首页> 外文会议>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:生物H2的最佳工作温度和嗜热性能的生物 - H2和Bio-CH4

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Effect of temperatures ranging from 16 °C to 50 °C 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 °C 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 °C to 16 °C. Results of batch tests at different temperatures (from 16 to 50 °C) 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 °C even if it is feasible to produce H2 also at extreme temperature (16 °C and 50 °C). In particular we obtained that hydrogen production increases with increasing temperature from 16 °C to 35 °C and it decreased with further increasing temperatures from 40 °C to 50 °C. 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:在用2升工作体积的搅拌批量反应器中研究了从16℃至50℃的温度从16℃到50℃的发酵培养物中的产生,用作接种物的厌氧污水污泥在pH = 3时用HCl预处理HCL预处理。24小时为了在发酵过程中避免甲烷化步骤。通过将未处理的厌氧污水污泥添加为接种物,进行35℃的测试,以转化在第1次缔酸性步骤结束时产生的VFA在第1次缔酸性步骤的末端产生的VFA。以评估作为BioH 2 + BioCH4产生的总能量。由于文献从35℃至16℃推断的平滑功能,对不同温度的BIOCH4的估计进行了估计。在不同温度(16至50℃)下仅用于第一个酸性步骤的批量测试结果表明,H2的最大数量(10L H2 / Lrefacter)和最大H2生产率(1.5L H2 L-1Day1)是即使在极端温度(16℃和50℃)下也可以在35℃下获得35℃。特别地,我们获得的是,氢气产生随温度的温度从16℃升高至35℃而增加,并且在40℃至50℃的进一步增加温度下降低。由于产生的液体代谢物(VFAs)的能量值,两步H2 + CH4过程显着提高了总能量产量。

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