IN2012DN00444A - - Google Patents
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- Publication number
- IN2012DN00444A IN2012DN00444A IN444DEN2012A IN2012DN00444A IN 2012DN00444 A IN2012DN00444 A IN 2012DN00444A IN 444DEN2012 A IN444DEN2012 A IN 444DEN2012A IN 2012DN00444 A IN2012DN00444 A IN 2012DN00444A
- Authority
- IN
- India
- Prior art keywords
- reactor
- fatty acid
- alkyl ester
- acid alkyl
- converting
- Prior art date
Links
- 235000014113 dietary fatty acids Nutrition 0.000 abstract 6
- 229930195729 fatty acid Natural products 0.000 abstract 6
- 239000000194 fatty acid Substances 0.000 abstract 6
- 150000004665 fatty acids Chemical class 0.000 abstract 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract 2
- 239000003054 catalyst Substances 0.000 abstract 2
- 239000003225 biodiesel Substances 0.000 abstract 1
- 239000000446 fuel Substances 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 239000002994 raw material Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C10L1/026—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression ignition
-
- 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
- B01J14/00—Chemical processes in general for reacting liquids with liquids; Apparatus specially adapted therefor
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/006—Baffles
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/1812—Tubular reactors
- B01J19/1818—Tubular reactors in series
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/1868—Stationary reactors having moving elements inside resulting in a loop-type movement
- B01J19/1875—Stationary reactors having moving elements inside resulting in a loop-type movement internally, i.e. the mixture circulating inside the vessel such that the upwards stream is separated physically from the downwards stream(s)
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/08—Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/12—Refining fats or fatty oils by distillation
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/003—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fatty acids with alcohols
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00002—Chemical plants
- B01J2219/00004—Scale aspects
- B01J2219/00006—Large-scale industrial plants
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00002—Chemical plants
- B01J2219/00027—Process aspects
- B01J2219/0004—Processes in series
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00761—Details of the reactor
- B01J2219/00763—Baffles
- B01J2219/00765—Baffles attached to the reactor wall
- B01J2219/00768—Baffles attached to the reactor wall vertical
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00761—Details of the reactor
- B01J2219/00763—Baffles
- B01J2219/00765—Baffles attached to the reactor wall
- B01J2219/0077—Baffles attached to the reactor wall inclined
-
- 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
- C10G2300/1014—Biomass of vegetal origin
-
- 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
- C10G2300/201—Impurities
-
- 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
- C10G2300/4006—Temperature
-
- 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
- C10G2300/4012—Pressure
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- General Chemical & Material Sciences (AREA)
- Microbiology (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Fats And Perfumes (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
The present invention relates to an apparatus for preparing fatty acid alkyl ester for bio-diesel fuels, the apparatus comprising a first reactor (11) for esterifying fatty acid raw material (1) with alcohol (2) without using catalyst under a temperature of 200°C to 350°C and a pressure of atmospheric pressure to 10 bar and for converting 80 to 90% of total fatty acid into fatty acid alkyl ester; and a second reactor (12) for converting remaining fatty acid unconverted at the first reactor (11) into fatty acid alkyl ester without using catalyst, wherein a mixture containing water produced at the first reactor (11) and the excess alcohol which is unreacted at the first reactor (11) is extracted in gas phase through the upper part of the first reactor (11).
