WO2006059571A1 - マルトトリオース比率の低い発酵原液を用いた発酵飲料の製造方法 - Google Patents
マルトトリオース比率の低い発酵原液を用いた発酵飲料の製造方法 Download PDFInfo
- Publication number
- WO2006059571A1 WO2006059571A1 PCT/JP2005/021805 JP2005021805W WO2006059571A1 WO 2006059571 A1 WO2006059571 A1 WO 2006059571A1 JP 2005021805 W JP2005021805 W JP 2005021805W WO 2006059571 A1 WO2006059571 A1 WO 2006059571A1
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- WIPO (PCT)
- Prior art keywords
- sugar
- fermentation
- concentration
- fermented beverage
- trisaccharides
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12C—BEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
- C12C7/00—Preparation of wort
- C12C7/04—Preparation or treatment of the mash
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12C—BEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
- C12C5/00—Other raw materials for the preparation of beer
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12C—BEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
- C12C11/00—Fermentation processes for beer
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12G—WINE; PREPARATION THEREOF; ALCOHOLIC BEVERAGES; PREPARATION OF ALCOHOLIC BEVERAGES NOT PROVIDED FOR IN SUBCLASSES C12C OR C12H
- C12G3/00—Preparation of other alcoholic beverages
- C12G3/02—Preparation of other alcoholic beverages by fermentation
Definitions
- the present invention relates to a fermented beverage using malt or the like as a raw material, and relates to a fermented beverage that does not contain off-flavors such as hydrogen sulfate and has little residual sugar feeling, and a method for producing the same.
- off-flavors such as hydrogen sulfate and has little residual sugar feeling
- Hydrogen sulfide is a typical off-flavor of brewed sake and has a rotten egg-like odor. Therefore, the content in the product should be as low as possible and below the sensory threshold.
- Hydrogen sulfide is produced as an intermediate product when yeast takes in and reduces sulfate ions present in fermentation raw materials and biosynthesizes sulfur-containing amino acids such as methionine and cysteine.
- Patent Document 2 As another method, as shown in Patent Document 2, there is a method of using yeast in which a sulfur-containing amino acid biosynthetic system is genetically modified. However, at present, it is accepted by consumers. It may be difficult and is not suitable as a method for producing commercial beverages.
- Patent Document 1 International Publication WO-2004 / 041992
- Patent Document 2 JP-A-7-303457
- Non-patent literature l J. Am. Soc. Brew. Chem. 53 (l): 24-29,1995 (Y. Kodama et.al) Disclosure of the invention
- An object of the present invention is to provide a fermented beverage with little off-flavor by a method that does not affect the main flavor characteristics and is easily accepted by consumers, in view of the above-described present situation.
- the present inventors analyzed changes in hydrogen sulfide concentration under various fermentation conditions. As a result, there is a relationship S between the sugar utilization rate (sugar concentration reduction rate per unit time) and the hydrogen sulfide concentration, and the concentration of hydrogen sulfide in the fermentation solution increases as the utilization rate decreases. I found the fact.
- Non-Patent Document 1 Based on these findings and the knowledge of Non-Patent Document 1 above that the rate of assimilation of trisaccharides is very slow compared to monosaccharides and disaccharides, a fermentation stock solution with reduced trisaccharide content was used. Inspired to prepare and ferment. As a result, the concentration of hydrogen sulfide in the fermented beverage can be significantly reduced, and the residual sugar sensation can be kept low, thus completing the present invention.
- the present invention provides a method for producing a fermented beverage as one aspect thereof.
- the present invention relates to a method for producing a fermented beverage having a low hydrogen sulfide concentration, comprising performing fermentation by controlling the proportion of trisaccharides in the fermentation stock solution or the assimilating sugar in the fermentation solution. is there.
- the present invention provides:
- a fermented beverage is produced by controlling the proportion of trisaccharides in the fermentation stock solution or assimilable sugar in the fermentation solution.
