Patents by Inventor John W. Moore, Jr.

John W. Moore, Jr. has filed for patents to protect the following inventions. This listing includes patent applications that are pending as well as patents that have already been granted by the United States Patent and Trademark Office (USPTO).

  • Patent number: 6773554
    Abstract: Contaminated glycol is refined by vacuum distillation. Specifically the evaporator is heated to a temperature below the degradation temperature of the glycol. The vacuum is used to bring the flashpoint down sufficiently so that glycol evaporates or flashes at that temperature. The glycol is condensed and filtered through activated granular carbon. The principal use of refining the glycol is to refine the triethylene glycol used in natural gas dehydration plants. For such purposes the equipment is mounted upon a trailer to be taken to the plant for cleaning glycol. In such instance, in addition to refining the glycol, a cleaning agent (which contains a degreaser) is added to the refined glycol. The glycol is refined while the natural gas dehydration plant is in normal operation and therefore it is not necessary to stop the natural gas dehydration plant for refining the glycol used therein. In addition, by the addition of the cleaning agent, the dehydrating plant equipment may be cleansed of hazardous waste.
    Type: Grant
    Filed: May 8, 2000
    Date of Patent: August 10, 2004
    Inventor: John W. Moore, Jr.
  • Patent number: 6080280
    Abstract: Contaminated glycol in a natural gas dehydration plant is refined by vacuum distillation. The equipment to perform the refining by vacuum distillation is mounted upon a trailer. The equipment on the trailer is connected by an inlet line to the dehydration plant to receive the contaminated glycol from the plant. The refined glycol is continuously pumped back to the dehydration plant by a conduit. Detergents may be added to the glycol unit so that the circulating glycol cleans the equipment of the dehydration plant as the hazardous materials is separated from the glycol. The dehydration plant remains in operation during the time that the glycol is refined and the dehydration plant equipment cleaned. When the process is complete at one dehydration plant the trailer is towed to another dehydration plant for refining the glycol and cleaning the dehydration plant.
    Type: Grant
    Filed: December 3, 1998
    Date of Patent: June 27, 2000
    Inventor: John W. Moore, Jr.
  • Patent number: 5882486
    Abstract: Contaminated glycol is refined by vacuum distillation. Specifically the evaporator is heated to a temperature below the degradation temperature of the glycol. The vacuum is used to bring the flashpoint down sufficiently so that glycol evaporates or flashes at that temperature. The glycol is condensed and filtered through activated granular carbon. The principal use of refining the glycol is to refine the triethylene glycol used in natural gas dehydration plants. For such purposes the equipment is mounted upon a trailer to be taken to the plant for cleaning glycol. In such instance, in addition to refining the glycol, a cleaning agent (which contains a degreaser) is added to the refined glycol. The glycol is refined while the natural gas dehydration plant is in normal operation and therefore it is not necessary to stop the natural gas dehydration plant for refining the glycol used therein.
    Type: Grant
    Filed: July 1, 1997
    Date of Patent: March 16, 1999
    Inventor: John W. Moore, Jr.