Browsing by Person "Hausmann, Rudolf"

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Applied molecular bioprocess control using RNA thermometers : exploiting temperature responsive elements for rhamnolipid production
(2022) Noll, Philipp; Hausmann, Rudolf
The highest titer reported for heterologous Rhamnolipid (RL) production is 14.9 g/L. However, biomass generation, as a large carbon sink, was a significant drawback in this process with roughly 50 more biomass than product produced. This problem is addressed in this thesis leveraging temperature as control variable and a molecular temperature sensor, an RNA thermometer (RNAT). RNAT generally refers to secondary loop structures, in the 5’ untranslated region of the mRNA, that form at certain temperatures and therefore regulate translation in dependence of temperature. The ROSE (repression of heat shock gene expression) RNAT evaluated in the first original research article in the heterologous system P. putida KT2440 pSynpro8oT_rhlAB originates from P. aeruginosa. The ROSE element regulates, in dependence of ambient temperature, the translation of rhlA and via a polar effect also the translation of rhlB therefore indirectly RL synthesis. It was found that in the ROSE RNAT-controlled system, the RL production rate was 60% higher at cultivations of 37°C than at 30°C. However, besides the regulatory effect of the RNAT, as revealed by control experiments, multiple unspecific metabolic effects may be equally responsible for the increase in production rate. After screening for even more efficient regulatory structures, a fourU RNAT was identified. Natively, this fourU RNAT regulates the expression of the heat shock gene agsA of Salmonella enterica and its regulatory capability can easily be modified by site-directed mutagenesis. The experimental data collected in the second original research article confirms the functionality of the fourU RNAT in the heterologous RL production system. The data suggested improved regulatory capabilities of the fourU RNAT compared to the ROSE element and a major effect of temperature on RL production rates and yields. The average RL production rate increased by a factor of 11 between 25°C and 38°C. Control experiments confirmed that a major part of this increase originates from the regulatory effect of the fourU RNAT rather than from an unspecific metabolic effect. With this system YP/X values well above 1 (about 1.4 gRL/gBM) could be achieved mitigating the problem of high biomass formation compared to product synthesis. Also, YP/S values of about 0.2 gRL/gGlc at elevated temperatures of 37-38°C were reached in shake flasks. The system was subsequently tested in a proof-of-concept bioreactor process involving a temperature switch. With this simple batch experiment and a temperature switch from 25°C to 38°C not only a partial decoupling of biomass formation from product synthesis was achieved but also an around 25% higher average specific rhamnolipid production rate reached compared to the so far best performing heterologous RL production process reported in literature (average specific production rate: 24 mg/(g h) vs. 32 mg/(g h)). However, to achieve higher titers while reducing side product formation a suitable feeding strategy and more complex temperature profiles may be required. Temperature variations in turn cause several metabolic changes, many of which are complex and interdependent. Models that describe biological processes as a function of temperature are thus essential for improved process understanding. The goal of the peer reviewed review article “Modeling and Exploiting Microbial Temperature Response”, shown in this thesis, was to present an overview of various temperature models, aid comprehension of model intent and to facilitate selection and application. Since not all metabolic interdependencies and mechanisms during temperature variation are known for the reasonable connection of input-output relationships, a suitable modeling approach seemed to be neural networks. Neural networks as black box models do not require mechanistic a priori knowledge but representative historic datasets. To collect training data, different temperature profiles or constant temperatures for a bioreactor process with P. putida KT2440 pSynpro8oT_rhlAB were applied and concentration curves for biomass, glucose and RL recorded. Subsequently, the data was fed into the neural network to compute RL titer as output. An exponential temperature profile yielded at the highest RL value of approx. 9 g (around 13 g/L) less biomass (around 12 g/L) than product. These values were reached after only 30 h consuming just 45 g of glucose. Hence, at this timepoint 36 weight-% of the consumed glucose could be assigned to mono-RL (YP/S = 0.19 gRL/gGlc) and biomass (YX/S = 0.17 gBM/gGlc. The so far best performing heterologous RL production process, yielded 23.2 g (14.9 g/L) mono-RL from >250 g of consumed glucose (YP/S = 0.10 gRL/gGlc) in >70 h using the same strain and medium but a constant temperature of 30°C.
