EA200800416A1 - Способы и конфигурации для извлечения газоконденсатных жидкостей - Google Patents
Способы и конфигурации для извлечения газоконденсатных жидкостейInfo
- Publication number
- EA200800416A1 EA200800416A1 EA200800416A EA200800416A EA200800416A1 EA 200800416 A1 EA200800416 A1 EA 200800416A1 EA 200800416 A EA200800416 A EA 200800416A EA 200800416 A EA200800416 A EA 200800416A EA 200800416 A1 EA200800416 A1 EA 200800416A1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- carbon dioxide
- configurations
- source gas
- methods
- demethanizer
- Prior art date
Links
Classifications
-
- 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
-
- 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
-
- 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
- F25J3/0238—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 2 carbon atoms or more
-
- 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
-
- 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
- F25J2200/70—Refluxing the column with a condensed part of the feed stream, i.e. fractionator top is stripped or self-rectified
-
- 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
- F25J2200/76—Refluxing the column with condensed overhead gas being cycled in a quasi-closed loop refrigeration cycle
-
- 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
-
- 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
- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/06—Splitting of the feed stream, e.g. for treating or cooling in different ways
-
- 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
- F25J2215/60—Methane
-
- 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
-
- 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
-
- 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
-
- 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
- F25J2245/00—Processes or apparatus involving steps for recycling of process streams
- F25J2245/02—Recycle of a stream in general, e.g. a by-pass stream
-
- 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
- F25J2280/02—Control in general, load changes, different modes ("runs"), measurements
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Fuel Cell (AREA)
Abstract
Рассматриваемые NGL-установки включают в себя байпасный контур исходного газа, благодаря которому обеспечивается часть исходного газа для объединения с паровой фракцией исходного газа ниже по потоку, чтобы увеличить при этом температуру на входе турбоэспандера и температуру деметанизатора. Рассматриваемые конфигурации особенно предпочтительны для исходных газов с относительно высоким содержанием диоксида углерода, поскольку они полностью устраняют замерзание диоксида углерода в деметанизаторе, обеспечивают дополнительное производство энергии турбоэспандером и извлечение компонентов C+ до уровней по меньшей мере 80%, в то же время обеспечивая низкое содержание диоксида углерода в NGL-продукте.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US70251605P | 2005-07-25 | 2005-07-25 | |
PCT/US2006/028471 WO2007014069A2 (en) | 2005-07-25 | 2006-07-20 | Ngl recovery methods and configurations |
Publications (2)
Publication Number | Publication Date |
---|---|
EA200800416A1 true EA200800416A1 (ru) | 2008-06-30 |
EA011523B1 EA011523B1 (ru) | 2009-04-28 |
Family
ID=37683843
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EA200800416A EA011523B1 (ru) | 2005-07-25 | 2006-07-20 | Способ извлечения газоконденсатных жидкостей и устройство для его реализации |
Country Status (7)
Country | Link |
---|---|
US (1) | US9410737B2 (ru) |
EP (1) | EP1907777A2 (ru) |
AU (1) | AU2006272800B2 (ru) |
CA (1) | CA2616450C (ru) |
EA (1) | EA011523B1 (ru) |
MX (1) | MX2008000718A (ru) |
WO (1) | WO2007014069A2 (ru) |
