Electrochemical Tuning of Alcohol Oxidase and Dehydrogenase Catalysis Via Biosensing Towards Butanol-1 Detection in Fermentation Media
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Adaptive Laboratory Evolution Enhances Methanol Tolerance and Conversion in Engineered Corynebacterium Glutamicum
ARTICLE https://doi.org/10.1038/s42003-020-0954-9 OPEN Adaptive laboratory evolution enhances methanol tolerance and conversion in engineered Corynebacterium glutamicum Yu Wang 1, Liwen Fan1,2, Philibert Tuyishime1, Jiao Liu1, Kun Zhang1,3, Ning Gao1,3, Zhihui Zhang1,3, ✉ ✉ 1234567890():,; Xiaomeng Ni1, Jinhui Feng1, Qianqian Yuan1, Hongwu Ma1, Ping Zheng1,2,3 , Jibin Sun1,3 & Yanhe Ma1 Synthetic methylotrophy has recently been intensively studied to achieve methanol-based biomanufacturing of fuels and chemicals. However, attempts to engineer platform micro- organisms to utilize methanol mainly focus on enzyme and pathway engineering. Herein, we enhanced methanol bioconversion of synthetic methylotrophs by improving cellular tolerance to methanol. A previously engineered methanol-dependent Corynebacterium glutamicum is subjected to adaptive laboratory evolution with elevated methanol content. Unexpectedly, the evolved strain not only tolerates higher concentrations of methanol but also shows improved growth and methanol utilization. Transcriptome analysis suggests increased methanol con- centrations rebalance methylotrophic metabolism by down-regulating glycolysis and up- regulating amino acid biosynthesis, oxidative phosphorylation, ribosome biosynthesis, and parts of TCA cycle. Mutations in the O-acetyl-L-homoserine sulfhydrylase Cgl0653 catalyzing formation of L-methionine analog from methanol and methanol-induced membrane-bound transporter Cgl0833 are proven crucial for methanol tolerance. This study demonstrates the importance of -
Acidogenic Properties of Carbohydrate-Rich Wasted Potato and Microbial Community Analysis: Effect of Ph
Journal of Bioscience and Bioengineering VOL. 128 No. 1, 50e55, 2019 www.elsevier.com/locate/jbiosc Acidogenic properties of carbohydrate-rich wasted potato and microbial community analysis: Effect of pH Yan Li,* Xiaodong Zhang, Haipeng Xu, Hui Mu, Dongliang Hua, Fuqiang Jin, and Guangfan Meng Energy Research Institute, Qilu University of Technology (Shandong Academy of Sciences), China Key Laboratory for Biomass Gasification Technology of Shandong Province, Jinan 250014, China Received 28 August 2018; accepted 18 December 2018 Available online 14 January 2019 Vegetable waste is one of the major organic solid residues available for sustainable biogas production. The aim of this study was to investigate the possibility and optimal controlling strategy for acidogenic fermentation of wasted potato (WP). Three leaching bed reactors (LBRs) were operated at various pH values (6.0, 7.0 and 8.0) with an organic loading rate (OLR) of 6.7 g volatile solid/(L$d) and hydraulic retention time of 6 d. Butyric acid-type fermentation with butyric acid as predominant volatile fatty acid (VFA) was observed with a concentration and proportion (of total VFAs) of butyric acid, which were 7.8 g/L, 49.7 % and 9.6 g/L and 52.2 % at pH 6.0 and 7.0, respectively. Conversely, at pH 8.0, mixed acid- type fermentation was observed with acetic and butyric acid as the major VFAs. Control experiment without pH manipulation didn’t perform well in VFAs production at first 6 days and then VFAs concentration increased as pH value was adjusted to 8. It was indicated that the inhibition was caused by high undissociated VFAs concentration due to low pH and the VFAs production could be improved through pH control strategy to regulate the undissociated VFAs con- centration. -
Enhanced Acidogenesis by the Degenerated Clostridium Sp. Strain on a Continuous Membrane Cell Recycle Reactor
