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    • 1. 发明申请
    • METHOD OF PRODUCING YEAST FERMENTED BEVERAGES
    • 生产YEAST FERMENED BEVERAGES的方法
    • WO2007136253A1
    • 2007-11-29
    • PCT/NL2007/050214
    • 2007-05-14
    • Heineken Supply Chain B.V.MULDER, HendrikusSNIP, Onno CornelisBLOEMEN, Herman Hendrik JanBANKS, Douglas John
    • MULDER, HendrikusSNIP, Onno CornelisBLOEMEN, Herman Hendrik JanBANKS, Douglas John
    • C12C11/07C12G3/00C12C11/00
    • C12C11/07C12C11/02
    • The present invention relates to a method of producing yeast fermented beverages, which method comprises the following consecutive continuous processing steps: a. introducing wort into a series of one or more propagation vessels in which it is combined with a recirculated stream of yeast-containing residue and in which the yeast is allowed to propagate under aerobic conditions whilst being kept suspended; b. transferring the yeast-containing wort from the propagation vessel into a series of one or more fermentation vessels in which the yeast is kept suspended under anaerobic conditions and is allowed to metabolise carbohydrates present in the wort; c. transferring at least a part of the fermented wort from the series of one or more fermentation vessels to one or more separators to remove a yeast-containing residue; d. recirculat ing part of the yeast-containing residue to the series of one or more propagation vessels; and e. feeding the remainder of the fermented wort to subsequent processing steps; wherein the wet yeast content of the wort in the series of one or more fermentation vessels is maintained at more than 100 g/l. The utilisation of very high yeast concentrations offers the advantage that fermentation times and/or fermenter volume can be reduced substantially. Furthermore, continuous fermentations conducted at high yeast concentrations are less vulnerable to microbial infections.
    • 本发明涉及一种生产酵母发酵饮料的方法,该方法包括以下连续的连续处理步骤:a。 将麦芽汁引入一系列一个或多个繁殖容器中,其中其与含酵母的残留物的再循环流组合,并且其中允许酵母在需氧条件下同时保持悬浮; 湾 将含酵母的麦芽汁从繁殖容器转移到一系列一个或多个发酵容器中,其中酵母在厌氧条件下保持悬浮并被允许代谢麦芽汁中存在的碳水化合物; C。 将至少一部分发酵麦芽汁从一系列一个或多个发酵容器转移至一个或多个分离器以除去含酵母的残留物; 天。 将含酵母的残余物的一部分再循环到一系列一个或多个繁殖容器中; 和e。 将剩余的发酵麦芽汁喂养到随后的加工步骤; 其中一系列一个或多个发酵容器中的麦芽汁的湿酵母含量保持在大于100g / l。 利用非常高的酵母浓度提供了发酵时间和/或发酵罐体积可以显着降低的优点。 此外,在高酵母浓度下进行的连续发酵不太容易受到微生物感染。
    • 2. 发明申请
    • CONTINUOUS METHOD FOR THE PRODUCTION OF A YEAST FERMENTED BEVERAGE
    • 用于生产YEAST FERMENED BEVERAGE的连续方法
    • WO2007136257A1
    • 2007-11-29
    • PCT/NL2007/050218
    • 2007-05-16
    • HEINEKEN SUPPLY CHAIN B.V.MULDER, HendrikusSNIP, Onno CornelisBANKS, Douglas JohnBLOEMEN, Herman Hendrik Jan
    • MULDER, HendrikusSNIP, Onno CornelisBANKS, Douglas JohnBLOEMEN, Herman Hendrik Jan
    • C12C7/00C12C11/07
    • C12C7/00C12C7/20C12C11/07
    • The present invention provides a continuous method for the production of a yeast fermented beverage, comprising the following consecutive continuous processing steps: a. mashing starch-containing and optionally malted raw materials with aqueous liquid; b. heat ing the mash and enzymatically hydrolysing the starch to fermentable sugars; c. removing spent grain from the heated mash to produce a mash extract, d. convert ing the mash extract into wort; e. removing organic volatiles from the hot wort; f. dilut ing the wort with additional water; g. feeding the diluted wort into a propagation vessel in which it is combined with a recirculated stream of yeast-containing residue and in which oxygen is supplied to initiate yeast growth; h. feeding the wort from the propagation vessel into a sequence of one or more fermentation vessels in which the yeast is kept suspended; i. feeding the fermented wort into one or more separators to remove a yeast- containing residue; j. recirculat ing part of the yeast-containing residue to the propagation vessel; and k. feeding the remainder of the fermented wort to subsequent processing steps; wherein the gravity of the mash extract is maintained at more than 22 ºP; the gravity of the wort is maintained at more than 22 ºP until said wort is diluted with additional water; and the gravity of the diluted wort is within the range of 10-35 ºP; and wherein less than 30 wt.% of the fermentable sugars in the mash extract and wort are derived from fermentable sugars added after hydrolysis of the starch contained in the mash. The present method offers the advantage that it is highly efficient in terms of energy consumption and extraction yields. Furthermore, it achieves extremely high productivity, especially in the operation of the brewhouse.
