RU2003133282A - Реакторы для полимеризации в объеме и способы такой полимеризации - Google Patents
Реакторы для полимеризации в объеме и способы такой полимеризации Download PDFInfo
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- RU2003133282A RU2003133282A RU2003133282/15A RU2003133282A RU2003133282A RU 2003133282 A RU2003133282 A RU 2003133282A RU 2003133282/15 A RU2003133282/15 A RU 2003133282/15A RU 2003133282 A RU2003133282 A RU 2003133282A RU 2003133282 A RU2003133282 A RU 2003133282A
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- cooler
- heat exchanger
- polymerization reactor
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- polymerization
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- 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
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/0206—Heat exchangers immersed in a large body of liquid
- F28D1/0213—Heat exchangers immersed in a large body of liquid for heating or cooling a liquid in a tank
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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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
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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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
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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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
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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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/247—Suited for forming thin films
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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
- 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
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- 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
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/03—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits
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- 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
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/06—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with the heat-exchange conduits forming part of, or being attached to, the tank containing the body of fluid
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- 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
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D21/0017—Flooded core heat exchangers
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- 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
- F28D9/0006—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 the plate-like or laminated conduits being enclosed within a pressure vessel
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- 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
- F28D9/0031—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 the conduits for one heat-exchange medium being formed by paired plates touching each other
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- 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
- F28D9/0081—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 the conduits for one heat-exchange medium being formed by a single plate-like element ; the conduits for one heat-exchange medium being integrated in one single plate-like element
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
- F28F19/02—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using coatings, e.g. vitreous or enamel coatings
- F28F19/04—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using coatings, e.g. vitreous or enamel coatings of rubber; of plastics material; of varnish
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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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
- B01J2219/00085—Plates; Jackets; Cylinders
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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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00182—Controlling or regulating processes controlling the level of reactants in the reactor vessel
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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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/02—Apparatus characterised by their chemically-resistant properties
- B01J2219/025—Apparatus characterised by their chemically-resistant properties characterised by the construction materials of the reactor vessel proper
- B01J2219/0277—Metal based
- B01J2219/0286—Steel
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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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/19—Details relating to the geometry of the reactor
- B01J2219/192—Details relating to the geometry of the reactor polygonal
- B01J2219/1923—Details relating to the geometry of the reactor polygonal square or square-derived
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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
- 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
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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
- 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
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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
- 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
- B01J2219/2491—Other constructional details
- B01J2219/2497—Size aspects, i.e. concrete sizes are being mentioned in the classified document
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Polymerisation Methods In General (AREA)
- Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Claims (20)
1. Реактор для полимеризации олефинов, включающий резервуар, имеющий, по крайней мере, три боковые стенки и дно, вместе образующие внутреннюю часть резервуара; по крайней мере, одну пластину теплообменника, соединенную посредством жидкости с источником охладителя; и крышку, имеющую наружную и внутреннюю поверхность, вдоль которой располагается, по крайней мере, одна пластина теплообменника.
2. Реактор для полимеризации, указанный в п.1, и имеющий четыре стенки.
3. Реактор для полимеризации, указанный в п.2, в котором каждая из четырех боковых стенок может иметь квадратную форму, характеризующуюся наличием длины и высоты.
4. Реактор для полимеризации, указанный в п.2, в котором две из четырех боковых стенок имеют длину не менее двух футов и высоту не менее двух футов; и другие две из четырех боковых стенок имеют длину не менее трех футов и высоту не менее двух футов.
5. Реактор для полимеризации, указанный в п.4, в котором крышка имеет прямоугольную форму, характеризующуюся наличием длины и ширины; при этом длина составляет не менее трех футов, а ширина - не менее двух футов.
6. Реактор для полимеризации, указанный в п.1, в котором крышка имеет, по крайней мере, две пластины теплообменника.
7. Реактор для полимеризации, указанный в п.6, в котором каждая, по крайней мере, из двух пластин теплообменника располагается на расстоянии не менее трех дюймов одна от другой.
8. Реактор для полимеризации, указанный в п.1, кроме того, включающий, по крайней мере, один впускной коллектор для охладителя, соединенный посредством жидкости с источником охладителя, и, по крайней мере, один выпускной коллектор, соединенный посредством жидкости с источником охладителя.