Families Citing this family (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2185878A1 (en) | 2007-08-14 | 2010-05-19 | Fluor Technologies Corporation | Configurations and methods for improved natural gas liquids recovery |
US9243842B2 (en) * | 2008-02-15 | 2016-01-26 | Black & Veatch Corporation | Combined synthesis gas separation and LNG production method and system |
US10113127B2 (en) | 2010-04-16 | 2018-10-30 | Black & Veatch Holding Company | Process for separating nitrogen from a natural gas stream with nitrogen stripping in the production of liquefied natural gas |
WO2012075266A2 (en) | 2010-12-01 | 2012-06-07 | Black & Veatch Corporation | Ngl recovery from natural gas using a mixed refrigerant |
US10451344B2 (en) | 2010-12-23 | 2019-10-22 | Fluor Technologies Corporation | Ethane recovery and ethane rejection methods and configurations |
FR2969745B1 (fr) * | 2010-12-27 | 2013-01-25 | Technip France | Procede de production d'un courant riche en methane et d'un courant riche en hydrocarbures en c2+ et installation associee. |
MX361725B (es) | 2011-06-20 | 2018-12-14 | Fluor Tech Corp | Configuraciones y metodos para reajustar una instalacion de recuperacion de gas natural licuado. |
WO2013083156A1 (en) | 2011-12-05 | 2013-06-13 | Blue Wave Co S.A. | Scavenging system |
US10139157B2 (en) | 2012-02-22 | 2018-11-27 | Black & Veatch Holding Company | NGL recovery from natural gas using a mixed refrigerant |
US20140260421A1 (en) * | 2013-03-14 | 2014-09-18 | Ipsi L.L.C | Systems and Methods for Enhanced Recovery of NGL Hydrocarbons |
WO2014151908A1 (en) | 2013-03-14 | 2014-09-25 | Fluor Technologies Corporation | Flexible ngl recovery methods and configurations |
CN103438661A (zh) * | 2013-08-30 | 2013-12-11 | 北京麦科直通石化工程设计有限公司 | 一种低能耗的新型天然气液化工艺 |
FR3012150B1 (fr) | 2013-10-23 | 2016-09-02 | Technip France | Procede de fractionnement d'un courant de gaz craque, mettant en oeuvre un courant de recycle intermediaire, et installation associee |
US10563913B2 (en) | 2013-11-15 | 2020-02-18 | Black & Veatch Holding Company | Systems and methods for hydrocarbon refrigeration with a mixed refrigerant cycle |
US9574822B2 (en) | 2014-03-17 | 2017-02-21 | Black & Veatch Corporation | Liquefied natural gas facility employing an optimized mixed refrigerant system |
US10017701B2 (en) | 2014-06-02 | 2018-07-10 | Aspen Engineering Services, Llc | Flare elimination process and methods of use |
EP3040405A1 (en) | 2014-12-30 | 2016-07-06 | Technip France | Method for improving propylene recovery from fluid catalytic cracker unit |
US10006701B2 (en) | 2016-01-05 | 2018-06-26 | Fluor Technologies Corporation | Ethane recovery or ethane rejection operation |
US10330382B2 (en) | 2016-05-18 | 2019-06-25 | Fluor Technologies Corporation | Systems and methods for LNG production with propane and ethane recovery |
MX2019001888A (es) | 2016-09-09 | 2019-06-03 | Fluor Tech Corp | Metodos y configuracion para readaptacion de planta liquidos de gas (ngl) para alta recuperacion de etano. |
EP3694959A4 (en) * | 2017-09-06 | 2021-09-08 | Linde Engineering North America Inc. | PROCESS FOR PROVIDING REFRIGERATION IN PLANTS FOR THE RECOVERY OF NATURAL GAS LIQUIDS |
US11112175B2 (en) | 2017-10-20 | 2021-09-07 | Fluor Technologies Corporation | Phase implementation of natural gas liquid recovery plants |
US12098882B2 (en) | 2018-12-13 | 2024-09-24 | Fluor Technologies Corporation | Heavy hydrocarbon and BTEX removal from pipeline gas to LNG liquefaction |
RU2727505C1 (ru) * | 2019-01-09 | 2020-07-22 | Андрей Владиславович Курочкин | Установка деэтанизации магистрального газа по технологии нтдр (варианты) |
EP4031822A1 (en) * | 2019-09-19 | 2022-07-27 | Exxonmobil Upstream Research Company (EMHC-N1-4A-607) | Pretreatment and pre-cooling of natural gas by high pressure compression and expansion |