- the proportion of trisaccharide is controlled so that the unutilized sugar remaining in the fermentation process (Step 2) is not only trisaccharide. Or, even if the remaining unutilized sugar is only trisaccharide, the residual sugar concentration in the fermentation broth of the trisaccharide is 0.5 wt. This is done by adjusting the proportion of trisaccharides in the assimilating sugars.
- the proportion of trisaccharides in the assimilating sugar in the fermentation stock solution at the start of fermentation (or step 1) may be controlled to a constant value.
- the trisaccharide content may be controlled by supplementing monosaccharides or disaccharides during fermentation.
- a fermented beverage with little residual sugar feeling and less sulfurous hydrogen odor is provided.
- the saccharides are assimilated by adjusting the sugar composition of the fermentation stock solution (for example, wort) and fermenting it, the increase in the concentration of hydrogen sulfate in the fermented beverage is suppressed. As a result, a fermented beverage with a little residual sulfur sensation and a sharpness with a little hydrogen sulfate smell is provided.
- the fermentation stock solution for example, wort
- the fermented beverage provided by the present invention is a beverage containing alcohol obtained by fermenting a fermentation stock solution prepared from malt or the like with yeast or the like.
- beer-taste beverages are beverages that are fermented with yeast from sugar raw materials such as malt and sugar solution, hops, etc., and have a beer-like flavor.
- beer, happoshu, miscellaneous sake, liqueurs, spirits, low alcohol malt fermented beverages (for example, malt fermented beverages having an alcohol content of less than 1%) and the like can be mentioned.
- the fermentation stock solution refers to a raw material solution before entering the fermentation process, which contains monosaccharides, disaccharides and trisaccharides for utilization by microorganisms.
- the process for producing the fermentation broth includes a step of dissolving these saccharides and a step of hydrolyzing (enzymatically or chemically) polysaccharides such as Z or starch.
- a sugar solution containing a mixture of sugars may be obtained and used as sugars.
- wort obtained from sugar cane using malt corresponds to the fermentation stock solution.
- the present invention will be explained mainly by using wort as a fermentation stock solution.
- the fermentation liquid in this specification refers to a liquid in an alcohol fermentation process using a fermentation stock solution as a raw material.
- the sugars utilized by yeast are mainly monosaccharides and disaccharides, but trisaccharides are also utilized.
- the fermentation stock solution there are a few saccharides more than tetrasaccharides, but yeast hardly assimilate them. Therefore, in the present invention, the sum of monosaccharides, disaccharides and trisaccharides is used as assimilable sugars. Called.
- Residual sugar concentration is the total amount of assimilating sugars (monosaccharide, disaccharide, trisaccharide) in the fermentation broth or fermented beverage.
- assimilating sugars monosaccharide, disaccharide, trisaccharide
- the total weight of glucose, maltose and maltotriose Z volume% Is displayed.
- examples of monosaccharides include glucose and fructose
- examples of disaccharides include maltose and sucrose
- examples of the trisaccharide include maltotriose and isomaltotriose.
- the trisaccharides are mostly maltotriose.
- the present invention it is important to perform fermentation by controlling the proportion of trisaccharides in the fermentation stock solution or assimilating sugars in the fermentation solution. Specifically, the proportion of trisaccharides is controlled so that monosaccharides or disaccharides with a fast utilization rate remain as far as possible in the fermentation process.
- the specific method for the control is not limited! /, But, for example, in the fermentation stock solution at the start of fermentation, the rate of utilization is high !, saccharides (monosaccharide + 2 saccharides) and It is possible to adjust the ratio of sugars (trisaccharides).
- a preferred sugar composition in the fermentation stock solution is such that the proportion of trisaccharides in the assimilating sugar is 25% by weight or less, preferably 20% by weight or less.
- the total concentration of the assimilable sugars in the fermentation stock solution is preferably 8-15 wt.
