WO2011103802A1 - 在线添加颗粒的无菌灌注*** - Google Patents
在线添加颗粒的无菌灌注*** Download PDFInfo
- Publication number
- WO2011103802A1 WO2011103802A1 PCT/CN2011/071206 CN2011071206W WO2011103802A1 WO 2011103802 A1 WO2011103802 A1 WO 2011103802A1 CN 2011071206 W CN2011071206 W CN 2011071206W WO 2011103802 A1 WO2011103802 A1 WO 2011103802A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- segment
- perfusion system
- addition according
- aseptic
- particle addition
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65B—MACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
- B65B55/00—Preserving, protecting or purifying packages or package contents in association with packaging
- B65B55/02—Sterilising, e.g. of complete packages
- B65B55/12—Sterilising contents prior to, or during, packaging
- B65B55/18—Sterilising contents prior to, or during, packaging by liquids or gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/45—Mixing liquids with liquids; Emulsifying using flow mixing
- B01F23/451—Mixing liquids with liquids; Emulsifying using flow mixing by injecting one liquid into another
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/45—Mixing liquids with liquids; Emulsifying using flow mixing
- B01F23/453—Mixing liquids with liquids; Emulsifying using flow mixing by moving the liquids in countercurrent
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/70—Spray-mixers, e.g. for mixing intersecting sheets of material
- B01F25/72—Spray-mixers, e.g. for mixing intersecting sheets of material with nozzles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/10—Maintenance of mixers
- B01F35/145—Washing or cleaning mixers not provided for in other groups in this subclass; Inhibiting build-up of material on machine parts using other means
- B01F35/146—Working under sterile conditions; Sterilizing the mixer or parts thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65B—MACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
- B65B9/00—Enclosing successive articles, or quantities of material, e.g. liquids or semiliquids, in flat, folded, or tubular webs of flexible sheet material; Subdividing filled flexible tubes to form packages
- B65B9/10—Enclosing successive articles, or quantities of material, in preformed tubular webs, or in webs formed into tubes around filling nozzles, e.g. extruded tubular webs
- B65B9/12—Subdividing filled tubes to form two or more packages by sealing or securing involving displacement of contents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/06—Mixing of food ingredients
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2215/00—Auxiliary or complementary information in relation with mixing
- B01F2215/04—Technical information in relation with mixing
- B01F2215/0413—Numerical information
- B01F2215/0418—Geometrical information
- B01F2215/0431—Numerical size values, e.g. diameter of a hole or conduit, area, volume, length, width, or ratios thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65B—MACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
- B65B2220/00—Specific aspects of the packaging operation
- B65B2220/14—Adding more than one type of material or article to the same package
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/8593—Systems
- Y10T137/87571—Multiple inlet with single outlet
- Y10T137/87652—With means to promote mixing or combining of plural fluids
Definitions
- the present invention relates to an aseptic filling system, and more particularly to an aseptic perfusion system for adding particles online. Background technique
- liquid product A is currently in demand in the market.
- Existing aseptic perfusion systems primarily include both infusion and cleaning, such as Tetra Pak's aseptic packaging technology.
- the liquid product A can be various liquid foods such as milk, juice, soy milk, flower milk, beverage, etc.
- the product B can be various types of nutrient and flavor liquid products, and the particles are solid. Therefore, it is necessary to design a device capable of injecting particles in the production process of the liquid phase product A.
- the final product is required to be a sterile product.
- the present invention provides an aseptic perfusion system for in-line addition of particles, including a perfusion system, characterized in that it further comprises an in-line addition of a particle system.
- the perfusion system includes a first AP valve group and an injection tube, the first AP valve group and the injection tube are in communication, and the on-line additive particle system includes a second AP valve group, A second AP valve block is in communication with the injection tube.
- the invention also includes an inline cleaning system.
- the cleaning system includes an external cleaning station and a plurality of flip tubes, the flip tube being detachably connected to the tubing of the perfusion system, and enabling inversion communication with the external washing station, the perfusion system, and the online A particle system is added to form a series of purge lines.
- the liquid phase product A is added into the injection pipe through the first AP valve group
- the liquid phase product B is introduced into the injection pipe through the second AP valve group
- the liquid product A and the liquid phase product B are
- the injection tube is thoroughly mixed to form a solid-liquid mixed product C, which is finally injected into the molding unit through the injection tube to form a aseptically packaged product.
- the entire process is packaged under aseptic conditions.