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/KR2006/001620 WO2007126166A1 (en) | 2006-04-28 | 2006-04-28 | Method and apparatus for preparing fatty acid alkyl ester using fatty acid |
Publications (1)
Publication Number | Publication Date |
---|---|
IN2012DN00444A true IN2012DN00444A (en) | 2015-05-15 |
Family
ID=38655672
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
IN444DEN2012 IN2012DN00444A (en) | 2006-04-28 | 2006-04-28 |
Country Status (10)
Country | Link |
---|---|
US (1) | US7951967B2 (en) |
EP (1) | EP2013319B1 (en) |
JP (1) | JP5232139B2 (en) |
CN (1) | CN101198677B (en) |
BR (1) | BRPI0621209B1 (en) |
ES (1) | ES2721427T3 (en) |
IN (1) | IN2012DN00444A (en) |
MX (1) | MX2008011595A (en) |
PL (1) | PL2013319T3 (en) |
WO (1) | WO2007126166A1 (en) |
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DE102006047617B4 (en) | 2006-10-09 | 2008-11-27 | Clariant International Limited | Process for the preparation of basic (meth) acrylamides |
EP2257518B1 (en) | 2008-04-01 | 2016-03-09 | SK Chemicals Co., Ltd. | Method for preparing fatty acid alkyl ester using fatty acid |
DE102008017216B4 (en) | 2008-04-04 | 2013-08-14 | Clariant International Ltd. | Continuous process for the preparation of fatty acid amides |
KR101554607B1 (en) * | 2008-11-07 | 2015-09-22 | 에스케이케미칼주식회사 | Method and apparatus for preparing fatty acid alkyl ester using fatty acid |
US8889932B2 (en) | 2008-11-26 | 2014-11-18 | Elevance Renewable Sciences, Inc. | Methods of producing jet fuel from natural oil feedstocks through oxygen-cleaved reactions |
ES2687776T3 (en) | 2008-11-26 | 2018-10-29 | Elevance Renewable Sciences, Inc. | Methods for producing airplane fuel from natural oil raw materials through metathesis reactions |
DE102009031054A1 (en) | 2009-06-30 | 2011-01-13 | Clariant International Ltd. | Continuous process for the preparation of esters of aromatic carboxylic acids |
DE102009031053A1 (en) | 2009-06-30 | 2011-01-13 | Clariant International Ltd. | Continuous process for the preparation of esters of aliphatic carboxylic acids |
DE102009031059A1 (en) | 2009-06-30 | 2011-01-05 | Clariant International Ltd. | Apparatus for continuously carrying out chemical reactions at high temperatures |
FI124686B (en) | 2009-08-14 | 2014-12-15 | Forchem Oy | Process for refining crude oil |
DE102009042522A1 (en) | 2009-09-22 | 2011-04-07 | Clariant International Ltd. | Continuous transesterification process |
DE102009042523B4 (en) | 2009-09-22 | 2012-02-16 | Clariant International Ltd. | Apparatus and method for the continuous performance of heterogeneously catalyzed chemical reactions at high temperatures |
US9365487B2 (en) | 2009-10-12 | 2016-06-14 | Elevance Renewable Sciences, Inc. | Methods of refining and producing dibasic esters and acids from natural oil feedstocks |
US9175231B2 (en) | 2009-10-12 | 2015-11-03 | Elevance Renewable Sciences, Inc. | Methods of refining natural oils and methods of producing fuel compositions |
US9000246B2 (en) | 2009-10-12 | 2015-04-07 | Elevance Renewable Sciences, Inc. | Methods of refining and producing dibasic esters and acids from natural oil feedstocks |
US8735640B2 (en) | 2009-10-12 | 2014-05-27 | Elevance Renewable Sciences, Inc. | Methods of refining and producing fuel and specialty chemicals from natural oil feedstocks |
US9382502B2 (en) | 2009-10-12 | 2016-07-05 | Elevance Renewable Sciences, Inc. | Methods of refining and producing isomerized fatty acid esters and fatty acids from natural oil feedstocks |
US9222056B2 (en) | 2009-10-12 | 2015-12-29 | Elevance Renewable Sciences, Inc. | Methods of refining natural oils, and methods of producing fuel compositions |
US9169447B2 (en) | 2009-10-12 | 2015-10-27 | Elevance Renewable Sciences, Inc. | Methods of refining natural oils, and methods of producing fuel compositions |
EP3170802B1 (en) | 2009-10-12 | 2019-06-19 | Elevance Renewable Sciences, Inc. | Methods of refining and producing fuel from natural oil feedstocks |
US9051519B2 (en) | 2009-10-12 | 2015-06-09 | Elevance Renewable Sciences, Inc. | Diene-selective hydrogenation of metathesis derived olefins and unsaturated esters |
