Enhancing the production and immobilization of cell-bound lipase from yeast-like fungus Magnusiomyces capitatus A4C for sustainable biodiesel production in a packed bed reactor
Khurshid Ahmed Baloch, Apichat Upaichit, Benjamas Cheirsilp, Fidia Fibriana
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引用次数: 0
Abstract
Magnusiomyces capitatus A4C, a mycelium-forming and lipase-producing yeast-like fungus, was employed in a five-level factorial design to optimize the collective and interactive influences of carbon, nitrogen and emulsifying sources and their possible effects on cell-bound lipase (CBL) and cell biomass production. The cell culture of M. capitatus A4C was incubated along with biomass support particles (BSPs) to immobilize the enzyme while anchoring CBL on their surfaces. Among the BSPs tested, CBL immobilized on loofah sponge under optimized conditions showed a substantial hydrolytic activity of 12.7 U mL−1 and a cell-loading capacity of 0.61 g g−1 of BSPs. Immobilized CBL was applied for biodiesel production via transesterification and esterification. The conversion percentage of triacylglycerides was approximately 100% at 24 h with the addition of water at 1:1 (v/v). The conversion of oleic acid into biodiesel via esterification was 100% at 48 h in the presence of 15% (v/v) isooctane. Further, biodiesel production was scaled up using a packed bed reactor. The batch production of biodiesel in a packed bed reactor through transesterification was 96.2%, with a circulation flow rate of 5.5 mL min−1 for 18 h. On the other hand, oleic acid conversion into biodiesel via esterification was 99.5%, with a circulation flow rate of 5.5 mL min−1 for 24 h. Further investigation revealed that the immobilized biocatalyst exhibited higher stability with esterification (85.3% fatty acid methyl ester) after ten repeated cycles.
本研究采用五水平因子设计,优化碳、氮和乳化源对细胞结合脂肪酶(CBL)和细胞生物量产生的共同和交互影响。将M. capitatus A4C细胞培养物与生物质支持颗粒(BSPs)一起孵育,固定化酶并将CBL锚定在其表面。其中,在优化条件下,丝瓜海绵固定化CBL的水解活性为12.7 U mL−1,BSPs的细胞负荷为0.61 g g−1。固定化CBL应用于酯交换和酯化生产生物柴油。在1:1 (v/v)的加水条件下,三酰甘油酯在24 h的转化率约为100%。在15% (v/v)异辛烷的存在下,油酸在48 h酯化反应中转化为生物柴油的转化率为100%。此外,利用填料床反应器扩大了生物柴油的生产规模。在填充床反应器中通过酯交换分批生产生物柴油的效率为96.2%,循环流量为5.5 mL min−1,循环时间为18 h。另一方面,油酸酯化成生物柴油的转化率为99.5%,循环流量为5.5 mL min - 1,循环24 h。进一步研究表明,经10次循环后,固定化生物催化剂具有较高的稳定性,酯化率为85.3%(脂肪酸甲酯)。
期刊介绍:
Biofuels, Bioproducts and Biorefining is a vital source of information on sustainable products, fuels and energy. Examining the spectrum of international scientific research and industrial development along the entire supply chain, The journal publishes a balanced mixture of peer-reviewed critical reviews, commentary, business news highlights, policy updates and patent intelligence. Biofuels, Bioproducts and Biorefining is dedicated to fostering growth in the biorenewables sector and serving its growing interdisciplinary community by providing a unique, systems-based insight into technologies in these fields as well as their industrial development.