Research Article Adv Biotech & Micro - Volume 7 Issue 4 November 2017 Copyright © All rights are reserved by Annamma AO DOI: 10.19080/AIBM.2017.07.555716 Enhanced Acidogenesis by the Degenerated Clostridium Sp. Strain on a Continuous Membrane Cell Recycle Reactor Hiral S, Abhishek M, Aruna GA, Annamma AO* and Arvind Lali DBT-ICT Centre for Energy Biosciences, Institute of Chemical Technology (Formerly UDCT), India Submission: July 13, 2017; Published: November 28, 2017 *Corresponding author: Annamma AO, DBT-ICT Centre for Energy Biosciences Institute of Chemical Technology (Formerly UDCT), Nathalal Parekh Marg, Mumbai-400019, India, Tel: 02233612310; Fax: 02233611020; Email: Abstract Microbial organic acids production is being extensively studied to achieve success at industrial scale. Commercial organic acid production employs homofermentative microbes while the use of heterofermentative organisms has been restricted due to expensive downstream processes. ClostridiumWith development acetobutylicum on appropriate inexpensive separation technology for separation of a mixture of organic acids, heterofermentative-1 and total organic acid fermentation may soon-1 become.h-1 feasible at large scale. Present work aims-1.h at-1 enhancing organic acid production by the degenerated strain of ATCC4259. At batch mode, pH 6 resulted in the highest total organic acid concentration of 10.22g.L acid productivity of 0.58g.L . The constant specific productivity of 1.1g.g obtained-1 for total organic acid at different pH values proved that total organic acid productivity is not governed by pH of the medium but is dependent on cell growth. However, the metabolic shifts in the cell were proved to be subject to external pH values. -
Hydrogen Production by Anaerobic Fermentation Using Agricultural and Food Processing Wastes Utilizing a Two-Stage Digestion System
Utah State University DigitalCommons@USU All Graduate Theses and Dissertations Graduate Studies 12-2008 Hydrogen Production By Anaerobic Fermentation Using Agricultural and Food Processing Wastes Utilizing a Two-Stage Digestion System Reese S. Thompson Utah State University Follow this and additional works at: https://digitalcommons.usu.edu/etd Part of the Environmental Engineering Commons Recommended Citation Thompson, Reese S., "Hydrogen Production By Anaerobic Fermentation Using Agricultural and Food Processing Wastes Utilizing a Two-Stage Digestion System" (2008). All Graduate Theses and Dissertations. 208. https://digitalcommons.usu.edu/etd/208 This Thesis is brought to you for free and open access by the Graduate Studies at DigitalCommons@USU. It has been accepted for inclusion in All Graduate Theses and Dissertations by an authorized administrator of DigitalCommons@USU. For more information, please contact [email protected]. HYDROGEN PRODUCTION BY ANAEROBIC FERMENTATION USING AGRICULTURAL AND FOOD PROCESSING WASTES UTILIZING A TWO-STAGE DIGESTION SYSTEM by Reese S. Thompson A thesis submitted in partial fulfillment of the requirements for the degree of MASTER OF SCIENCE in Biological Engineering Approved: _______________________ _______________________ Dr. Conly L. Hansen Dr. Carl S. Hansen Major Professor Committee Member _______________________ _______________________ Dr. Sridhar Viamajala Dr. Byron Burnhan Committee Member Dean of Graduate Studies UTAH STATE UNIVERSITY Logan, Utah 2008 ii Copyright © Reese S. Thompson 2008 All Rights Reserved iii ABSTRACT Hydrogen Production by Anaerobic Fermentation Using Agricultural and Food Processing Wastes Utilizing a Two-Stage Digestion System by Reese S. Thompson, Master of Science Utah State University, 2008 Major Professor: Dr. Conly L. Hansen Department: Biological and Irrigation Engineering Hydrogen production by means of anaerobic fermentation was researched utilizing three different substrates. -
