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光合细菌固定化细胞处理废水产氢过程中底物利用动力学研究。

Studies on kinetics of substrate utilization of hydrogen production from wastewater with immobilized cells of photosynthetic bacteria.

作者信息

Xu X, Yu X, Zheng P, Chen W, Feng X

机构信息

Department of Environmental Science, Zhejiang Agricultural University, Hangzhou, China.

出版信息

Chin J Biotechnol. 1995;11(1):69-77.

PMID:7548773
Abstract

The kinetic characteristics of substrate utilization by immobilized cells of Rhodopseudomonas capsulata 386 and Rhodopseudomonas sp. D for H2 production was investigated. The results showed that substrate utilization did not proceed simultaneously with H2 evolution, H2 producing capacity of immobilized cells with agar was higher than that of alginate immobilized cells, but the appearance of maximum H2 producing activity was later than the last one. The kinetics of substrate utilization (glucose) by immobilized cells of strain D followed the first-order reaction, rate constant k value was 1.2 x 10(-2) L/h, analysis of macrokinetics indicated that substrate utilization by immobilized cells in H2 evolution process was governed by biochemical reaction other than diffusion transfer limitation, because of the Thiele modulus were 0.125 and 0.154 for immobilized cells with D = 3.6 mm and 4.4 mm particles, the corresponding effective factor were determined as 0.998 and 0.988, respectively. An immobilized cell bioreactor, fed by glucose and lactate, was employed for continuous H2 evolving system. It was found that hydrogen production were 0.659 L/d and 0.477 L/d in immobilized cells system of strain 386 and D when lactate used as H2 evolving substrate, while the volumetric H2 rate were all up to 1.0 L/L.d.

摘要

研究了荚膜红假单胞菌386和红假单胞菌属D固定化细胞利用底物产氢的动力学特性。结果表明,底物利用与氢气产生不同步进行,琼脂固定化细胞的产氢能力高于海藻酸钠固定化细胞,但最大产氢活性出现的时间晚于后者。菌株D固定化细胞利用底物(葡萄糖)的动力学符合一级反应,速率常数k值为1.2×10(-2) L/h,宏观动力学分析表明,在产氢过程中固定化细胞利用底物受生化反应控制,而非扩散传递限制,因为对于粒径D = 3.6 mm和4.4 mm的固定化细胞,西勒模数分别为0.125和0.154,相应的有效因子分别确定为0.998和0.988。采用以葡萄糖和乳酸为进料的固定化细胞生物反应器用于连续产氢系统。结果发现,当以乳酸作为产氢底物时,386菌株和D菌株的固定化细胞系统中产氢量分别为0.659 L/d和0.477 L/d,而氢气产率均达到1.0 L/L·d。

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