WO2010150980A2 - 음양 추출장치 및 추출방법 - Google Patents
음양 추출장치 및 추출방법 Download PDFInfo
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- WO2010150980A2 WO2010150980A2 PCT/KR2010/003189 KR2010003189W WO2010150980A2 WO 2010150980 A2 WO2010150980 A2 WO 2010150980A2 KR 2010003189 W KR2010003189 W KR 2010003189W WO 2010150980 A2 WO2010150980 A2 WO 2010150980A2
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- extraction
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47J—KITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
- A47J31/00—Apparatus for making beverages
- A47J31/24—Coffee-making apparatus in which hot water is passed through the filter under pressure, i.e. in which the coffee grounds are extracted under pressure
- A47J31/34—Coffee-making apparatus in which hot water is passed through the filter under pressure, i.e. in which the coffee grounds are extracted under pressure with hot water under liquid pressure
- A47J31/36—Coffee-making apparatus in which hot water is passed through the filter under pressure, i.e. in which the coffee grounds are extracted under pressure with hot water under liquid pressure with mechanical pressure-producing means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/02—Solvent extraction of solids
- B01D11/0215—Solid material in other stationary receptacles
- B01D11/0253—Fluidised bed of solid materials
- B01D11/0257—Fluidised bed of solid materials using mixing mechanisms, e.g. stirrers, jets
-
- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47J—KITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
- A47J31/00—Apparatus for making beverages
Definitions
- the present invention relates to a pressure swing extraction device and method.
- low-temperature extraction may be used, but this can prevent degeneration of the active ingredient, but the extraction efficiency is significantly lowered, making it difficult to use commercially.
- an extraction method using an organic solvent is also used, there is a problem that the use is limited due to the human hazards of the solvent remaining after the extraction.
- Another object of one embodiment of the present invention is to provide an extract and a composition comprising the same extracted through a pressure-cyclic extraction device.
- Extraction unit for receiving and extracting the extraction object
- It includes a decompression unit for reducing the internal pressure of the extraction unit
- the extractor is characterized in that it comprises a bubbling nozzle for providing a bubble to the extraction object.
- the present invention provides a pressure swing extraction method that alternately performs a pressurization process and a pressure reduction process.
- Pressure-circulating extraction apparatus and method according to the present invention the extraction at a relatively low temperature, there is an advantage that the extraction efficiency is very excellent. In addition, it is possible to prevent discoloration, odor and heat degeneration of the extraction target.
- the extracting device is capable of various applications in the food and cosmetic fields.
- FIG. 1 is a cross-sectional view schematically showing an extraction apparatus according to an embodiment of the present invention.
- Figure 2 is an enlarged view showing a coupling structure of the extraction tank and the upper plate of the pressure-circulating extraction device.
- Figure 3 is a graph comparing the analysis of the extraction rate by temperature by each extraction method.
- extraction unit 110 extraction tank
- bubbling nozzle 120 top plate
- Extraction unit for receiving and extracting the extraction object
- It includes a decompression unit for reducing the internal pressure of the extraction unit
- the pressurizing unit and the depressurizing unit may be operated alternately to pressurize or depressurize the internal pressure of the extracting unit.
- Pressure-circulating extraction device it is possible to adjust the frequency and the number of times of pressurization and decompression according to the characteristics of the extraction object. Further, by adjusting the pressurization and decompression time in accordance with the characteristics of the extraction target, it is possible to create an optimum extraction condition.
- the extraction device may further include a bubbling nozzle and / or spray nozzle to improve the extraction efficiency.
- the bubbling nozzle facilitates agitation of the extraction target by bubbles generated through the nozzle.
- extraction conditions such as temperature and pressure may vary locally. Air or an inert gas bubble is supplied through the bubbling nozzle to activate the agitation of the extraction target, thereby providing a more uniform extract.
- the bubbling nozzle can be extracted even at low temperatures by increasing the extraction efficiency. Through low temperature extraction, the volatile component of the extract can be maintained as it is, thereby significantly increasing the quality of the extract.
- the inert gas supplied through the bubbling nozzle is nitrogen or helium, specifically nitrogen.
- the spray nozzle sprays liquid onto the extraction object while the extraction is in progress, and serves to remove bubbles generated during the extraction process.
- the spray nozzle is used to spray the extraction solvent or water, more specifically to cool the cold water.
- the extraction solvent sprayed through the spray nozzle is a C 1 to C 5 lower alcohol.
- the form of the extracting section is not particularly limited, and may be, for example, an integral tank structure.
- the extracting unit includes an inlet for supplying an extract object and a solvent, and an outlet for discharging the extract to the outside.
