AR064618A1 - CONTROLLED FREEZING AREA TOWER - Google Patents
CONTROLLED FREEZING AREA TOWERInfo
- Publication number
- AR064618A1 AR064618A1 ARP070105783A ARP070105783A AR064618A1 AR 064618 A1 AR064618 A1 AR 064618A1 AR P070105783 A ARP070105783 A AR P070105783A AR P070105783 A ARP070105783 A AR P070105783A AR 064618 A1 AR064618 A1 AR 064618A1
- Authority
- AR
- Argentina
- Prior art keywords
- methane
- stream
- section
- nozzles
- freezing zone
- Prior art date
Links
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/16—Fractionating columns in which vapour bubbles through liquid
- B01D3/24—Fractionating columns in which vapour bubbles through liquid with sloping plates or elements mounted stepwise
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0204—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the feed stream
- F25J3/0209—Natural gas or substitute natural gas
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0233—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of CnHm with 1 carbon atom or more
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0266—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of carbon dioxide
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/16—Fractionating columns in which vapour bubbles through liquid
- B01D3/166—Heating and/or cooling of plates
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/26—Fractionating columns in which vapour and liquid flow past each other, or in which the fluid is sprayed into the vapour, or in which a two-phase mixture is passed in one direction
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/02—Processes or apparatus using separation by rectification in a single pressure main column system
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/74—Refluxing the column with at least a part of the partially condensed overhead gas
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/90—Details relating to column internals, e.g. structured packing, gas or liquid distribution
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/02—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
- F25J2205/04—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum in the feed line, i.e. upstream of the fractionation step
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/20—Processes or apparatus using other separation and/or other processing means using solidification of components
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2215/00—Processes characterised by the type or other details of the product stream
- F25J2215/04—Recovery of liquid products
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/60—Separating impurities from natural gas, e.g. mercury, cyclic hydrocarbons
- F25J2220/66—Separating acid gases, e.g. CO2, SO2, H2S or RSH
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2240/00—Processes or apparatus involving steps for expanding of process streams
- F25J2240/02—Expansion of a process fluid in a work-extracting turbine (i.e. isentropic expansion), e.g. of the feed stream
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2240/00—Processes or apparatus involving steps for expanding of process streams
- F25J2240/40—Expansion without extracting work, i.e. isenthalpic throttling, e.g. JT valve, regulating valve or venturi, or isentropic nozzle, e.g. Laval
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2260/00—Coupling of processes or apparatus to other units; Integrated schemes
- F25J2260/80—Integration in an installation using carbon dioxide, e.g. for EOR, sequestration, refrigeration etc.
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2270/00—Refrigeration techniques used
- F25J2270/12—External refrigeration with liquid vaporising loop
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2270/00—Refrigeration techniques used
- F25J2270/60—Closed external refrigeration cycle with single component refrigerant [SCR], e.g. C1-, C2- or C3-hydrocarbons
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2280/00—Control of the process or apparatus
- F25J2280/40—Control of freezing of components
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/40—Vertical layout or arrangement of cold equipments within in the cold box, e.g. columns, condensers, heat exchangers etc.
