RU2569301C2 - Многостадийный способ крекинга и отпарки в установке fcc - Google Patents
Многостадийный способ крекинга и отпарки в установке fcc Download PDFInfo
- Publication number
- RU2569301C2 RU2569301C2 RU2013122113/04A RU2013122113A RU2569301C2 RU 2569301 C2 RU2569301 C2 RU 2569301C2 RU 2013122113/04 A RU2013122113/04 A RU 2013122113/04A RU 2013122113 A RU2013122113 A RU 2013122113A RU 2569301 C2 RU2569301 C2 RU 2569301C2
- Authority
- RU
- Russia
- Prior art keywords
- stripping
- cracking
- stage
- catalyst
- grains
- Prior art date
Links
- 238000005336 cracking Methods 0.000 title claims abstract description 136
- 238000000034 method Methods 0.000 title claims abstract description 71
- 239000003054 catalyst Substances 0.000 claims abstract description 156
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- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 90
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 31
- 238000006243 chemical reaction Methods 0.000 claims abstract description 31
- 238000004523 catalytic cracking Methods 0.000 claims abstract description 29
- 238000000926 separation method Methods 0.000 claims abstract description 16
- 238000009835 boiling Methods 0.000 claims abstract description 12
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- 238000005086 pumping Methods 0.000 claims description 5
- 239000002028 Biomass Substances 0.000 claims description 3
- 238000004517 catalytic hydrocracking Methods 0.000 claims description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 2
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- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 abstract 3
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- 125000003118 aryl group Chemical group 0.000 description 1
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- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
- C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
- C07C4/06—Catalytic processes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
- B01J38/06—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst using steam
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
- B01J38/12—Treating with free oxygen-containing gas
- B01J38/14—Treating with free oxygen-containing gas with control of oxygen content in oxidation gas
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
- C10G11/182—Regeneration
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
- C10G51/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
- C10G51/026—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only only catalytic cracking steps
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1011—Biomass
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/301—Boiling range
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4081—Recycling aspects
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4093—Catalyst stripping
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/70—Catalyst aspects
- C10G2300/708—Coking aspect, coke content and composition of deposits
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/80—Additives
- C10G2300/805—Water
- C10G2300/807—Steam
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/20—C2-C4 olefins
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR1058432 | 2010-10-15 | ||
| FR1058432A FR2966161B1 (fr) | 2010-10-15 | 2010-10-15 | Procede de reaction et de stripage etage dans une unite de fcc pour maximisation de la production d'olefines |
| PCT/FR2011/052366 WO2012049416A2 (fr) | 2010-10-15 | 2011-10-11 | Procede de craquage et de stripage multi-etage dans une unite de fcc. |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| RU2013122113A RU2013122113A (ru) | 2014-11-20 |
| RU2569301C2 true RU2569301C2 (ru) | 2015-11-20 |