- the specific method of adjusting the sugar composition of the fermentation stock solution is not particularly limited.
- the amount and composition of the sugar solution added to the fermentation broth such as wort, the conditions for the process of sugaring the starch, etc. (temperature, pH, reaction time, type and amount of enzyme agent, etc.), production of the fermentation stock solution
- the sugar composition can be adjusted by controlling the conditions (temperature, pH, reaction time, type and amount of enzyme agent, etc.).
- the “sugar solution” used in the present specification refers to a solution containing a raw material that yeast can assimilate as a carbon source without going through a sugar koji process in producing a fermented beverage. For example, it is obtained by hydrolyzing mainly cereal raw materials such as starch with enzymes or acids or alkalis. Alternatively, it can be obtained by dissolving in water water what is marketed as starch syrup or liquid sugar, or saccharide obtained by synthesis or the like.
- a sugar solution having a low proportion of trisaccharides in assimilating sugars can be produced by selecting enzymes and reaction conditions for decomposing starch.
- the sugar ratio can also be adjusted using purified monosaccharides, disaccharides and Z or trisaccharides.
- Sugar solutions suitable for use in the present invention include, for example, commercially available Himal Top (Kato Yigaku Co., Ltd., the proportion of 3 saccharides in the assimilating sugar is 20% by weight) and Maltau force (Kato Yi Gakaku Co., Ltd. It can be prepared by dissolving 23% by weight of trisaccharides in the chelating sugar in water.
- control of the proportion of trisaccharides in the assimilating sugar can also be performed by a method of supplementing the fermentation stock solution or fermentation solution with monosaccharides and disaccharides before fermentation or during fermentation such as the latter stage of fermentation.
- the present invention is particularly useful in the production of fermented beverages that use saccharides as raw materials in addition to malt.
- the proportion of trisaccharides in the assimilating sugar is contained at a ratio of approximately 25-30% by weight that can be adjusted relatively freely, yeast Depending on the type and fermentation conditions, the trisaccharide remains even when the monosaccharide or disaccharide almost dies out.
- a fermented beverage with a feeling of residual sugar is obtained. Therefore, normally, further utilization of trisaccharides is promoted, but the concentration of hydrogen sulfide increases rapidly during the subsequent fermentation. This fact was revealed for the first time by the present invention. Therefore, in the present invention, the proportion of trisaccharides in the fermentation stock solution or assimilating sugars in the fermentation solution so that unutilized sugars do not become trisaccharides due to the progress of fermentation during the fermentation process. Is adjusted.
- the proportion of trisaccharides in the assimilating sugar is usually around 20% by weight, but if the proportion of trisaccharides is In the case where it exceeds 25% by weight of the chelating sugar, it is preferable to reduce the proportion of trisaccharides in the fermentation stock solution by mixing with different raw materials or fermentation stock solutions prepared by different production methods.
- fermentation is performed by controlling the proportion of trisaccharides, and fermented beverages are obtained.
- the fermentation method is performed by mixing the fermentation stock solution and the yeast using a known method.
- the yeast to be used can be appropriately selected from yeasts usually used in fermented beverages intended for production (Weihenstephan-34 etc.). Fermentation conditions vary depending on the type and production scale of the fermented beverage. For example, in the case of a beer beverage, fermentation is performed at 5 to 20 ° C. for 3 to 15 days using beer yeast. The obtained beer is aged for a certain period of time if necessary.
- a purification step for removing solids may be performed.
- known ones such as filtration and centrifugation may be used.
- the hydrogen sulfide concentration was measured by a known gas chromatography method (Analytica- EBC 1998.9.39).
- Hydrogen sulfide odor Five trained panelists evaluated the presence or absence of hydrogen sulfide odor according to the following four levels. No odor at all: 0 points, slightly odors: 1 point, odors felt: 2 points, strong odors: 3 points. When the average point force was less than 1 point, there was no sulfur hydrogen odor ( ⁇ ), and when the average point force was S1 point or more, sulfur hydrogen odor was detected (X). The temperature of the sample during the sensory test was about 5 ° C.