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/72—Processing device is used off-shore, e.g. on a platform or floating on a ship or barge
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
Abstract
Se proporciona una torre de destilacion criogénica para la separacion de una corriente de fluido que contiene por lo menos metano y dioxido de carbono. La torre de destilacion criogénica tiene una seccion de separacion inferior, una seccion de rectificacion superior y una seccion de pulverizacion intermedia. La seccion de pulverizacion intermedia incluye una pluralidad de boquillas de pulverizacion que inyectan una corriente de zona de congelamiento de líquido. Las boquillas están configuradas de modo que se proporciona cobertura de líquido sustancial a través del diámetro interno de la seccion de pulverizacion intermedia. La corriente de zona de congelamiento de líquido generalmente incluye metano a una temperatura y presion por lo cual se forman tanto partículas de dioxido de carbono como una corriente de vapor enriquecida con metano. La torre puede incluir además uno o más desviadores por debajo de las boquillas para crear resistencia friccional al flujo gravitacional de la corriente de la zona de congelamiento de líquido. Esto ayuda en la disolucion y recuperacion de gas metano. Se proporcionan componentes internos adicionales para mejorar la transferencia de calor y para facilitar la disolucion de gas metano.A cryogenic distillation tower is provided for the separation of a fluid stream containing at least methane and carbon dioxide. The cryogenic distillation tower has a lower separation section, an upper rectification section and an intermediate spray section. The intermediate spray section includes a plurality of spray nozzles that inject a stream of liquid freezing zone. The nozzles are configured so that substantial liquid coverage is provided through the internal diameter of the intermediate spray section. The liquid freezing zone stream generally includes methane at a temperature and pressure whereby both carbon dioxide particles and a vapor stream enriched with methane are formed. The tower may also include one or more diverters below the nozzles to create frictional resistance to the gravitational flow of the liquid freezing zone stream. This helps in the dissolution and recovery of methane gas. Additional internal components are provided to improve heat transfer and to facilitate the dissolution of methane gas.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US88139507P | 2007-01-19 | 2007-01-19 |
Publications (1)
Publication Number | Publication Date |
---|---|
AR064618A1 true AR064618A1 (en) | 2009-04-15 |
Family
ID=38139480
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP070105783A AR064618A1 (en) | 2007-01-19 | 2007-12-20 | CONTROLLED FREEZING AREA TOWER |
Country Status (7)
Country | Link |
---|---|
US (1) | US20100018248A1 (en) |
AR (1) | AR064618A1 (en) |
AU (1) | AU2007345352B2 (en) |
CA (1) | CA2675063A1 (en) |
GB (1) | GB2460193B (en) |
MY (1) | MY151148A (en) |
WO (1) | WO2008091316A1 (en) |
Families Citing this family (53)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8027571B2 (en) | 2005-04-22 | 2011-09-27 | Shell Oil Company | In situ conversion process systems utilizing wellbores in at least two regions of a formation |
WO2008091317A2 (en) | 2007-01-19 | 2008-07-31 | Exxonmobil Upstream Research Company | Integrated controlled freeze zone (cfz) tower and dividing wall (dwc) for enhanced hydrocarbon recovery |
US8061413B2 (en) | 2007-09-13 | 2011-11-22 | Battelle Energy Alliance, Llc | Heat exchangers comprising at least one porous member positioned within a casing |
