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Enhancement of Biohydrogen Production via Thermophilic Cell Culture Immobilized on Glass Beads and Raschig Rings of Different Sizes in a Packed Bed Reactor

机译:通过固定在填充床反应器中不同尺寸的玻璃微珠和Raschig环上的嗜热细胞培养提高生物氢的生产量

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摘要

In this study, two different types of support material of different size, namely glass bead and Raschig ring, packed in a plug flow reactor, were used in order to compare their biohydrogen production performances with that of a CSTR reactor. All experiments were conducted under thermophilic conditions (55 °C ± 2 °C). The best results in terms of volumetric hydrogen productivity were obtained with large-sized glass beads (LSG: 2.98 L H2 L–1 bioreactor day–1) at 3 h hydraulic retention time (HRT). Raschig ring materials were able to produce 42 % less hydrogen than glass beads. Hydrogen productivity in the CSTR type reactor was 0.5 L H2 L–1 bioreactor day–1. In conclusion, the immobilized cell type bioreactor configuration provided 7–11 times better results in terms ofvolumetric hydrogen production values compared to the CSTR reactor. It was demonstrated that both glass beads and Raschig ring type support materials, which are readily available, showed promising results for hydrogen production.
机译:在这项研究中,使用了两种不同类型的不同尺寸的载体材料,即玻璃珠和Raschig环,填充在活塞流反应器中,以便将其生物氢生产性能与CSTR反应器进行比较。所有实验均在高温条件下(55°C±2°C)进行。在3 h的水力停留时间(HRT)下,使用大尺寸玻璃珠(LSG:2.98 L H2 L–1生物反应器第1天)可获得关于体积氢生产率的最佳结果。 Raschig环材料比玻璃珠产生的氢少42%。 CSTR型反应器的氢气生产率为0.5 L H2 L–1生物反应器第1天。总之,就体积氢产值而言,固定化细胞型生物反应器配置提供的结果比CSTR反应器好7-11倍。事实证明,容易获得的玻璃珠和Raschig环型载体材料均显示出可观的制氢结果。

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