- Residual sugar sensation Five trained panelists evaluated the presence or absence of residual sugar sensation when tasting in the following four stages. No residual sugar feeling: 0 points, slight residual sugar feeling: 1 point, residual sugar feeling: 2 points, strong residual sugar feeling: 3 points. When the average point force was less than S1, there was no residual sugar sensation ( ⁇ ), and when the average point force was 1 point or more, there was residual sugar sensation (X). The temperature of the sample during the sensory test was about 5 ° C. [0032] Example 1
- wort was produced using a sugar solution in which the content of trisaccharides was reduced by about half compared to that used in Control Product 1 and fermented beverages were similarly prepared (Invention Product 1). .
- the trisaccharide-reduced sugar solution was obtained by adjusting the sugar composition using glucose, maltose, and maltotriose based on a commercially available sugar solution (Haimaru Top (Kato Igaku)).
- the total amount of assimilating sugars in the control and invention fermentation stock solutions was 12%.
- the hydrogen sulfide concentration at a residual sugar concentration of 1% was about 2 ppb, and the hydrogen sulfide odor was not recognized even in the sensory evaluation.
- the hydrogen sulfide concentration increased to about lOppb and a hydrogen sulfide odor was observed.
- the hydrogen sulfate concentration was Oppb at both the residual sugar concentration of 1% and the residual sugar concentration of 0.5%, and the hydrogen hydrogen odor was strong. .
- wort was produced using a sugar solution in which the content rate of trisaccharides was reduced by about half compared to that used in control product 2, and fermented beverages were similarly prepared (Invention product 2). .
- the trisaccharide-reduced sugar solution was obtained by adjusting the sugar composition using glucose, maltose, and maltotriose based on a commercially available sugar solution (Haimaru Top (Kato Igaku)).
- the total amount of assimilating sugars in the control and invention fermentation stock solutions was 12%.
- the hydrogen sulfide concentration at a residual sugar concentration of 1% was about 5 ppb.
- the hydrogen sulfate concentration increased to about 18 ppb and a hydrogen sulfide odor was observed.
- a wort was produced in a usual manner using raw materials having a composition of 25% malt and 75% sugar solution.
- the total amount of assimilating sugar in the fermentation broth was 12%.
- the sugar solution used was obtained by mixing a commercially available sugar solution alone or mixed, or by dissolving powdered maltose or maltotriose in water and adding it to a commercially available sugar solution.
- the assimilating sugars are mainly composed of glucose (monosaccharide), maltose (disaccharide), and maltotriose (trisaccharide).
- Worts with different proportions (30, 25, 20, 15, 10% by weight) were prepared.
- wort was produced in which the proportion of trisaccharides in assimilating sugar was approximately 20%.
- sugar solution a commercially available sugar solution (Haimaru Top, Kato Yigakusha) was used.
- a commercially available brewer's yeast was added to the wort thus produced, and fermented beverages were prepared by fermenting in a conventional manner on a 70 L scale (Invention 3).
- the residual sugar concentration was about 0.5%, a sensory evaluation of the fermentation mash was carried out.
- a fermentation stock solution was produced from various cereals or protein degradation products and sugar solution without using malt.
- the proportion of trisaccharides in the assimilating sugar was set to approximately 15%.
- Proteolytic enzymes were used as necessary when producing the fermentation stock solution.
- a commercially available maltose power Kato Igakusha
- powdered sugar maltose
- Commercial beer yeast was added to the fermented undiluted solution thus produced and fermented according to a conventional method to prepare a fermented beverage (Invention product 5). Perform sensory evaluation when residual sugar concentration is about 0.5% As a result, hydrogen sulfur odor was not detected.