9. Реактор для полимеризации, указанный в п.8, кроме того, включающий, по крайней мере, одну впускную трубку для охладителя, по крайней мере, с одним впускным коллектором для охладителя, соединенную посредством жидкости с каждой (по крайней мере, с одной) из пластин теплообменника, и, по крайней мере, одну выпускную трубку для охладителя, по крайней мере, с одним выпускным коллектором для охладителя, соединенную посредством жидкости с каждой (по крайней мере, с одной) из пластин теплообменника.
10. Реактор для полимеризации, указанный в п.1, в котором крышка имеет расположенный вдоль внутренней поверхности держатель пластин, служащий для крепления каждой (по крайней мере, одной) из пластин теплообменника к внутренней поверхности крышки.
11. Реактор для полимеризации, указанный в п.1, в котором каждая (по крайней мере, одна) из пластин теплообменника соединена посредством жидкости с впускной трубкой для охладителя и с выпускной трубкой для охладителя.
12. Реактор для полимеризации, указанный в п.11, в котором каждая из впускных трубок для охладителя соединена посредством жидкости с впускным коллектором для охладителя, и каждая из выпускных трубок для охладителя соединена посредством жидкости с выпускным коллектором для охладителя.
13. Реактор для полимеризации, указанный в п.12, в котором впускной коллектор для охладителя и выпускной коллектор для охладителя соединены посредством жидкости с источником охладителя.
14. Реактор для полимеризации, указанный в п.1, в котором резервуар включает четыре стенки, характеризующиеся наличием длины, составляющей не менее четырех футов, и ширины, составляющей не менее двух футов.
15. Реактор для полимеризации, указанный в п.1, в котором на внутренней поверхности крышки может располагаться, по крайней мере, шесть пластин теплообменника.
16. Реактор для полимеризации, указанный в п.1, в котором каждая (по крайней мере, одна) из пластин теплообменника снабжена съемной пленкой.
17. Реактор для полимеризации олефинов, включающий резервуар, имеющий, по крайней мере, три боковые стенки и дно, вместе образующие внутреннюю часть резервуара; теплообменник с держателем пластин, впускной коллектор для охладителя, соединенный посредством жидкости с источником охладителя, по крайней мере, одну впускную трубку для охладителя, соединенную посредством жидкости, по крайней мере, с одной пластиной теплообменника, по крайней мере, одну выпускную трубку для охладителя, соединенную посредством жидкости с каждой (по крайней мере, с одной) из пластин теплообменника и соединенную посредством жидкости с выпускным коллектором, выпускной коллектор, соединенный посредством жидкости с источником охладителя; и крышку, имеющую наружную и внутреннюю поверхность, вдоль которой располагается, по крайней мере, одна пластина теплообменника.
18. Реактор для полимеризации, указанный в п.17, в котором реактор для полимеризации включает четыре боковых стенки, две из четырех боковых стенок имеют длину не менее двух футов и высоту не менее двух футов, другие две из четырех боковых стенок имеют длину не менее трех футов и высоту не менее двух футов, крышка имеет прямоугольную форму, характеризующуюся наличием длины и ширины; при этом длина составляет не менее трех футов, а ширина - не менее двух футов.
19. Метод полимеризации, включающий следующие этапы соединение, по крайней мере, одного мономера, по крайней мере, с одним катализатором в резервуаре с образованием реакционной смеси для полимеризации, при этом резервуар имеет, по крайней мере, три боковые стенки и дно, вместе образующие внутреннюю часть резервуара; помещение, по крайней мере, одной пластины теплообменника, имеющей полость, соединенную посредством жидкости с источником охладителя, во внутреннюю часть резервуара, обеспечив, таким образом, контакт с реакционной смесью для полимеризации; и удаление, по крайней мере, одной пластины теплообменника из реакционной смеси по прошествии времени, достаточного для того, чтобы большая часть, по крайней мере, одного мономера превратилась в полимер.