Engineering Alcohol Oxidases for Substrate Scope and Their Application in Flow and Cascade Biocatalysis
ENGINEERING ALCOHOL OXIDASES FOR SUBSTRATE SCOPE AND THEIR APPLICATION IN FLOW AND CASCADE BIOCATALYSIS Rachel Heath, University of Manchester [email protected] Matthew Thompson, EnginZyme Jeremy Ramsden, University of Manchester Sebastian Cosgrove, University of Manchester William Finnigan, University of Manchester Nicholas Turner, University of Manchester Key Words: oxidation, primary alcohol, secondary alcohol, high-throughput screening, thermostability Alcohol oxidases have significant advantages over alcohol dehydrogenases (ADHs) for biocatalytic oxidation of alcohols: they don’t require addition of (expensive) nicotinamide cofactors (or a recycling system for cofactor regeneration) and the catalytic reaction is irreversible. Although alcohol oxidases generate hydrogen peroxide when they turn over, this issue can be alleviated by addition of catalase, which, not only removes the peroxide, but also creates more oxygen for cofactor regeneration. Alcohol oxidases are perceived to have a limited substrate scope preventing their wider use in synthesis. Thus, we present the engineering of two alcohol oxidases for increased substrate scope, one for the selective oxidation of primary alcohols and one for secondary alcohol oxidation. Arthrobacter chlorophenolicus choline oxidase and Streptomyces hygroscopicus cholesterol oxidase were selected as the primary and secondary alcohol oxidase, respectively. Examination of crystal structures of homologous alcohol oxidases revealed positions in the active site and entrance channel to target for saturation mutagenesis. Libraries were screened using a high-throughput assay based on the detection of hydrogen peroxide using hexanol as the substrate for evolution of choline oxidase and cyclohexanol for evolution of cholesterol oxidase. Mutations from positive hits were combined and, in these cases, resulted in variants with further improvements in both kcat and conversion to the carbonyl in biotransformations. -
Solarbio Catalogue with PRICES
CAS Name Grade Purity Biochemical Reagent Biochemical Reagent 75621-03-3 C8390-1 3-((3-Cholamidopropyl)dimethylammonium)-1-propanesulfonateCHAPS Ultra Pure Grade 1g 75621-03-3 C8390-5 3-((3-Cholamidopropyl)dimethylammonium)-1-propanesulfonateCHAPS 5g 57-09-0 C8440-25 Cetyl-trimethyl Ammonium Bromide CTAB High Pure Grade ≥99.0% 25g 57-09-0 C8440-100 Cetyl-trimethyl Ammonium Bromide CTAB High Pure Grade ≥99.0% 100g 57-09-0 C8440-500 Cetyl-trimethyl Ammonium Bromide CTAB High Pure Grade ≥99.0% 500g E1170-100 0.5M EDTA (PH8.0) 100ml E1170-500 0.5M EDTA (PH8.0) 500ml 6381-92-6 E8030-100 EDTA disodium salt dihydrate EDTA Na2 Biotechnology Grade ≥99.0% 100g 6381-92-6 E8030-500 EDTA disodium salt dihydrate EDTA Na2 Biotechnology Grade ≥99.0% 500g 6381-92-6 E8030-1000 EDTA disodium salt dihydrate EDTA Na2 Biotechnology Grade ≥99.0% 1kg 6381-92-6 E8030-5000 EDTA disodium salt dihydrate EDTA Na2 Biotechnology Grade ≥99.0% 5kg 60-00-4 E8040-100 Ethylenediaminetetraacetic acid EDTA Ultra Pure Grade ≥99.5% 100g 60-00-4 E8040-500 Ethylenediaminetetraacetic acid EDTA Ultra Pure Grade ≥99.5% 500g 60-00-4 E8040-1000 Ethylenediaminetetraacetic acid EDTA Ultra Pure Grade ≥99.5% 1kg 67-42-5 E8050-5 Ethylene glycol-bis(2-aminoethylether)-N,N,NEGTA′,N′-tetraacetic acid Ultra Pure Grade ≥97.0% 5g 67-42-5 E8050-10 Ethylene glycol-bis(2-aminoethylether)-N,N,NEGTA′,N′-tetraacetic acid Ultra Pure Grade ≥97.0% 10g 50-01-1 G8070-100 Guanidine Hydrochloride Guanidine HCl ≥98.0%(AT) 100g 50-01-1 G8070-500 Guanidine Hydrochloride Guanidine HCl ≥98.0%(AT) 500g 56-81-5 -
Optimization of Hydrolysis-Acidogenesis Phase of Swine Manure for Biogas Production Using Two-Stage Anaerobic Fermentation