- FIG. 1 is a schematic view of the working principle of the present invention.
- Figure 2 is a schematic view showing the structure of the product of the present invention.
- Fig. 3 is a schematic view showing the structure of the cleaning pipe of the present invention.
- Figure 4 is a schematic view of the working principle of the mixing nozzle.
- 5 and 6 are a plan view and a side view of the first embodiment of the mixing nozzle.
- 7 and 8 are a plan view and a side view of a second embodiment of the mixing nozzle.
- 9 and 10 are a plan view and a side view of a third embodiment of the mixing nozzle.
- 11 and 12 are top and side views of a fourth embodiment of the mixing nozzle.
- the reference numerals are as follows:
- Embodiment 8 The liquid phase product B is liquid. When it encounters the liquid phase product A, the liquid phase product B is rapidly solidified to form solid particles. Therefore, in the production process of the liquid phase product A, the liquid phase product B is vigorously introduced, and by using the mixing characteristics of the two products, the solid particles can be added in the liquid phase product A, thereby forming solid particles in the final product. Sterile solid-liquid mixed product c. As shown in Fig. 1, the principle of the present invention is to perform aseptic delivery of the liquid phase product A while the liquid phase product A is aseptically transported, and the liquid phase product A and the liquid phase product B are mixed in a sterile environment.
- the mixed product C with solid particles is formed, and the mixed product C is poured into the sterilized packaging material to form a sterile granule package.
- the transport and filling process ensure that the liquid phase product A that reaches the first AP valve block 11 is sterile, ensuring that the liquid phase product B that reaches the second AP valve group 21 is sterile, ensuring a sterile liquid phase product A and
- the sterile liquid phase product B is mixed in a sterile state at the mixing nozzle 25, and forms a sterile solid-liquid mixed product C containing solid particles. Sterilization is carried out at various points in the process of producing the sterile solid-liquid mixed product C to achieve sterilization.
- the present invention includes a perfusion system, an on-line addition particle system.
- the invention includes an injection tube 31, a first AP valve group 11 (sterile product valve group) and a second AP valve group 21 (sterile product valve group), the first AP valve group 11 passing through the first flow regulating valve 12 and injecting
- the tubes 31 are in communication.
- the second AP valve group 21 is in communication with the injection pipe 31.
- the second AP valve group 21 is open
- the second flow regulating valve 22 is in communication with the injection pipe 31.
- the second flow regulating valve 22 and the injection pipe 31 communicate with each other through the second communication pipe 26.
- the second communication pipe 26 is provided with a flow rate sensor 23 and a quantitative metering valve 24, and at the junction of the second communication pipe 26 and the injection pipe 31, a mixing nozzle 25 is provided at the end of the second communication pipe 26.
- the mixing nozzle 25 is simultaneously in communication with the injection pipe 31.
- the first AP valve group 11 is used to add the liquid phase product A into the injection pipe 31, and the second AP valve group 21 is used to force the liquid product B into the injection pipe 31, and the liquid product A and the liquid product B are At the mixing nozzles 25, the particles are formed in the injection tube 31, thereby injecting the particles into the package at the molding unit 33 of the sterile solid-liquid mixed product C.
- the content ratio of the solid particles of the sterile solid-liquid mixed product C is controlled by controlling the first flow rate adjusting valve 12 and the second flow rate adjusting valve 22.
- the flow sensor 23 and the quantitative metering valve 24 are selected, by controlling the first flow regulating valve 12, the second flow regulating valve 22, the flow sensor 23, and the quantitative metering valve 24, the sterile solid-liquid mixing product C can be accurately controlled.
- the flow sensor 23 is for monitoring the flow rate of the liquid phase product B in the second communication pipe 26. As shown in FIG.
- the working principle and function of the mixing nozzle 25 are: when the product pressure of the liquid phase product B is greater than that of the liquid phase product A, the liquid phase product B is ejected from the through hole 250 of the mixing nozzle 25.
- the liquid product A is rapidly solidified to form solid particles. Therefore, by using the mixing characteristics of the two products, solid particles can be added in-line in the liquid phase product A, thereby forming a sterile solid-liquid mixed product containing solid particles in the final product.
- Sterilization methods mainly include sterilization with hot air and sterilization with hydrogen peroxide.
- the injection tube 31 is disposed within the sterile chamber 32. As shown in FIG.
- the cleaning of the present invention employs a series cleaning method including a cleaning line that sequentially connects the second AP valve group 21, the first AP valve group 11, and the injection tube 31.
