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Method for adjustment of membrane separation in the membrane bioreactor and the membrane bioreactor serving for the execution of this method

机译:调节膜生物反应器中的膜分离的方法和用于执行该方法的膜生物反应器

摘要

way of regulating separation membrane in the bioreactor membrane intended especially for use in processes in which appears a strong foulingu phenomenon is of surface membranes of large quantities of substances present in rozdzielanej mixture that renders the process of them are acjonarnym,in which the connector (2) using a pump (3) is supplied to the membrane module retentate and permeate stream (6) of decreasing in value from hints to membranes is of him being drained out, and furthermore, intervals shall be pumped feedback membrane module, the membrane (6) is characterised by thehaving established the maximum time separation between cycles of membrane separation in which rinsing feedback is stepping out of the membrane module (6) stream of decreasing in time values permeate is introduced into reservoir (8a) which nastu0119pn ie is discharged him using a pump (10) with fixed valueand to ensure a constant value permeatu stream discharged from a (8a), the stream with a decreasing value for reservoir (8a) is permeate, in relation to the value of wyprowadzanej in abundance, which is in excess emptied washing a, c zym in the situationwhile maintaining constant in time permeatu stream discharged from a fixed time maximum reservoir (8a) does not fill to raised level activates opru00f3u017cniaju0105ce partially filled container (8a) lavage and subsequently increases the pressure feedback tra nsmembranowe,however, when less than during fixed time interval immediately preceding the time the maximum reservoir (8a) fill to raised level then activates opru00f3u017cniaju0105ce reservoir (8a) lavage feedback and decreasing pressure transmemb ranowe,the adjustment according to the above two patterns is in situations when filling reservoir (8a) to a given level and operated it zapeu0142nieniem lavage feedback is not fixed time interval immediately preceding the predetermined time until the maximum and achieve maximum or possible to obtain pressure transmembranowego.bioreaktor membrane reactor built with a connector (2), which through the pump (3) channel retentatu (4) is connected to a valve (5) transmembranowego module, pressure membrane (6), which in turn is connected permeatu channel (7) in which the mip boost is rinsing system feedback (8),and successively in the stop valve (9) and a pump (10) is characterized by the fact that the system with feedback (8) is a reservoir (8a) which is installed in przesuwnie piston (8b) made him drive attached (8c) and a reservoir (8a) is equipped in the valve odpowietrzaju0105c y (11) and the sensor device, which advantageously is composed of two electrodes (12), konduktometryczneone of which is fixed in the bottom of the reservoir (8a) and the other to a piston (8b).
机译:在生物反应器膜中调节分离膜的方法,特别是用于出现强烈污垢现象的过程中,是在rozdzielanej混合物中存在大量物质的表面膜,使它们的过程很亲密,其中连接器(2 )使用泵(3)向膜组件提供渗余物,并且渗出液(6)的值从提示到膜递减,将其排出,并且还应抽空反馈膜组件,膜(6 )的特征在于,在膜分离循环之间建立了最大时间间隔,在该间隔中,冲洗反馈从膜组件(6)出来,时间值减小的流被引入到储液器(8a)中,该储液器(nast)排出他使用具有固定值的泵(10),并确保从(8a)排出的流量恒定,而流量减小相对于wyprowadzanej的丰度值,水库(8a)的渗透率很高,在这种情况下,如果从固定时间最大水库(8a)排出的水流保持恒定的时间不变,则冲洗a,c zym过量达到升高的液位会激活opr u00f3 u017cniaj u0105ce部分填充的容器(8a)灌洗并随后增加压力反馈流量nsmembranowe,但是当小于紧接最大贮液器(8a)填充到升高液位之前的固定时间间隔时然后激活opr u00f3 u017cniaj u0105ce储液器(8a)反馈并降低压力传递系数,在将储液器(8a)填充到给定水平并操作储油器(8a)的情况下,根据上述两种模式进行调整。不是紧接在预定时间之前的固定时间间隔,直到达到最大值并达到最大值或可能获得压力跨膜wego.bioreakt或带有连接器(2)的膜反应器,该连接器通过泵(3)的通道retentatu(4)连接到阀(5)跨膜测压组件,压力膜(6),该模块又连接了permeatu通道(7)其中mip boost冲洗系统反馈(8),并依次在截止阀(9)和泵(10)中,其特点是带有反馈(8)的系统是一个已安装的储液器(8a)在przesuwnie活塞(8b)中安装驱动器(8c),在阀odpowietrzaj u0105c y(11)和传感器装置中装有一个储液器(8a),该传感器装置有利地由两个电极(12)组成,其中两个电极活塞固定在容器(8a)的底部,另一个固定在活塞(8b)上。

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