Biotechnological conversion of lignocellulose hydrolyzates : model microorganisms for a bio-based economy
(2020) Horlamus, Felix; Hausmann, Rudolf
Lignocellulose has substantial potential as a carbon source in a bio-based economy. It is the most abundant renewable raw material on earth and is available in large quantities as waste from the agriculture, food and wood industry. It is composed mainly of the polymers lignin, cellulose and hemicellulose. In contrast to glucose derived from cellulose, hemicellulose sugars often remain unused although 60 billion tons of hemicelluloses are produced annually. Hemicelluloses are a group of heterogeneous polysaccharides consisting of different monomers such as D xylose, D arabinose, D mannose and D galactose. Lignocellulose is mostly depolymerized in order to obtain fermentable sugars. During the depolymerization process, inhibitors such as organic acids or furan aldehydes can be formed or released, which could be problematical for biotechnological processes. The aim of this thesis was to develop and evaluate bacterial-based biotechnological processes capable of using hemicellulose sugars as a source of carbon. First, Pseudomonas putida KT2440 was chosen. Pseudomonades are claimed as a promising chassis in biotechnology due to their versatile and robust metabolism. Unlike other Pseudomonades, the strain KT2440 is classified as biosafety level 1 in the American Type Culture Collection (ATCC). However, these bacteria can metabolize glucose as the only lignocellulose monosaccharide. Cellvibrio japonicus was the second selected bacterium. This strain is not yet established as a microbial host in biotechnology, but can degrade a huge portfolio of plant cell wall polysaccharides and is also classified as biosafety level 1 in ATCC. The topic of the first publication was to engineer P. putida KT2440 strains for metabolizing the hemicellulose monosaccharides xylose and arabinose and characterize their growth behavior. Initially, an arabinose metabolizing strain with the araBAD operon and a xylose metabolizing strain with xylAB operon was constructed. Later on, these strains were cultivated in minimal salt medium with glucose, xylose and arabinose as carbon sources in Erlenmeyer flasks. The recombinant P. putida KT2440 strains metabolized xylose and arabinose with high growth rates comparable to glucose. It turned out that both engineered strains were able to grow on both pentoses as well as on mixtures of glucose xylose and arabinose. The intent of the second publication was to evaluate P. putida KT2440 as a platform model organism for bioconversion of lignocellulose hydrolyzates. Strains were cultivated in minimal salt medium with several hydrolyzates as carbon source in Erlenmeyer flask and bioreactor. In addition, the growth-inhibiting effect of major toxic substances contained in lignocellulose hydrolyzates on P. putida KT2440 was analyzed via cultivation experiments. Several suitable hydrolyzates were figured out for this strain. Formic acid and acetic acid proved to be relatively unproblematic under pH neutral conditions, whereas furfural and hydroxymethylfurfural (HMF) had a negative effect on the bacterial growth. A diauxic-like growth behavior was revealed via fed batch bioreactor cultivations, since pentoses were almost not consumed with sufficient glucose supply. Consequently, feed-medium was added step-by-step in the next experiment. The applied feed profile did lead to an almost complete metabolization of xylose. The purpose of the third publication was to evaluate C. japonicus as a potential host strain for the one‐step bioconversion of xylans into rhamnolipids. Cultivation experiments were performed in Erlenmeyer flasks filled with minimal salt medium and containing different carbon sources. Furthermore, the strain was transformed with the plasmid pSynPro8oT carrying rhlA (encodes acetyltransferase) and rhlB (encodes rhamnosyltransferase I) to complete the rhamnolipid metabolism. The strain grew on all main lignocellulose monosaccharides as well as, on different xylans. Mono rhamnolipids were produced with the engineered strain using xylans as carbon source. This is particularly interesting as most industrially relevant bacteria are not able to depolymerize wood polymers. As the product yields were quite low, there are still many challenges in order to achieve an economically efficient process. Nevertheless, to the best of our knowledge, it is the first published one step bioconversion of hemicellulose polymers into rhamnolipids. In total, P. putida KT2440 turned out as a flexible and powerful model organism and two xylose and arabinose metabolizing strains were constructed. Moreover, bioreactor cultivations with lignocellulose hydrolyzates were performed and a feeding strategy to overcome diauxic-like growth behavior was presented. A proof of concept for a one-step bioconversion of xylans into rhamnolipids with a recombinant C. japonicus strain was successfully demonstrated.
