RU2009113257A - Изотермический реактор - Google Patents

Изотермический реактор Download PDF

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RU2009113257A
RU2009113257A RU2009113257/05A RU2009113257A RU2009113257A RU 2009113257 A RU2009113257 A RU 2009113257A RU 2009113257/05 A RU2009113257/05 A RU 2009113257/05A RU 2009113257 A RU2009113257 A RU 2009113257A RU 2009113257 A RU2009113257 A RU 2009113257A
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catalyst layer
heat exchangers
longitudinal axis
isothermal reactor
side walls
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RU2009113257/05A
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RU2435639C2 (ru
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Эрманно ФИЛИППИ (CH)
Эрманно Филиппи
Энрико РИЦЦИ (IT)
Энрико РИЦЦИ
Мирко ТАРОЦЦО (CH)
Мирко ТАРОЦЦО
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Метанол Касале С.А. (Ch)
Метанол Касале С.А.
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    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0207—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
    • B01J8/0221—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal in a cylindrical shaped bed
    • 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
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/248—Reactors comprising multiple separated flow channels
    • B01J19/249—Plate-type reactors
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0285—Heating or cooling the reactor
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0496—Heating or cooling the reactor
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0058—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for only one medium being tubes having different orientations to each other or crossing the conduit for the other heat exchange medium
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00123—Fingers
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00132—Tubes
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/0015—Plates; Cylinders
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
    • B01J2208/021—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles comprising a plurality of beds with flow of reactants in parallel
    • B01J2208/022—Plate-type reactors filled with granular catalyst
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2451—Geometry of the reactor
    • B01J2219/2453—Plates arranged in parallel
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2451—Geometry of the reactor
    • B01J2219/2456—Geometry of the plates
    • B01J2219/2458—Flat plates, i.e. plates which are not corrugated or otherwise structured, e.g. plates with cylindrical shape
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2461—Heat exchange aspects
    • B01J2219/2462—Heat exchange aspects the reactants being in indirect heat exchange with a non reacting heat exchange medium
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2469—Feeding means
    • B01J2219/247—Feeding means for the reactants
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2476—Construction materials
    • B01J2219/2477—Construction materials of the catalysts
    • B01J2219/2481—Catalysts in granular from between plates
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2476—Construction materials
    • B01J2219/2483—Construction materials of the plates
    • B01J2219/2485—Metals or alloys

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Fluid Mechanics (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

1. Изотермический реактор (1) для проведения экзотермических или эндотермических гетерогенных реакций, содержащий ! по существу, цилиндрический наружный корпус (2), имеющий продольную ось (X), ! по меньшей мере один слой (6) катализатора, размещенный в корпусе (2) и снабженный противолежащими перфорированными боковыми стенками (7, 8), соответственно, для ввода газового потока реагентов и вывода газового потока, содержащего продукты реакции, и ! теплообменный блок (12), погруженный в указанный по меньшей мере один слой (6) катализатора и предназначенный для пропуска через него теплоносителя, ! отличающийся тем, что указанный по меньшей мере один слой (6) катализатора ограничен по краям противолежащими перфорированными боковыми стенками (7, 8), причем между корпусом (2) и этими перфорированными боковыми стенками (7, 8) образованы первый и второй промежутки (9, 10), а теплообменный блок (12) содержит по меньшей мере один ряд теплообменников (13), расположенных, по существу, параллельно друг другу и, по существу, параллельно направлению, в котором указанный по меньшей мере один слой (6) катализатора пересекается газовым потоком реагентов. ! 2. Изотермический реактор (1) по п.1, отличающийся тем, что каждый из указанного по меньшей мере одного ряда теплообменников (13) проходит в по меньшей мере одном слое (6) катализатора вдоль направления, по существу, параллельного продольной оси (X) корпуса. ! 3. Изотермический реактор по п.1 или 2, отличающийся тем, что теплообменники (13) имеют, по существу, коробчатую конструкцию в основном удлиненной и плоской прямоугольной формы, у которой противолежащие длинные стенки (13а) параллельны продольной оси (X) корпу

Claims (4)