- the extraction unit may be a coupling structure consisting of the extraction tank and the upper plate accommodated in the extraction object.
- the extraction target is accommodated in the extraction tank and can accommodate a solvent, etc. as needed
- the upper plate is located on the top of the extraction tank to seal the extraction tank.
- the coupling structure of the extraction tank and the upper plate is not particularly limited as long as it is a structure capable of sealing the extraction object contained in the extraction tank.
- the joint surface of the extraction tank and the upper plate may include a protrusion structure formed at an upper end of the extraction tank.
- the protrusion structure formed at the bottom of the upper plate may be in a staggered form.
- the extraction device may further include a temperature control unit, and the temperature control unit heats the extraction object accommodated in the extraction unit. By heating the extraction target through the temperature control unit, it is possible to improve the extraction efficiency.
- the extraction device will alternately form the pressure and pressure conditions.
- the pressurizing unit injects gas into the extraction unit, thereby applying pressure.
- the gas injected by the pressurizing portion is not particularly limited, but is air or inert gas, specifically nitrogen (N 2 ) or helium (He) gas, and more specifically nitrogen gas.
- the pressure reducing unit may reduce the pressure by applying a vacuum to the extraction unit or by forming a vent to discharge the internal air.
- the present invention provides a pressure-circulating extraction method in which pressure and pressure are alternately applied.
- the pressure-circulating extraction method (a) a pressure step to increase the pressure; And (b) alternately undergoing a depressurization process to reduce pressure.
- the extraction method may further include a bubbling process of providing a bubble to the extraction object during the pressurization process and / or the decompression process.
- the extraction method may further include (d) a spray process of spraying a liquid on the extraction object during the extraction process.
- the extraction method may be a solvent extraction method of extracting the extraction object by impregnating the solvent.
- the solvent used in the extraction method is not particularly limited, and may be water or a lower alcohol of C 1 to C 5 , more specifically water.
- the pressure in the pressing process is not particularly limited, and may be, for example, in the range of 1 to 10 kgf / cm 2 , specifically, in the range of 1.5 to 3 kgf / cm 2 . In some cases, a medium pressure extraction of about 5 kgf / cm 2 is also possible.
- the pressure of the decompression process may be in the range of 100 to 760 mmHg, specifically, in the range of 500 to 700 mmHg. In some cases, a vacuum may be formed in the depressurization process.
- the extraction method according to the present invention depending on the characteristics of the extraction object, it is possible to alternately apply pressure and reduced pressure, and if necessary, conditions to be applied during the pressure and pressure reduction process may be set differently.
- the time required and the number of repetitions of the pressurization process and the depressurization process are not particularly limited and may be set differently according to the characteristics of the extraction target.
- the time required for the pressurization process and the depressurization process may be 10 minutes to 1 hour, respectively, and specifically 30 minutes may be set.
- the number of repetitions of the pressing and depressurizing processes is 1 to 30 times, specifically 2 to 10 times, more specifically 4 to 5 times.
- the extraction method according to the present invention by repeating the pressing step and the depressurization step 2 to 3 times, a sufficient extraction effect can be seen.
- the extraction method according to the present invention applies pressure and pressure alternately, it is possible to extract at a relatively low temperature compared to the conventional hot water extraction method. Therefore, the extraction temperature according to the extraction method may be 0 to 100 °C, specifically 30 to 85 °C. In addition, the extraction method can be effective extraction even at a relatively low temperature of 50 to 75 °C, in some cases may be by cold soaking.
- an extract extracted by the extraction apparatus or extraction method according to the present invention is an extract extracted by the extraction apparatus or extraction method according to the present invention.
- Extract according to the present invention there is little discoloration, discoloration and heat loss, there is an advantage that can effectively implement the flavor and nutritional components inherent in the extract.
- the extract can be utilized as an active ingredient or additives in food, cosmetics and pharmaceuticals. In one embodiment, it provides a food composition comprising the extract. In another embodiment, it provides a cosmetic composition comprising the extract.
- the extraction apparatus includes an extraction unit 100 in which extraction is performed on the extraction object, a pressing unit 200 for increasing the internal pressure of the extraction apparatus, and a pressure reduction unit 300 for reducing the internal pressure.
- Extraction unit 100 is composed of an extraction tank 110 for receiving the object to be extracted, and the upper plate 120 to serve as a cap of the extraction tank (110).
- a bubbling nozzle 111 is provided below the extraction tank 110, and the bubbling nozzle 111 supplies air bubbles during the extraction process to promote stirring of the extraction target.
