AR100317A1 - Método y sistema para la puesta en marcha de una torre de destilación - Google Patents
Método y sistema para la puesta en marcha de una torre de destilaciónInfo
- Publication number
- AR100317A1 AR100317A1 ARP150101207A ARP150101207A AR100317A1 AR 100317 A1 AR100317 A1 AR 100317A1 AR P150101207 A ARP150101207 A AR P150101207A AR P150101207 A ARP150101207 A AR P150101207A AR 100317 A1 AR100317 A1 AR 100317A1
- Authority
- AR
- Argentina
- Prior art keywords
- section
- lower section
- distillation tower
- commissioning
- rectification
- 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
- F25J3/0266—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
-
- 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
- F25J3/0295—Start-up or control of the process; Details of the apparatus used, e.g. sieve plates, packings
-
- 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
- F25J2200/30—Processes or apparatus using separation by rectification using a side column in a single pressure 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
- F25J2200/50—Processes or apparatus using separation by rectification using multiple (re-)boiler-condensers at different heights of the column
-
- 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
-
- 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
- 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
-
- 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
- F25J2210/60—Natural gas or synthetic natural gas [SNG]
-
- 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
- F25J2235/00—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams
- F25J2235/60—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams the fluid being (a mixture of) 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
- F25J2280/10—Control for or during start-up and cooling down of the installation
-
- 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
-
- 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.
-
- 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
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)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
La presente proporciona un método para la puesta en marcha con metano limpio de una torre de destilación. El método incluye mantener una sección de rectificación y una sección inferior en la torre de destilación, alimentar una corriente a la sección inferior, alimentar metano directamente a por lo menos uno de la sección de rectificación y un conducto de salida de sección de rectificación de la sección de rectificación cuando una concentración de contaminante que sale en forma de vapor en una porción superior de la sección inferior se encuentra por afuera de los valores de una concentración predeterminada e introducir el vapor proveniente de la sección inferior a la sección de rectificación cuando la concentración de contaminante que abandona la porción superior de la sección inferior se encuentra dentro de los valores de concentración predeterminados.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201461982689P | 2014-04-22 | 2014-04-22 |
Publications (1)
Publication Number | Publication Date |
---|---|
AR100317A1 true AR100317A1 (es) | 2016-09-28 |
Family
ID=52815295
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP150101207A AR100317A1 (es) | 2014-04-22 | 2015-04-22 | Método y sistema para la puesta en marcha de una torre de destilación |
Country Status (10)
Country | Link |
---|---|
US (1) | US9739528B2 (es) |
CN (1) | CN105992922B (es) |
AR (1) | AR100317A1 (es) |
AU (1) | AU2015250244B2 (es) |
CA (1) | CA2936715C (es) |
EA (1) | EA032849B1 (es) |
MX (1) | MX363831B (es) |
MY (1) | MY190546A (es) |
SG (1) | SG11201605538VA (es) |
WO (1) | WO2015163997A2 (es) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU2015350515B2 (en) | 2014-11-17 | 2018-11-15 | Exxonmobil Upstream Research Company | Heat exchange mechanism for removing contaminants from a hydrocarbon vapor stream |
AU2016281501B2 (en) | 2015-06-22 | 2019-02-21 | Exxonmobil Upstream Research Company | Purge to intermediate pressure in cryogenic distillation |
CA2998466C (en) * | 2015-09-24 | 2021-06-29 | Exxonmobil Upstream Research Company | Treatment plant for hydrocarbon gas having variable contaminant levels |
WO2019040154A1 (en) * | 2017-08-24 | 2019-02-28 | Exxonmobil Upstream Research Company | METHOD AND SYSTEM FOR GENERATING LNG USING STANDARD MULTI-SHAFT GAS TURBINES, COMPRESSORS AND REFRIGERANT SYSTEMS |
WO2020040952A1 (en) * | 2018-08-22 | 2020-02-27 | Exxonmobil Upstream Research Company | Primary loop start-up method for a high pressure expander process |
Family Cites Families (29)