1. Изотермический реактор (1) для проведения экзотермических или эндотермических гетерогенных реакций, содержащий
по существу, цилиндрический наружный корпус (2), имеющий продольную ось (X),
по меньшей мере один слой (6) катализатора, размещенный в корпусе (2) и снабженный противолежащими перфорированными боковыми стенками (7, 8), соответственно, для ввода газового потока реагентов и вывода газового потока, содержащего продукты реакции, и
теплообменный блок (12), погруженный в указанный по меньшей мере один слой (6) катализатора и предназначенный для пропуска через него теплоносителя,
отличающийся тем, что указанный по меньшей мере один слой (6) катализатора ограничен по краям противолежащими перфорированными боковыми стенками (7, 8), причем между корпусом (2) и этими перфорированными боковыми стенками (7, 8) образованы первый и второй промежутки (9, 10), а теплообменный блок (12) содержит по меньшей мере один ряд теплообменников (13), расположенных, по существу, параллельно друг другу и, по существу, параллельно направлению, в котором указанный по меньшей мере один слой (6) катализатора пересекается газовым потоком реагентов.
2. Изотермический реактор (1) по п.1, отличающийся тем, что каждый из указанного по меньшей мере одного ряда теплообменников (13) проходит в по меньшей мере одном слое (6) катализатора вдоль направления, по существу, параллельного продольной оси (X) корпуса.
3. Изотермический реактор по п.1 или 2, отличающийся тем, что теплообменники (13) имеют, по существу, коробчатую конструкцию в основном удлиненной и плоской прямоугольной формы, у которой противолежащие длинные стенки (13а) параллельны продольной оси (X) корпуса, а противолежащие короткие стенки (13b, 13с) расположены перпендикулярно этой оси, при этом теплообменники (13) также имеют внутреннюю камеру, предназначенную для направления через нее рабочего теплоносителя.
4. Изотермический реактор по п.1 или 2, отличающийся тем, что теплообменники (13) имеют, по существу, трубчатую конструкцию, причем каждая трубка вытянута в направлении, по существу, перпендикулярном продольной оси (X) корпуса.
RU2009113257/05A 2006-09-11 2007-08-20 Изотермический реактор RU2435639C2 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP06018961.0 2006-09-11
EP06018961A EP1900424A1 (en) 2006-09-11 2006-09-11 Isothermal reactor

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US (1) US8007734B2 (ru)
EP (2) EP1900424A1 (ru)
CN (1) CN101511463B (ru)
AR (1) AR062692A1 (ru)
AT (1) ATE451963T1 (ru)
AU (1) AU2007296992A1 (ru)
BR (1) BRPI0716979A2 (ru)
CA (1) CA2670069C (ru)
CL (1) CL2007002528A1 (ru)
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Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8318131B2 (en) 2008-01-07 2012-11-27 Mcalister Technologies, Llc Chemical processes and reactors for efficiently producing hydrogen fuels and structural materials, and associated systems and methods
US9188086B2 (en) 2008-01-07 2015-11-17 Mcalister Technologies, Llc Coupled thermochemical reactors and engines, and associated systems and methods
US9352973B2 (en) * 2009-01-29 2016-05-31 Gert Ungar Apparatus and process for the synthesis of ammonia
US8441361B2 (en) 2010-02-13 2013-05-14 Mcallister Technologies, Llc Methods and apparatuses for detection of properties of fluid conveyance systems
EP2292326A1 (en) 2009-09-02 2011-03-09 Methanol Casale S.A. Vertical isothermal shell-and-tube reactor
EP2534095A2 (en) 2010-02-13 2012-12-19 McAlister Technologies, LLC Reactor vessels with transmissive surfaces for producing hydrogen-based fuels and structural elements, and associated systems and methods
US8888408B2 (en) 2011-08-12 2014-11-18 Mcalister Technologies, Llc Systems and methods for collecting and processing permafrost gases, and for cooling permafrost
US8826657B2 (en) 2011-08-12 2014-09-09 Mcallister Technologies, Llc Systems and methods for providing supplemental aqueous thermal energy
WO2013025650A1 (en) * 2011-08-12 2013-02-21 Mcalister Technologies, Llc Mobile transport platforms for producing hydrogen and structural materials and associated systems and methods
EP2742207A4 (en) 2011-08-12 2016-06-29 Mcalister Technologies Llc SYSTEMS AND METHODS FOR EXTRACTING AND PROCESSING GASES FROM SUBMERGED SOURCES
WO2013025647A2 (en) 2011-08-12 2013-02-21 Mcalister Technologies, Llc Fuel-cell systems operable in multiple modes for variable processing of feedstock materials and associated devices, systems, and methods
US8911703B2 (en) 2011-08-12 2014-12-16 Mcalister Technologies, Llc Reducing and/or harvesting drag energy from transport vehicles, including for chemical reactors, and associated systems and methods
WO2013025659A1 (en) 2011-08-12 2013-02-21 Mcalister Technologies, Llc Reducing and/or harvesting drag energy from transport vehicles, includings for chemical reactors, and associated systems and methods
US8734546B2 (en) 2011-08-12 2014-05-27 Mcalister Technologies, Llc Geothermal energization of a non-combustion chemical reactor and associated systems and methods
WO2013025655A2 (en) 2011-08-12 2013-02-21 Mcalister Technologies, Llc Systems and methods for providing supplemental aqueous thermal energy
US8669014B2 (en) 2011-08-12 2014-03-11 Mcalister Technologies, Llc Fuel-cell systems operable in multiple modes for variable processing of feedstock materials and associated devices, systems, and methods
WO2014160301A1 (en) 2013-03-14 2014-10-02 Mcalister Technologies, Llc Method and apparatus for generating hydrogen from metal
US20140260195A1 (en) * 2013-03-15 2014-09-18 Mcalister Technologies, Llc Engine exhaust manifold endothermic reactor and associated systems and methods
RU2706050C2 (ru) * 2016-09-02 2019-11-13 Владимир Васильевич Каданцев Реактор с греющей стенкой
CN115414872B (zh) * 2022-08-11 2023-11-03 安徽润衍科技有限公司 管式等温反应器及由1,2-环氧戊烷生产1,2-戊二醇的方法