- the cleaning fluid passes from the external cleaning station 42 through the inverting tube 43 to the second AP valve group 21, and sequentially passes through the second flow regulating valve 22, the flow sensor 23 (optional component), and the quantitative metering valve 24 ( The selected component) flows through the inverting tubes 45, 44 to the first AP valve block 11, and then passes through the first flow regulating valve 12 in sequence, and flows to the injection pipe 31.
- the injection pipe 31 communicates with the external washing station 42 through the filling pipe 41.
- the cleaning pipeline of the present invention realizes the in-situ cleaning (CIP) function of the system by means of the original pipeline at the time of production.
- the function of the filling tube 41 is as follows: The filling tube 41 can be thoroughly cleaned in the cleaning circuit during cleaning, and after the cleaning is completed, the inlet injection tube 31 is taken out and a final perfusion line is formed, so as to mix the solid-liquid mixture C.
- Liquid level monitoring for clear perfusion control After the production is completed, when the present invention needs to be cleaned, only the first inverting tube 43, the second inverting tube 44, and the third inverting tube 45 shown in FIG. 3 are required to be from the lower (dashed line portion) to the upper portion (solid line portion).
- the inversion is communicated with the corresponding purge line to alter the connection of the tubing in the production of the present invention to form a new purge line.
- the first inverting tube 43, the second inverting tube 44, and the third inverting tube 45 are detachably coupled to the production line.
- the second AP valve group 21 communicates with the injection pipe 31 through the mixing nozzle 25, and the second AP valve group 21 communicates with the first AP valve group 11 through the mixing nozzle 25.
- the second AP valve group 21 communicates with the second communication tube 26, the first AP valve group 11 communicates with the first communication tube 13, the second communication tube 26 and the first communication tube 13 meet at the node J, and the injection tube 31 bends at the bend.
- the injection pipe 31 includes a horizontal injection pipe and a vertical injection pipe 31.
- a mixing nozzle 25 is disposed on the second communication tube 26, and the mixing nozzle 25 is adjacent to the node.
- the near-node end of the mixing nozzle 25 is lm ⁇ 3m away from the bend.
- the near nozzle end of the mixing nozzle 25 is 2m ⁇ 2.5m away from the bend.
- the near nozzle end of the mixing nozzle 25 is 1.5 m 2 2 m away from the bend.
- the mixing nozzle 25 is provided with a plurality of through holes 250.
- the through holes 250 communicate with the second AP valve group 21 and the injection pipe 31.
- the through holes 250 also communicate with the second AP valve group 21 and the first AP valve. Group 11.
- the number of the through holes 250 of the mixing nozzle 25 is 16 to 24.
- the 4 non-column manner of the via 250 can be selected as a uniform 4 non-column.
- the mixing nozzle 25 is shaped like a cylinder, a cone or a truncated cone.
- the length of the ⁇ L of the mixing nozzle 25 is 10 mm to 60 mm.
- the length of the mixing nozzle 25 is determined by its shape and the large displacement of the J-end and the bend of the near-node of the mixing jet 11 ⁇ 25.
- Embodiment 2 As shown in FIG. 7 and FIG. 8, the mixing nozzle 25 is set to two sections, including a first section 251 and a second section 252.
- the first section 251 and the second section 252 have different radial dimensions, the first section.
- the 251 is connected to the second segment 252 and has a stepped shape as a whole.
- the first section 251 and the second section 252 are provided with the through holes 250, and the number of the through holes 250 is 8 ⁇ 16.
- the arrangement of the through holes 250 can be selected to be evenly arranged.
- the lengths of the first segment 251 and the second segment 252 are respectively one of 15 mm/20 mm, 20 mm/20 mm, and 30 mm/30 mm.
- Embodiment 3 As shown in FIG. 9 and FIG.
- the mixing nozzle 25 is set to three segments, including a third segment 253, a fourth segment 254, and a fifth segment 255, a third segment 253, a fourth segment 254, and a fifth segment 255.
- the third segment 253 is coupled to the fourth segment 254, and the fourth segment 254 is coupled to the fifth segment 255 and is generally stepped.
- the third segment 253, the fourth segment 254, and the fifth segment 255 are provided with through holes 250, and the number of the through holes 250 is 16-22.
- the lengths of the third segment 253, the fourth segment 254, and the fifth segment 255 are divided into one group of 15 mm/15 mm/20 mm, 15 mm/20 mm/20 mm, and 20 mm/20 mm/20 mm.
