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Performance of oscillatory flow reactor and stir tank reactor in solvent fermentation from palm oil mill effluent

机译:振荡流反应器和搅拌釜反应器在棕榈油厂废液发酵中的性能

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摘要

Advance in mixing technology has developed a new way of mixing fluids by introducing an oscillatory motion to replace the conventional mechanical agitation or an air bubble displacement. This new way of mixing breakthrough has been implemented in an Oscillatory Flow Reactor (OFR). This research will be focus on the performance of OFR as a bioreactor by comparing with Stir Tank Reactor (STR), which is the traditional device in fermentation. The experimental work was conducted in an OFR and a STR with a working volume of 1.5 l. Solvent production strain, Clostridium acetobutylicum NCIMB 13357 was grown in OFR and STR, using fresh Palm Oil Mill Effluent (POME) as growth medium. All of the experiments were conducted anaerobically under batch mode for 72 hours at constant temperature of 35°C. Comparisons of the growth trend and solvent fermentation performance for both devices were investigated. Total solvents (acetone, butanol and ethanol) produced in an OFR was comparable with that of STR. Total solvents production in OFR is 1.8 times higher than that of STR resulted in total 1.6 g/l of solvents. The results of this investigation showed that OFR has an excellent potential as an alternative device in fermentation processes.
机译:混合技术的进步通过引入振荡运动来代替传统的机械搅拌或气泡置换,从而开发了一种混合流体的新方法。这种新的混合突破方式已在振荡流反应器(OFR)中实现。通过与搅拌的传统装置“搅拌釜反应器”(STR)进行比较,本研究将集中于OFR作为生物反应器的性能。实验工作在OFR和STR中进行,工作容积为1.5 l。溶剂生产菌株丙酮丁醇梭菌NCIMB 13357在OFR和STR中生长,使用新鲜的棕榈油厂出水(POME)作为生长培养基。所有的实验都是在35°C的恒温下以间歇模式厌氧进行72小时。研究了两种设备的生长趋势和溶剂发酵性能的比较。在OFR中产生的总溶剂(丙酮,丁醇和乙醇)与STR相当。 OFR中的总溶剂产量是STR的1.8倍,因此总溶剂量为1.6 g / l。这项研究的结果表明,OFR作为发酵过程中的替代设备具有巨大的潜力。

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