US8555672B2 (en) | 2009-10-22 | 2013-10-15 | Battelle Energy Alliance, Llc | Complete liquefaction methods and apparatus |
US8899074B2 (en) | 2009-10-22 | 2014-12-02 | Battelle Energy Alliance, Llc | Methods of natural gas liquefaction and natural gas liquefaction plants utilizing multiple and varying gas streams |
US9254448B2 (en) | 2007-09-13 | 2016-02-09 | Battelle Energy Alliance, Llc | Sublimation systems and associated methods |
US9574713B2 (en) | 2007-09-13 | 2017-02-21 | Battelle Energy Alliance, Llc | Vaporization chambers and associated methods |
US9217603B2 (en) * | 2007-09-13 | 2015-12-22 | Battelle Energy Alliance, Llc | Heat exchanger and related methods |
US7866386B2 (en) * | 2007-10-19 | 2011-01-11 | Shell Oil Company | In situ oxidation of subsurface formations |
WO2010023238A1 (en) * | 2008-08-29 | 2010-03-04 | Shell Internationale Research Maatschappij B.V. | Process and apparatus for removing gaseous contaminants from gas stream comprising gaseous contaminants |
US8323457B2 (en) * | 2008-10-30 | 2012-12-04 | Kellogg Brown & Root Llc | Dividing wall column with a heat pump |
WO2010123598A1 (en) | 2009-04-20 | 2010-10-28 | Exxonmobil Upstream Research Company | Cryogenic system for removing acid gases from a hyrdrocarbon gas stream, and method of removing acid gases |
JP5791609B2 (en) * | 2009-09-09 | 2015-10-07 | エクソンモービル アップストリーム リサーチ カンパニー | A cryogenic system for removing acid gases from hydrocarbon gas streams. |
MX337923B (en) * | 2009-11-02 | 2016-03-28 | Exxonmobil Upstream Res Co | Cryogenic system for removing acid gases from a hydrocarbon gas stream, with removal of hydrogen sulfide. |
CA2786574C (en) | 2010-01-22 | 2016-06-28 | Exxonmobil Upstream Research Company | Removal of acid gases from a gas stream, with co2 capture and sequestration |
CA2786498C (en) * | 2010-02-03 | 2018-06-26 | Exxonmobil Upstream Research Company | Systems and methods for using cold liquid to remove solidifiable gas components from process gas streams |
FR2956900B1 (en) * | 2010-03-01 | 2012-06-01 | Air Liquide | APPARATUS AND METHOD FOR SEPARATING A MIXTURE CONTAINING CARBON DIOXIDE BY DISTILLATION |
EP2365265B1 (en) * | 2010-03-03 | 2018-10-31 | General Electric Technology GmbH | Method and installation for separating carbon dioxide from flue gas of combustion plants |
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US8562792B2 (en) | 2010-10-28 | 2013-10-22 | Uop Llc | Vapor and liquid flow control in a dividing wall fractional distillation column |
US10852060B2 (en) * | 2011-04-08 | 2020-12-01 | Pilot Energy Solutions, Llc | Single-unit gas separation process having expanded, post-separation vent stream |
GB201121931D0 (en) | 2011-12-20 | 2012-02-01 | Mann Christopher M | Self contained,standalone,liquid methane storage system |
MY166180A (en) | 2012-03-21 | 2018-06-07 | Exxonmobil Upstream Res Co | Separating carbon dioxide and ethane from mixed stream |
US10655911B2 (en) | 2012-06-20 | 2020-05-19 | Battelle Energy Alliance, Llc | Natural gas liquefaction employing independent refrigerant path |
US9874395B2 (en) * | 2013-12-06 | 2018-01-23 | Exxonmobil Upstream Research Company | Method and system for preventing accumulation of solids in a distillation tower |
US9562719B2 (en) * | 2013-12-06 | 2017-02-07 | Exxonmobil Upstream Research Company | Method of removing solids by modifying a liquid level in a distillation tower |
AU2014357669B2 (en) * | 2013-12-06 | 2017-12-21 | Exxonmobil Upstream Research Company | Method and device for separating hydrocarbons and contaminants with a heating mechanism to destabilize and/or prevent adhesion of solids |