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US4417909A (en) | 1978-12-04 | 1983-11-29 | Airco, Inc. | Gas separation process |
US4462814A (en) | 1979-11-14 | 1984-07-31 | Koch Process Systems, Inc. | Distillative separations of gas mixtures containing methane, carbon dioxide and other components |
US4383841A (en) | 1980-04-23 | 1983-05-17 | Koch Process Systems, Inc. | Distillative separation of carbon dioxide from hydrogen sulfide |
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 |
US4761167A (en) | 1986-12-12 | 1988-08-02 | Air Products And Chemicals, Inc. | Hydrocarbon recovery from fuel gas |
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 |
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 |
US5819555A (en) | 1995-09-08 | 1998-10-13 | Engdahl; Gerald | Removal of carbon dioxide from a feed stream by carbon dioxide solids separation |
GB2344416B (en) * | 1997-07-01 | 2001-09-12 | Exxonmobil Upstream Res Co | Process for separating a multi-component gas stream containingat least one freezable component |
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 |
US6082133A (en) | 1999-02-05 | 2000-07-04 | Cryo Fuel Systems, Inc | Apparatus and method for purifying natural gas via cryogenic separation |
US6755965B2 (en) | 2000-05-08 | 2004-06-29 | Inelectra S.A. | Ethane extraction process for a hydrocarbon gas stream |
US6516631B1 (en) | 2001-08-10 | 2003-02-11 | Mark A. Trebble | Hydrocarbon gas processing |
EA006001B1 (ru) | 2002-01-18 | 2005-08-25 | Кертин Юниверсити Оф Текнолоджи | Способ и устройство для получения сжиженного природного газа с удалением замерзающих твёрдых частиц |
WO2006062595A1 (en) | 2004-12-03 | 2006-06-15 | Exxonmobil Upstream Research Company Corp-Urc-Sw348 | Integrated acid gas and sour gas reinjection process |
US20100018248A1 (en) | 2007-01-19 | 2010-01-28 | Eleanor R Fieler | Controlled Freeze Zone Tower |
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 |
BRPI1014038A2 (pt) | 2009-04-20 | 2016-04-12 | Exxonmobil Upstream Res Co | sistema e método para remover gases ácidos de uma corrente de gás bruto. |
BR112012001970A2 (pt) | 2009-07-30 | 2016-03-08 | Exxonmobil Upstream Res Co | sistema para remover gases ácidos de uma corrente de gás ácida |
CN102483300B (zh) * | 2009-09-09 | 2015-06-17 | 埃克森美孚上游研究公司 | 从烃气体流中去除酸性气体的低温系统 |
JP2013509300A (ja) | 2009-11-02 | 2013-03-14 | 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 | 硫化水素の除去によって、炭化水素ガス流から酸性ガスを除去するための極低温システム |
SG10201500515QA (en) | 2010-01-22 | 2015-04-29 | Exxonmobil Upstream Res Co | Removal of acid gases from a gas stream, with co2 capture and sequestration |
EP2531269A4 (en) | 2010-02-03 | 2014-02-19 | Exxonmobil Upstream Res Co | SYSTEM AND METHOD FOR USING A COLD LIQUID TO REMOVE COMPATIBLE GAS COMPONENTS FROM PROCESS GAS FLOWS |
AU2011283134B2 (en) * | 2010-07-30 | 2014-04-24 | Exxonmobil Upstream Research Company | Cryogenic systems for removing acid gases from a hydrocarbon gas stream using co-current separation devices |
WO2013015907A1 (en) | 2011-07-22 | 2013-01-31 | Exxonmobil Upstream Research Company | Helium recovery from natural gas streams |
CA2857122C (en) | 2011-12-20 | 2020-08-04 | Exxonmobil Upstream Research Company | Method of separating carbon dioxide from liquid acid gas streams |
MY166180A (en) | 2012-03-21 | 2018-06-07 | Exxonmobil Upstream Res Co | Separating carbon dioxide and ethane from mixed stream |
-
2015
- 2015-03-18 MY MYPI2016001258A patent/MY190546A/en unknown
- 2015-03-18 CN CN201580007801.3A patent/CN105992922B/zh active Active
- 2015-03-18 WO PCT/US2015/021237 patent/WO2015163997A2/en active Application Filing
- 2015-03-18 AU AU2015250244A patent/AU2015250244B2/en active Active
- 2015-03-18 EA EA201692099A patent/EA032849B1/ru not_active IP Right Cessation
- 2015-03-18 MX MX2016009545A patent/MX363831B/es active IP Right Grant
- 2015-03-18 US US14/661,621 patent/US9739528B2/en active Active
- 2015-03-18 CA CA2936715A patent/CA2936715C/en active Active
- 2015-03-18 SG SG11201605538VA patent/SG11201605538VA/en unknown
- 2015-04-22 AR ARP150101207A patent/AR100317A1/es unknown
Also Published As
Publication number | Publication date |
---|---|
EA032849B1 (ru) | 2019-07-31 |
CA2936715C (en) | 2018-07-17 |
US20150300735A1 (en) | 2015-10-22 |
CN105992922B (zh) | 2019-06-18 |
EA201692099A1 (ru) | 2017-02-28 |
AU2015250244B2 (en) | 2018-04-26 |
US9739528B2 (en) | 2017-08-22 |
MY190546A (en) | 2022-04-27 |
MX363831B (es) | 2019-04-04 |
WO2015163997A3 (en) | 2016-02-04 |
AU2015250244A1 (en) | 2016-08-11 |
MX2016009545A (es) | 2016-10-28 |
SG11201605538VA (en) | 2016-11-29 |
WO2015163997A2 (en) | 2015-10-29 |
CA2936715A1 (en) | 2015-10-29 |
CN105992922A (zh) | 2016-10-05 |
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