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Continuous hydrogen and methane production in a two-stage cheese whey fermentation system

机译:两阶段奶酪乳清发酵系统中连续生产氢气和甲烷

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The feasibility of integrating biological hydrogen and methane production in a two-stage processnusing mixed cultures and cheese whey powder (CWP) as substrate was studied. The effect ofnoperational parameters such as hydraulic retention time (HRT) and organic loading rate (OLR) on thenvolumetric hydrogen (VHPR) and methane (VMPR) production rates was assessed. The highest VHPRnwas 28 L H2/L/d, obtained during stable operation in a CSTR at HRT and OLR of 6 h and 142 g lactosenL/d, respectively. Moreover, hydrogen (13 L/L/d) was produced even at HRT as low as 3.5 h and OLRnof 163 g lactose/L/d, nonetheless, the reactor operation was not stable. Regarding methanenproduction in an UASB reactor, the acidified effluent from the hydrogen-producing bioreactor wasnefficiently treated obtaining COD removals above 90% at OLR and HRT of 20 g COD/L/d and 6 h,nrespectively. The two-stage process for continuous production of hydrogen and methane recoverednover 70% of the energy present in the substrate. This study demonstrated that hydrogen productionncan be efficiently coupled to methane production in a two-stage system and that CWP is an adequatensubstrate for energy production.
机译:研究了以混合培养物和干酪乳清粉(CWP)为底物,在两阶段过程中整合生物制氢和甲烷生产的可行性。评估了诸如水力停留时间(HRT)和有机负载率(OLR)等非运行参数对体积氢(VHPR)和甲烷(VMPR)生产率的影响。最高的VHPRn为28 L H2 / L / d,在CSTR中在HRT和OLR分别为6 h和142 g lactosenL / d的稳定运行期间获得。此外,即使在低至3.5 h的HRT和163 g乳糖/ L / d的OLRn下,仍会产生氢气(13 L / L / d),但反应器的运行仍不稳定。关于在UASB反应器中产生甲烷,对产氢生物反应器中酸化的流出物进行了有效处理,分别在OLR和HRT为20 g COD / L / d和6 h时获得了90%以上的COD去除率。连续生产氢气和甲烷的两阶段过程可回收基质中70%的能量。这项研究表明,在一个两阶段系统中,氢气的生产可以有效地与甲烷的生产相结合,而CWP是能源生产的适当基质。

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