Method for the recovery of enzymes after the treatment of
starch-containing raw materials used for the production of fermentation
alcohol
    1.
    发明授权
    Method for the recovery of enzymes after the treatment of starch-containing raw materials used for the production of fermentation alcohol 失效
    用于生产发酵酒精的含淀粉原料处理后酶的回收方法

    公开(公告)号:US4436814A

    公开(公告)日:1984-03-13

    申请号:US325819

    申请日:1981-11-30

    摘要: In a method for the recovery of enzymes, the activity of which after the treatment of starch-containing raw materials used for the production of fermentation alcohol is still not exhausted, the liquid phase containing solutions with still active enzymes after the first separation of the protein fraction is led to a fermentation, then a distillation. The wash water for the protein fraction is provided with a portion of the total amount of alpha-amylase necessary for starch hydrolysis of the raw material and then solids are again separated. The enzyme-containing wash water for the second separated solids is led back into the first enzymatic degradation stage simultaneously with a portion of the slop coming from the distillation.

    摘要翻译: 在回收酶的方法中,用于生产发酵酒精的含淀粉原料处理后的活性仍未消耗,在第一次分离蛋白质后,含有活性酶的液相含有活性酶 馏分导致发酵,然后进行蒸馏。 用于蛋白质级分的洗涤水提供了原料淀粉水解所需的α-淀粉酶总量的一部分,然后再分离固体。 用于第二分离固体的含酶洗涤水与来自蒸馏的一部分斜率同时引导回到第一酶促降解阶段。

    Continuous fermentation in series of main vessels with auxiliary vessel
provided
    2.
    发明授权
    Continuous fermentation in series of main vessels with auxiliary vessel provided 失效
    连续发酵,配备辅助容器的主要容器系列

    公开(公告)号:US4419448A

    公开(公告)日:1983-12-06

    申请号:US285135

    申请日:1981-07-20

    申请人: Rolf H. Kretz

    发明人: Rolf H. Kretz

    IPC分类号: C12P7/06 C12M1/00

    摘要: An apparatus for continuously producing alcohol by fermenting a mash containing starch, sugar, and similar carbohydrates includes a series of main fermentation vessels and an auxiliary fermentation vessel. The mash, in mixture with yeast, is transferred in succession through the main vessels during normal operation of the apparatus. When the main fermentation vessels are to be cleaned, the further flow of the mash is diverted into the auxiliary fermentation vessel for a period of time sufficient to empty and clean the first main fermentation vessel in the series, whereupon the supply of the mash to the first main fermentation vessel is restored. The gap in the mash supply propagates through the series of the main fermentation vessels so that the remaining vessels can be in turn cleaned as well. By the time the last of the main fermentation vessels is empty, the mash in the auxiliary fermentation vessel is completely fermented so that it can be used to provide continuity in the stream of fermented product leaving the apparatus. The carbon dioxide developing in the fermentation vessels during the fermentation operation is scrubbed with water and the thus CO.sub.2 -enriched water is used for washing the inner walls of the fermentation vessels.

    摘要翻译: 通过发酵含有淀粉,糖和类似碳水化合物的糊状物连续生产醇的设备包括一系列主发酵容器和辅助发酵容器。 与酵母混合的醪液在设备的正常操作期间被连续转移通过主容器。 当主要发酵容器要被清洁时,将醪液的进一步流动转移到辅助发酵容器中一段足以使该系列中的第一个主发酵罐排空和清洁的时间段,从而向 第一主发酵容器恢复。 泥浆供应中的间隙通过一系列主要发酵容器传播,从而可以依次清洁剩余的容器。 在最后一个主发酵罐是空的时候,辅助发酵容器中的糊状物被完全发酵,从而可以用于提供离开设备的发酵产品流的连续性。 在发酵操作期间在发酵容器中发生的二氧化碳用水洗涤,因此将富含二氧化碳的水用于洗涤发酵容器的内壁。

    Method of continuous treatment of grain mash for producing ethanol
    3.
    发明授权
    Method of continuous treatment of grain mash for producing ethanol 失效
    连续处理谷物糊状物生产乙醇的方法

    公开(公告)号:US4416989A

    公开(公告)日:1983-11-22

    申请号:US321897

    申请日:1981-11-16

    申请人: Rolf H. Kretz

    发明人: Rolf H. Kretz

    IPC分类号: C12P7/06 C12C7/04

    CPC分类号: C12P7/06 Y02E50/17

    摘要: A method of continuous treatment of grain mash for production of ethanol includes enzymatic liquefying of starch-containing particles of raw material in a liquefying container, separating not decomposed coarser particles of raw material in the container, withdrawing the coarse particles of raw material from the container and comminuting the same, and recirculating the comminuted particles of raw material into the container. The starch-containing particles are not ground very fine such as to pass through 1-3 mm diameter sieve openings, and coarse particles withdrawn from the container are comminuted to a fine particle size preferably with a wet comminuting device. By this method, fine particles are obtained with low energy consumption.

    摘要翻译: 用于生产乙醇的谷物糊状物的连续处理方法包括在液化容器中酶原液化原料的含淀粉颗粒,分离容器中未分解的较粗颗粒的原料,从容器中取出粗颗粒 并粉碎,并将粉碎的原料颗粒再循环到容器中。 含淀粉颗粒不能被非常细磨,例如通过1-3mm直径的筛孔,从容器中取出的粗颗粒最好用湿式粉碎装置粉碎成细粒度。 通过该方法,能够获得低能耗的微粒子。