1
Marion Charles P, Schlinger Warren G, Brent Albert, Muenger James R: Gas turbine process utilizing purified fuel gas. Texaco, Whaley T H, Ries C G, March 4, 1975: US3868817 (118 worldwide citation)

Gas turbines for producing mechanical and electrical power without polluting the atmosphere are fueled by an improved clean fuel gas having a heat of combustion in the range of about 75-350 BTU/SCF and a mole ratio (CO/H.sub.2) of at least 0.30. The fuel-gas is produced by partial oxidation of a hyd ...


2
Marion Charles P, Schlinger Warren G, Brent Albert, Muenger James R: Gas turbine process utilizing purified fuel and recirculated flue gases. Texaco, Whaley T H, Ries C G, February 18, 1975: US3866411 (73 worldwide citation)

Gas turbines for producing mechanical and electrical power without polluting the atmosphere are fueled by an improved clean fuel gas having a heat of combustion of preferably about 70-100 BTU/SCF. Fuel-gas is produced by the partial oxidation of a hydrocarbonaceous fuel in a free-flow non-catalytic ...


3
Muenger James R: Heat exchange apparatus for catalytic system. Texaco, Whaley T H, Ries C G, March 12, 1974: US3796547 (42 worldwide citation)

A heat exchange apparatus for an exothermic catalytic system comprising a closed cylindrical vessel containing a removable axial spine which extends through the top and bottom heads of said vessel. Two separate heat exchangers are embedded in catalyst within said vessel and are supported by said axi ...


4
Alexander David L, Muenger James R: Two-stage ammonia absorption refrigeration system with at least three evaporation stages. Texaco, Whaley T H, Reis C G, June 18, 1974: US3817050 (29 worldwide citation)

A two-stage ammonia absorption refrigeration system can be operated with at least three evaporators maintained at decreasing temperatures but only two pressures by separating two ammonia streams of different ammonia purities from the strong ammonia water solution produced by the two stages of ammoni ...


5
Muenger James R: Water-gas shift conversion process. Texaco, May 30, 1972: US3666682 (27 worldwide citation)

A water-gas shift conversion process in which a feed gas mixture is subjected to successive contacts with catalyst and the temperature of the reacting gases contacting the shift conversion catalyst is controlled by indirect concurrent heat exchange with the feed gas mixture.


6
Muenger James R: Quench ring and dip tube assembly.. Texaco Development, November 6, 1985: EP0160424-A2 (8 worldwide citation)

An assembly of a quench liquid distribution ring and dip tube with or without a draft tube for use in a hot effluent gas quench cooling zone containing a pool of quench liquid in the bottom in combination with a vertical cylindrical freeflow refractory lined reaction zone of a partial oxidation gas ...


7
Muenger James R: Ensemble bague dextinction et tube plongeur, Quench ring and dip tube assembly. Muenger James R, Texaco Development Corporation, SMART & BIGGAR, July 31, 1990: CA1272030

QUENCH RING AND DIP TUBE ASSEMBLY ABSTRACT An assembly of a quench liquid distribution ring anddip tube with or without a draft tube for use in a hot effluentgas quench cooling zone containing a pool of quench liquid inthe bottom in combination with a vertical cylindrical free-flowrefractory lined r ...


8
Muenger James R, Child Edward T, Brent Albert: Production de gaz de snythese epure et refroidi, Production of cleaned and cooled synthesis gas. Texaco Development Corporation, SMART & BIGGAR, September 7, 1982: CA1131026

ABSTRACT The hot raw synthesis gas stream leaving thereaction zone of a free flow partial oxidation gas generatorat a temperature in the range of about 1800� to 3000�F. ispassed through a first gas diversion and residue separationzone where the velocity of the gas stream is reduced and itsdirection ...


9
Paull Peter L, Gilmer William N, Muenger James R: Procede pour produire de lenergie a partir de combustibles carbones solides, Process for the generation of power from solid carbonaceous fuels. Texaco Development Corporation, SMART & BIGGAR, June 22, 1982: CA1126029

- 1 - Abstract: A process for the efficient production of power from non-gaseous carbonaceous fuels, such as coal, or heavy fueloil, in a steam power plant in which the carbonaceous fuelis first gasified at relatively high pressure and tempera-ture by partial oxidation with oxygen to produce a fuelg ...


10
Barber Everett M, Muenger James R, Alexander David L, Schlinger Warren G: Procede doxydation partielle, et energie engendree par ladite oxydation, Partial oxidation process with production of power. Texaco Development Corporation, SMART & BIGGAR, September 1, 1981: CA1107965

PARTIAL OXIDATION PROCESSWITH PRODUCTION OF POWER (D#70,519-F) ABSTRACT Power is developed by an expansion turbine inwhich the working fluid is a gaseous mixture comprisingall of the hot raw gas stream leaving an unpacked partialoxidation gas generator, after removing if present aportion of the entr ...