Accelerated Methanogenesis for the Conversion of Biomethane from Carbon Dioxide and Biohydrogen at Hyperthermophilic Condition

Ivy Chai Ching Hsia, Mohd Firdaus Abdul Wahab, Nur Kamilah Abdul Jalil, A.H. Goodman, H. M. Lahuri, S. S. Md Shah
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Abstract

Methanogenesis is the conversion of carbon dioxide (CO2) to methane (CH4) using microbes. In the context CO2 utilization, methanogenesis process in the utilizing native microbes from a particular reservoir can be a very slow process without any external intervention. To accelerate the conversion rate and methane yield, this study investigates the use of agriculture by-product such as palm oil mill effluent (POME) as substrates as well as potential microbial isolates that can produce biohydrogen at high temperatures. This paper covers the three laboratory assessments of microbes from anaerobic sludge from a local palm oil mill, use of POME to augment the microbial growth, and physicochemical manipulation to identify key parameters that increases CH4 yield and rate: i) biohydrogen production ii) biomethane production, and iii) syntrophic reactions. All experiments are conducted at 70°C which is considered a hyperthermophilic condition for many microbes. Biohydrogen production achieved with highest H2 production of 66.00 (mL/Lmedium). For biomethane production, the highest production rate achieved was 0.0768 CH4 µmol/mL/day which 10,000X higher than 19.6 pmol/mL/day used as a benchmark. Syntrophic reaction with both types of hydrogen-producing and methanogen in the same reactor, and pure H2 and CO2 supplemented externally was able to achieve the highest methane production of 10.095 µmol/mL and 2.524 µmol/ml/day. Methane production rate is 2.5 times faster than without external gasses being introduced. Introduction of external CO2 to the syntrophic reaction is to mimic actual carbon injection and storage in the reservoir. Our paper shows that stimulation of microbes using POME as substrates and H2/CO2 supplementation are important in accelerating the rate of methane production and yield. Future work will focus on optimizing the gas ratio, pH of growth media, and performing syntrophic reaction in porous media to emulate conditions of a reservoir.
超嗜热条件下二氧化碳和生物氢转化生物甲烷的加速产甲烷
甲烷生成是利用微生物将二氧化碳(CO2)转化为甲烷(CH4)。在二氧化碳利用的背景下,利用来自特定储层的原生微生物的产甲烷过程可能是一个非常缓慢的过程,没有任何外部干预。为了加快转化率和甲烷产量,本研究研究了利用农业副产品,如棕榈油厂废水(POME)作为底物,以及可以在高温下产生生物氢的潜在微生物分离物。本文涵盖了对当地棕榈油厂厌氧污泥微生物的三个实验室评估,使用POME来增加微生物生长,以及物理化学操作来确定增加CH4产量和速率的关键参数:i)生物氢气生产ii)生物甲烷生产iii)合成反应。所有实验都在70°C下进行,对于许多微生物来说,70°C被认为是超嗜热的条件。产氢量最高达到66.00 (mL/Lmedium)。对于生物甲烷的生产,最高产量为0.0768 CH4µmol/mL/day,比作为基准的19.6 pmol/mL/day高出10,000倍。两种产氢菌和产甲烷菌在同一反应器中进行共养反应,外加纯H2和纯CO2,产甲烷量最高,分别为10.095µmol/mL和2.524µmol/mL /d。甲烷的产率比没有引入外部气体时快2.5倍。在共生反应中引入外部CO2是为了模拟实际的碳注入和储层中的储存。我们的研究表明,以POME为底物的微生物刺激和H2/CO2补充对于加快甲烷的生产和产量是重要的。未来的工作将集中在优化气体比、生长介质的pH值,以及在多孔介质中进行协同反应来模拟储层的条件。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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