Family
ID=43837994
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| RU2013122113/04A RU2569301C2 (ru) | 2010-10-15 | 2011-10-11 | Многостадийный способ крекинга и отпарки в установке fcc |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US9388095B2 (enExample) |
| EP (1) | EP2627736B1 (enExample) |
| JP (1) | JP6140076B2 (enExample) |
| KR (1) | KR101880161B1 (enExample) |
| CN (1) | CN103154204B (enExample) |
| ES (1) | ES2772139T3 (enExample) |
| FR (1) | FR2966161B1 (enExample) |
| RU (1) | RU2569301C2 (enExample) |
| WO (1) | WO2012049416A2 (enExample) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2650154C1 (ru) * | 2016-12-16 | 2018-04-09 | Общество с ограниченной ответственностью "Биологические Источники Энергии" (ООО "БиоИстЭн") | Устройство с псевдоожиженным фонтанирующим слоем кольцеобразной формы и способ его работы |
| RU2836396C1 (ru) * | 2024-04-08 | 2025-03-14 | Акционерное общество "Газпромнефть - Омский НПЗ" (АО "Газпромнефть-ОНПЗ") | Способ отпаривания отработанного катализатора и устройство отпаривания отработанного катализатора установки каталитического крекинга |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9604321B1 (en) * | 2013-05-02 | 2017-03-28 | 360° Ballistics, LLC | Repair of ballistic concrete panels |
| WO2016009333A1 (en) | 2014-07-17 | 2016-01-21 | Sabic Global Technologies B.V. | Upgrading hydrogen deficient streams using hydrogen donor streams in a hydropyrolysis process |
| TW201802061A (zh) | 2016-03-21 | 2018-01-16 | 諾沃梅爾公司 | 丙烯酸及其製造方法 |
| WO2019227049A1 (en) * | 2018-05-24 | 2019-11-28 | Technip Process Technology, Inc. | Stripper and packing apparatuses |
| CN108753356B (zh) * | 2018-06-21 | 2020-09-11 | 清华大学 | 一种多级逆流催化裂化/裂解系统及方法 |
| US11167258B2 (en) * | 2019-05-14 | 2021-11-09 | Uop Llc | Apparatus and process for separating gases from catalyst and revamp |
| US11873452B1 (en) | 2022-12-12 | 2024-01-16 | Saudi Arabian Oil Company | Methods for processing hydrocarbons to produce light olefins using catalyst formulations or mixtures |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2079541C1 (ru) * | 1991-11-13 | 1997-05-20 | Юоп | Способ проведения каталитического крекинга сырья в псевдоожиженном слое и устройство для его осуществления |
| RU2276183C2 (ru) * | 2001-02-22 | 2006-05-10 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Реактор каталитического крекинга с псевдоожиженным слоем катализатора и его применение |
| US20090159497A1 (en) * | 2007-12-21 | 2009-06-25 | Hedrick Brian W | System and method of producing heat in a fluid catalytic cracking unit |
Family Cites Families (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3928172A (en) * | 1973-07-02 | 1975-12-23 | Mobil Oil Corp | Catalytic cracking of FCC gasoline and virgin naphtha |
| FR2728805B1 (fr) | 1994-12-29 | 1997-03-28 | Total Raffinage Distribution | Procede et dispositif pour le strippage de solides fluidises et utilisation dans un procede de craquage a l'etat fluide |
| JP2906086B2 (ja) * | 1995-04-27 | 1999-06-14 | エービービー ルーマス グローバル インコーポレイテッド | 使用済みｆｃｃ触媒を使用するオレフィン系炭化水素の転化法 |
| FR2757785B1 (fr) * | 1996-12-31 | 1999-11-26 | Total Raffinage Distribution | Dispositif pour le traitement de particules solides en lit fluidise, et son utilisation |
| US6224833B1 (en) | 1998-12-15 | 2001-05-01 | Koch-Glitsch, Inc. | Apparatus for contacting of gases and solids in fluidized beds |
| US6740227B2 (en) | 1999-12-29 | 2004-05-25 | Uop Llc | Stripping process with fully distributed openings on baffles |
| US7077997B1 (en) | 2002-08-16 | 2006-07-18 | Uop Llc | Stripping apparatus |
| US7022221B1 (en) | 2002-08-16 | 2006-04-04 | Uop Llc | Stripping apparatus and process |
