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首页> 外文期刊>Biotechnology and Bioengineering >Hydrogen sulfide production from elemental sulfur by Desulfovibrio desulfuricans in an anaerobic bioreactor
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Hydrogen sulfide production from elemental sulfur by Desulfovibrio desulfuricans in an anaerobic bioreactor

机译:厌氧生物反应器中的脱硫弧菌脱硫尿素从元素硫生产硫化氢

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摘要

Feasibility of elemental sulfur reduction by Desulfovibrio desulfuricans in anaerobic conditions in a stirred reactor was studied. Hydrogen was used as energy source, whereas the carbonated species were bicarbonate and yeast extract. Attention was paid to reactor engineering aspects, biofilm formation on the sulfur surface, hydrogen sulfide formation rate and kinetics limitations of the sulfur reduction. D. desulfuricans formed stable biofilms on the sulfur surface. It was found that active sulfur surface availability limits the reaction rate. The reaction rate was first order with respect to sulfur and hydrogen velocity had no effect in the reaction rate for the range 8.2 x 10(-2) to 4.1 x 10(-1) Nm(3) m(-2) min(-1). At a superficial gas velocity (u(G))=3.1 x 1.0(-2) Nm(3) m(-2) min(-1), H2S(g) production rate decreased due to a deficient H2S stripping. A maximum H2S(g) production rate of 2.1 g H2S L-1 d(-1) was achieved during 5 days with an initial sulfur density of 4.7% (w/v).
机译:研究了在搅拌条件下厌氧条件下,脱硫弧菌脱硫尿嘧啶还原单质硫的可行性。氢被用作能源,而碳酸盐种类是碳酸氢盐和酵母提取物。注意反应器工程方面,硫表面上生物膜的形成,硫化氢的形成速率以及硫还原的动力学限制。脱硫葡萄球菌在硫表面上形成了稳定的生物膜。发现活性硫的表面可用性限制了反应速率。关于硫的反应速率是一阶的,在8.2 x 10(-2)到4.1 x 10(-1)Nm(3)m(-2)min(-)的范围内,氢速度对反应速率没有影响1)。在表观气体速度(u(G))= 3.1 x 1.0(-2)Nm(3)m(-2)min(-1)下,由于H2S汽提不足,H2S(g)生产率降低。在5天内达到了2.1 g H2S L-1 d(-1)的最大H2S(g)生产率,初始硫密度为4.7%(w / v)。

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