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Abstract
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Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP05809551A EP1829957A1 (en) | 2004-11-30 | 2005-11-28 | Method of producing fermented drink by using raw fermentation liquor with low maltotriose content |
AU2005310715A AU2005310715B8 (en) | 2004-11-30 | 2005-11-28 | Process for producing fermented beverages using fermentation raw material solutions of low maltotriose ratio |
JP2006547904A JP4343958B2 (ja) | 2004-11-30 | 2005-11-28 | マルトトリオース比率の低い発酵原液を用いた発酵飲料の製造方法 |
KR1020077014694A KR101194626B1 (ko) | 2004-11-30 | 2005-11-28 | 말토트리오스 비율이 낮은 발효 원액을 사용한 발효 음료의제조 방법 |
US11/791,758 US20090110769A1 (en) | 2004-11-30 | 2005-11-28 | Process for Producing Fermented Beverages Using Fermentation Raw Material Solutions of Low Maltotriose Ratio |
CA002589812A CA2589812A1 (en) | 2004-11-30 | 2005-11-28 | Process for producing fermented beverages using fermentation raw material solutions of low maltotriose ratio |
Applications Claiming Priority (2)
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JP2004347440 | 2004-11-30 | ||
JP2004-347440 | 2004-11-30 |
Publications (1)
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WO2006059571A1 true WO2006059571A1 (ja) | 2006-06-08 |
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PCT/JP2005/021805 WO2006059571A1 (ja) | 2004-11-30 | 2005-11-28 | マルトトリオース比率の低い発酵原液を用いた発酵飲料の製造方法 |
Country Status (9)
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US (1) | US20090110769A1 (ja) |
EP (1) | EP1829957A1 (ja) |
JP (2) | JP4343958B2 (ja) |
KR (1) | KR101194626B1 (ja) |
CN (2) | CN100516189C (ja) |
AU (1) | AU2005310715B8 (ja) |
CA (1) | CA2589812A1 (ja) |
TW (1) | TW200626712A (ja) |
WO (1) | WO2006059571A1 (ja) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2010130902A (ja) * | 2008-11-10 | 2010-06-17 | Suntory Holdings Ltd | 新しいタイプの低糖質発酵飲料及びその製造方法 |
JP2015154742A (ja) * | 2014-02-20 | 2015-08-27 | アサヒビール株式会社 | 発酵麦芽飲料 |
JP2015154740A (ja) * | 2014-02-20 | 2015-08-27 | アサヒビール株式会社 | 発酵麦芽飲料 |
JP2015154745A (ja) * | 2014-02-20 | 2015-08-27 | アサヒビール株式会社 | 発酵麦芽飲料 |
JP2015154743A (ja) * | 2014-02-20 | 2015-08-27 | アサヒビール株式会社 | 発酵麦芽飲料 |
JP2015154747A (ja) * | 2014-02-20 | 2015-08-27 | アサヒビール株式会社 | 発酵麦芽飲料 |
JP2015154737A (ja) * | 2014-02-20 | 2015-08-27 | アサヒビール株式会社 | 発酵麦芽飲料 |
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WO2009051127A1 (ja) * | 2007-10-16 | 2009-04-23 | Suntory Holdings Limited | 低糖質発酵飲料及びその製造方法 |
JP5291257B1 (ja) * | 2011-11-22 | 2013-09-18 | サントリーホールディングス株式会社 | 単糖類及び二糖類の比率が高いノンアルコールのビールテイスト飲料 |
WO2014103011A1 (ja) | 2012-12-28 | 2014-07-03 | サントリーホールディングス株式会社 | 味の締まりが付与された、ノンアルコールのビールテイスト飲料 |