- a spray nozzle 121 is formed at a lower end of the upper plate 120, and sprays low temperature water through the spray nozzle 121 to remove bubbles generated during the extraction process.
- the pressurizing part 200 and the decompression part 300 are connected to the upper plate 120.
- air or nitrogen (N 2 ) gas is supplied.
- N 2 nitrogen
- the pressurizing unit 200 and the decompression unit 300 adjust the operation time and cycle through a pressure control unit (not shown).
- the temperature control unit 400 is connected to the extraction apparatus, and the extract heated by the temperature control unit 400 is circulated into the extraction tank 110 through the circulation pump 500.
- FIG. 2 shows the junction structure of the extraction tank and the top plate of the extraction apparatus according to an embodiment of the present invention.
- Two protrusions are formed on the top surface of the extraction tank 110, which is interlocked with the protrusions formed on the bottom surface of the upper plate 120.
- Puerarin was extracted from the roots using the extractor of FIG. 1. Specifically, the roots were immersed in a 10-fold volume of water, and then extracted for 2 hours while circulating pressurization and depressurization in units of 30 minutes. The pressure during extraction was 2 kgf / cm 2 , the pressure during extraction under reduced pressure was 600 50 mmHg, and the extraction temperature was set at 75 ° C.
- Pueran was extracted from the root through hot water extraction. Specifically, the roots were immersed in 10 times the volume of water, and then extracted at 75 ° C. for 2 hours. No pressure was applied or reduced separately during the extraction process.
- Example 3 In the same manner as in Example 1 and Comparative Example 1, the extraction rate of Puerarin in the root was measured. However, the extraction time was 4 hours, repeated pressurization and depressurization in units of 1 hour, and the extraction temperature was different from 30 ⁇ 100 °C. The measurement results are shown in FIG. 3. The extraction rate (%) of FIG. 3 is expressed as a ratio of methanol reflux extraction by the Pharmacopoeia test method.
- the pressure cyclic extraction has a difference in extraction rate of 20% or more, up to 40%.
- the difference in extraction rate was relatively large in the low temperature range.
- the extraction rate is less than 10% at 30 ° C and not more than 40% at 50 ° C.
- the extraction rate is at least 50% even at 30 ° C, and reaches 70% at 50 ° C.
- the existing hot water extraction is hardly extracted at a low temperature, it can be seen that in the case of pressure-circulating extraction according to the present invention effective extraction even at a relatively low temperature. Therefore, through the pressure circulation extraction according to the present invention, it can be effectively utilized for the extraction of heat sensitive components.
- the purpose of this experiment is to verify the effects of pressure circulation extraction by observing changes in hot water extraction and pressure circulation extraction over time.
- Hot water extraction and pressure circulation extraction were carried out in the same manner as in Experiment 1.
- the extraction time was 2 hours, and after the extraction was stored refrigerated after 0.45 ⁇ m sterilization filtration was observed precipitate formation.
- the observation results are shown in Table 1 below.
- the extraction rates of hot water, pressurized, reduced pressure, and pressure circulation were compared and observed.
- the extraction time was 8 hours, and the extraction rate was measured by taking samples at 1 hour intervals.
- the extraction temperature may be a component that is not extracted at low temperatures, and heat sensitive components at high temperatures may be affected during the extraction process. Specific extraction conditions are shown in Table 2 below, and the measurement results are shown in FIG. 4.
- Extraction apparatus and method according to the present invention it is possible to prevent discoloration, odor and heat denaturation to the extraction target, it is possible to efficiently extract the natural or herbal medicines.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Food Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Extraction Or Liquid Replacement (AREA)
- Cosmetics (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Apparatus For Making Beverages (AREA)
- Meat, Egg Or Seafood Products (AREA)
- Soy Sauces And Products Related Thereto (AREA)
Abstract
Description
경과일수 | 1일 | 7일 | 15일 | 30일 | ||||
추출온도 | 열수추출 | 압력순환 | 열수추출 | 압력순환 | 열수추출 | 압력순환 | 열수추출 | 압력순환 |
30℃ | - | - | - | - | - | - | - | - |
50℃ | - | - | - | - | * | - | * | - |
75℃ | - | - | - | - | * | * | * | * |
95℃ | * | - | ** | ** | *** | *** | *** | *** |
추출법 | 추출온도 | 가압조건 | 감압조건 | 비고 |
열수추출 | 75℃ | - | - | |
열수순환추출 | 75℃ | - | - | 열수추출에 순환펌프 가동 |
가압추출 | 75℃ | 2kgf/cm2 | - | |
감압추출 | 75℃ | - | 600 50mmHg | |
압력순환추출 | 75℃ | 2kgf/cm2 | 600 50mmHg | 30분 단위로 가압 및 감압 순환 |
압력순환+버블링추출 | 75℃ | 2kgf/cm2 | 600 50mmHg | 진공파기 및 감압시버블링에 의한 질소주입30분 단위로 가압 및 감압 순환 |
Claims (15)
- 추출대상물을 수용 및 추출하는 추출부;추출부의 내부 압력을 증가시키는 가압부; 및추출부의 내부 압력을 감소시키는 감압부를 포함하며,상기 가압부 및 감압부를 교대로 작동하여 추출부의 내부 압력을 가압 또는 감압하며,상기 추출부는 추출대상물에 버블을 제공하는 버블링 노즐을 포함하는 압력순환형 추출장치.
