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利用Ljungdahlii梭菌从合成气发酵生产生物燃料的动力学研究。

Kinetic studies on fermentative production of biofuel from synthesis gas using Clostridium ljungdahlii.

作者信息

Mohammadi Maedeh, Mohamed Abdul Rahman, Najafpour Ghasem D, Younesi Habibollah, Uzir Mohamad Hekarl

机构信息

Faculty of Chemical Engineering, Babol Noushirvani University of Technology, Babol 47148, Iran.

Low Carbon Economy (LCE) Research Group, School of Chemical Engineering, Engineering Campus, Universiti Sains Malaysia, 14300 Nibong Tebal, Penang, Malaysia.

出版信息

ScientificWorldJournal. 2014 Jan 30;2014:910590. doi: 10.1155/2014/910590. eCollection 2014.

DOI:10.1155/2014/910590
PMID:24672390
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC3925604/
Abstract

The intrinsic growth, substrate uptake, and product formation biokinetic parameters were obtained for the anaerobic bacterium, Clostridium ljungdahlii, grown on synthesis gas in various pressurized batch bioreactors. A dual-substrate growth kinetic model using Luong for CO and Monod for H2 was used to describe the growth kinetics of the bacterium on these substrates. The maximum specific growth rate (μ(max) = 0.195 h(-1)) and Monod constants for CO (K s,CO = 0.855 atm) and H2 (K(s,H2) = 0.412 atm) were obtained. This model also accommodated the CO inhibitory effects on cell growth at high CO partial pressures, where no growth was apparent at high dissolved CO tensions (P(CO)(∗) > 0.743 atm). The Volterra model, Andrews, and modified Gompertz were, respectively, adopted to describe the cell growth, substrate uptake rate, and product formation. The maximum specific CO uptake rate (q(max) = 34.364 mmol/g cell/h), CO inhibition constant (K(I) = 0.601 atm), and maximum rate of ethanol (R(max) = 0.172 mmol/L/h at P(CO) = 0.598 atm) and acetate (R(max) = 0.096 mmol/L/h at P(CO) = 0.539 atm) production were determined from the applied models.

摘要

在各种加压间歇式生物反应器中,以合成气为原料培养厌氧细菌Ljungdahlii梭菌,获得了其内在生长、底物摄取和产物形成的生物动力学参数。使用Luong方程描述CO的生长动力学,Monod方程描述H2的生长动力学,建立了双底物生长动力学模型,以描述该细菌在这些底物上的生长动力学。获得了最大比生长速率(μ(max)=0.195 h(-1))以及CO(Ks,CO = 0.855 atm)和H2(K(s,H2)=0.412 atm)的Monod常数。该模型还考虑了高CO分压下CO对细胞生长的抑制作用,在高溶解CO张力(P(CO)(∗)>0.743 atm)下无明显生长。分别采用Volterra模型、Andrews模型和修正的Gompertz模型来描述细胞生长、底物摄取速率和产物形成。从应用模型中确定了最大比CO摄取速率(q(max)=34.364 mmol/g细胞/h)、CO抑制常数(K(I)=0.601 atm)以及乙醇(在P(CO)=0.598 atm时,R(max)=0.172 mmol/L/h)和乙酸盐(在P(CO)=0.539 atm时,R(max)=0.096 mmol/L/h)的最大生成速率。

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本文引用的文献

1
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2
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Proc Natl Acad Sci U S A. 2010 Jul 20;107(29):13087-92. doi: 10.1073/pnas.1004716107. Epub 2010 Jul 2.
3
Generalization of monod kinetics for analysis of growth data with substrate inhibition.用于分析存在底物抑制的生长数据的单底物动力学的推广
将工业规模的合成气发酵规模缩小,以模拟频繁且不规则的溶解气体浓度冲击。
Bioengineering (Basel). 2023 Apr 25;10(5):518. doi: 10.3390/bioengineering10050518.
4
Reactor Designs and Configurations for Biological and Bioelectrochemical C1 Gas Conversion: A Review.用于生物和生物电化学 C1 气体转化的反应器设计和构型:综述。
Int J Environ Res Public Health. 2021 Nov 7;18(21):11683. doi: 10.3390/ijerph182111683.
5
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Biotechnol Biofuels. 2021 Aug 6;14(1):168. doi: 10.1186/s13068-021-02017-6.
6
Identifying and Engineering Bottlenecks of Autotrophic Isobutanol Formation in Recombinant by Systemic Analysis.通过系统分析鉴定和改造重组体中自养异丁醇形成的瓶颈
Front Bioeng Biotechnol. 2021 Mar 3;9:647853. doi: 10.3389/fbioe.2021.647853. eCollection 2021.
7
Metabolic modeling of bacterial co-culture systems predicts enhanced carbon monoxide-to-butyrate conversion compared to monoculture systems.与单一培养系统相比,细菌共培养系统的代谢模型预测一氧化碳到丁酸盐的转化率会提高。
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8
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9
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10
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Biotechnol Biofuels. 2020 Mar 27;13:59. doi: 10.1186/s13068-020-01695-y. eCollection 2020.
Biotechnol Bioeng. 1987 Feb;29(2):242-8. doi: 10.1002/bit.260290215.
4
Acetate yield increased by gas circulation and fed-batch fermentation in a novel syntrophic acetogenesis and homoacetogenesis coupling system.在一种新型的互营产乙酸与同型产乙酸耦合系统中,通过气体循环和补料分批发酵提高了乙酸产量。
Bioresour Technol. 2008 May;99(8):2989-95. doi: 10.1016/j.biortech.2007.06.018. Epub 2007 Aug 2.
5
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Bioresour Technol. 2006 Jul;97(11):1302-7. doi: 10.1016/j.biortech.2005.05.014. Epub 2005 Aug 1.
6
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7
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Biotechnol Prog. 1999 Oct 1;15(5):834-844. doi: 10.1021/bp990108m.