A novel inverse membrane bioreactor for efficient bioconversion from methane gas to liquid methanol using a microbial gas-phase reaction.

Yan-Yu Chen, Masahito Ishikawa, Katsutoshi Hori
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Abstract

Background: Methane (CH4), as one of the major energy sources, easily escapes from the supply chain into the atmosphere, because it exists in a gaseous state under ambient conditions. Compared to carbon dioxide (CO2), CH4 is 25 times more potent at trapping radiation; thus, the emission of CH4 to the atmosphere causes severe global warming and climate change. To mitigate CH4 emissions and utilize them effectively, the direct biological conversion of CH4 into liquid fuels, such as methanol (CH3OH), using methanotrophs is a promising strategy. However, supplying biocatalysts in an aqueous medium with CH4 involves high energy consumption due to vigorous agitation and/or bubbling, which is a serious concern in methanotrophic processes, because the aqueous phase causes a very large barrier to the delivery of slightly soluble gases.

Results: An inverse membrane bioreactor (IMBR), which combines the advantages of gas-phase bioreactors and membrane bioreactors, was designed and constructed for the bioconversion of CH4 into CH3OH in this study. In contrast to the conventional membrane bioreactor with bacterial cells that are immersed in an aqueous phase, the filtered cells were placed to face a gas phase in the IMBR to supply CH4 directly from the gas phase to bacterial cells. Methylococcus capsulatus (Bath), a representative methanotroph, was used to demonstrate the bioconversion of CH4 to CH3OH in the IMBR. Cyclopropanol was supplied from the aqueous phase as a selective inhibitor of methanol dehydrogenase, preventing further CH3OH oxidation. Sodium formate was added as an electron donor to generate NADH, which is necessary for CH3OH production. After optimizing the inlet concentration of CH4, the mass of cells, the cyclopropanol concentration, and the gas flow rate, continuous CH3OH production can be achieved over 72 h with productivity at 0.88 mmol L-1 h-1 in the IMBR, achieving a longer operation period and higher productivity than those using other types of membrane bioreactors reported in the literature.

Conclusions: The IMBR can facilitate the development of gas-to-liquid (GTL) technologies via microbial processes, allowing highly efficient mass transfer of substrates from the gas phase to microbial cells in the gas phase and having the supplement of soluble chemicals convenient.

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一种利用微生物气相反应将甲烷气体高效转化为液态甲醇的新型反膜生物反应器。
背景:甲烷(CH4)作为主要能源之一,在环境条件下以气态存在,容易从供应链逃逸到大气中。与二氧化碳(CO2)相比,CH4捕获辐射的能力是二氧化碳的25倍;因此,向大气排放CH4造成了严重的全球变暖和气候变化。为了减少CH4的排放并有效地利用它们,利用甲烷氧化菌将CH4直接生物转化为液体燃料,如甲醇(CH3OH)是一种很有前途的策略。然而,在含有CH4的水介质中供应生物催化剂涉及由于剧烈搅拌和/或鼓泡而产生的高能量消耗,这在甲烷化过程中是一个严重的问题,因为水相对微可溶性气体的输送造成了非常大的障碍。结果:本研究设计并构建了一种结合气相生物反应器和膜生物反应器优点的反相膜生物反应器(IMBR),用于将CH4生物转化为CH3OH。与传统的膜生物反应器中浸泡在水相中的细菌细胞不同,经过过滤的细胞被放置在IMBR中面对气相,从而直接从气相向细菌细胞提供CH4。利用具有代表性的甲烷化菌——荚膜甲基球菌(Methylococcus capsulatus, Bath)在IMBR中进行了CH4到CH3OH的生物转化实验。环丙醇作为甲醇脱氢酶的选择性抑制剂从水相中供给,防止进一步的CH3OH氧化。加入甲酸钠作为电子供体生成生成CH3OH所必需的NADH。通过对进口CH4浓度、细胞质量、环丙醇浓度、气体流速进行优化,可在72 h内连续生产CH3OH,产率为0.88 mmol L-1 h-1,与文献报道的其他类型膜生物反应器相比,具有更长的运行周期和更高的产率。结论:IMBR可以通过微生物过程促进气-液(GTL)技术的发展,实现底物从气相到气相微生物细胞的高效传质,并且方便了可溶性化学物质的补充。
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