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Effect of Oil Content on Biogas Production, Process Performance and Stability of Food Waste Anaerobic Digestion

机译:含油量对餐厨垃圾厌氧消化沼气产量,工艺性能和稳定性的影响

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The primary cause of anaerobic digester failure includes accumulation of inhibitory substances and intermediate products such as volatile fatty acids (VFAs), free ammonia (NH3+), and ammonium (NH4+). They (except VFAs) are however required as essential nutrients for bacteria growth. The current study specifically investigated the effect of oil content on the biogas production and the stability of anaerobic digestion of food waste. Two lab scale reactors were designed with different organic loading rates and feeding adjustment of used oil addition to testing the effects of lipids on biodegradation and biogas production. The results indicate that, at 2.0g VS L-1 d(-1), the addition of oil (5% v/v), caused the reactor failure, whereas, at 4.0g VS L-1 d(-1), the reactor remained stable for 10 days before the accumulation of VFAs, which resulted in low pH, and thus reduced the biogas and methane production. The addition of NaOH to reactivate the reactors can only improve pH, alkalinity and negatively increased viscosity, but there was no significant effect on biogas production and VFAs concentration. An effective solution to reactivate the reactors was achieved by recirculating 50% of both reactor's effluent back to the reactors. This resulted in biogas recovery and stable process performance of the reactors. Surprisingly, NH4+-N remained stable (1400mg L-1) throughout the period, far less than the critical concentration of 3000mg L-1. On the contrary, the low NH4+-N couldn't contribute to buffering the reactor's high VFA concentration during the unstable period, thereby raising new questions on its roles in anaerobic digestion process.
机译:厌氧消化器故障的主要原因包括抑制性物质和中间产物的积累,例如挥发性脂肪酸(VFA),游离氨(NH3 +)和铵(NH4 +)。但是,它们(VFA除外)是细菌生长的必需营养素。当前的研究专门研究了含油量对沼气生产和餐厨垃圾厌氧消化稳定性的影响。设计了两个实验室规模的反应器,它们具有不同的有机负荷率和废油添加的进料调节,以测试脂质对生物降解和沼气生产的影响。结果表明,在2.0克VS L-1 d(-1)时,添加油(5%v / v)会导致反应堆故障,而在4.0克VS L-1 d(-1)时,反应器在VFA积累之前保持稳定10天,这导致pH值降低,从而减少了沼气和甲烷的产生。添加NaOH以重新活化反应器只能提高pH值,碱度和负面增加的粘度,但对沼气生产和VFA浓度没有显着影响。通过将两种反应器的流出物的50%再循环回反应器,可以实现有效的解决方案,以重新激活反应器。这导致了沼气的回收和反应器稳定的工艺性能。出乎意料的是,在此期间,NH4 + -N保持稳定(1400mg L-1),远低于3000mg L-1的临界浓度。相反,在不稳定时期,低的NH4 + -N不能起到缓冲反应器高VFA浓度的作用,从而提出了关于其在厌氧消化过程中作用的新问题。

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