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    • 2. 发明申请
    • METHOD FOR HYDROGENATION OF ISO-ALPHA-ACIDS AND TETRAHYDRO-ISO-ALPHA-ACIDS TO HEXAHYDRO-ISO-ALPHA-ACIDS
    • 将ISO-ALPHA-酸和四氢叶酸-ISO-阿拉伯酸加成到HEXAHYDRO-ISO-ALPHA-酸的方法
    • WO2011157692A1
    • 2011-12-22
    • PCT/EP2011/059814
    • 2011-06-14
    • KATHOLIEKE UNIVERSITEIT LEUVENMERTENS, PascalDE VOS, DirkSTEENACKERS, Bart
    • MERTENS, PascalDE VOS, DirkSTEENACKERS, Bart
    • C12C3/12
    • C07C45/66C07C51/36C12C3/12C07C59/90
    • The invention relates to a process for the production of hexahydro-iso-alpha-acids starting from iso-alpha-acids (or tetrahydro-iso-alpha-acids) in which iso-alpha-acids (or tetrahydro- iso-alpha-acids) are mixed with a heterogeneous ruthenium containing catalyst, that catalyzes the hydrogenation from iso-alpha-acids or tetrahydro-iso-alpha-acids to hexahydro- iso-alpha-acids, either in solvent-free conditions, or in the presence of a solvent phase (e.g. carbon dioxide, water, ethanol or another organic solvent, or mixtures thereof), and in the absence or presence of other hop compounds (such as beta-acids). The resulting mixture is then subjected to a temperature at which the iso-alpha-acid (or tetrahydro-iso-alpha-acid) containing reaction medium is sufficiently low in viscosity to allow easy mixing with the heterogeneous ruthenium containing catalyst and held under a hydrogen containing atmosphere (either pure hydrogen gas or mixed with an inert gas) for a reaction time sufficient to effect high conversion of the iso-alpha-acid (or tetrahydro-iso-alpha-acid) reactant into the hexahydro-iso-alpha-acid product. The molar ratio of iso-alpha-acid or tetrahydro-iso-alpha-acid to ruthenium varies between 1:1 and 2000:1. After the hydrogenation process, the heterogeneous ruthenium containing catalyst can be separated from the hexahydro-iso-alpha-acid product phase by centrifugation, filtration, decantation or other liquid-solid separation techniques. The hydrogenation process can be performed batch-wise or alternatively in continuous mode.
    • 本发明涉及从异-α-酸(或四氢异-α-酸)开始制备六氢异-5-酸的方法,其中异-α-酸(或四氢异α-酸) )与含异丁烯的含钌催化剂混合,其催化从异-α-酸或四氢异α-酸氢化成六氢异-α-酸,无溶剂条件下或在 溶剂相(如二氧化碳,水,乙醇或其他有机溶剂,或其混合物),以及其它啤酒花化合物(如β-酸)不存在或不存在时。 然后将所得混合物进行含有异-α-酸(或四氢异α-酸)的反应介质的粘度足够低的温度,以便容易地与非均相含钌催化剂混合并保持在氢气 反应时间足以使异α酸(或四氢异α-酸)反应物转化为六氢异-α酸的反应时间(或纯氢气或与惰性气体混合) 产品。 异-α-酸或四氢异-α-酸与钌的摩尔比在1:1至2000:1之间变化。 在氢化过程之后,通过离心,过滤,倾析或其它液固分离技术,可以将异质含钌催化剂与六氢异异构酸产物相分离。 氢化过程可以分批进行或以连续模式进行。
    • 3. 发明申请
    • IMPROVED METHOD FOR ISOMERISATION OF HOP ALPHA-ACIDS TO ISO-ALPHA-ACIDS
    • 用于将异丁烯酸酸化成ISO-ALPHA-ACIDS的改进方法
    • WO2012041994A1
    • 2012-04-05
    • PCT/EP2011/067055
    • 2011-09-29
    • KATHOLIEKE UNIVERSITEIT LEUVENDE VOS, DirkMERTENS, Pascal
    • DE VOS, DirkMERTENS, Pascal
    • C12C3/12
    • C12C3/12
    • The invention relates to a process for the production of iso-alpha-acids starting from alpha-acids in which an alpha-acid containing hop extract is mixed with a carbon-containing chemical compound with one or more functional groups containing a (basic) nitrogen atom with a lone pair (or mixtures thereof), either in solvent-free conditions or in the presence of solvents and preferably under an oxygen-free atmosphere. The resulting mixture is subjected to a temperature of at least 278 K for a time sufficient to effect the intended conversion of the alpha-acid reactant into the iso-alpha-acid product. The present invention further relates to iso-alpha-acid compositions obtained by said improved isomerisation process and to the use of said iso-alpha-acid compositions as bittering formulation and/or as source to obtain reduced or hydrogenated iso-alpha-acid compositions.
    • 本发明涉及从α-酸开始生产异α酸的方法,其中将含有α-酸的啤酒花提取物与含碳化合物与含有(碱)氮的一个或多个官能团混合 原子与一对(或其混合物),在无溶剂条件下或在溶剂存在下,优选在无氧气氛下。 将所得混合物经受至少278K的温度足以实现将α-酸反应物预期转化成异α酸产物的时间。 本发明还涉及通过所述改进的异构化方法获得的异-α酸组合物,以及所述异-α-酸组合物作为苦味制剂和/或来源以获得还原或氢化异-α酸组合物的用途。