首页> 外文会议>The 3rd international conference on engineering for waste and biomass valorisation. >OPTIMAL WORKING TEMPERATURE OF BIO-H2 AND BIO-CH4 FROM PSICHROPHILIC vs. THERMOPHILIC REGIME
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OPTIMAL WORKING TEMPERATURE OF BIO-H2 AND BIO-CH4 FROM PSICHROPHILIC vs. THERMOPHILIC REGIME

机译:亲热与热热系统中生物-H2和生物-CH4的最佳工作温度

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Effect of temperatures ranging from 16 ℃ to 50 ℃ on fermentative hydrogen production by mixed cultures was investigated in a stirred batch reactor with 2 liter of working volume, using as inoculum the anaerobic sewage sludge pretreated with HCl at pH=3 for 24 h in order to avoid methanogenesis step during fermentation. Test at 35 ℃ was conducted to convert VFAs produced at the end of the 1st acidogenic step into bioCH4 by adding an untreated anaerobic sewage sludge as inoculum in order to evaluate the total energy produced as bioH2+bioCH4. An estimation of the bioCH4 at different temperatures was carried out thanks to a smoothing function extrapolated by literature from 35 ℃ to 16 ℃. Results of batch tests at different temperatures (from 16 to 50 ℃) for only the first acidogenic step show that the biggest quantity (10 L H2/ Lreactor) of H2 and the maximum H2 production rate (1.5 L H2 l-1day1) were obtained at 35 ℃ even if it is feasible to produce H2 also at extreme temperature (16 ℃ and 50 ℃). In particular we obtained that hydrogen production increases with increasing temperature from 16 ℃ to 35 ℃ and it decreased with further increasing temperatures from 40 ℃ to 50 ℃. The two-step H2+CH4 process significantly increases the total energy production thanks to an energetic valorization of the produced liquid metabolites (VFAs).
机译:在2升工作量的搅拌间歇反应器中,研究了温度在16℃至50℃对混合培养产生发酵产氢的影响,以接种的厌氧污水污泥经pH = 3的HCl预处理24小时。避免发酵过程中产甲烷的步骤。在35℃下进行测试,通过添加未经处理的厌氧污水污泥作为接种物,将在第一个产酸步骤结束时产生的VFA转化为bioCH4,以评估产生的总能量bioH2 + bioCH4。归功于文献从35℃到16℃推算出的平滑函数,对不同温度下的bioCH4进行了估算。仅在第一个产酸步骤的不同温度(16至50℃)下的分批测试结果表明,获得了最大量的H2(10 L H2 / Lreactor)和最大的H2产生速率(1.5 L H2 l-1day1)。即使在35℃的极端温度(16℃和50℃)下也可以生产H2也是可行的。特别是,我们得到的氢气产量随着温度从16℃增加到35℃而增加,而随着温度从40℃增加到50℃而减少。由于生成的液体代谢物(VFA)的能量价高,两步H2 + CH4工艺可显着提高总能量产量。

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