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Effect of Effluent Recirculation on Biogas Production Using Two-Stage Anaerobic Digestion of Citrus Waste

机译:两阶段厌氧消化柑橘废物对废水再循环的影响

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Citrus waste is a promising potential feedstock for anaerobic digestion, yet the presence of inhibitors such as d-limonene is known to limit the process. Effluent recirculation has been proven to increase methane yield in a semi-continuous process for recalcitrant material, but it has never been applied to toxic materials. This study was aimed to investigate the effect of recirculation on biogas production from citrus waste as toxic feedstock in two-stage anaerobic digestion. The first digestion was carried out in a stirred tank reactor (STR). The effluent from the first-stage was filtered using a rotary drum filter to separate the solid and the liquid phase. The solid phase, rich in hydrophobic D-limonene, was discarded, and the liquid phase containing less D-limonene was fed into the second digester in an up-flow anaerobic sludge bed (UASB) reactor. A high organic loading rate (OLR 5 g VS/(L;day)) of citrus waste was fed into the first-stage reactor every day. The effluent of the first-stage was then fed into the second-stage reactor. This experiment was run for 120 days. A reactor configuration without recirculation was used as control. The result shows that the reactor with effluent recirculation produced a higher methane yield (160-203 NmL/g;VS) compared to that without recirculation (66-113 NmL/g;VS). More stable performance was also observed in the reactor with recirculation as shown by the pH of 5-6, while without recirculation the pH dropped to the range of 3.7-4.7. The VS reduction for the reactor with recirculation was 33-35% higher than that of the control without recirculation. Recirculation might affect the hydrolysis-acidogenesis process by regulating pH in the first-stage and removing most of the D-limonene content from the substrate through filtration.
机译:柑橘废物是厌氧消化的有希望的潜在原料,但是已知抑制剂如d-柠檬烯的存在会限制该过程。废水再循环已被证明可以在顽固材料的半连续过程中提高甲烷的产率,但是从未将其应用于有毒材料。这项研究旨在调查再循环对两阶段厌氧消化中作为有毒原料的柑橘废物产生沼气的影响。第一次消化在搅拌釜反应器(STR)中进行。使用转鼓式过滤器过滤来自第一阶段的流出物,以分离固相和液相。丢弃富含疏水性D-柠檬烯的固相,将含有较少D-柠檬烯的液相进料到上流式厌氧污泥床(UASB)反应器中的第二个蒸煮器中。每天将高有机负荷的柑桔废物有机负荷率(OLR 5 g VS /(L; day))送入第一阶段反应器。然后将第一阶段的流出物进料到第二阶段反应器中。该实验进行了120天。没有再循环的反应器构造用作对照。结果表明,与没有再循环的反应器(66-113 NmL / g; VS)相比,具有废水再循环的反应器产生更高的甲烷产率(160-203 NmL / g; VS)。如pH为5-6所示,在具有再循环的反应器中也观察到更稳定的性能,而在没有再循环的情况下,pH下降至3.7-4.7的范围。具有再循环的反应器的VS降低比没有再循环的对照的VS降低高33-35%。再循环可通过在第一阶段调节pH值并通过过滤从底物中除去大部分D-柠檬烯含量来影响水解-产酸过程。

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