processes Article Optimization of Hydrolysis-Acidogenesis Phase of Swine Manure for Biogas Production Using Two-Stage Anaerobic Fermentation Chiu-Yue Lin 1,2,3,†, Wai Siong Chai 4,†, Chyi-How Lay 1,2,5,* , Chin-Chao Chen 6, Chun-Yi Lee 2 and Pau Loke Show 4,* 1 Green Energy and Biotechnology Industry Research Center, Feng Chia University, Taichung City 40724, Taiwan; [email protected] 2 Master’s Program of Green Energy Science and Technology, Feng Chia University, Taichung City 40724, Taiwan; [email protected] 3 Department of Environmental Engineering and Science, Feng Chia University, Taichung City 40724, Taiwan 4 Department of Chemical and Environmental Engineering, Faculty of Science and Engineering, University of Nottingham Malaysia, Semenyih 43500, Selangor, Malaysia; [email protected] 5 Professional Master’s Program for Intelligent Manufacturing and Engineering Management, Feng Chia University, Taichung City 40724, Taiwan 6 Department of Landscape Architecture, Chung Chou University of Science and Technology, Changhwa 51000, Taiwan; [email protected] * Correspondence: [email protected] (C.-H.L.); [email protected] (P.L.S.) † These authors contributed equally to this work. Abstract: The traditional pig manure wastewater treatment in Taiwan has been low in methane production efficiency due to unstable influent concentration, wastewater volume, and quality. Two- Citation: Lin, C.-Y.; Chai, W.S.; Lay, stage anaerobic systems, in contrast, have the advantage of buffering the organic loading rate C.-H.; Chen, C.-C.; Lee, C.-Y.; Show, in the first stage (hydrolysis-acidogenesis phase), allowing a more constant feeding rate to the P.L. Optimization of second stage (methanogenesis phase). -
ANAEROBIC DIGESTION PROCESSES Functional Definition Of
ANAEROBIC DIGESTION PROCESSES Functional definition of “Anaerobic” = absence of oxygen or nitrate. Role of anaerobic processes in wastewater treatment 1. Enhanced biological phosphate removal (EBPR) 2. Sludge stabilization = reduction in volatile (bioreactive) solids from primary, biofilm, and waste activated sludge 3. Reduction in pathogens in sludge 4. Energy recovery as biofuels production, primarily methane (CH4) For 2-4, the unit process is the anaerobic digester. General characteristics: mixed suspended solids, complex microorganism communities, long hydraulic and solids residence time (30-60 days), mesophilic temperature (~35 C) Dominant Microbial populations: Bacteria and Archaea Rate and extent of stabilization and methane production depend strongly on population interactions. Three groups of anaerobic microorganisms in digester populations: • Group I: hydrolytic fermentative bacteria • Group II: Syntrophic acetogenic bacteria (SAB) • Group III: Archaea (methanogens) Populations, substrates, products and reaction stoichiometries are shown in Figure 1 and Table 1, following. 1 Fig 1. PARTICULATE HYDROLYSIS: HYDROLYTIC FERMENTATIVE BACTERIA (Xf) Complex Biodegradable Particulates, XS Proteins and carbohydrates, SP Lipids, SP Amino acids and simple Long Chain Fatty Acids, SP sugars, SP FERMENTATION, Xf AND ACIDOGENESIS: SYNTROPIC ACIDOGENIC BACTERIA, XSAB Volatile (Fatty) Acids: propionate, butyrate, etc. (R-COOH), SVA Acetic Acid Hydrogen (H2) (CH3COOH) SA METHANOGENESIS: ARCHAEA, XM Methane (CH4), SCH 2 Table 1. MICROBIAL REACTIONS (MOLAR STOICHIOMETRIES) I. Fermentation reaction examples (glucose substrate, various VA products) Product Reaction ΔG (kJ/mole glucose) - + Lactate C6H12O6 à 2CH3CH(OH)COO + 2H -198.1 - - + Butyrate C6H12O6 + 2H2O à CH32(CH2)COO + 2HCO3 +2H2 + 3H -254.4 - - - + Propionate + acetate 1.5C6H12O6 à 2CH3CH2COO + CH3COO + HCO3 + 3H -109.9 Genera: Bacteroides, Clostridium, etc. -
Production of Butyric Acid and Hydrogen by Metabolically Engineered Mutants of Clostridium Tyrobutyricum