- Each section of the mixing nozzle 25 has a cylindrical or sinuous tubular shape.
- the third segment 253 and the fourth segment 254 are set to be in the shape of a push tube.
- the so-called push tube shape is a gear-like shape as shown in FIG.
- a through hole 250 is provided in each of the thick teeth.
- the mixing nozzle 25 is set to four segments, including a sixth segment 256, a seventh segment 257, an eighth segment 258, and a ninth segment 259, and the sixth segment 256 to the ninth segment 259 have The different radial dimensions, the sixth segment 256 to the ninth segment 259 are sequentially connected, and the whole is stepped.
- the sixth segment 256 to the ninth segment 259 are provided with through holes 250, and the number of the through holes 250 is 16-22.
- the total length of the mixing nozzle 25 is 45 mm to 80 mm.
- the lengths from the sixth segment 256 to the ninth segment 259 are further divided into 15 mm/15 mm/20 mm/20 mm.
- Each section of the mixing nozzle 25 has a cylindrical or sinuous tubular shape.
- the through holes 250 of the above various embodiments have a diameter in the range of 1.2 mm to 3.0 mm.
- the number of through holes 250 in the mixing nozzle 25 described above depends on the need for user sterilization and the ratio of solid particles to be added.
- the number of stages of the mixing nozzle 25 may be four or more, and the mixing nozzle Each segment of 25 (the first segment 251 to the ninth segment 252) is in the range of 10 mm to 50 mm, respectively.
- the plurality described in the present invention means two or more.
- the sterilization step mainly includes steps of drying, pre-sterilization, spraying, drying, and the like. First, the drying step. The system piping is blown for approximately 6 minutes to dry the residual moisture in the piping and to dry the piping. Second, the pre-sterilization step. High temperature sterilization of system piping.
- the B valve 21B of the second AP valve group When the pre-sterilization temperature K is less than a certain set value, the B valve 21B of the second AP valve group is closed, and the sterile air flows through the first AP valve group B valve 11B, the first flow regulating valve 12, and the injection pipe 31 to none. Inside the fungus gun 32.
- the pre-sterilization temperature K is greater than the set value within a certain range, the first AP valve group B valve 11B is closed, and the sterile air flows through the first inversion pipe 43, the second AP valve group B valve 21B, and the second flow regulating valve 22
- the second AP valve group B valve 21B and the first AP valve group B valve 11B are simultaneously opened.
- the spray step The system needs to be sprayed twice, and hydrogen peroxide (H 2 0 2 ) is sprayed into the system piping for sterilization.
- the first spray After the first spray is started, the second AP valve group B valve 21B is closed, and the first AP valve group B valve 11 B is opened.
- the H 2 0 2 of the mist is sterilized by the first AP valve group B valve 11 B , the first flow regulating valve 12 , the injection pipe 31 , and the sterile gun 32 to the liquid product A line.
- the second AP valve block B valve 21 B and the first AP valve group B valve 11 B are simultaneously closed for a certain period of time before the end of the first spray.
- the second spray When the pre-sterilization temperature K reaches the set spray temperature again and is delayed, a second spray is started. When the second spray starts, the second AP valve group B valve 21B is opened, and the first is closed.
- the liquid phase product B line is sterilized by the injection tube 31 into the aseptic tank 32.
- the second AP valve block B valve 21B and the first AP valve group B valve 11B are simultaneously closed for a certain period of time before the end of the second spray.
- 4 bar second AP valve group B valve 21B is opened for 5 seconds and then closed.
- the second AP valve group 21 is first opened, and after the delay, the first AP valve group 11 is opened, and the solid-liquid mixed product C flows through the injection pipe 31 to the molding unit 33 to form a final aseptic package product.
