Eugene R. Thomas - Houston TX Harry W. Deckman - Clinton NJ Donald J. Victory - Sugar Land TX Ronald R. Chance - Annandale NJ Russell H. Oelfke - Houston TX
Assignee:
ExxonMobil Upstream Research Company - Houston TX
International Classification:
B01D 5322
US Classification:
95 49, 95 50, 95 51
Abstract:
The invention relates to a method of separating one or more components from a multi-component gas stream comprising at least one non-acid gas component and at least one acid gas component. A multi-component gas stream at a pressure above 1,200 psia (82. 8 bar) and a temperature above 120Â F. (48. 9Â C. ) with the concentration of at least one acid gas component in the gas stream being at least 20 mole percent is passed to a membrane system that selectively separates at least one acid gas component from the multi-component gas stream as a permeate stream. The permeate stream has a pressure at least 20% of the pressure of the feed pressure.
Eugene R. Thomas - Houston TX Thomas A. Paulley - Houston TX Donald J. Victory - Sugar Land TX Harry W. Deckman - Clinton NJ
Assignee:
ExxonMobil Upstream Research Company - Houston TX
International Classification:
E21B 4308
US Classification:
166265, 166266, 166227
Abstract:
The invention is a method and system of separating a multi-component fluid in a wellbore. At least one fluid separation membrane comprising a feed side and a permeate side is incorporated in the wellbore. A flowing stream of the multi-component fluid obtained from a subterranean zone being in fluid communication with the wellbore is passed across the feed side of the membrane at a first pressure. A retentate stream depleted in at least one component compared to the multi-component fluid is withdrawn from the feed side of the membrane and passed to the earths surface. A permeate stream at a second pressure is withdrawn from the permeate side, in which the permeate stream is enriched in at least one component compared with the multi-component fluid. The second pressure is controlled to maintain the second pressure below the first pressure.
This invention is method of recovering gas from a gas-bearing subterranean formation in which gas is produced from an upper portion of the formation and a waste gas is injected into a lower portion of the formation to dispose of the waste gas. The waste gas is injected within a 3000 foot (914 m) radial distance from the production of the gas. The injection and production can be carried out using one well or a plurality of wells.
Removal Of Heavy Hydrocarbons From Gas Mixtures Containing Heavy Hydrocarbons And Methane
Bruce T. Kelley - Kingwood TX, US Paul S. Northrop - Spring TX, US Ronald R. Chance - Annandale NJ, US Harry W. Deckman - Clinton NJ, US Eugene R. Thomas - Houston TX, US
Assignee:
ExxonMobil Research and Engineering Company - Annandale NJ
International Classification:
B01D 53/047
US Classification:
95 96, 95148
Abstract:
A process for the separation of one or more heavy hydrocarbon gases from a gas mixture containing heavy hydrocarbon gas components and methane. The process is conducted in swing adsorption apparatus containing adsorbent contactor having a plurality of flow channels and wherein 20 volume percent or less of the open pore volume of the contactors, is in the mesopore and macropore range.
Process For Removing Contaminants From Dialkyl Ethers Of Polyalkylene Glycols
Eugene R. Thomas - Houston TX Robert E. Steele - Houston TX
Assignee:
Exxon Production Research Company - Houston TX
International Classification:
C07C 3772
US Classification:
568621
Abstract:
A process is described for removing contaminants from a contaminant-laden solution of dialkyl ethers of polyethylene glycols (polyether solvent) by mixing the solution with an aqueous base solution. The mixture produces at least two liquid phases of different densities, which are then separated from each other. The lighter liquid phase is predominantly the polyether solvent while the heavier liquid phase is predominantly the aqueous base solution and the contaminants. The process is particularly useful in removing triethylene glycol and other glycol-based dehydration solvents.
Multi-Component Refrigeration Process For Liquefaction Of Natural Gas
Ronald R. Bowen - Magnolia TX Eric T. Cole - Kingwood TX Edward L. Kimble - Sugar Land TX Eugene R. Thomas - Houston TX Lonny R. Kelley - Houston TX
Assignee:
Exxon Production Research Company - Houston TX
International Classification:
F25J 300
US Classification:
62612
Abstract:
This invention relates to a process for liquefying a pressurized gas stream rich in methane in which the liquefication of the gas stream occurs in a heat exchanger being cooled by a closed-loop multi-component refrigeration system to produce a methane-rich liquid product having a temperature above about -112. degree. C. (-170. degree. F. ) and a pressure sufficient for the liquid product to be at or below its bubble point. The liquefied gas product is then introduced to a storage means at a temperature above about -112. degree. C. (-170. degree. F. ).
Eugene R. Thomas - Houston TX Ronald R. Bowen - Magnolia TX Eric T. Cole - Kingwood TX Edward L. Kimble - Sugar Land TX
Assignee:
Exxon Production Research Company - Houston TX
International Classification:
F25J 100
US Classification:
62613
Abstract:
This invention relates to a process for liquefying a gas stream rich in methane and having a pressure above about 3103 kPa (450 psia). The gas stream is expanded to a lower pressure to produce a gas phase and a liquid product having a temperature above about -112. degree. C. (-170. degree. F. ) and a pressure sufficient for the liquid product to be at or below its bubble point. The gas phase and the liquid product are then phase separated in a suitable separator, and the liquid product is introduced to a storage means for storage at a temperature above about -112. degree. C. (-170. degree. F. ).
Method For Separating A Multi-Component Feed Stream Using Distillation And Controlled Freezing Zone
William A. Potts - Houston TX Eugene R. Thomas - Midland TX
Assignee:
Exxon Production Research Company - Houston TX
International Classification:
F25J 500
US Classification:
62 12
Abstract:
The invention relates to a method for separating two primary components of a multi-component feed stream (e. g. , methane and nitrogen) in the presence of a third, freezable component (e. g. , carbon dioxide) having a relative volatility less than that of either primary component. The inventive process employs both a distillation section and a controlled freezing zone ("CFZ"). The freezable component is allowed to freeze in the CFZ, and the resulting solids are collected at the bottom of the CFZ. The CFZ also produces a vapor overhead product enriched in one of the primary components and a liquid bottom product enriched in the other primary component. The solids of the freezable component are melted and mixed with the CFZ liquid bottom product to form a liquid feed stream for the distillation section which operates like a conventional distillation section, while tolerating significantly high concentrations (i. e. , >0. 1 mole %) of the freezable component without solids formation, at temperatures well below the freezable component's freezing point.
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