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1. 发明授权

EP2408897B1 BRAUEREIANLAGE ZUR HERSTELLUNG UND ABFÜLLUNG VON BIER 无效
标题翻译：啤酒厂生产的啤酒灌装
公开(公告)号：EP2408897B1
公开(公告)日：2012-11-07
申请号：EP10714844.7
申请日：2010-03-02
申请人： GEA BREWERY SYSTEMS GMBH , Radeberger Gruppe KG
发明人： MICHEL, Rudolf , SCHELLER, Ludwig , WIEGAND, Gerd
IPC分类号： C12C13/00
CPC分类号： C12F3/06 , C02F11/04 , C02F2103/32 , C02F2303/10 , C12C13/00 , F24S21/00 , F24T10/00 , F28D15/00 , Y02E10/10 , Y02W10/23 , Y02W10/30 , Y02W10/37

2. 发明公开

EP2699336A1 VERFAHREN UND VORRICHTUNG ZUR HOPFENGABE BEI DER BIER HER STELLUNG, SOWIE HOPFENPRODUKT 失效
标题翻译：方法和装置HOPS切换时的啤酒自己的地位和啤酒花产品
公开(公告)号：EP2699336A1
公开(公告)日：2014-02-26
申请号：EP12723821.0
申请日：2012-03-08
申请人： GEA BREWERY SYSTEMS GMBH
发明人： SCHELLER, Ludwig , MICHEL, Rudolf , BAHNS, Patrick
IPC分类号： B01F3/08 , C12C7/22 , C12C13/00 , B01F5/02 , B01F5/06
CPC分类号： C12C3/00 , B01F3/0807 , B01F5/0661 , B01F13/103 , B01F2003/0849 , C12C7/22 , C12C13/00
摘要： The invention relates to a process for adding hops in beer manufacture, having the following process steps: a) separation of a subquantity (07a) of water and/or wort (07) and/or beer as aqueous fluid, b) addition of hop extract (10) in liquid or pasty form to the separated aqueous fluid (07a), c) production of a macroemulsion (13) of the hop extract by emulsifying the hop extract (10) in the aqueous fluid (07a), d) increasing the pressure in the macroemulsion (13) of the hop extract to a supply pressure of in particular greater than 100 bar, e) production of a microemulsion (17) of the hop extract by transporting the pressurized macroemulsion (13) through a gap or a valve (16) or by transporting the pressurized macroemulsion against a baffle plate, f) at least partial return of the microemulsion (17) of the hop extract to the beer manufacturing process.
摘要翻译：本发明涉及一种用于在啤酒的制造在将啤酒花，具有以下处理步骤的方法; 一个）的水和/或字（07的子量（07A）的分离）和/或啤酒作为wässrige流体，b）加入啤酒花提取物（10）（以液体或糊状形式的向分离wässrige流体07A ），C）的生产所述啤酒花提取物的宏乳液（13）的通过在含水流体（07A）乳化啤酒花提取物（10）中，d）增加的啤酒花提取物的宏乳液（13）中的压力至进料压力的特别是高于100巴，E）生产的啤酒花提取物的微乳状液（17）的通过将通过间隙或一个阀（16）的加压宏乳液（13）或通过针对一个挡板，F供给加压宏乳液）在啤酒花提取物到啤酒制造过程中的微乳状液（17）的至少部分返回。

3. 发明授权

EP2699336B1 Verfahren zur Hopfengabe bei der Bierherstellung, sowie Hopfenprodukt 失效
标题翻译：在啤酒生产中添加啤酒花的方法，以及啤酒花产品
公开(公告)号：EP2699336B1
公开(公告)日：2018-05-09
申请号：EP12723821.0
申请日：2012-03-08
申请人： GEA BREWERY SYSTEMS GMBH
发明人： SCHELLER, Ludwig , MICHEL, Rudolf , BAHNS, Patrick
IPC分类号： B01F3/08 , C12C7/22 , C12C13/00 , B01F5/02 , B01F5/06
CPC分类号： C12C3/00 , B01F3/0807 , B01F5/0661 , B01F13/103 , B01F2003/0849 , C12C7/22 , C12C13/00

4. 发明公开

EP3535378A1 VORRICHTUNG UND VERFAHREN ZUR EXTRAKTION VON AROMASTOFFEN AUS PFLANZLICHEN AROMATRÄGERN IN EINER BRAUFLÜSSIGKEIT 有权
公开(公告)号：EP3535378A1
公开(公告)日：2019-09-11
申请号：EP17803821.2
申请日：2017-11-07
申请人： Gea Brewery Systems GmbH
发明人： SCHELLER, Ludwig
IPC分类号： C12C3/08 , C12C7/20 , C12C7/24 , C12C13/00 , C12C7/28 , C12C3/12

5. 发明公开

EP2408897A2 BRAUEREIANLAGE ZUR HERSTELLUNG UND ABFÜLLUNG VON BIER 无效
标题翻译：啤酒厂生产的啤酒灌装
公开(公告)号：EP2408897A2
公开(公告)日：2012-01-25
申请号：EP10714844.7
申请日：2010-03-02
申请人： GEA BREWERY SYSTEMS GMBH , Radeberger Gruppe KG
发明人： MICHEL, Rudolf , SCHELLER, Ludwig
IPC分类号： C12C13/00
CPC分类号： C12F3/06 , C02F11/04 , C02F2103/32 , C02F2303/10 , C12C13/00 , F24S21/00 , F24T10/00 , F28D15/00 , Y02E10/10 , Y02W10/23 , Y02W10/30 , Y02W10/37
摘要： The invention relates to a brewery facility (12) for producing and bottling beer, comprising a brewhouse facility (01) in which wort is produced from raw materials while employing process energy, and further comprising a bottling facility (02) in which the beer produced from the wort is bottled into packaging containers, in particular bottles, while employing process energy, wherein in order to supply the brewhouse facility (01) with process energy a first energy supply network (16) is provided, into which process energy having a first temperature level is fed from at least one first energy generation facility (17) and distributed by a heat exchanger to different energy consumers (14, 15) in the brewhouse facility (01), and wherein in order to supply the bottling facility (02) with process energy a second energy supply network (21) is provided, into which process energy having a second temperature level is fed from at least one second energy generation facility (22) and distributed by a heat exchanger to different energy consumers (23, 24, 25) in the bottling facility (02), wherein the maximum temperature of the heat exchanger in the first energy supply network is above the maximum temperature of the heat exchanger in the second energy supply network.

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