辐射聚合法制备共聚物载体中的乳酸克鲁维菌固定化细胞生产乙醇。

Acta microbiologica Polonica Pub Date : 2000-01-01
A I El-Batal, L M Farahat, H A El-Rehim
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引用次数: 0

摘要

对固定化克鲁维酵母细胞分批连续生产乙醇的工艺条件进行了优化。采用辐射共聚技术,将酵母细胞固定在聚乙烯醇(PVA)与各种亲水性单体组成的水凝胶共聚物载体上。通过酵母细胞自身的粘附和增殖来固定化酵母细胞。这些水凝胶载体固定化生长酵母细胞的乙醇产量与共聚物的单体组成有关,最佳单体组成为甲基丙烯酸羟乙酯(HEMA)。在这种情况下,采用间歇发酵的细胞,乙醇产量为32.9 g L(-1),比自由体系的细胞高出约4倍。讨论了固定化酵母细胞的活性与共聚物载体含水量的关系。在PVA: HEMA (7%: 10%, w/w)水凝胶共聚物载体中固定化生长酵母细胞,在填充床塔式反应器中以不同浓度(50、100和150)g L(-1)的乳糖连续生产乙醇。对于所有乳糖饲料浓度,稀释率从0.1 h(-1)增加到0.3 h(-1)降低了发酵液中的乙醇浓度,但提高了体积乙醇产率和体积乳糖摄取率。发酵效率随着稀释率的增加和饲料培养基中乳糖浓度的升高而降低,最低乳糖浓度为50 g L(-1)时,发酵效率最高,为70.2%。
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Ethanol production by Kluyveromyces lactis immobilized cells in copolymer carriers produced by radiation polymerization.

The conditions for batch and continuous production of ethanol, using immobilized growing yeast cells of Kluyveromyces lactis, have been optimized. Yeast cells have been immobilized in hydrogel copolymer carriers composed of polyvinyl alcohol (PVA) with various hydrophilic monomers, using radiation copolymerization technique. Yeast cells were immobilized through adhesion and multiplication of yeast cells themselves. The ethanol production of immobilized growing yeast cells with these hydrogel carriers was related to the monomer composition of the copolymers and the optimum monomer composition was hydroxyethyl methacrylate (HEMA). In this case by using batch fermentation, the superior ethanol production was 32.9 g L(-1) which was about 4 times higher than that of cells in free system. The relation between the activity of immobilized yeast cells and the water content of the copolymer carriers was also discussed. Immobilized growing yeast cells in PVA: HEMA (7%: 10%, w/w) hydrogel copolymer carrier, were used in a packed-bed column reactor for the continuous production of ethanol from lactose at different levels of concentrations (50, 100 and 150) g L(-1). For all lactose feed concentrations, an increase in dilution rates from 0.1 h(-1) to 0.3 h(-1) lowered ethanol concentration in fermented broth, but the volumetric ethanol productivity and volumetric lactose uptake rate were improved. The fermentation efficiency was lowered with the increase in dilution rate and also at higher lactose concentration in feed medium and a maximum of 70.2% was obtained at the lowest lactose concentration 50 g L(-1).

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