US9752827B2 (en) * | 2013-12-06 | 2017-09-05 | Exxonmobil Upstream Research Company | Method and system of maintaining a liquid level in a distillation tower |
US10139158B2 (en) * | 2013-12-06 | 2018-11-27 | Exxonmobil Upstream Research Company | Method and system for separating a feed stream with a feed stream distribution mechanism |
US9869511B2 (en) * | 2013-12-06 | 2018-01-16 | Exxonmobil Upstream Research Company | Method and device for separating hydrocarbons and contaminants with a spray assembly |
WO2015084499A2 (en) * | 2013-12-06 | 2015-06-11 | Exxonmobil Upstream Research Company | Method and system of modifying a liquid level during start-up operations |
CA2925404C (en) | 2013-12-06 | 2018-02-06 | Exxonmobil Upstream Research Company | Method and system of dehydrating a feed stream processed in a distillation tower |
US20150159942A1 (en) * | 2013-12-06 | 2015-06-11 | Jaime A. Valencia | Method and device for separating hydrocarbons and contaminants with a surface treatment mechanism |
AU2014357665B2 (en) * | 2013-12-06 | 2017-06-22 | Exxonmobil Upstream Research Company | Method and device for separating a feed stream using radiation detectors |
US9504984B2 (en) | 2014-04-09 | 2016-11-29 | Exxonmobil Upstream Research Company | Generating elemental sulfur |
MX363831B (en) | 2014-04-22 | 2019-04-04 | Exxonmobil Upstream Res Co | Method and system for starting up a distillation tower. |
CA2951637C (en) | 2014-06-11 | 2019-01-08 | Russell H. Oelfke | Method for separating a feed gas in a column |
MY177735A (en) | 2014-07-08 | 2020-09-23 | Exxonmobil Upstream Res Co | Method and system for separating fluids in a distillation tower |
CA2962608C (en) * | 2014-10-22 | 2019-01-08 | Exxonmobil Upstream Research Company | Method and system of controlling a temperature within a melt tray assembly of a distillation tower |
US10281205B2 (en) * | 2014-11-17 | 2019-05-07 | Exxonmobil Upstream Research Company | Heat exchange mechanism for removing contaminants from a hydrocarbon vapor stream |
SG11201703814YA (en) * | 2014-12-30 | 2017-07-28 | Exxonmobil Upstream Res Co | Accumulation and melt tray assembly for a distillation tower |
CA2972796C (en) | 2015-02-27 | 2019-08-13 | Exxonmobil Upstream Research Company | Reducing refrigeration and dehydration load for a feed stream entering a cryogenic distillation process |
AU2016281501B2 (en) | 2015-06-22 | 2019-02-21 | Exxonmobil Upstream Research Company | Purge to intermediate pressure in cryogenic distillation |
AU2016323618B2 (en) | 2015-09-18 | 2019-06-13 | Exxonmobil Upsteam Research Company | Heating component to reduce solidification in a cryogenic distillation system |
CA2998466C (en) | 2015-09-24 | 2021-06-29 | Exxonmobil Upstream Research Company | Treatment plant for hydrocarbon gas having variable contaminant levels |
CA3024545C (en) | 2016-03-30 | 2020-08-25 | Exxonmobile Upstream Research Company | Self-sourced reservoir fluid for enhanced oil recovery |
US20190099693A1 (en) * | 2017-10-04 | 2019-04-04 | Larry Baxter | Combined Solids-Producing Direct-Contact Exchange and Separations |
US20190128603A1 (en) * | 2017-10-27 | 2019-05-02 | Larry Baxter | Vapor Stripping by Desublimation and Dissolution |
US10786751B2 (en) * | 2018-05-08 | 2020-09-29 | Process Consulting Services, Inc. | Coker fractionator spray wash chamber |
WO2020005552A1 (en) | 2018-06-29 | 2020-01-02 | Exxonmobil Upstream Research Company | Hybrid tray for introducing a low co2 feed stream into a distillation tower |
WO2020005553A1 (en) | 2018-06-29 | 2020-01-02 | Exxonmobil Upstream Research Company (Emhc-N1.4A.607) | Mixing and heat integration of melt tray liquids in a cryogenic distillation tower |