- 제 1 항에 있어서,상기 추출부는,추출대상물에 액체를 분사하는 스프레이 노즐,추출온도를 조절하는 온도조절부, 또는스프레이 노즐 및 온도조절부를 더 포함하는 압력순환형 추출장치.
- 제 1 항에 있어서,상기 추출부는,추출대상물을 수용하는 추출조; 및추출조의 상부에 위치하며 추출조를 밀폐시키는 상부판을 포함하는 압력순환형 추출장치.
- 제 3 항에 있어서,추출조와 상부판의 접합면은,추출조 상단에 형성된 돌기 구조와 상부판 하단에 형성된 돌기 구조가 엇갈려 맞물린 형태인 압력순환형 추출장치.
- 제 1 항에 있어서,가압부는 추출부 내부에 가스를 주입함으로써 압력을 가하고,감압부는 추출기 내부에 진공을 걸어주거나 벤트를 형성하여 내부 공기를 배출함으로써 압력을 감소시키는 것을 특징으로 하는 압력순환형 추출장치.
- 제 5 항에 있어서,추출기 내부에 주입하는 가스는 공기(air) 또는 질소(N2) 가스인 압력순환형 추출장치.
- 추출대상물을 용매에 함침시켜 추출하는 방법으로서,압력을 가하는 가압공정; 및압력을 감소시키는 감압공정을 교대로 수행하는 것을 포함하며,추출과정 동안 추출대상물에 버블을 제공하는 버블링 공정을 수행하는 압력순환형 추출방법.
- 제 7 항에 있어서,상기 방법은, 추출과정 동안 추출대상물에 액체를 분사하는 스프레이 공정을 더 포함하는 압력순환형 추출방법.
- 제 7 항에 있어서,상기 용매는 물 또는 C1 내지 C5의 저급 알코올인 압력순환형 추출방법.
- 제 7 항에 있어서,가압공정의 압력은 1 내지 10 kgf/cm2 범위이고,감압공정의 압력은 100 내지 760 mmHg 범위인 압력순환형 추출방법.
- 제 7 항에 있어서,가압공정 및 감압공정은, 각 공정별로,10 분 내지 1 시간 동안 진행되며,2 내지 10 회 반복되는 것을 특징으로 하는 압력순환형 추출방법.
- 제 7 항에 있어서,추출온도는 30 내지 85℃ 범위인 압력순환형 추출방법.
- 제 7 항 내지 제 12 항 중 어느 한 항에 따른 추출방법으로 추출된 추출물.
- 제 13 항의 추출물을 포함하는 식품 조성물.