Characterization of Bacillus velezensis UTB96, demonstrating improved lipopeptide production compared to the strain B. velezensis FZB42
(2022) Vahidinasab, Maliheh; Adiek, Isabel; Hosseini, Behnoush; Akintayo, Stephen Olusanmi; Abrishamchi, Bahar; Pfannstiel, Jens; Henkel, Marius; Lilge, Lars; Vögele, Ralf ; Hausmann, Rudolf
Bacillus strains can produce various lipopeptides, known for their antifungal properties. This makes them attractive metabolites for applications in agriculture. Therefore, identification of productive wild-type strains is essential for the development of biopesticides. Bacillus velezensis FZB42 is a well-established strain for biocontrol of plant pathogens in agriculture. Here, we characterized an alternative strain, B. velezensis UTB96, that can produce higher amounts of all three major lipopeptide families, namely surfactin, fengycin, and iturin. UTB96 produces iturin A. Furthermore, UTB96 showed superior antifungal activity towards the soybean fungal pathogen Diaporthe longicolla compared to FZB42. Moreover, the additional provision of different amino acids for lipopeptide production in UTB96 was investigated. Lysine and alanine had stimulatory effects on the production of all three lipopeptide families, while supplementation of leucine, valine and isoleucine decreased the lipopeptide bioproduction. Using a 45-litre bioreactor system for upscaling in batch culture, lipopeptide titers of about 140 mg/L surfactin, 620 mg/L iturin A, and 45 mg/L fengycin were achieved. In conclusion, it becomes clear that B. velezensis UTB96 is a promising strain for further research application in the field of agricultural biological controls of fungal diseases.
Characterization ofantifungal properties of lipopeptide-producing Bacillus velezensis strains and their proteome-based response to the phytopathogens, Diaporthe spp
(2023) Akintayo, Stephen Olusanmi; Hosseini, Behnoush; Vahidinasab, Maliheh; Messmer, Marc; Pfannstiel, Jens; Bertsche, Ute; Hubel, Philipp; Henkel, Marius; Hausmann, Rudolf; Vögele, Ralf; Lilge, Lars
Introduction: B. velezensis strains are of interest in agricultural applications due to their beneficial interactions with plants, notable through their antimicrobial activity. The biocontrol ability of two new lipopeptides-producing B. velezensis strains ES1-02 and EFSO2-04, against fungal phytopathogens of Diaporthe spp., was evaluated and compared with reference strains QST713 and FZB42. All strains were found to be effective against the plant pathogens, with the new strains showing comparable antifungal activity to QST713 and slightly lower activity than FZB42. Methods: Lipopeptides and their isoforms were identified by high-performance thin-layer chromatography (HPTLC) and mass spectrometric measurements. The associated antifungal influences were determined in direct in vitro antagonistic dual culture assays, and the inhibitory growth effects on Diaporthe spp. as representatives of phytopathogenic fungi were determined. The effects on bacterial physiology of selected B. velezensis strains were analyzed by mass spectrometric proteomic analyses using nano-LC-MS/MS. Results and Discussion: Lipopeptide production analysis revealed that all strains produced surfactin, and one lipopeptide of the iturin family, including bacillomycin L by ES1-02 and EFSO2-04, while QST713 and FZB42 produced iturin A and bacillomycin D, respectively. Fengycin production was however only detected in the reference strains. As a result of co-incubation of strain ES1-02 with the antagonistic phytopathogen D. longicolla, an increase in surfactin production of up to 10-fold was observed, making stress induction due to competitors an attractive strategy for surfactin bioproduction. An associated global proteome analysis showed a more detailed overview about the adaptation and response mechanisms of B. velezensis, including an increased abundance of proteins associated with the biosynthesis of antimicrobial compounds. Furthermore, higher abundance was determined for proteins associated with oxidative, nitrosative, and general stress response. In contrast, proteins involved in phosphate uptake, amino acid transport, and translation were decreased in abundance. Altogether, this study provides new insights into the physiological adaptation of lipopeptide-producing B. velezensis strains, which show the potential for use as biocontrol agents with respect to phytopathogenic fungi.
