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The kinetics of process dependent ammonia inhibition of methanogenesis from acetic acid

机译:依赖过程的氨抑制乙酸甲烷生成的动力学

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7%Advanced anaerobic digestion processes aimed at improving the methanization of sewage sludge may be potentially impaired by the production of inhibitory compounds (e.g. free ammonia). The result of methanogenic inhibition is relatively high effluent concentrations of acetic acid and other soluble organics, as well as reduced methane yields. An extreme example of such an advanced process is the thermal hydrolytic pretreatment of sludge prior to high solids digestion (THD). Compared to a conventional mesophilic anaerobic digestion process (MAD), THD operates in a state of constant inhibition driven by high free ammonia concentrations, and elevated pH values. As such, previous investigations of the kinetics of methanogenesis from acetic acid under uninhibited conditions do not necessarily apply well to the modeling of extreme processes such as THD. By conducting batch ammonia toxicity assays using biomass from THD and MAD reactors, we compared the response of these communities over a broad range of ammonia inhibition. For both processes, increased inhibitor concentrations resulted in a reduction of biomass growth rate (r_(max) = μ_(max)·X) and a resulting decrease in the substrate half saturation coefficient (K_s). These two parameters exhibited a high degree of correlation, suggesting that for a constant transport limited system, the K_s was mostly a linear function of the growth rate. After correcting for reactor pH and temperature, we found that the THD and MAD biomass were both able to perform methanogenesis from acetate at high free ammonia concentrations (equivalent to 3-5 g/L total ammonia nitrogen), albeit at less than 30% of their respective maximum rates. The reduction in methane production was slightly less pronounced for the THD biomass than for MAD, suggesting that the long term exposure to ammonia had selected for a methanogenic pathway less dependent on those organisms most sensitive to ammonia inhibition (i.e. aceticlastic methanogens).
机译:7%的先进厌氧消化过程旨在改善污水污泥的甲烷化程度,这可能会因抑制性化合物(例如游离氨)的产生而受到损害。产甲烷抑制作用的结果是乙酸和其他可溶性有机物的废水浓度相对较高,以及甲烷产率降低。这种先进工艺的一个极端示例是在高固体消化(THD)之前对污泥进行热水解预处理。与常规的嗜温厌氧消化工艺(MAD)相比,THD在高游离氨浓度和高pH值的驱动下,处于恒定抑制状态。因此,以前在不受抑制的条件下对乙酸甲烷化反应动力学的研究未必能很好地应用于极端过程(如THD)的建模。通过使用THD和MAD反应器中的生物质进行批量氨毒性试验,我们比较了这些群落在广泛范围内的氨抑制反应。对于这两个过程,增加的抑制剂浓度会导致生物量增长率降低(r_(max)=μ_(max)·X),并导致底物半饱和系数(K_s)降低。这两个参数显示出高度的相关性,这表明对于恒定输运受限的系统,K_s主要是增长率的线性函数。校正反应器的pH和温度后,我们发现THD和MAD生物量都能够在高游离氨浓度(相当于3-5 g / L的总氨氮)下由乙酸盐进行甲烷生成,尽管少于30%。它们各自的最高费率。与MAD相比,THD生物质的甲烷生成量减少程度不那么明显,这表明长期暴露于氨中已选择了一种产甲烷途径,而该途径较少依赖于对氨抑制最敏感的那些生物(即,弹塑性产甲烷菌)。

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