GB2602318A (en) * | 2020-12-23 | 2022-06-29 | Ricardo Uk Ltd | Processing system and method |
CN115228103A (en) * | 2022-07-06 | 2022-10-25 | 彩源科技股份有限公司 | Ammonia water treatment device |
Family Cites Families (93)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE569932A (en) * | 1957-07-31 | |||
US3050950A (en) * | 1960-08-31 | 1962-08-28 | Linde Eismasch Ag | Process for the separation of solid carbon dioxide from air as it decomposes in which the carbon dioxide containing air is previously cooled below the solidification temperature of the carbon dioxide |
US3393527A (en) * | 1966-01-03 | 1968-07-23 | Pritchard & Co J F | Method of fractionating natural gas to remove heavy hydrocarbons therefrom |
US3400512A (en) * | 1966-07-05 | 1968-09-10 | Phillips Petroleum Co | Method for removing water and hydrocarbons from gaseous hci |
US3767766A (en) * | 1971-02-22 | 1973-10-23 | Chevron Res | Method of removing gaseous sulfides from gaseous mixtures |
US3824080A (en) * | 1972-04-27 | 1974-07-16 | Texaco Inc | Vertical reactor |
US3842615A (en) * | 1972-11-06 | 1974-10-22 | Standard Havens | Evaporative cooler |
US3933001A (en) * | 1974-04-23 | 1976-01-20 | Airco, Inc. | Distributing a carbon dioxide slurry |
DE2551717C3 (en) * | 1975-11-18 | 1980-11-13 | Basf Ag, 6700 Ludwigshafen | and possibly COS from gases |
JPS5842649B2 (en) * | 1975-12-01 | 1983-09-21 | 東光株式会社 | Atsuden Rohaki |
US4319964A (en) * | 1976-04-28 | 1982-03-16 | Jerome Katz | Apparatus for high volume distillation of liquids |
US4270937A (en) * | 1976-12-01 | 1981-06-02 | Cng Research Company | Gas separation process |
US4609388A (en) * | 1979-04-18 | 1986-09-02 | Cng Research Company | Gas separation process |
US4318723A (en) * | 1979-11-14 | 1982-03-09 | Koch Process Systems, Inc. | Cryogenic distillative separation of acid gases from methane |
US4462814A (en) * | 1979-11-14 | 1984-07-31 | Koch Process Systems, Inc. | Distillative separations of gas mixtures containing methane, carbon dioxide and other components |
US4246015A (en) * | 1979-12-31 | 1981-01-20 | Atlantic Richfield Company | Freeze-wash method for separating carbon dioxide and ethane |
US4383841A (en) * | 1980-04-23 | 1983-05-17 | Koch Process Systems, Inc. | Distillative separation of carbon dioxide from hydrogen sulfide |
US4405585A (en) * | 1982-01-18 | 1983-09-20 | Exxon Research And Engineering Co. | Process for the selective removal of hydrogen sulfide from gaseous mixtures with severely sterically hindered secondary aminoether alcohols |
US4441900A (en) * | 1982-05-25 | 1984-04-10 | Union Carbide Corporation | Method of treating carbon-dioxide-containing natural gas |
US4459142A (en) * | 1982-10-01 | 1984-07-10 | Standard Oil Company (Indiana) | Cryogenic distillative removal of CO2 from high CO2 content hydrocarbon containing streams |
DE3303651A1 (en) * | 1983-02-03 | 1984-08-09 | Linde Ag, 6200 Wiesbaden | METHOD AND DEVICE FOR DISASSEMBLING A GAS MIXTURE |
US4511382A (en) * | 1983-09-15 | 1985-04-16 | Exxon Production Research Co. | Method of separating acid gases, particularly carbon dioxide, from methane by the addition of a light gas such as helium |
US4533372A (en) * | 1983-12-23 | 1985-08-06 | Exxon Production Research Co. | Method and apparatus for separating carbon dioxide and other acid gases from methane by the use of distillation and a controlled freezing zone |
GB8420644D0 (en) * | 1984-08-14 | 1984-09-19 | Petrocarbon Dev Ltd | Ammonia synthesis gas |
US4563202A (en) * | 1984-08-23 | 1986-01-07 | Dm International Inc. | Method and apparatus for purification of high CO2 content gas |