- 제 13 항의 추출물을 포함하는 화장료 조성물.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
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JP2012517367A JP2012531247A (ja) | 2009-06-26 | 2010-05-20 | 陰陽抽出装置及び抽出方法 |
CN2010800285449A CN102802474A (zh) | 2009-06-26 | 2010-05-20 | 正压和负压萃取装置以及萃取方法 |
US13/379,890 US20120095208A1 (en) | 2009-06-26 | 2010-05-20 | Positive and negative extraction device and extraction method |
EP10792262.7A EP2446786B1 (en) | 2009-06-26 | 2010-05-20 | Method for extracting puerarin from kudzu by pressure-cycling extraction |
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KR10-2009-0057901 | 2009-06-26 | ||
KR1020090057901A KR101587871B1 (ko) | 2009-06-26 | 2009-06-26 | 음양 추출장치 및 추출방법 |
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WO2010150980A2 true WO2010150980A2 (ko) | 2010-12-29 |
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US (1) | US20120095208A1 (ko) |
EP (1) | EP2446786B1 (ko) |
JP (1) | JP2012531247A (ko) |
KR (1) | KR101587871B1 (ko) |
CN (1) | CN102802474A (ko) |
WO (1) | WO2010150980A2 (ko) |
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CN113388453A (zh) * | 2021-07-08 | 2021-09-14 | 中香香料(深圳)有限公司 | 一种提取香精油设备及工艺方法 |
CN114210092A (zh) * | 2021-11-30 | 2022-03-22 | 中科优术(黑龙江)科技产业有限公司 | 一种低温负压式萃取一体装置及萃取方法 |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE878150A (fr) * | 1978-08-09 | 1980-02-08 | Atomic Energy Authority Uk | Perfectionnements a un procede pour extraire une matiere par lixiviation |
JPH01159004A (ja) * | 1987-12-16 | 1989-06-22 | Niigata Eng Co Ltd | 固体抽出法 |
US4984511A (en) * | 1988-11-25 | 1991-01-15 | Sanden Corporation | Beverage brewing apparatus for vending machines |
JPH0687740B2 (ja) * | 1990-03-08 | 1994-11-09 | 株式会社ニチレイ | 抽出飲料液製造方法及び同装置 |
JP3484612B2 (ja) * | 1993-07-12 | 2004-01-06 | 株式会社ニッセー | 茶類等の抽出方法並びに装置 |
US5558006A (en) * | 1994-08-04 | 1996-09-24 | Kuboyama; Nobuyoshi | Health beverage plant extraction apparatus |
CN1156566A (zh) * | 1996-10-09 | 1997-08-13 | 桂林朗臣饮料有限公司 | 一种葛根茶的生产方法 |
UA35292C2 (uk) * | 1999-09-17 | 2001-10-15 | Інститут Технічної Теплофізики Національної Академії Наук України | Установка для одержання екстрактів |
JP4526155B2 (ja) * | 2000-04-24 | 2010-08-18 | 株式会社ニッセー | 多機能抽出器 |
KR100411746B1 (ko) * | 2000-12-13 | 2003-12-18 | 주식회사 한국닛소 | 식물성 테르펜정유 추출장치 |
JP3693664B2 (ja) * | 2003-07-23 | 2005-09-07 | 株式会社イズミフードマシナリ | 飲料および調味だし用抽出装置および抽出方法 |
CN1236836C (zh) * | 2003-12-08 | 2006-01-18 | 曹培生 | 一种萃取方法及其装置 |
JP4427666B2 (ja) * | 2004-11-22 | 2010-03-10 | 国立大学法人徳島大学 | 低圧ガス加圧法による液体中の溶存酸素除去方法 |
CN1788822A (zh) * | 2004-12-15 | 2006-06-21 | 刘乡乡 | 低温差压式提取技术 |
CN2912753Y (zh) * | 2005-11-10 | 2007-06-20 | 上海大学 | 喷雾萃取设备 |
WO2007088593A1 (ja) * | 2006-01-31 | 2007-08-09 | Shi Mechanical & Equipment Inc. | 圧力容器のシール構造 |
JP2008001658A (ja) * | 2006-06-23 | 2008-01-10 | Nitta Gelatin Inc | 化粧料組成物 |
WO2008061418A1 (fr) * | 2006-11-22 | 2008-05-29 | Institute Of Process Engineering, Chinese Academy Of Sciences | Procédé et dispositif pour une utilisation globale de radix pueraria |
-
2009
- 2009-06-26 KR KR1020090057901A patent/KR101587871B1/ko active IP Right Grant
-
2010
- 2010-05-20 EP EP10792262.7A patent/EP2446786B1/en active Active
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- 2010-05-20 CN CN2010800285449A patent/CN102802474A/zh active Pending
- 2010-05-20 JP JP2012517367A patent/JP2012531247A/ja active Pending
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---|
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU169873U1 (ru) * | 2016-06-20 | 2017-04-04 | федеральное государственное бюджетное образовательное учреждение высшего образования "Казанский национальный исследовательский технологический университет" (ФГБОУ ВО "КНИТУ") | Экстрактор |
CN115300933A (zh) * | 2022-07-28 | 2022-11-08 | 黄淮学院 | 一种天然产物的分离纯化设备 |
CN115300933B (zh) * | 2022-07-28 | 2023-11-24 | 黄淮学院 | 一种天然产物的分离纯化设备 |
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US20120095208A1 (en) | 2012-04-19 |
WO2010150980A3 (ko) | 2011-03-10 |
KR101587871B1 (ko) | 2016-01-25 |
JP2012531247A (ja) | 2012-12-10 |
EP2446786B1 (en) | 2020-09-30 |
CN102802474A (zh) | 2012-11-28 |
EP2446786A4 (en) | 2015-01-07 |
KR20110000433A (ko) | 2011-01-03 |
EP2446786A2 (en) | 2012-05-02 |
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