RU2017116832A - Интеграция получения синтез-газа от парового риформинга и сухого риформинга - Google Patents
Интеграция получения синтез-газа от парового риформинга и сухого риформинга Download PDFInfo
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- RU2017116832A RU2017116832A RU2017116832A RU2017116832A RU2017116832A RU 2017116832 A RU2017116832 A RU 2017116832A RU 2017116832 A RU2017116832 A RU 2017116832A RU 2017116832 A RU2017116832 A RU 2017116832A RU 2017116832 A RU2017116832 A RU 2017116832A
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- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/83—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with rare earths or actinides
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- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/382—Multi-step processes
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- C—CHEMISTRY; METALLURGY
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- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
- C07C1/04—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
- C07C1/0485—Set-up of reactors or accessories; Multi-step processes
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- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
- C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
- C07C29/1516—Multisteps
- C07C29/1518—Multisteps one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
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- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
- C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
- C01B2203/0238—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a carbon dioxide reforming step
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
- C01B2203/0244—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being an autothermal reforming step, e.g. secondary reforming processes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
- C01B2203/048—Composition of the impurity the impurity being an organic compound
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/06—Integration with other chemical processes
- C01B2203/061—Methanol production
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/06—Integration with other chemical processes
- C01B2203/062—Hydrocarbon production, e.g. Fischer-Tropsch process
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
- C01B2203/1047—Group VIII metal catalysts
- C01B2203/1052—Nickel or cobalt catalysts
- C01B2203/1058—Nickel catalysts
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1205—Composition of the feed
- C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
- C01B2203/1235—Hydrocarbons
- C01B2203/1241—Natural gas or methane
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/14—Details of the flowsheet
- C01B2203/141—At least two reforming, decomposition or partial oxidation steps in parallel
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/80—Aspect of integrated processes for the production of hydrogen or synthesis gas not covered by groups C01B2203/02 - C01B2203/1695
- C01B2203/82—Several process steps of C01B2203/02 - C01B2203/08 integrated into a single apparatus
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
- C07C2523/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36
- C07C2523/83—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36 with rare earths or actinides
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/40—Ethylene production
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- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Materials Engineering (AREA)
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- Hydrogen, Water And Hydrids (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Claims (26)
1. Способ конверсии метана в олефин и метанол, включающий:
a. контакт метана, диоксида углерода и кислорода с катализатором окислительного сухого риформинга с получением продукционной смеси окислительного сухого риформинга, содержащей монооксид углерода, водород и воду;
b. контакт метана и воды с катализатором парового риформинга с получением продукционной смеси парового риформинга, содержащей монооксид углерода и водород;
c. контакт продукционной смеси окислительного сухого риформинга с катализатором получения олефинов с получением олефиновой продукционной смеси, содержащей олефин и монооксид углерода;
d. выделение монооксида углерода из олефиновой продукционной смеси с получением выделенного монооксида углерода;
e. объединение выделенного монооксида углерода, по меньшей мере, с частью продукционной смеси парового риформинга с получением смеси для получения метанола и
f. контакт смеси для получения метанола с катализатором получения метанола с получением метанола.
2. Способ по п. 1, в котором катализатор окислительного сухого риформинга содержит твердый носитель.
3. Способ по п. 2, в котором твердый носитель содержит по меньшей мере один носитель, выбранный из группы, состоящей из оксида алюминия, диоксида кремния и оксида магния.
4. Способ по п. 1, в котором катализатор окислительного сухого риформинга содержит никель.
5. Способ по п. 4, в котором катализатор окислительного сухого риформинга содержит никель в количестве от приблизительно 2 масс. % до приблизительно 15 масс. % относительно общей массы катализатора.
6. Способ по п. 4, в котором катализатор окислительного сухого риформинга содержит основной оксид металла.
7. Способ по п. 6, в котором основной оксид металла содержит оксид лантана (III).
8. Способ по п. 4, в котором катализатор окислительного сухого риформинга содержит благородный металл.
9. Способ по п. 8, в котором благородный металл содержит по меньшей мере один благородный металл, выбранный из группы, состоящей из платины и рутения.
10. Способ по п. 8, в котором катализатор окислительного сухого риформинга содержит благородный металл в количестве от приблизительно 0,1 масс. % до приблизительно 2 масс. % относительно общей массы катализатора.
11. Способ по п. 1, в котором смесь для получения метанола содержит водород и монооксид углерода в мольном отношении приблизительно 2:1.
12. Способ по п. 1, в котором контакт метана, диоксида углерода и кислорода с катализатором окислительного сухого риформинга, контакт метана и воды с катализатором парового риформинга, контакт продукционной смеси окислительного сухого риформинга с катализатором получения олефинов и контакт смеси для получения метанола с катализатором получения метанола происходит одновременно.
13. Способ по п. 1, в котором олефин содержит этилен.