PRODUCTION OF BUTYRIC ACID AND HYDROGEN BY METABOLICALLY ENGINEERED MUTANTS OF CLOSTRIDIUM TYROBUTYRICUM DISSERTATION Presented in Partial Fulfillment of the Requirements for the Degree Doctor of Philosophy in the Graduate School of The Ohio State University By Xiaoguang Liu, M.S. ***** The Ohio State University 2005 Dissertation committee: Approved by Professor Shang-Tian Yang, Adviser Professor Barbara E Wyslouzil Adviser Professor Hua Wang Department of Chemical Engineering ABSTRACT Butyric acid has many applications in chemical, food and pharmaceutical industries. The production of butyric acid by fermentation has become an increasingly attractive alternative to current petroleum-based chemical synthesis. Clostridium tyrobutyricum is an anaerobic bacterium producing butyric acid, acetic acid, hydrogen and carbon dioxide as its main products. Hydrogen, as an energy byproduct, can add value to the fermentation process. The goal of this project was to develop novel bioprocess to produce butyric acid and hydrogen economically by Clostridial mutants. Conventional fermentation technologies for butyric acid and hydrogen production are limited by low reactor productivity, product concentration and yield. In this project, novel engineered mutants of C. tyrobutyricum were created by gene manipulation and cell adaptation. Fermentation process was also optimized using immobilizing cells in the fibrous-bed bioreactor (FBB) to enhance butyric acid and hydrogen production. First, metabolic engineered mutants with knocked-out acetate formation pathway were created and characterized. Gene inactivation technology was used to delete the genes of phosphotransacetylase (PTA) and acetate kinase (AK), two key enzymes in the acetate-producing pathway of C. tyrobutyricum, through homologous recombination. The metabolic engineered mutants were characterized by Southern hybridization, enzyme assay, protein expression and metabolites production. -
Purification and Some Properties of Alcohol Oxidase from Alkane-Grown Candida Tropicalis
Biochem. J. (1992) 282, 325-331 (Printed in Great Britain) 325 Purification and some properties of alcohol oxidase from alkane-grown Candida tropicalis Francis M. DICKINSON and Catherine WADFORTH Department of Applied Biology, University of Hull, Cottingham Road, Hull HU6 7RX, U.K. Alcohol oxidase was purified to homogeneity from membrane fractions obtained from alkane-grown Candida tropicalis. The enzyme appears to be a dimer ofequal-sized subunits of Mr 70000. The purified enzyme is photosensitive and contains flavin-type material which is released by a combination of boiling and proteolytic digestion. The identity of the flavin material is not yet known, but it is not FMN, FAD or riboflavin. The enzyme is most active with dodecan-l-ol, but other long-chain alcohols are also attacked. The enzyme shows a weak, but significant activity towards long-chain aldehydes. Detailed kinetic studies with decan-1-ol as substrate suggest a group-transfer (Ping-Pong)-type mechanism of catalysis. INTRODUCTION portions of this culture were inoculated into each of six 3-litre conical flasks containing 500 ml of minimal salts Work from this laboratory has shown that growth of the yeast medium, which contained (g/l) KH2PO4, 7.0; Na2HPO4, 2.0; MgSO4, 1.5; yeast Candida tropicalis on long-chain alkane substrates induces the extract, 1.5; CaCI2, 0.1; FeCl2, 0.008; ZnSO4, 0.0001; synthesis of a long-chain-specific alcohol oxidase (Kemp et al., diammonium tartrate, 15; in distilled water at pH 6.5. The 1988). The enzyme presumably catalyses one of the steps in the pathway in which alkanes undergo monoterminal oxidation carbon source was hexadecane (1 %). -
Up-Flow Anaerobic Sludge Blanket (UASB) Technology for Energy Recovery: a Review on State-Of-The-Art and Recent Technological Advances