JP5695688B2 (ja) * | 2013-03-08 | 2015-04-08 | サントリー食品インターナショナル株式会社 | 飲料 |
CN103320294B (zh) * | 2013-07-17 | 2014-11-05 | 四川郎酒集团有限责任公司 | 浓酱兼香型白酒的生产方法 |
JP6652965B2 (ja) * | 2015-04-21 | 2020-02-26 | アサヒビール株式会社 | ビール様発泡性飲料の製造方法 |
JP6822762B2 (ja) * | 2015-11-13 | 2021-01-27 | サッポロビール株式会社 | アルコール飲料、アルコール飲料の製造方法、及びアルコール飲料にアルコール吸収抑制効果を付与する方法 |
CN108701662B (zh) | 2016-02-25 | 2020-06-09 | 日本瑞翁株式会社 | 导热片及其制造方法、以及散热装置 |
EP3543328A4 (en) | 2016-11-21 | 2020-11-11 | Asahi Group Holdings, Ltd. | BEER-TYPE DRINK |
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2005
- 2005-11-28 AU AU2005310715A patent/AU2005310715B8/en not_active Ceased
- 2005-11-28 TW TW094141742A patent/TW200626712A/zh not_active IP Right Cessation
- 2005-11-28 EP EP05809551A patent/EP1829957A1/en not_active Withdrawn
- 2005-11-28 WO PCT/JP2005/021805 patent/WO2006059571A1/ja active Application Filing
- 2005-11-28 JP JP2006547904A patent/JP4343958B2/ja active Active
- 2005-11-28 US US11/791,758 patent/US20090110769A1/en not_active Abandoned
- 2005-11-28 KR KR1020077014694A patent/KR101194626B1/ko active IP Right Grant
- 2005-11-28 CA CA002589812A patent/CA2589812A1/en not_active Abandoned
- 2005-11-30 CN CNB2005101290322A patent/CN100516189C/zh not_active Expired - Fee Related
- 2005-11-30 CN CN2009101415383A patent/CN101601492B/zh not_active Expired - Fee Related
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010130902A (ja) * | 2008-11-10 | 2010-06-17 | Suntory Holdings Ltd | 新しいタイプの低糖質発酵飲料及びその製造方法 |
JP2015154742A (ja) * | 2014-02-20 | 2015-08-27 | アサヒビール株式会社 | 発酵麦芽飲料 |
JP2015154740A (ja) * | 2014-02-20 | 2015-08-27 | アサヒビール株式会社 | 発酵麦芽飲料 |
JP2015154745A (ja) * | 2014-02-20 | 2015-08-27 | アサヒビール株式会社 | 発酵麦芽飲料 |
JP2015154743A (ja) * | 2014-02-20 | 2015-08-27 | アサヒビール株式会社 | 発酵麦芽飲料 |
JP2015154747A (ja) * | 2014-02-20 | 2015-08-27 | アサヒビール株式会社 | 発酵麦芽飲料 |
JP2015154737A (ja) * | 2014-02-20 | 2015-08-27 | アサヒビール株式会社 | 発酵麦芽飲料 |
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AU2005310715B2 (en) | 2011-06-02 |
EP1829957A1 (en) | 2007-09-05 |
CN100516189C (zh) | 2009-07-22 |
KR20070092241A (ko) | 2007-09-12 |
CN101601492A (zh) | 2009-12-16 |
CN101601492B (zh) | 2013-04-24 |
US20090110769A1 (en) | 2009-04-30 |
AU2005310715A1 (en) | 2006-06-08 |
JP4732528B2 (ja) | 2011-07-27 |
TWI355417B (ja) | 2012-01-01 |
JP4343958B2 (ja) | 2009-10-14 |
TW200626712A (en) | 2006-08-01 |
CA2589812A1 (en) | 2006-06-08 |
CN1814731A (zh) | 2006-08-09 |
JP2009142290A (ja) | 2009-07-02 |
AU2005310715B8 (en) | 2011-06-23 |
KR101194626B1 (ko) | 2012-10-29 |
JPWO2006059571A1 (ja) | 2008-06-05 |
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