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批式产氢发酵剩余洗净固体的再发酵——从城市固体废物有机部分生产生物氢。

Re-fermentation of washed spent solids from batch hydrogenogenic fermentation for additional production of biohydrogen from the organic fraction of municipal solid waste.

机构信息

Environmental Biotechnology and Renewable Energies R&D Group, Department of Biotechnology and Bioengineering, Centro de Investigación y de Estudios Avanzados del Instituto Politécnico Nacional, P.O. Box 14-740, México D.F. 07000, Mexico.

出版信息

J Environ Manage. 2012 Mar;95 Suppl:S355-9. doi: 10.1016/j.jenvman.2011.01.017. Epub 2011 Feb 12.

Abstract

In the first batch solid substrate anaerobic hydrogenogenic fermentation with intermittent venting (SSAHF-IV) of the organic fraction of municipal solid waste (OFMSW), a cumulative production of 16.6 mmol H(2)/reactor was obtained. Releases of hydrogen partial pressure first by intermittent venting and afterward by flushing headspace of reactors with inert gas N(2) allowed for further hydrogen production in a second to fourth incubation cycle, with no new inoculum nor substrate nor inhibitor added. After the fourth cycle, no more H(2) could be harvested. Interestingly, accumulated hydrogen in 4 cycles was 100% higher than that produced in the first cycle alone. At the end of incubation, partial pressure of H(2) was near zero whereas high concentrations of organic acids and solvents remained in the spent solids. So, since approximate mass balances indicated that there was still a moderate amount of biodegradable matter in the spent solids we hypothesized that the organic metabolites imposed some kind of inhibition on further fermentation of digestates. Spent solids were washed to eliminate organic metabolites and they were used in a second SSAHF-IV. Two more cycles of H(2) production were obtained, with a cumulative production of ca. 2.4 mmol H(2)/mini-reactor. As a conclusion, washing of spent solids of a previous SSAHF-IV allowed for an increase of hydrogen production by 15% in a second run of SSAHF-IV, leading to the validation of our hypothesis.

摘要

在第一批有机固体废物(OFMSW)的固态基质间歇放氢(SSAHF-IV)中,共获得了 16.6mmol H2/反应器的累积产量。通过间歇放气和随后用惰性气体 N2冲洗反应器顶部空间来释放氢气分压,允许在第二至第四孵育循环中进一步生产氢气,而无需添加新的接种物、底物或抑制剂。在第四周期之后,无法再收获氢气。有趣的是,在 4 个周期中积累的氢气比单独在第一周期中产生的氢气高 100%。在孵育结束时,氢气的分压接近零,而在废固体中仍存在高浓度的有机酸和溶剂。因此,由于近似质量平衡表明废固体中仍有相当数量的可生物降解物质,我们假设有机代谢物对进一步发酵消化物施加了某种抑制作用。废固体被洗涤以除去有机代谢物,并将其用于第二个 SSAHF-IV。又获得了两个 H2 生产周期,每个 mini-反应器的累积产量约为 2.4mmol H2。因此,在第二个 SSAHF-IV 运行中,洗涤前一个 SSAHF-IV 的废固体可使氢气产量增加 15%,从而验证了我们的假设。

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