bioengineering Review Up-Flow Anaerobic Sludge Blanket (UASB) Technology for Energy Recovery: A Review on State-of-the-Art and Recent Technological Advances Matia Mainardis * , Marco Buttazzoni and Daniele Goi Department Polytechnic of Engineering and Architecture (DPIA), University of Udine, Via del Cotonificio 108, 33100 Udine, Italy; [email protected] (M.B.); [email protected] (D.G.) * Correspondence: [email protected] Received: 23 March 2020; Accepted: 8 May 2020; Published: 10 May 2020 Abstract: Up-flow anaerobic sludge blanket (UASB) reactor belongs to high-rate systems, able to perform anaerobic reaction at reduced hydraulic retention time, if compared to traditional digesters. In this review, the most recent advances in UASB reactor applications are critically summarized and discussed, with outline on the most critical aspects for further possible future developments. Beside traditional anaerobic treatment of soluble and biodegradable substrates, research is actually focusing on the treatment of refractory and slowly degradable matrices, thanks to an improved understanding of microbial community composition and reactor hydrodynamics, together with utilization of powerful modeling tools. Innovative approaches include the use of UASB reactor for nitrogen removal, as well as for hydrogen and volatile fatty acid production. Co-digestion of complementary substrates available in the same territory is being extensively studied to increase biogas yield and provide smooth continuous operations in a circular economy perspective. Particular importance is being given to decentralized treatment, able to provide electricity and heat to local users with possible integration with other renewable energies. Proper pre-treatment application increases biogas yield, while a successive post-treatment is needed to meet required effluent standards, also from a toxicological perspective. -
Supplementary File 1 Figure Captions
Electronic Supplementary Material (ESI) for Molecular BioSystems. This journal is © The Royal Society of Chemistry 2014 Supplementary file 1 Figure captions Figure S1 Schematic representation of elementary modes (EMs) involved in Group 1 (acidogenesis), Group 2 (solventogenesis) and Group 3 (acidogenesis and solventogenesis) in metabolic network of C. acetobutylicum. Arrows in red show activated reactions in respective elementary mode. Dotted black arrows show inactive reactions. Dotted box indicates cell membrane. “ ”and “ ” denotes reversible and irreversible reactions. For abbreviation and net reaction representation of elementary modes can be seen in Table S1 and Table S2 respectively. Figure S2 Feasible solution spaces for ethanol synthesis with respect to acetic acid and butyric acid consumption in C. acetobutylicum. Consumption rate of glucose was fixed (100 mM h-1), and consumption rate of acetic acid and butyric acid were varied within the determined feasible range of 0-400 mM h-1 and 0-100 nM h-1 respectively. Ethanol was considered as objective function to find its optimized solution spaces. Figure S3 Feasible solution spaces for hydrogen synthesis with respect to acetic acid and butyric acid consumption in C. acetobutylicum. Consumption rate of glucose was fixed (100 mM h-1), and consumption rate of acetic acid and butyric acid were varied within the determined feasible range of 0-400 mM h-1 and 0-100 nM h-1 respectively. Hydrogen was considered as objective function to find its optimized solution spaces. Figure S4 Flux variability analysis. Figure shows flux variation range (maximum - minimum) of all 67 EMs because of alternate solution spaces. Maximum and minimum values of all fluxes were calculated using methodology described in Mahadevan and Schilling (2003) for all growth conditions.