US4602477A (en) * | 1985-06-05 | 1986-07-29 | Air Products And Chemicals, Inc. | Membrane-aided distillation for carbon dioxide and hydrocarbon separation |
US4695672A (en) * | 1986-04-21 | 1987-09-22 | Advanced Extraction Technologies, Inc. | Process for extractive-stripping of lean hydrocarbon gas streams at high pressure with a preferential physical solvent |
US4717408A (en) * | 1986-08-01 | 1988-01-05 | Koch Process Systems, Inc. | Process for prevention of water build-up in cryogenic distillation column |
US4720294A (en) * | 1986-08-05 | 1988-01-19 | Air Products And Chemicals, Inc. | Dephlegmator process for carbon dioxide-hydrocarbon distillation |
US4761167A (en) * | 1986-12-12 | 1988-08-02 | Air Products And Chemicals, Inc. | Hydrocarbon recovery from fuel gas |
US4831206A (en) * | 1987-03-05 | 1989-05-16 | Uop | Chemical processing with an operational step sensitive to a feedstream component |
US4762543A (en) * | 1987-03-19 | 1988-08-09 | Amoco Corporation | Carbon dioxide recovery |
FR2615184B1 (en) * | 1987-05-15 | 1989-06-30 | Elf Aquitaine | CRYOGENIC PROCESS FOR SELECTIVE DESULFURIZATION AND SIMULTANEOUS DEGAZOLINATION OF A GAS MIXTURE MAINLY CONSISTING OF METHANE AND CONTAINING H2S AS WELL AS C2 AND MORE HYDROCARBONS |
US4822393A (en) * | 1988-06-30 | 1989-04-18 | Kryos Energy Inc. | Natural gas pretreatment prior to liquefaction |
US4923493A (en) * | 1988-08-19 | 1990-05-08 | Exxon Production Research Company | Method and apparatus for cryogenic separation of carbon dioxide and other acid gases from methane |
US5011521A (en) * | 1990-01-25 | 1991-04-30 | Air Products And Chemicals, Inc. | Low pressure stripping process for production of crude helium |
US5062270A (en) * | 1990-08-31 | 1991-11-05 | Exxon Production Research Company | Method and apparatus to start-up controlled freezing zone process and purify the product stream |
US5265428A (en) * | 1990-10-05 | 1993-11-30 | Exxon Production Research Company | Bubble cap tray for melting solids and method for using same |
US5120338A (en) * | 1991-03-14 | 1992-06-09 | Exxon Production Research Company | Method for separating a multi-component feed stream using distillation and controlled freezing zone |
US5233837A (en) * | 1992-09-03 | 1993-08-10 | Enerfex, Inc. | Process and apparatus for producing liquid carbon dioxide |
FR2697835B1 (en) * | 1992-11-06 | 1995-01-27 | Inst Francais Du Petrole | Method and device for catalytic dehydrogenation of a C2 + paraffinic charge comprising means for inhibiting the water in the effluent. |
US5335504A (en) * | 1993-03-05 | 1994-08-09 | The M. W. Kellogg Company | Carbon dioxide recovery process |
US5403560A (en) * | 1993-05-13 | 1995-04-04 | Texaco Inc. | Fluids mixing and distributing apparatus |
US5620144A (en) * | 1995-02-10 | 1997-04-15 | The Babcock & Wilcox Company | Stacked interspacial spray header for FGD wet scrubber |
US5819555A (en) * | 1995-09-08 | 1998-10-13 | Engdahl; Gerald | Removal of carbon dioxide from a feed stream by carbon dioxide solids separation |
US6082373A (en) * | 1996-07-05 | 2000-07-04 | Kabushiki Kaisha Toshiba | Cleaning method |
US6336334B1 (en) * | 1997-06-16 | 2002-01-08 | Institut Francais De Petrole | Device for crystallization by isentropic expansion and its use |
ID24280A (en) * | 1997-07-01 | 2000-07-13 | Exxon Production Research Co | PROCESS FOR SEPARATING MULTI-COMPONENT GAS FLOWS CONTAINING MOST NOT THE COMPONENTS WHICH CAN FROZE |
TW366409B (en) * | 1997-07-01 | 1999-08-11 | Exxon Production Research Co | Process for liquefying a natural gas stream containing at least one freezable component |
MY117066A (en) * | 1998-10-22 | 2004-04-30 | Exxon Production Research Co | Process for removing a volatile component from natural gas |