Design and evaluation of a 3D‐printed, lab‐scale perfusion bioreactor for novel biotechnological applications
(2023) Merkel, Manuel; Noll, Philipp; Lilge, Lars; Hausmann, Rudolf; Henkel, Marius
3D‐printing increased in significance for biotechnological research as new applications like lab‐on‐a‐chip systems, cell culture devices or 3D‐printed foods were uncovered. Besides mammalian cell culture, only few of those applications focus on the cultivation of microorganisms and none of these make use of the advantages of perfusion systems. One example for applying 3D‐printing for bioreactor development is the microbial utilization of alternative substrates derived from lignocellulose, where dilute carbon concentrations and harmful substances present a major challenge. Furthermore, quickly manufactured and affordable 3D‐printed bioreactors can accelerate early development phases through parallelization. In this work, a novel perfusion bioreactor system consisting of parts manufactured by fused filament fabrication (FFF) is presented and evaluated. Hydrophilic membranes are used for cell retention to allow the application of dilute substrates. Oxygen supply is provided by membrane diffusion via hydrophobic polytetrafluoroethylene membranes. An exemplary cultivation of Corynebacterium glutamicum ATCC 13032 supports the theoretical design by achieving competitive biomass concentrations of 18.4 g L−1 after 52 h. As a proof‐of‐concept for cultivation of microorganisms in perfusion mode, the described bioreactor system has application potential for bioconversion of multi‐component substrate‐streams in a lignocellulose‐based bioeconomy, for in‐situ product removal or design considerations of future applications for tissue cultures. Furthermore, this work provides a template‐based toolbox with instructions for creating reference systems in different application scenarios or tailor‐made bioreactor systems.
Evaluation and method development for the biosynthesis of microbial lipopeptides by bacillus species
(2023) Vahidinasab, Maliheh; Hausmann, Rudolf
Microbial lipopeptides are secondary metabolites produced by bacteria and single-celled microorganisms. They consist of a cyclic or linear peptide chain linked to a lipid residue. Due to their high-foaming biosurfactant properties, they have various industrial applications such as in detergents, food emulsifiers, bioremediation, and enhanced oil recovery. Additionally, they possess other functional properties such as antifungal activity, making them an environmentally friendly alternative to synthetic fertilizers and fungicides. Bacillus species produce cyclic lipopeptides known for their potent antifungal activity, which makes them a potential source of bio-fungicides in agriculture. However, the production titer of wild-type Bacillus species does not meet industrial needs. Thereby, genetic modification of producer strains and bioprocess engineering can help increase the production of lipopeptides. Nevertheless, the regulation and basis of biosynthesis for Bacillus lipopeptides are still not completely understood, and ongoing research aims to enhance their production. In general, three main lipopeptide families, including surfactins, iturins, and fengycins are produced by different Bacillus species. Among these, surfactin as the strong biosurfactant is the most extensively studied lipopeptide produced by Bacillus species. The focus of this doctoral thesis was mainly to evaluate the biosynthesis of iturin and fengycin families, which are strong antimicrobial lipopeptides produced by Bacillus subtilis and Bacillus velezensis. This involved developing strains through genetic engineering and enhancing the lipopeptide titer by evaluating the cultivation medium. Initially, the entire genome of the bacteria used in this thesis was examined in terms of lipopeptide biosynthesis, and the structure and yield of the different produced lipopeptides were analyzed. Regarding the lipopeptide producer derivatives of the domesticated laboratory model strain B. subtilis 168 and B. subtilis 3NA, a spore deficient strain appropriate for bioreactor cultivation, surfactin is the lipopeptide with the highest yield, while plipastatin which is a member of fengycin family, is produced in lower quantities. In the present thesis, the biosynthesis of plipastatin by B. subtilis BMV9 as the lipopeptide producer derivative of strain 3NA was evaluated. The study aimed to convert BMV9 to a constitutive plipastatin mono-producer strain. In this sense, overexpressing plipastatin biosynthesis operon using the stronger constitutive Pveg promoter led to a five-fold increase in plipastatin production. Interestingly, it was observed that deletion of srfAA-AD operon in BMV9 and the constructed constitutive plipastatin producer strain has not improved plipastatin production. Therefore, it can be stated that presumably the biosynthesis of plipastatin may be positively influenced in a post-transcriptional manner by the surfactin synthetase or some of its subunits. However, the regulatory mechanism behind this effect remained unknown and requires further research. Another attempt to enhance the plipastatin biosynthesis in strain BMV9 was repairing the degQ expression. One main genome characterization of strains with B. subtilis 168 and 3NA background is that the pleiotropic degQ gene expression, which is known to have a positive effect on plipastatin biosynthesis, is silenced due to a mutation in the promoter area. However, while repair of degQ expression in BMV9 increased the plipastatin production, combination of both repaired degQ expression and promoter exchange (Ppps::Pveg) has not significantly increased the plipastatin yield. To further evaluate the impact of degQ expression on surfactin and plipastatin biosynthesis, two strains of B. subtilis were selected: JABs24, a lipopeptide producer derived from the 168 strain, and DSM10T, the wild-type strain expressing native degQ. The findings demonstrated that surfactin biosynthesis is negatively affected by DegQ-associated DegU