Thomas C Tillman
Engineers at Williams Gln Dr, Sugar Land, TX
License number
Colorado 27077
Issued Date
Jul 12, 1990
Renew Date
Aug 1, 2004
Expiration Date
Jul 31, 2006
Type
Professional Engineer
Address
Address
3114 Williams Glen Dr, Sugar Land, TX 77479
Professional information
System And Method For Recovery Of Fuel Products From Subterranean Carbonaceous Deposits Via An Electric Device
US Patent:
7735554, Jun 15, 2010
Filed:
Mar 27, 2008
Appl. No.:
12/056960
Inventors:
Thomas C. Tillman - Sugar Land TX, US
Assignee:
Texyn Hydrocarbon, LLC - Houston TX
International Classification:
E21B 43/24
US Classification:
1662723, 1662727, 166 60, 166302
Abstract:
A system for gasification of carbonaceous deposits below the ground surface comprising: an injection well assembly comprising one end positioned at the ground surface and the opposite end of the injection well assembly located within the carbonaceous deposit; a production well assembly comprising one end positioned at the ground surface and the opposite end of the production well assembly located within the carbonaceous deposit; a non-vertical reaction shaft assembly located within the carbonaceous deposit a distance below ground surface, the non-vertical reaction shaft having a length and comprising an injection end in communication with the end of the injection well assembly located within the carbonaceous deposit and a production end in communication with the end of the production well assembly located within the carbonaceous deposit; and a mobile electric device configured to move within the non-vertical reaction shaft assembly. A method for gasifying underground carbonaceous deposits using an electric device.
System And Method For Generation Of Synthesis Gas From Subterranean Coal Deposits Via Thermal Decomposition Of Water By An Electric Torch
US Patent:
2010027, Nov 4, 2010
Filed:
May 6, 2010
Appl. No.:
12/775263
Inventors:
Thomas Tillman - Sugar Land TX, US
Assignee:
TEXYN HYDROCARBON, LLC - Houston TX
International Classification:
E21B 43/24
US Classification:
1662511, 166 57
Abstract:
A system for gasification of coal deposits below the ground surface comprising an injection well assembly comprising one end positioned at the surface and the opposite end located adjacent or within the coal deposit; a production well assembly comprising one end positioned at the surface and the opposite end of the production well assembly located adjacent or within the coal deposit; a non-vertical reaction shaft assembly located adjacent or within the coal deposit, the non-vertical reaction comprising an injection end in communication with the end of the injection well assembly located adjacent or within the coal deposit and a production end in communication with the end of the production well assembly located adjacent or within the coal deposit; and an electric torch configured to move within the non-vertical reaction shaft assembly and create an oxidant and moderator downhole. A method for gasifying coal deposits is also provided.
System And Method For High Pressure Synthesis Gas Processing
US Patent:
2009012, May 14, 2009
Filed:
Nov 14, 2008
Appl. No.:
12/271010
Inventors:
Thomas Tillman - Sugar Land TX, US
Assignee:
Texyn Hydrocarbon, LLC - Houston TX
International Classification:
C01B 3/38, B01J 10/00, C01B 31/20, C01B 21/00
US Classification:
252373, 422187, 4234371, 423359, 423365
Abstract:
A system for production of CO-rich product gas, the system including a steam shift reactor for production of shifted synthesis gas from high pressure raw synthesis gas; a hydrogen separation unit to separate the shifted synthesis gas into a hydrogen-rich product comprising a greater volume percentage of hydrogen than the shifted synthesis gas and a hydrogen-lean tailgas comprising a reduced volume percentage of hydrogen than the shifted synthesis gas; an oxidizing unit adapted to oxidize the hydrogen-lean tailgas with purified oxygen comprising primarily oxygen, to produce an oxidized product gas comprising water vapor and carbon dioxide; and dehydration apparatus adapted for removal of water vapor from the oxidized product gas to provide CO-rich product gas comprising at least 95% COby volume; wherein the proportional critical temperature of the CO-rich product gas is near or greater than the critical temperature of pure CO.