EP1016457B1 (en) * | 1998-12-28 | 2003-05-07 | Nippon Sanso Corporation | Vapour-liquid contactor, cryogenic air separation unit and method of gas separation |
US6082133A (en) * | 1999-02-05 | 2000-07-04 | Cryo Fuel Systems, Inc | Apparatus and method for purifying natural gas via cryogenic separation |
US6416729B1 (en) * | 1999-02-17 | 2002-07-09 | Crystatech, Inc. | Process for removing hydrogen sulfide from gas streams which include or are supplemented with sulfur dioxide |
US6605138B2 (en) * | 1999-04-21 | 2003-08-12 | Matthew T. Frondorf | Apparatus and method for exclusively removing VOC from regeneratable solvent in a gas sweetening system |
US6267358B1 (en) * | 1999-06-18 | 2001-07-31 | The Babcock & Wilcox Company | Low pressure drop inlet for high velocity absorbers with straight tanks |
US6240744B1 (en) * | 1999-12-13 | 2001-06-05 | Air Products And Chemicals, Inc. | Process for distillation of multicomponent fluid and production of an argon-enriched stream from a cryogenic air separation process |
US7390459B2 (en) * | 1999-12-13 | 2008-06-24 | Illumina, Inc. | Oligonucleotide synthesizer |
DE10004311A1 (en) * | 2000-02-01 | 2001-08-02 | Basf Ag | Purification of ammonia by distillation |
CA2342136A1 (en) * | 2000-04-05 | 2001-10-05 | Vijay Ramanand Balse | Treatment of gas streams containing hydrogen sulphide |
FR2807504B1 (en) * | 2000-04-07 | 2002-06-14 | Air Liquide | COLUMN FOR CRYOGENIC SEPARATION OF GASEOUS MIXTURES AND METHOD FOR CRYOGENIC SEPARATION OF A HYDROGEN AND CO-CONTAINING MIXTURE USING THE SAME |
FR2808223B1 (en) * | 2000-04-27 | 2002-11-22 | Inst Francais Du Petrole | PROCESS FOR THE PURIFICATION OF AN EFFLUENT CONTAINING CARBON GAS AND HYDROCARBONS BY COMBUSTION |
FR2808460B1 (en) * | 2000-05-02 | 2002-08-09 | Inst Francais Du Petrole | METHOD AND DEVICE FOR SEPARATING AT LEAST ONE ACID GAS CONTAINED IN A GAS MIXTURE |
DE10022465A1 (en) * | 2000-05-09 | 2001-11-15 | Basf Ag | Processing a four carbon cut from the fractionation of crude oil, useful for the recovery of 1,4-butadiene, comprises extractive distillation, selective hydrogenation and distillation |
US6401486B1 (en) * | 2000-05-18 | 2002-06-11 | Rong-Jwyn Lee | Enhanced NGL recovery utilizing refrigeration and reflux from LNG plants |
FR2814378B1 (en) * | 2000-09-26 | 2002-10-31 | Inst Francais Du Petrole | PROCESS FOR PRETREATMENT OF A NATURAL GAS CONTAINING ACID GASES |
FR2820052B1 (en) * | 2001-01-30 | 2003-11-28 | Armines Ass Pour La Rech Et Le | ANTI-SUBLIMATION CARBON DIOXIDE EXTRACTION PROCESS FOR ITS STORAGE |
TW573112B (en) * | 2001-01-31 | 2004-01-21 | Exxonmobil Upstream Res Co | Process of manufacturing pressurized liquid natural gas containing heavy hydrocarbons |
AU785419B2 (en) * | 2001-05-11 | 2007-05-03 | Institut Francais Du Petrole | Process for pretreating a natural gas containing acid compounds |
US6516631B1 (en) * | 2001-08-10 | 2003-02-11 | Mark A. Trebble | Hydrocarbon gas processing |
US7004985B2 (en) * | 2001-09-05 | 2006-02-28 | Texaco, Inc. | Recycle of hydrogen from hydroprocessing purge gas |
US6755251B2 (en) * | 2001-09-07 | 2004-06-29 | Exxonmobil Upstream Research Company | Downhole gas separation method and system |
DE10164264A1 (en) * | 2001-12-27 | 2003-07-17 | Bayer Ag | Process for the preparation of trimethylolpropane |
CN1623074A (en) * | 2002-01-18 | 2005-06-01 | 哥廷理工大学 | Process and device for production of lng by removal of freezable solids |
DE10233387A1 (en) * | 2002-07-23 | 2004-02-12 | Basf Ag | Process for the continuous distillation of oxiranes, especially propylene oxide |
