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Capture of Bacteria from Fermentation Broth by Body Feed Filtration:A Solved Problem?

机译:通过身体饲料过滤从发酵液中捕获细菌:一个解决的问题?

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摘要

The direct capture of bacteria produced in high cell density fermentation by filtration is not possible once the milliliter-scale has been surpassed.Filtration in the presence of a filter aid (body feed filtration) constitutes a putative and scalable alternative,but only if conditions proposed by industry for large-scale filtration processes,namely,flow rates (for aqueous solutions) in the range of 500-1500 L/(m~2 centre dot h) and a filter aid concentration of <=20 g/L,can be met.To this end several filter aids (grades of cellulose,diatomaceous earth,mixes thereof) were tested,albeit with no success.Capture and retention of bacteria was low (not possible in the case of cellulose),and the produced filter cakes were unstable and of low permeability.In the case of the diatomaceous earth close to 100% bacterial capture was possible,but only with filter aid concentrations that were 1 order of magnitude above the proposed limit.By using flocculating agents (Fe~(3+)/Al~(3+),PEI) either alone or in combination with diatomaceous earth and also the use of positively charged cellulose,bacteria capture could be achieved from several liters of cell suspension (OD_(600)<=15) in filtration experiments adhering to the industrial recommendations.However,the bacteria were only weakly retained in such cakes and easily released by sudden pressure pulses.Satisfactory results were only obtained by filtration of the bacteria suspension at slightly alkaline pH (8.0,50 mM Tris buffer) after treatment with sodium-activated bentonite (5 g/L) and PEI (50 mg/L) in the presence of 250 mM NaCl.In such cases 100% of the bacteria could reproducibly be captured in a filtration using 20 g/L of diatomaceous earth as filter aid.The thus produced filter cakes strongly retained the bacteria and showed good filtration performance.The procedure is at present limited to E.coli culture with biomass contents of OD_(600)<=15.Cultures with higher OD_(600) have to be diluted prior to filtration.
机译:一旦超过毫升级,就不可能通过过滤直接捕获在高细胞密度发酵中产生的细菌。在存在助滤剂(体饲料过滤)的情况下进行过滤是公认且可扩展的替代方法,但前提是提出了条件按工业用于大规模过滤过程,即流速(水溶液)在500-1500 L /(m〜2中心点h)范围内,助滤剂浓度<= 20 g / L为此,对几种助滤剂(纤维素,硅藻土及其混合物的等级)进行了测试,尽管没有成功。细菌的捕获和保留率很低(在纤维素的情况下是不可能的),并且生产的滤饼是在硅藻土中可能会接近100%的细菌捕获,但仅在助滤剂浓度比建议的限值高1个数量级时才能使用。通过使用絮凝剂(Fe〜(3+) / Al〜(3 +),PEI)或与硅藻土结合使用以及还使用带正电的纤维素,在遵循工业建议的过滤实验中,可以通过几升细胞悬浮液(OD_(600)<= 15)实现细菌捕获。仅通过用钠活化的膨润土(5 g / L)和水处理过的弱碱性pH(8.0,50 mM Tris缓冲液)过滤细菌悬浮液才能获得满意的结果。在250 mM NaCl存在下,PEI(50 mg / L)在这种情况下,使用20 g / L硅藻土作为助滤剂的过滤可重复捕获100%的细菌。目前该程序仅限于生物量OD_(600)<= 15的大肠杆菌培养,OD_(600)较高的培养物必须在过滤前进行稀释。

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