regulation, while increased plipastatin biosynthesis is achieved in the presence of native degQ expression. In addition to production of lipopeptides, the DegU regulatory system also plays a role in the formation of secretory proteases. A comparison of extracellular protease activities between JABs24 and DSM10T showed that degQ expression led to DSM10T having five times higher protease activity than JABs24. Interestingly, production of extracellular proteases has not affected the stability of both plipastatin and surfactin during cultivation, suggesting that lipopeptides are less targeted by extracellular proteases. The identification of proficient wild-type strains is critical to the advancement of bio-fungicide in agriculture. Therefore, the subsequent approach of this thesis centered on the production of microbial lipopeptide by wild-type B. velezensis strains. Here, the lipopeptide productivity and antifungal ability of B. velezensis UTB96 was higher than B. velezensis FZB42, as a well-established strain for biocontrol of plant pathogens in agriculture. Furthermore, addition of certain amino acids stimulated lipopeptide production, and using a bioreactor system resulted in enhancement of lipopeptide production, especially iturin A by UTB96. Overall, the doctoral thesis evaluates the biosynthesis of antimicrobial lipopeptides produced by B. subtilis and B. velezensis. The study involves genetic engineering such as promoter exchange, deletion of genes involved in competing biosynthetic pathways and cultivation medium development with amino acid supplementation to enhance the lipopeptide titer. The thesis also identifies B. velezensis UTB96 as a promising candidate for further research to be used as a wild-type antifungal agent in agriculture.
Evaluation of an external foam column for in situ product removal in aerated surfactin production processes
(2023) Treinen, Chantal; Claassen, Linda; Hoffmann, Mareen; Lilge, Lars; Henkel, Marius; Hausmann, Rudolf
In Bacillus fermentation processes, severe foam formation may occur in aerated bioreactor systems caused by surface-active lipopeptides. Although they represent interesting compounds for industrial biotechnology, their property of foaming excessively during aeration may pose challenges for bioproduction. One option to turn this obstacle into an advantage is to apply foam fractionation and thus realize in situ product removal as an initial downstream step. Here we present and evaluate a method for integrated foam fractionation. A special feature of this setup is the external foam column that operates separately in terms of, e.g., aeration rates from the bioreactor system and allows recycling of cells and media. This provides additional control points in contrast to an internal foam column or a foam trap. To demonstrate the applicability of this method, the foam column was exemplarily operated during an aerated batch process using the surfactin-producing Bacillus subtilis strain JABs24. It was also investigated how the presence of lipopeptides and bacterial cells affected functionality. As expected, the major foam formation resulted in fermentation difficulties during aerated processes, partially resulting in reactor overflow. However, an overall robust performance of the foam fractionation could be demonstrated. A maximum surfactin concentration of 7.7 g/L in the foamate and enrichments of up to 4 were achieved. It was further observed that high lipopeptide enrichments were associated with low sampling flow rates of the foamate. This relation could be influenced by changing the operating parameters of the foam column. With the methodology presented here, an enrichment of biosurfactants with simultaneous retention of the production cells was possible. Since both process aeration and foam fractionation can be individually controlled and designed, this method offers the prospect of being transferred beyond aerated batch processes.
Evaluation of an oxygen‐dependent self‐inducible surfactin synthesis in B. subtilis by substitution of native promoter PsrfA by anaerobically active PnarG and PnasD
(2021) Hoffmann, Mareen; Braig, Alina; Fernandez Cano Luna, Diana Stephanie; Rief, Katharina; Becker, Philipp; Treinen, Chantal; Klausmann, Peter; Morabbi Heravi, Kambiz; Henkel, Marius; Lilge, Lars; Hausmann, Rudolf
A novel approach targeting self-inducible surfactin synthesis under oxygen-limited conditions is presented. Because both the nitrate (NarGHI) and nitrite (NasDE) reductase are highly expressed during anaerobic growth of B. subtilis, the native promoter PsrfA of the surfactin operon in strain B. subtilis JABs24 was replaced by promoters PnarG and PnasD to induce surfactin synthesis anaerobically. Shake flask cultivations with varying oxygen availabilities indicated no significant differences in native PsrfA expression. As hypothesized, activity of PnarG and PnasD increased with lower oxygen levels and surfactin was not produced by PsrfA::PnarG as well as PsrfA::PnasD mutant strains under conditions with highest oxygen availability. PnarG showed expressions similar to PsrfA at lowest oxygen availability, while maximum value of PnasD was more than 5.5-fold higher. Although the promoter exchange PsrfA::PnarG resulted in a decreased surfactin titer at lowest oxygen availability, the strain carrying PsrfA::PnasD reached a 1.4-fold increased surfactin concentration with 696 mg/L and revealed an exceptional high overall YP/X of 1.007 g/g. This value also surpassed the YP/X of the reference strain JABs24 at highest and moderate oxygen availability. Bioreactor cultivations illustrated that significant cell lysis occurred when the process of “anaerobization” was performed too fast. However, processes with a constantly low agitation and aeration rate showed promising potential for process improvement, especially by employing the strain carrying PsrfA::PnasD promoter exchange. Additionally, replacement of other native promoters by nitrite reductase promoter PnasD represents a promising tool for anaerobic-inducible bioprocesses in Bacillus.