- the invention is illustrated by way of example only, and is not intended to limit the scope of the invention. It will be apparent to those skilled in the art that various changes and modifications may be made without departing from the scope of the appended claims.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Basic Packing Technique (AREA)
- Filling Of Jars Or Cans And Processes For Cleaning And Sealing Jars (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
- Materials For Medical Uses (AREA)
- Supply Of Fluid Materials To The Packaging Location (AREA)
Description
Claims
Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BR112012020997A BR112012020997A2 (pt) | 2010-02-23 | 2011-02-23 | sistema de enchimento estéril para adição de partículas em linha |
MX2012009704A MX336704B (es) | 2010-02-23 | 2011-02-23 | Sistema de llenado esteril para agregar particulas en linea. |
US13/580,854 US9346025B2 (en) | 2010-02-23 | 2011-02-23 | Sterile filling system for on-line particle adding |
JP2012554207A JP5683611B2 (ja) | 2010-02-23 | 2011-02-23 | オンラインで粒子を添加する無菌充填システム |
CN201180009558.0A CN102892677B (zh) | 2010-02-23 | 2011-02-23 | 在线添加颗粒的无菌灌注*** |
RU2012140478/13A RU2556391C2 (ru) | 2010-02-23 | 2011-02-23 | Система стерильного розлива для поточного добавления частиц |
EP11746844.7A EP2540627A4 (en) | 2010-02-23 | 2011-02-23 | ASEPTIC FILLING SYSTEM WITH ONLINE ADDITION OF PARTICLES |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010201365556U CN201647160U (zh) | 2010-02-23 | 2010-02-23 | 在线添加颗粒的无菌灌注*** |
CN201020136555.6 | 2010-02-23 |
Publications (1)
Publication Number | Publication Date |
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WO2011103802A1 true WO2011103802A1 (zh) | 2011-09-01 |
Family
ID=43112388
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/CN2011/071206 WO2011103802A1 (zh) | 2010-02-23 | 2011-02-23 | 在线添加颗粒的无菌灌注*** |
Country Status (8)
Country | Link |
---|---|
US (1) | US9346025B2 (zh) |
EP (1) | EP2540627A4 (zh) |
JP (1) | JP5683611B2 (zh) |
CN (2) | CN201647160U (zh) |
BR (1) | BR112012020997A2 (zh) |
MX (1) | MX336704B (zh) |
RU (1) | RU2556391C2 (zh) |
WO (1) | WO2011103802A1 (zh) |
Families Citing this family (6)
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CN201647160U (zh) * | 2010-02-23 | 2010-11-24 | 利乐拉瓦尔集团及财务有限公司 | 在线添加颗粒的无菌灌注*** |
WO2016001144A1 (en) * | 2014-06-30 | 2016-01-07 | Tetra Laval Holdings & Finance S.A. | A method for efficiently emptying a system with liquid product |
PL3160243T3 (pl) * | 2014-06-30 | 2018-07-31 | Tetra Laval Holdings & Finance Sa | Sposób efektywnego napełniania układu produktem ciekłym |
CN105129118B (zh) * | 2015-06-12 | 2017-11-17 | 青海青海湖乳业有限责任公司 | 一种用于向发酵乳中填充可食用粒状物的设备及其方法 |
CN106085840B (zh) * | 2016-06-21 | 2018-04-10 | 上海艾魁英生物科技有限公司 | 溶菌酶二聚体海藻酸钠微球生产线的管道输送***与就地清洗*** |
CN107258903A (zh) * | 2017-06-19 | 2017-10-20 | 吴再盛 | “还原”高温处理后牛奶里维生素a的工艺及设备 |
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- 2011-02-23 BR BR112012020997A patent/BR112012020997A2/pt not_active Application Discontinuation
- 2011-02-23 EP EP11746844.7A patent/EP2540627A4/en not_active Withdrawn
- 2011-02-23 US US13/580,854 patent/US9346025B2/en not_active Expired - Fee Related
- 2011-02-23 JP JP2012554207A patent/JP5683611B2/ja not_active Expired - Fee Related
- 2011-02-23 WO PCT/CN2011/071206 patent/WO2011103802A1/zh active Application Filing
- 2011-02-23 MX MX2012009704A patent/MX336704B/es unknown
- 2011-02-23 RU RU2012140478/13A patent/RU2556391C2/ru not_active IP Right Cessation
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Also Published As
Publication number | Publication date |
---|---|
CN102892677B (zh) | 2014-07-30 |
CN201647160U (zh) | 2010-11-24 |
JP2013520373A (ja) | 2013-06-06 |
MX336704B (es) | 2016-01-28 |
BR112012020997A2 (pt) | 2016-05-03 |
RU2012140478A (ru) | 2014-03-27 |
US9346025B2 (en) | 2016-05-24 |
EP2540627A4 (en) | 2016-01-20 |
JP5683611B2 (ja) | 2015-03-11 |
EP2540627A1 (en) | 2013-01-02 |
MX2012009704A (es) | 2012-10-01 |
RU2556391C2 (ru) | 2015-07-10 |
CN102892677A (zh) | 2013-01-23 |
US20120312405A1 (en) | 2012-12-13 |
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