首页> 外文期刊>Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies >Biogas production from potato-juice, a by-product from potato-starch processing, in upflow anaerobic sludge blanket (UASB) and expanded granular sludge bed (EGSB) reactors
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Biogas production from potato-juice, a by-product from potato-starch processing, in upflow anaerobic sludge blanket (UASB) and expanded granular sludge bed (EGSB) reactors

机译:马铃薯汁生产的沼气(马铃薯淀粉加工的副产品)在上流厌氧污泥床(UASB)和膨胀式颗粒污泥床(EGSB)反应器中生产

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摘要

In this study, the utilization of potato-juice, the organic by-product from potato-starch processing, for biogas production was investigated in batch assay and in high rate anaerobic reactors. The maximum methane potential of the potato-juice determined by batch assay was 470mL-CH_4/gVS-added. Anaerobic digestion of potato-juice in an EGSB reactor could obtain a methane yield of 380mL-CH_4/gVS-added at the organic loading rate of 3.2gCOD/(L-reactor.d). In a UASB reactor, higher organic loading rate of 5.1gCOD/(L-reactor.d) could be tolerated, however, it resulted in a lower methane yield of 240mL-CH_4/gVS-added. The treatment of reactor effluent was also investigated. By acidification with sulfuric acid to pH lower than 5, almost 100% of the ammonia content in the effluent could be retained during the successive up-concentration process step. The reactor effluent could be up-concentrated by evaporation to minimize its volume, and later be utilized as fertilizer.
机译:在这项研究中,通过分批测定法和高速率厌氧反应器研究了马铃薯汁(马铃薯淀粉加工中的有机副产品)用于生产沼气的利用。通过分批测定确定的马铃薯汁的最大甲烷潜能为470mL-CH_4 / gVS添加。在3.2gCOD /(L-reactor.d)的有机负载量下,在EGSB反应器中厌氧消化马铃薯汁可获得甲烷产量为380mL-CH_4 / gVS。在UASB反应器中,可以容许较高的有机负载率5.1gCOD /(L-reactor.d),但是,这导致较低的甲烷产率为240mL-CH_4 / gVS-加成。还研究了反应器废水的处理。通过用硫酸酸化至pH值低于5,在后续的浓缩过程中,废水中氨的含量几乎可以保留100%。反应器的流出物可以通过蒸发浓缩,以使其体积最小,然后用作肥料。

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