WO2021247713A1 (en) * | 2020-06-03 | 2021-12-09 | Chart Energy & Chemicals, Inc. | Gas stream component removal system and method |
RU2770377C2 (ru) * | 2020-10-09 | 2022-04-15 | Общество С Ограниченной Ответственностью "Пегаз Инжиниринг" | Установка комплексной подготовки природного газа путем низкотемпературной конденсации |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3355901A (en) * | 1964-08-10 | 1967-12-05 | Air Reduction | Control of degree of superheat in expansion engine exhaust |
US3595782A (en) * | 1968-12-05 | 1971-07-27 | Fluor Corp | Method for separating crabon dioxide from hydrocarbons |
US3793157A (en) * | 1971-03-24 | 1974-02-19 | Phillips Petroleum Co | Method for separating a multicomponent feedstream |
US4278457A (en) * | 1977-07-14 | 1981-07-14 | Ortloff Corporation | Hydrocarbon gas processing |
US4203741A (en) * | 1978-06-14 | 1980-05-20 | Phillips Petroleum Company | Separate feed entry to separator-contactor in gas separation |
US4322225A (en) * | 1980-11-04 | 1982-03-30 | Phillips Petroleum Company | Natural gas processing |
US4456461A (en) | 1982-09-09 | 1984-06-26 | Phillips Petroleum Company | Separation of low boiling constituents from a mixed gas |
US4854955A (en) | 1988-05-17 | 1989-08-08 | Elcor Corporation | Hydrocarbon gas processing |
US5992175A (en) * | 1997-12-08 | 1999-11-30 | Ipsi Llc | Enhanced NGL recovery processes |
US6237365B1 (en) * | 1998-01-20 | 2001-05-29 | Transcanada Energy Ltd. | Apparatus for and method of separating a hydrocarbon gas into two fractions and a method of retrofitting an existing cryogenic apparatus |
US6354105B1 (en) | 1999-12-03 | 2002-03-12 | Ipsi L.L.C. | Split feed compression process for high recovery of ethane and heavier components |
US6401486B1 (en) * | 2000-05-18 | 2002-06-11 | Rong-Jwyn Lee | Enhanced NGL recovery utilizing refrigeration and reflux from LNG plants |
FR2817766B1 (fr) * | 2000-12-13 | 2003-08-15 | Technip Cie | Procede et installation de separation d'un melange gazeux contenant du methane par distillation,et gaz obtenus par cette separation |
US6554105B2 (en) * | 2001-02-05 | 2003-04-29 | E. F. Bavis & Associates, Inc. | Conveyor system with stabilized carrier |
US6564580B2 (en) * | 2001-06-29 | 2003-05-20 | Exxonmobil Upstream Research Company | Process for recovering ethane and heavier hydrocarbons from methane-rich pressurized liquid mixture |
US6516631B1 (en) | 2001-08-10 | 2003-02-11 | Mark A. Trebble | Hydrocarbon gas processing |
US7484385B2 (en) * | 2003-01-16 | 2009-02-03 | Lummus Technology Inc. | Multiple reflux stream hydrocarbon recovery process |
CN100565061C (zh) | 2003-10-30 | 2009-12-02 | 弗劳尔科技公司 | 柔性液态天然气工艺和方法 |
-
2006
- 2006-07-20 CA CA2616450A patent/CA2616450C/en not_active Expired - Fee Related
- 2006-07-20 AU AU2006272800A patent/AU2006272800B2/en not_active Ceased
- 2006-07-20 US US11/917,392 patent/US9410737B2/en not_active Expired - Fee Related
- 2006-07-20 EP EP06788176A patent/EP1907777A2/en not_active Withdrawn
- 2006-07-20 MX MX2008000718A patent/MX2008000718A/es active IP Right Grant
- 2006-07-20 EA EA200800416A patent/EA011523B1/ru not_active IP Right Cessation
- 2006-07-20 WO PCT/US2006/028471 patent/WO2007014069A2/en active Application Filing
Also Published As
Publication number | Publication date |
---|---|
WO2007014069B1 (en) | 2007-06-21 |
EP1907777A2 (en) | 2008-04-09 |
AU2006272800A1 (en) | 2007-02-01 |
WO2007014069A3 (en) | 2007-05-10 |
EA011523B1 (ru) | 2009-04-28 |
CA2616450C (en) | 2011-07-12 |
US20100043488A1 (en) | 2010-02-25 |
US9410737B2 (en) | 2016-08-09 |
WO2007014069A2 (en) | 2007-02-01 |
AU2006272800B2 (en) | 2009-08-27 |
MX2008000718A (es) | 2008-03-19 |
CA2616450A1 (en) | 2007-02-01 |
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