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在固定化细胞和无硫沉降的游离细胞循环反应器中嗜硫代硫酸盐绿菌去除硫化氢的研究

Removal of hydrogen sulfide by Chlorobium thiosulfatophilum in immobilized-cell and sulfur-settling free-cell recycle reactors.

作者信息

Kim B W, Chang H N

机构信息

Department of Chemical Engineering, Korea Advanced Institute of Science and Technology, Taejon, Korea.

出版信息

Biotechnol Prog. 1991 Nov-Dec;7(6):495-500. doi: 10.1021/bp00012a003.

Abstract

Bioconversion of hydrogen sulfide to elementary sulfur by the photosynthetic bacterium Chlorobium thiosulfatophilum was studied in immobilized-cell and sulfur-settling free-cell recycle reactors. The cells immobilized in strontium alginate beads excreted elementary sulfur and accumulated it as crystal in the bead matrices, which made it possible that the reactor broth remained clear and the light penetrated the reactor deeper than with the free cells. In comparison with the free cells, the immobilized cells required 30% less light energy at a H2S removal rate of 2 mM/(L.h) and showed an activity of 2.4 times that of the free cells. However, in 40 h after the reaction the deterioration of the H2S removal efficiency became significant due to the accumulation of sulfur in the beads. The scanning electron micrograph (SEM) and energy-dispersive X-ray spectrometer (EDS) studies showed that the sulfur in the beads existed within a layer of 0.4 mm from the bead surface. In the sulfur-settling free-cell recycle reactor, about 80% of the sulfur excreted by the free cells could be removed in a settler. The 4-L fed batch reactor with the settler improved the light transmission to result in a H2S removal rate of 3 mumol/(mg of protein.h), 50% higher than that without it. The settling recycle reactor was much better in the removal of H2S than the immobilized-cell reactor because the former was a continuous system with the constant removal of sulfur particles by settling and of spent medium by supplying fresh medium at the same rate as the filtering rate of the reactor broth, while the latter was essentially a batch system where toxic metabolites and produced sulfur could not be removed.

摘要

利用固定化细胞和无硫沉降的游离细胞循环反应器,对光合细菌嗜硫绿菌将硫化氢生物转化为单质硫的过程进行了研究。固定在藻酸锶珠中的细胞分泌单质硫,并将其作为晶体积累在珠基质中,这使得反应器肉汤保持澄清,并且光比游离细胞时能穿透反应器更深。与游离细胞相比,在硫化氢去除率为2 mM/(L·h)时,固定化细胞所需光能减少30%,活性是游离细胞的2.4倍。然而,反应40小时后,由于珠中硫的积累,硫化氢去除效率的恶化变得显著。扫描电子显微镜(SEM)和能量色散X射线光谱仪(EDS)研究表明,珠中的硫存在于距珠表面0.4 mm的层内。在无硫沉降的游离细胞循环反应器中,游离细胞分泌的硫约80%可在沉降器中去除。带有沉降器的4-L补料分批反应器改善了光传输,使硫化氢去除率达到3 μmol/(mg蛋白质·h),比没有沉降器时高50%。沉降循环反应器在硫化氢去除方面比固定化细胞反应器好得多,因为前者是一个连续系统,通过沉降不断去除硫颗粒,并以与反应器肉汤过滤速率相同的速率供应新鲜培养基来去除用过的培养基,而后者本质上是一个分批系统,有毒代谢产物和产生的硫无法去除。

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