AU2002951005A0 (en) * | 2002-08-27 | 2002-09-12 | Shell Internationale Research Maatschappij B.V. | Method of removing carbon dioxide fouling from cryogenic equipment |
DE60237046D1 (en) * | 2002-09-17 | 2010-08-26 | Fluor Corp | CONFIGURATIONS AND METHOD FOR REMOVING ACID GASES |
AU2002351210A1 (en) * | 2002-12-04 | 2004-06-30 | Fluor Corporation | Improved distillation systems |
AU2003900534A0 (en) * | 2003-02-07 | 2003-02-20 | Shell Internationale Research Maatschappij B.V. | Process and apparatus for removal of a contaminant from a natural gas feed stream |
US6946017B2 (en) * | 2003-12-04 | 2005-09-20 | Gas Technology Institute | Process for separating carbon dioxide and methane |
EA010565B1 (en) * | 2004-07-12 | 2008-10-30 | Эксонмобил Апстрим Рисерч Компани | Methods for removing sulfur-containing compounds from hydrocarbon-containing gases (embodiments) |
CA2583120C (en) * | 2004-12-03 | 2014-03-25 | Exxonmobil Upstream Research Company | Integrated acid gas and sour gas reinjection process |
US7722289B2 (en) * | 2004-12-08 | 2010-05-25 | Casella Waste Systems, Inc. | Systems and methods for underground storage of biogas |
CN1847766A (en) * | 2005-02-11 | 2006-10-18 | 林德股份公司 | Process and apparatus for cooling a gas by direct heat exchange with a liquid refrigerant |
EP1871511A4 (en) * | 2005-04-20 | 2011-05-04 | Fluor Tech Corp | Configurations and methods for claus plant operation with variable sulfur content |
FR2893515A1 (en) * | 2005-11-18 | 2007-05-25 | Inst Francais Du Petrole | Pretreatment of pressurized natural gas to remove acid gases and water by distillation comprises recycling part of the bottoms stream from the distillation column |
FR2895271B1 (en) * | 2005-12-22 | 2008-12-19 | Total France Sa | DEVICE FOR DISCHARGING A TREATMENT ENCLOSURE, IN PARTICULAR HYDROCARBONS, AND CORRESPONDING ENCLOSURE |
NZ573217A (en) * | 2006-05-05 | 2011-11-25 | Plascoenergy Ip Holdings S L Bilbao Schaffhausen Branch | A facility for conversion of carbonaceous feedstock into a reformulated syngas containing CO and H2 |
US8020408B2 (en) * | 2006-12-06 | 2011-09-20 | Praxair Technology, Inc. | Separation method and apparatus |
US7575624B2 (en) * | 2006-12-19 | 2009-08-18 | Uop Pllc | Molecular sieve and membrane system to purify natural gas |
NO329177B1 (en) * | 2007-06-22 | 2010-09-06 | Kanfa Aragon As | Process and system for forming liquid LNG |
US7814975B2 (en) * | 2007-09-18 | 2010-10-19 | Vast Power Portfolio, Llc | Heavy oil recovery with fluid water and carbon dioxide |
US20090220406A1 (en) * | 2008-02-29 | 2009-09-03 | Greatpoint Energy, Inc. | Selective Removal and Recovery of Acid Gases from Gasification Products |
US20100107687A1 (en) * | 2008-11-06 | 2010-05-06 | Diki Andrian | Process for removing gaseous contaminants from a feed gas stream comprising methane and gaseous contaminants |
-
2007
- 2007-10-20 US US12/518,863 patent/US20100018248A1/en not_active Abandoned
- 2007-11-20 WO PCT/US2007/024216 patent/WO2008091316A1/en active Application Filing
- 2007-11-20 GB GB0913741A patent/GB2460193B/en not_active Expired - Fee Related
- 2007-11-20 CA CA002675063A patent/CA2675063A1/en not_active Abandoned
- 2007-11-20 AU AU2007345352A patent/AU2007345352B2/en not_active Ceased
- 2007-12-14 MY MYPI20072254 patent/MY151148A/en unknown
- 2007-12-20 AR ARP070105783A patent/AR064618A1/en not_active Application Discontinuation
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AU2007345352A1 (en) | 2008-07-31 |
WO2008091316A1 (en) | 2008-07-31 |
GB2460193A (en) | 2009-11-25 |
MY151148A (en) | 2014-04-30 |
US20100018248A1 (en) | 2010-01-28 |
AU2007345352B2 (en) | 2013-03-14 |
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