Specific Organic Loading Rate Control for Improving Fermentative Hydrogen Production

M. Anzola-Rojas, L. Fuess, Marcelo Zaiat
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Abstract

Inhibiting homoacetogens is one of the main challenges in fermentative hydrogen production because these hydrogen consumers have similar growth features to hydrogen producers. Homoacetogens have been related to the excessive accumulation of biomass in fermentative reactors. Therefore, a suitable food/microorganism ratio has the potential to minimize the homoacetogenic activity. In this work, the specific organic loading rate (SOLR) was controlled in two fermentative fixed-bed up-flow reactors through scheduled biomass discharges. Reactors were differentiated by the bed arrangement, namely, packed and structured conformation. The SOLR decay along the time in both reactors was previously simulated according to the literature data. The volume and volatile suspended solids (VSS) concentration of discharges was estimated from the first discharge, and then additional discharges were planned. Biomass discharges removed 21% of the total biomass produced in the reactors, maintaining SOLR values of 3.0 ± 0.4 and 3.9 ± 0.5 g sucrose g−1 VSS d−1 in the packed-bed and structured-bed reactors, respectively. Such a control of the SOLR enabled continuous and stable hydrogen production at 2.2 ± 0.2 L H2 L−1 d−1 in the packed-bed reactor and 1.0 ± 0.3 L H2 L−1 d−1 in the structured-bed one. Controlling biomass was demonstrated to be a suitable strategy for keeping the continuous hydrogen production, although the fermentative activity was impaired in the structured-bed reactor. The homoacetogenic was partially inhibited, accounting for no more than 30% of the total acetic acid produced in the reactor. Overall, the high amount of attached biomass in the packed-bed reactor provided more robustness to the system, offsetting the periodic suspended biomass losses via the planned discharges. Better characterizing both the VSS composition (aiming to differentiate cells from polymeric substances) and the bed hydrodynamics could be useful to optimize the online SOLR control.
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控制特定有机物装载率以提高发酵制氢能力
抑制同源乙酸原是发酵法制氢过程中面临的主要挑战之一,因为这些氢消费者与氢生产者具有相似的生长特征。发酵反应器中生物量的过度积累与同源乙酸菌有关。因此,合适的食物/微生物比例有可能最大限度地降低同乙酰活性。在这项研究中,两个发酵固定床上流式反应器中的特定有机负荷率(SOLR)是通过预定的生物质排放来控制的。反应器按床层排列方式(即填料式和结构式)进行区分。之前根据文献数据模拟了两个反应器中 SOLR 随时间的衰减情况。排出物的体积和挥发性悬浮固体(VSS)浓度由第一次排出物估算得出,然后计划了更多的排出物。生物质排放清除了反应器中产生的生物质总量的 21%,使填料床反应器和结构床反应器中的 SOLR 值分别保持在 3.0 ± 0.4 和 3.9 ± 0.5 g sucrose g-1 VSS d-1 的水平。对 SOLR 的这种控制使填料床反应器能够以 2.2 ± 0.2 L2 L-1 d-1 的速度持续稳定地制氢,而结构床反应器则以 1.0 ± 0.3 L2 L-1 d-1 的速度持续稳定地制氢。尽管结构床反应器中的发酵活性受到影响,但控制生物量被证明是保持连续制氢的合适策略。同乙酸生成受到部分抑制,占反应器总乙酸生成量的比例不超过 30%。总之,填料床反应器中大量的附着生物质为系统提供了更强的稳健性,抵消了通过计划排放造成的周期性悬浮生物质损失。更好地描述 VSS 成分(目的是区分细胞和聚合物质)和床流体力学有助于优化在线 SOLR 控制。
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