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT362397B (de) * 1976-10-13 1981-05-11 Schober Robert Dipl Ing Dr Tec Vorrichtung zur erhoehung des ammoniakaufbaues bei der katalytischen ammoniaksynthese
DE19624433C1 (de) * 1996-06-19 1997-12-11 Daimler Benz Ag Reformierungsreaktor, insbesondere zur Wasserdampfreformierung von Methanol
EP0940172A1 (en) * 1998-02-25 1999-09-08 Ammonia Casale S.A. Process for effecting mass transfer between a liquid phase and a gaseous phase
DE19905429A1 (de) * 1999-02-10 2000-08-17 Eisenmann Kg Maschbau Reaktor zur Durchführung einer katalytischen, mit einer Wärmetönung verbundenen Reaktion an Substanzen, die in einer Gasströmung enthalten sind
EP1221339A1 (en) * 2001-01-05 2002-07-10 Methanol Casale S.A. Catalytic reactor with heat exchanger for exothermic and endothermic heterogeneous chemical reactions
EP1306126A1 (en) * 2001-10-19 2003-05-02 Methanol Casale S.A. Heat exchange unit for isothermal chemical reactors
EP1304159A1 (en) * 2001-10-19 2003-04-23 Methanol Casale S.A. Method and reactor for carrying out chemical reactions in pseudo-isothermal conditions
DE10361517A1 (de) * 2003-12-23 2005-07-28 Basf Ag Verfahren zur Herstellung von Formaldehyd
EP1600208A1 (en) * 2004-05-24 2005-11-30 Methanol Casale S.A. Plate-type heat-exchanger

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EP1900424A1 (en) 2008-03-19
AR062692A1 (es) 2008-11-26
EG26182A (en) 2013-04-07
RU2435639C2 (ru) 2011-12-10
US8007734B2 (en) 2011-08-30
CN101511463B (zh) 2012-09-05
DK2066435T3 (da) 2010-04-26
CN101511463A (zh) 2009-08-19
EP2066435B1 (en) 2009-12-16
AU2007296992A1 (en) 2008-03-20
US20100135871A1 (en) 2010-06-03
WO2008031488A1 (en) 2008-03-20
CA2670069A1 (en) 2008-03-20
MX2009002636A (es) 2009-03-25
ATE451963T1 (de) 2010-01-15
DE602007003855D1 (en) 2010-01-28
BRPI0716979A2 (pt) 2013-09-24
CL2007002528A1 (es) 2008-01-18
EP2066435A1 (en) 2009-06-10
CA2670069C (en) 2015-05-19

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