20. Метод полимеризации, указанный в п.19, включающий, кроме того, этап покрытия съемной пленкой каждой (по крайней мере, одной) из пластин теплообменника перед помещением, по крайней мере, одной пластины теплообменника во внутреннюю часть резервуара.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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US29793101P | 2001-06-13 | 2001-06-13 | |
US60/297,931 | 2001-06-13 |
Publications (2)
Publication Number | Publication Date |
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RU2003133282A true RU2003133282A (ru) | 2005-04-10 |
RU2297877C2 RU2297877C2 (ru) | 2007-04-27 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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RU2003133282/15A RU2297877C2 (ru) | 2001-06-13 | 2002-06-12 | Реакторы для полимеризации в объеме и способы такой полимеризации |
Country Status (10)
Country | Link |
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US (5) | US7582708B2 (ru) |
EP (1) | EP1401570B1 (ru) |
CN (1) | CN1319638C (ru) |
AT (1) | ATE369909T1 (ru) |
CA (1) | CA2447769C (ru) |
DE (1) | DE60221834T2 (ru) |
ES (1) | ES2290309T3 (ru) |
NO (1) | NO329226B1 (ru) |
RU (1) | RU2297877C2 (ru) |
WO (1) | WO2002100532A1 (ru) |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
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US7582708B2 (en) * | 2001-06-13 | 2009-09-01 | Beta Technologie Ag | Bulk polymerization reactor methods |
US6906150B2 (en) | 2003-02-24 | 2005-06-14 | Baker Hughes Incorporated | Heat exchanger polymerization reactors for manufacturing drag reducing agents |
US7015290B2 (en) * | 2003-02-24 | 2006-03-21 | Baker Hughes Incorporated | Method of preparing a polymer under predetermined temperature conditions, and apparatus therefor |
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JP2007268555A (ja) * | 2006-03-30 | 2007-10-18 | Xenesys Inc | 熱交換器製造方法 |
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2002
- 2002-06-12 US US10/170,785 patent/US7582708B2/en not_active Expired - Lifetime
- 2002-06-12 CA CA2447769A patent/CA2447769C/en not_active Expired - Fee Related
- 2002-06-12 CN CNB028119126A patent/CN1319638C/zh not_active Expired - Fee Related
- 2002-06-12 DE DE60221834T patent/DE60221834T2/de not_active Expired - Lifetime
- 2002-06-12 WO PCT/US2002/019007 patent/WO2002100532A1/en active IP Right Grant
- 2002-06-12 ES ES02737514T patent/ES2290309T3/es not_active Expired - Lifetime
- 2002-06-12 AT AT02737514T patent/ATE369909T1/de not_active IP Right Cessation
- 2002-06-12 RU RU2003133282/15A patent/RU2297877C2/ru not_active IP Right Cessation
- 2002-06-12 EP EP02737514A patent/EP1401570B1/en not_active Expired - Lifetime
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2003
- 2003-12-05 NO NO20035403A patent/NO329226B1/no not_active IP Right Cessation
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2006
- 2006-04-18 US US11/406,110 patent/US7534403B2/en not_active Expired - Lifetime
- 2006-08-21 US US11/507,138 patent/US20060281876A1/en not_active Abandoned
- 2006-08-21 US US11/507,271 patent/US8105547B2/en not_active Expired - Lifetime
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Also Published As
Publication number | Publication date |
---|---|
ES2290309T3 (es) | 2008-02-16 |
CA2447769A1 (en) | 2002-12-19 |
US7534403B2 (en) | 2009-05-19 |
US8110150B2 (en) | 2012-02-07 |
US20060281877A1 (en) | 2006-12-14 |
US20020192133A1 (en) | 2002-12-19 |
US8105547B2 (en) | 2012-01-31 |
EP1401570B1 (en) | 2007-08-15 |
EP1401570A1 (en) | 2004-03-31 |
CN1319638C (zh) | 2007-06-06 |
NO329226B1 (no) | 2010-09-20 |
RU2297877C2 (ru) | 2007-04-27 |
DE60221834T2 (de) | 2008-06-26 |
US20060182666A1 (en) | 2006-08-17 |
DE60221834D1 (de) | 2007-09-27 |
US7582708B2 (en) | 2009-09-01 |
ATE369909T1 (de) | 2007-09-15 |
WO2002100532A1 (en) | 2002-12-19 |
US20110097244A1 (en) | 2011-04-28 |
CN1516616A (zh) | 2004-07-28 |
CA2447769C (en) | 2011-07-26 |
NO20035403D0 (no) | 2003-12-05 |
US20060281876A1 (en) | 2006-12-14 |
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