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以厌氧消化的城市污水生物固体为电子供体对二氧化硫进行微生物还原。

Microbial reduction of sulfur dioxide with anaerobically digested municipal sewage biosolids as electron donors.

作者信息

Selvaraj P T, Sublette K L

机构信息

Center for Environmental Research and Technology, University of Tulsa, Oklahoma 74104, USA.

出版信息

Biotechnol Prog. 1995 Mar-Apr;11(2):153-8. doi: 10.1021/bp00032a006.

Abstract

A concentrated stream of sulfur dioxide (SO2) is produced by regeneration of the sorbent in certain new regenerable processes for the desulfurization of flue gas. We have previously proposed that this SO2 can be converted to elemental sulfur for disposal or byproduct recovery using a microbial/Claus process. In this process, two-thirds of the SO2-reducing gas stream would be contacted with a mixed culture containing sulfate-reducing bacteria (SRB), where SO2 would act as an electron acceptor with reduction to hydrogen sulfide (H2S). This H2S could then be recombined with the remaining SO2 and sent to a Claus unit to produce elemental sulfur. The sulfate-reducing bacterium, Desulfovibrio desulfuricans, has been immobilized by coculture with flocforming heterotrophs from an anaerobic digester, resulting in a SO2-reducing floc that may be collected from the effluent of a continuous reactor for recycle by gravity sedimentation. The carbon and energy source for these cultures was anaerobically digested municipal sewage solids. The maximum specific activity for SO2 reduction in these cultures, in terms of dry weight of D. desulfuricans biomass, was 9.1 mmol of SO2/h.g. The stoichiometry with respect to the electron donor was 15.5 mg of soluble COD/mmol of SO2 reduced.

摘要

在某些新型可再生活化的烟气脱硫工艺中,吸附剂的再生会产生一股高浓度的二氧化硫(SO₂)气流。我们之前曾提出,利用微生物/克劳斯工艺可将这种SO₂转化为元素硫以便处置或回收副产物。在此工艺中,三分之二的SO₂还原气流会与一种含有硫酸盐还原菌(SRB)的混合培养物接触,在该培养物中SO₂会作为电子受体被还原为硫化氢(H₂S)。然后,这种H₂S可与剩余的SO₂重新组合,并送入克劳斯装置以生产元素硫。通过与来自厌氧消化器的絮凝性异养菌共培养,已将硫酸盐还原菌脱硫脱硫弧菌固定化,从而形成一种可从连续反应器的流出物中收集的用于SO₂还原的絮凝物,以便通过重力沉降进行循环利用。这些培养物的碳源和能源是经过厌氧消化的城市污水固体。就脱硫脱硫弧菌生物质的干重而言,这些培养物中SO₂还原的最大比活性为9.1 mmol SO₂/(h·g)。相对于电子供体的化学计量比为每还原1 mmol SO₂消耗15.5 mg可溶性化学需氧量。

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