14. Способ конверсии метана в этилен и метанол, включающий:
a. контакт метана, диоксида углерода и кислорода с катализатором окислительного сухого риформинга с получением продукционной смеси окислительного сухого риформинга, содержащей монооксид углерода, водород и воду, причем катализатор окислительного сухого риформинга содержит никель, основной оксид металла и благородный металл;
b. контакт метана и воды с катализатором парового риформинга с получением продукционной смеси парового риформинга, содержащей монооксид углерода и водород;
c. контакт продукционной смеси окислительного сухого риформинга с катализатором получения олефинов с получением олефиновой продукционной смеси, содержащей этилен и монооксид углерода;
d. выделение монооксида углерода из олефиновой продукционной смеси с получением выделенного монооксида углерода;
e. объединение выделенного монооксида углерода, по меньшей мере, с частью продукционной смеси парового риформинга с получением смеси для получения метанола и
f. контакт смеси для получения метанола с катализатором получения метанола с получением метанола.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201462068812P | 2014-10-27 | 2014-10-27 | |
US62/068,812 | 2014-10-27 | ||
PCT/US2015/057039 WO2016069385A1 (en) | 2014-10-27 | 2015-10-23 | Integration of syngas production from steam reforming and dry reforming |
Publications (1)
Publication Number | Publication Date |
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RU2017116832A true RU2017116832A (ru) | 2018-11-30 |
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Application Number | Title | Priority Date | Filing Date |
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RU2017116832A RU2017116832A (ru) | 2014-10-27 | 2015-10-23 | Интеграция получения синтез-газа от парового риформинга и сухого риформинга |
Country Status (6)
Country | Link |
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US (1) | US20170320730A1 (ru) |
EP (1) | EP3212568A1 (ru) |
JP (1) | JP2017534624A (ru) |
CN (1) | CN107001172A (ru) |
RU (1) | RU2017116832A (ru) |
WO (1) | WO2016069385A1 (ru) |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
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GB2556929A (en) * | 2016-11-26 | 2018-06-13 | Avocet Infinite Plc | Apparatus and method for producing methanol |
GB2556930A (en) * | 2016-11-27 | 2018-06-13 | Avocet Infinite Plc | Apparatus and method for producing methanol |
WO2019021141A1 (en) * | 2017-07-24 | 2019-01-31 | Sabic Global Technologies B.V. | PROCESS FOR PRODUCTION OF METHANOL |
US11103844B2 (en) * | 2018-08-09 | 2021-08-31 | Exxonmobil Research And Engineering Company | Advanced steam cracking |
WO2020116474A1 (ja) * | 2018-12-03 | 2020-06-11 | 古河電気工業株式会社 | 低級オレフィン含有ガスの製造装置および低級オレフィン含有ガスの製造方法 |
US11322766B2 (en) | 2020-05-28 | 2022-05-03 | Saudi Arabian Oil Company | Direct hydrocarbon metal supported solid oxide fuel cell |
US11639290B2 (en) | 2020-06-04 | 2023-05-02 | Saudi Arabian Oil Company | Dry reforming of methane with carbon dioxide at elevated pressure |
US20220154087A1 (en) * | 2020-11-18 | 2022-05-19 | L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude | Carbon dioxide buffer vessel process design |
US20220234889A1 (en) * | 2021-01-25 | 2022-07-28 | Bradley D. Damstedt | Method to control syngas composition by reactor temperature |
EP4105170A1 (en) * | 2021-06-18 | 2022-12-21 | Technip Energies France | Process and plant for flexible production of syngas from hydrocarbons |
US11578016B1 (en) | 2021-08-12 | 2023-02-14 | Saudi Arabian Oil Company | Olefin production via dry reforming and olefin synthesis in a vessel |
US11787759B2 (en) | 2021-08-12 | 2023-10-17 | Saudi Arabian Oil Company | Dimethyl ether production via dry reforming and dimethyl ether synthesis in a vessel |
US11718575B2 (en) | 2021-08-12 | 2023-08-08 | Saudi Arabian Oil Company | Methanol production via dry reforming and methanol synthesis in a vessel |
US11617981B1 (en) | 2022-01-03 | 2023-04-04 | Saudi Arabian Oil Company | Method for capturing CO2 with assisted vapor compression |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
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US2960518A (en) * | 1957-09-27 | 1960-11-15 | Peters Kurt | Ethylene production process |
US6486219B1 (en) * | 2000-09-27 | 2002-11-26 | Exxonmobil Chemical Patents, Inc. | Methanol, olefin, and hydrocarbon synthesis process |
US6444712B1 (en) * | 2000-09-28 | 2002-09-03 | Exxonmobil Chemical Patents, Inc. | Methanol, olefin, and hydrocarbon synthesis process |
US20040122267A1 (en) * | 2002-12-23 | 2004-06-24 | Jaimes Sher | Integrated gas to olefins process with recovery and conversion of by-products |
EP1491494A1 (en) * | 2003-06-20 | 2004-12-29 | Saudi Basic Industries Corporation | Process for producing benzene, ethylene and synthesis gas |
EP2152408A2 (en) * | 2007-04-25 | 2010-02-17 | HRD Corp | Catalyst and method for converting natural gas to higher carbon compounds |
KR100903439B1 (ko) * | 2007-10-15 | 2009-06-18 | 한국화학연구원 | 천연가스로부터 경질탄화수소의 직접 제조방법 |
CN102388117A (zh) * | 2009-04-10 | 2012-03-21 | 南加州大学 | 使石油油料成为环境上二氧化碳中性燃料源材料、衍生产物和再生碳源 |
JP6031289B2 (ja) * | 2012-07-26 | 2016-11-24 | エア・ウォーター株式会社 | 合成ガス製造方法および装置 |
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2015
- 2015-10-23 US US15/520,606 patent/US20170320730A1/en not_active Abandoned
- 2015-10-23 EP EP15797730.7A patent/EP3212568A1/en not_active Withdrawn
- 2015-10-23 RU RU2017116832A patent/RU2017116832A/ru unknown
- 2015-10-23 JP JP2017522943A patent/JP2017534624A/ja active Pending
- 2015-10-23 CN CN201580058313.5A patent/CN107001172A/zh active Pending
- 2015-10-23 WO PCT/US2015/057039 patent/WO2016069385A1/en active Application Filing
Also Published As
Publication number | Publication date |
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CN107001172A (zh) | 2017-08-01 |
WO2016069385A1 (en) | 2016-05-06 |
EP3212568A1 (en) | 2017-09-06 |
JP2017534624A (ja) | 2017-11-24 |
US20170320730A1 (en) | 2017-11-09 |
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