| US7267759B2 (en) * | 2003-02-28 | 2007-09-11 | Exxonmobil Research And Engineering Company | Fractionating and further cracking a C6 fraction from a naphtha feed for propylene generation |
| US7276210B2 (en) * | 2003-08-20 | 2007-10-02 | Petroleo Brasileiro S.A. -Petrobras | Stripping apparatus and process |
| US7332132B2 (en) * | 2004-03-19 | 2008-02-19 | Uop Llc | Stripping apparatus and process |
| BRPI0403184B1 (pt) * | 2004-07-30 | 2015-04-07 | Petroleo Brasileiro Sa | Processo para alterar a distribuição de produtos de craqueamento catalítico fluido de hidrocarbonetos |
| CN1332747C (zh) | 2004-10-22 | 2007-08-22 | 中国石油化工股份有限公司 | 一种催化裂化汽提器内构件及其设置方法 |
| KR101279321B1 (ko) | 2006-02-13 | 2013-06-26 | 유오피 엘엘씨 | 탈리 장치 및 탈리 방법 |
| US20090269252A1 (en) * | 2008-04-23 | 2009-10-29 | Stone & Webster Process Technology, Inc. | Operation of catalyst withdrawal wells with packing |
-
2010
- 2010-10-15 FR FR1058432A patent/FR2966161B1/fr active Active
-
2011
- 2011-10-11 RU RU2013122113/04A patent/RU2569301C2/ru not_active IP Right Cessation
- 2011-10-11 CN CN201180049853.9A patent/CN103154204B/zh not_active Expired - Fee Related
- 2011-10-11 US US13/877,788 patent/US9388095B2/en active Active
- 2011-10-11 KR KR1020137012601A patent/KR101880161B1/ko active Active
- 2011-10-11 ES ES11832095T patent/ES2772139T3/es active Active
- 2011-10-11 EP EP11832095.1A patent/EP2627736B1/fr active Active
- 2011-10-11 WO PCT/FR2011/052366 patent/WO2012049416A2/fr not_active Ceased
- 2011-10-11 JP JP2013533260A patent/JP6140076B2/ja active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2079541C1 (ru) * | 1991-11-13 | 1997-05-20 | Юоп | Способ проведения каталитического крекинга сырья в псевдоожиженном слое и устройство для его осуществления |
| RU2276183C2 (ru) * | 2001-02-22 | 2006-05-10 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Реактор каталитического крекинга с псевдоожиженным слоем катализатора и его применение |
| US20090159497A1 (en) * | 2007-12-21 | 2009-06-25 | Hedrick Brian W | System and method of producing heat in a fluid catalytic cracking unit |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2650154C1 (ru) * | 2016-12-16 | 2018-04-09 | Общество с ограниченной ответственностью "Биологические Источники Энергии" (ООО "БиоИстЭн") | Устройство с псевдоожиженным фонтанирующим слоем кольцеобразной формы и способ его работы |
| WO2018111151A1 (ru) * | 2016-12-16 | 2018-06-21 | Сергей Юрьевич ВИЛЬЧЕК | Устройство с псевдоожиженным фонтанирующим слоем кольцеобразной формы и способ его работы |
| EA039940B1 (ru) * | 2016-12-16 | 2022-03-30 | Сиа "Эмпирио" | Устройство с псевдоожиженным фонтанирующим слоем кольцеобразной формы и способ его работы |
| US11369933B2 (en) | 2016-12-16 | 2022-06-28 | Sia “Empyrio” | Device with annular spouted fluidized bed and operating method therefor |
| RU2836396C1 (ru) * | 2024-04-08 | 2025-03-14 | Акционерное общество "Газпромнефть - Омский НПЗ" (АО "Газпромнефть-ОНПЗ") | Способ отпаривания отработанного катализатора и устройство отпаривания отработанного катализатора установки каталитического крекинга |
Also Published As
| Publication number | Publication date |
|---|---|
| ES2772139T3 (es) | 2020-07-07 |
| FR2966161B1 (fr) | 2013-12-20 |
| CN103154204A (zh) | 2013-06-12 |
| FR2966161A1 (fr) | 2012-04-20 |
| JP2013541617A (ja) | 2013-11-14 |
| WO2012049416A9 (fr) | 2012-08-09 |
| US9388095B2 (en) | 2016-07-12 |
| CN103154204B (zh) | 2015-05-20 |
| WO2012049416A2 (fr) | 2012-04-19 |
| KR20130106856A (ko) | 2013-09-30 |
| JP6140076B2 (ja) | 2017-05-31 |
| US20130267747A1 (en) | 2013-10-10 |
| KR101880161B1 (ko) | 2018-07-20 |
| WO2012049416A3 (fr) | 2012-06-21 |
| EP2627736B1 (fr) | 2019-12-04 |
| EP2627736A2 (fr) | 2013-08-21 |
| RU2013122113A (ru) | 2014-11-20 |
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