignee:
FlexEnergy, Inc. - Irvine CA
International Classification:
F02C 3/22, F23K 5/00, F23B 99/00, F23N 5/00
US Classification:
60 39465, 110185, 110101 R, 110234
Abstract:
Described herein are embodiments of systems and methods for oxidizing gases. In some embodiments, a reaction chamber is configured to receive a fuel gas and maintain the gas at a temperature within the reaction chamber that is above an autoignition temperature of the gas. The reaction chamber may also be configured to maintain a reaction temperature within the reaction chamber below a flameout temperature. In some embodiments, heat and product gases from the oxidation process can be used, for example, to drive a turbine, reciprocating engine, and injected back into the reaction chamber.