    • 本发明提供了用于生产酵母发酵饮料的连续方法,包括以下连续的连续处理步骤:a。 用含水液体糖化含淀粉和任选的麦芽原料; 湾 加热糊状物并将淀粉酶促水解成可发酵糖; C。 从加热的糊状物中除去废谷物以产生糊状物提取物,d。 将麦芽汁提取物转成麦芽汁; 即 从热麦芽汁中除去有机挥发物; F。 用额外的水稀释麦芽汁; G。 将稀释的麦芽汁进料到繁殖容器中,其中将其与含酵母的残留物的再循环流组合,并且其中供应氧以引发酵母生长; H。 将麦芽汁从繁殖容器喂入一个或多个酵母保持悬浮的发酵容器的序列; 一世。 将发酵的麦芽汁喂入一个或多个分离器以除去含酵母的残渣; 学家 将含酵母的残余物的一部分再循环到繁殖容器; 和k。 将剩余的发酵麦芽汁喂养到随后的加工步骤; 其中麦芽汁提取物的重力保持在22℃以上; 麦芽汁的重力保持在22ºP以上,直到用额外的水稀释麦芽汁; 稀释麦芽汁的重力在10-35ºP范围内; 并且其中小麦提取物和麦芽汁中少于30重量%的可发酵糖衍生自在醪液中包含的淀粉水解后加入的可发酵糖。 本方法提供的优点是在能量消耗和提取产率方面是高效的。 此外,它实现了极高的生产率,特别是在酿造厂的操作中。
    • 3. 发明公开
    • METHOD OF PRODUCING YEAST FERMENTED BEVERAGES
    • 用于生产HEFEVERGORENER饮料
    • EP2024486A1
    • 2009-02-18
    • EP07747438.5
    • 2007-05-14
    • Heineken Supply Chain B.V.
    • MULDER, HendrikusSNIP, Onno CornelisBLOEMEN, Herman Hendrik JanBANKS, Douglas John
    • C12C11/07C12G3/00C12C11/00
    • C12C11/07C12C11/02
    • The present invention relates to a method of producing yeast fermented beverages, which method comprises the following consecutive continuous processing steps: a. introducing wort into a series of one or more propagation vessels in which it is combined with a recirculated stream of yeast-containing residue and in which the yeast is allowed to propagate under aerobic conditions whilst being kept suspended; b. transferring the yeast-containing wort from the propagation vessel into a series of one or more fermentation vessels in which the yeast is kept suspended under anaerobic conditions and is allowed to metabolise carbohydrates present in the wort; c. transferring at least a part of the fermented wort from the series of one or more fermentation vessels to one or more separators to remove a yeast-containing residue; d. recirculat ing part of the yeast-containing residue to the series of one or more propagation vessels; and e. feeding the remainder of the fermented wort to subsequent processing steps; wherein the wet yeast content of the wort in the series of one or more fermentation vessels is maintained at more than 100 g/l. The utilisation of very high yeast concentrations offers the advantage that fermentation times and/or fermenter volume can be reduced substantially. Furthermore, continuous fermentations conducted at high yeast concentrations are less vulnerable to microbial infections.
    • 4. 发明公开
    • CONTINUOUS METHOD FOR THE PRODUCTION OF A YEAST FERMENTED BEVERAGE
    • 用于生产饮料连续过程HEFEFERMENTIERTEN
    • EP2024484A1
    • 2009-02-18
    • EP07747442.7
    • 2007-05-16
    • Heineken Supply Chain B.V.
    • MULDER, HendrikusSNIP, Onno CornelisBANKS, Douglas JohnBLOEMEN, Herman Hendrik Jan
    • C12C7/00C12C11/07
    • C12C7/00C12C7/20C12C11/07
    • The present invention provides a continuous method for the production of a yeast fermented beverage, comprising the following consecutive continuous processing steps: a. mashing starch-containing and optionally malted raw materials with aqueous liquid; b. heat ing the mash and enzymatically hydrolysing the starch to fermentable sugars; c. removing spent grain from the heated mash to produce a mash extract, d. convert ing the mash extract into wort; e. removing organic volatiles from the hot wort; f. dilut ing the wort with additional water; g. feeding the diluted wort into a propagation vessel in which it is combined with a recirculated stream of yeast-containing residue and in which oxygen is supplied to initiate yeast growth; h. feeding the wort from the propagation vessel into a sequence of one or more fermentation vessels in which the yeast is kept suspended; i. feeding the fermented wort into one or more separators to remove a yeast- containing residue; j. recirculat ing part of the yeast-containing residue to the propagation vessel; and k. feeding the remainder of the fermented wort to subsequent processing steps; wherein the gravity of the mash extract is maintained at more than 22 ºP; the gravity of the wort is maintained at more than 22 ºP until said wort is diluted with additional water; and the gravity of the diluted wort is within the range of 10-35 ºP; and wherein less than 30 wt.% of the fermentable sugars in the mash extract and wort are derived from fermentable sugars added after hydrolysis of the starch contained in the mash. The present method offers the advantage that it is highly efficient in terms of energy consumption and extraction yields. Furthermore, it achieves extremely high productivity, especially in the operation of the brewhouse.