FR2966457B1 (en) | 2010-10-21 | 2012-10-19 | IFP Energies Nouvelles | PROCESS FOR THE PRODUCTION OF ALKYL ESTERS FROM VEGETABLE OR ANIMAL OIL AND AN ALIPHATIC MONOALCOOL WITH THERMAL INTEGRATION |
CN102559393B (en) * | 2010-12-23 | 2015-02-25 | 中国石油化工股份有限公司 | Method for preparing biodiesel with low acid value |
DE102010056565A1 (en) | 2010-12-30 | 2012-07-05 | Clariant International Ltd. | Process for modifying hydroxyl-bearing polymers |
DE102010056564A1 (en) | 2010-12-30 | 2012-07-05 | Clariant International Limited | Hydroxyl groups and ester-bearing polymers and processes for their preparation |
WO2013026739A1 (en) * | 2011-08-24 | 2013-02-28 | Basf Se | Process for preparing mercaptoalkyl carboxylates |
US9133416B2 (en) | 2011-12-22 | 2015-09-15 | Elevance Renewable Sciences, Inc. | Methods for suppressing isomerization of olefin metathesis products |
US9169174B2 (en) | 2011-12-22 | 2015-10-27 | Elevance Renewable Sciences, Inc. | Methods for suppressing isomerization of olefin metathesis products |
US9139493B2 (en) | 2011-12-22 | 2015-09-22 | Elevance Renewable Sciences, Inc. | Methods for suppressing isomerization of olefin metathesis products |
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US9388098B2 (en) | 2012-10-09 | 2016-07-12 | Elevance Renewable Sciences, Inc. | Methods of making high-weight esters, acids, and derivatives thereof |
CN102965201B (en) * | 2012-12-12 | 2014-08-06 | 中国科学院长春应用化学研究所 | Preparation method of diesel antiwear agent |
CN103112968B (en) * | 2013-03-01 | 2014-09-10 | 山东潍坊润丰化工股份有限公司 | Method for treating high-COD (Chemical Oxygen Demand) components in phenoxyalkanoic acid production wastewater |
EP3686264A1 (en) * | 2013-06-19 | 2020-07-29 | Argent Energy Limited | Process for purifying a fatty mixture and related products including fuels |
KR102327852B1 (en) * | 2013-07-22 | 2021-11-18 | 에스케이에코프라임 주식회사 | Method for preparing fatty acid alkyl ester using fat |
US9328054B1 (en) | 2013-09-27 | 2016-05-03 | Travis Danner | Method of alcoholisis of fatty acids and fatty acid gyicerides |
CN104496802B (en) * | 2014-11-28 | 2016-05-04 | 浙江赞宇科技股份有限公司 | A kind of esterifying reaction method and esterification device of producing fatty acid triglycercide |
CN105112168B (en) * | 2015-08-21 | 2018-10-26 | 中国石油大学(华东) | A kind of device and method producing biodiesel |
CN105482898A (en) * | 2015-12-31 | 2016-04-13 | 陕西合盛生物柴油技术开发有限公司 | Biodiesel continuous esterification reaction tower |
CN112979462B (en) * | 2019-12-12 | 2023-01-10 | 中国石油天然气股份有限公司 | Method for improving conversion rate of fatty acid esterification reaction |
US20230100175A1 (en) * | 2020-01-31 | 2023-03-30 | Sk Eco Prime Co., Ltd. | Method for preparing bio-oil from fatty acid with high acid value |
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2006
- 2006-04-28 JP JP2009507569A patent/JP5232139B2/en active Active
- 2006-04-28 CN CN2006800214589A patent/CN101198677B/en active Active
- 2006-04-28 ES ES06757588T patent/ES2721427T3/en active Active
- 2006-04-28 IN IN444DEN2012 patent/IN2012DN00444A/en unknown
- 2006-04-28 MX MX2008011595A patent/MX2008011595A/en active IP Right Grant
- 2006-04-28 US US12/161,784 patent/US7951967B2/en active Active
- 2006-04-28 PL PL06757588T patent/PL2013319T3/en unknown
- 2006-04-28 EP EP06757588.6A patent/EP2013319B1/en active Active
- 2006-04-28 BR BRPI0621209A patent/BRPI0621209B1/en active IP Right Grant
- 2006-04-28 WO PCT/KR2006/001620 patent/WO2007126166A1/en active Application Filing
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WO2007126166A1 (en) | 2007-11-08 |
CN101198677B (en) | 2012-11-14 |
US20100228042A1 (en) | 2010-09-09 |
US7951967B2 (en) | 2011-05-31 |
EP2013319A4 (en) | 2012-06-13 |
CN101198677A (en) | 2008-06-11 |
MX2008011595A (en) | 2008-09-22 |
EP2013319A1 (en) | 2009-01-14 |
EP2013319B1 (en) | 2019-01-23 |
PL2013319T3 (en) | 2019-07-31 |
JP2009535442A (en) | 2009-10-01 |
BRPI0621209A2 (en) | 2011-12-06 |
JP5232139B2 (en) | 2013-07-10 |
BRPI0621209B1 (en) | 2016-03-22 |
ES2721427T3 (en) | 2019-07-31 |
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