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Novel procedure for lager beer clarification and stabilization using sequential enzymatic, centrifugal, regenerable PVPP and crossflow microfiltration processing.

机译:使用顺序的酶促,离心,可再生PVPP和错流微滤工艺对啤酒进行澄清和稳定的新程序。

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In this work, the crossflow microfiltration (CFMF) performance of different lots of lager beer, produced in a pilot scale at the Italian Brewing Research Centre (CERB, Perugia, Italy), was assessed in a bench-top plant, equipped with a 0.8-m ceramic tubular membrane module, under constant crossflow velocity of 6 m s -1, transmembrane pressure difference of 3.74 bar, temperature of ~10掳C, and periodic CO 2 backflushing. By feeding different beer samples (i.e., as such, precentrifuged (C), or pretreated with a commercial enzyme preparation to degrade the original arabinoxylans and beta-glucans and then centrifuged (EC) to minimize the fouling contribution of yeast cells, aggregates, and polysaccharides), it was possible to increase the average permeation flux (expressed as mean valuestandard deviation) from 11213 to 19917 or 33022 L m -2 h -1, respectively. Only when using the EC-pretreated beer specimens, the permeate turbidity at 20掳C approached the limiting one (<0.6 EBC unit) recommended by the European Brewery Convention standards. As expected, the permeate chill haze at 0掳C was generally higher than the above haze target. By submitting EC-pretreated beer seeded with 0.5 g L -1 of regenerable polyvinylpolypyrrolidone (PVPP) to CFMF, it was possible to reduce the initial total polyphenol content by 30% and permeate chill haze to 0.600.01 EBC unit, but the average permeation flux fell to 844 L m -2 h -1. By performing sequentially EC pretreatments, PVPP stabilization, cartridge filtration, and CFMF, it was possible not only to re-enhance the average permeation flux at about 230 L m -2 h -1 near to those achievable with DE filters, but also to obtain a chill haze-free permeate ready for aseptic packaging. CT 8th CIGR Section VI International Symposium on Advanced Food Processing and Quality Management Guangzhou, China, 3-7 November 2013.
机译:在这项工作中,在配备了0.8升水的台式工厂中,在意大利酿造研究中心(CERB,意大利佩鲁贾)以中试规模生产的不同批次的啤酒的错流微滤(CFMF)性能进行了评估。 -m陶瓷管状膜组件,在恒定的错流速度为6 ms -1的情况下,跨膜压差为3.74 bar,温度为〜10,C,并定期进行CO 2反吹。通过饲喂不同的啤酒样品(例如,预先离心(C),或用商业酶制剂预处理以降解原始的阿拉伯木聚糖和β-葡聚糖,然后离心(EC)以最小化酵母细胞,聚集体和多糖),可以将平均渗透通量(表示为平均值标准偏差)从11213分别增加到19917或33022 L m -2 h -1。仅当使用经过EC预处理的啤酒样品时,在20°C时的透过率浊度才达到欧洲啤酒公约标准所建议的极限值(<0.6 EBC单位)。不出所料,0°C时的渗透物冷雾通常高于上述雾度目标。通过将用0.5 g L -1的可再生聚乙烯基聚吡咯烷酮(PVPP)播种的EC预处理的啤酒加入CFMF,可以将最初的总多酚含量降低30%,并且使冷雾透过率降至0.600.01 EBC单位,但平均透过率通量降至844 L m -2 h -1。通过依次进行EC预处理,PVPP稳定化,滤芯过滤和CFMF,不仅可以将平均渗透通量重新提高到约230 L m -2 h -1,接近于DE过滤器可以达到的平均通量,而且还可以获得不含冷雾的渗透物,可用于无菌包装。 CT第八届CIGR第六节高级食品加工和质量管理国际研讨会,中国广州,2013年11月3日至7日。

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