Evaluation of bio-oil produced from fast pyrolysis of lignocellulosic biomass as carbon source for bacterial bioconversion
(2020) Arnold, Stefanie; Hausmann, Rudolf
Scarcity of fossil resources, climate change and growing world population demand the transition from a fossil-based economy towards a bioeconomy – a knowledge-based strategy which relies on the efficient and sustainable integration of bio-based resources into value-added process chains. As lignocellulosic biomass is an abundant renewable resource which does not directly compete with food and feed, its deployment in biorefineries is of special interest for a sustainable bioeconomy. Owing to its compact and complex structure, suitable conversion techniques need to be selected. Combinations of thermochemical and biochemical conversion technologies are considered to be a promising approach regarding a fast and efficient conversion of lignocellulosic biomass into value-added products. Bio-oil derived from fast pyrolysis of lignocellulosic biomass is a complex mixture and composed of water and a wide variety of organic components. Among these components pyrolytic sugars and small organic acids are particularly interesting as potential carbon sources for microbial processes. However, bio-oil also comprises many unidentified substances, as well as components which are known to display adverse effects on microbial growth. To evaluate the potential and challenges of bio-oil as an alternative and sustainable carbon source for bacterial bioconversion this thesis was divided into three parts (Figure 1). In Part I different pretreatment strategies were applied and evaluated regarding their effect on stability and detoxification of bio-oil fractions. For this purpose, the organic solvent tolerant bacterial strain Pseudomonas putida KT2440 was applied as a reference system and cultivated on different pretreated bio-oil fractions. It was shown that solid phase extraction is a suitable tool to obtain bio-oil fractions with significantly increased stability along with less inhibitory substances. Part II is focused on the evaluation of small organic acids mainly present in bio-oil with respect to their suitability as feedstock for bacterial growth. Four biotechnological production hosts Escherchia coli, Pseudomonas putida, Bacillus subtilis and Corynebacterium glutamicum were cultivated on different concentrations of acetate, mixtures of small organic acids, as well as pretreated bio-oil fractions as carbon source for their growth. Results reveal that P. putida, as well as C. glutamicum metabolizes acetate – the major small organic acid generated during fast pyrolysis of lignocellulosic biomass – as sole carbon source over a wide concentration range and grow on mixtures of small organic acids present in bio-oil. Moreover, both strains show a distinct potential to tolerate inhibitory substances within bio-oil. Part III describes the growth behavior of a genetically engineered, nonpathogenic bacterium Pseudomonas putida KT2440 and its simultaneous heterologous production of rhamnolipid biosurfactants on bio-oil derived small organic acids and pretreated fractions. Results suggest that both maximum achievable productivities and substrate-to-biomass yields are in a comparable range for glucose, acetate, as well as the mixture of acetate, formate and propionate. Similar yields were obtained for a pretreated bio-oil fraction, although with significantly lower titers. In conclusion, this thesis shows that microbial valorization of bio-oil is a challenging task due to its highly complex and variable composition, as well as its adverse effects on microbial growth and issues with analytical procedures. This work depicts a proof of concept by outlining a potential biorefinery route for microbial valorization of pretreated bio-oil and its unexploited side streams. It provides a step in search of suitable bacterial strains for bioconversion of lignocellulosicbased feedstocks into value-added products and thus contributes to establishing bioprocesses within a future bioeconomy.
Exploiting novel strategies for the production of surfactin in Bacillus subtilis cultures
(2021) Hoffmann, Mareen; Hausmann, Rudolf
Biosurfactants are synthesized by various microorganisms. These surface-active molecules are a promising alternative to petrochemically and oleochemically produced surfactants. Advantageously, biosurfactants are reported to be better biodegradable and less toxic. The cyclic lipopeptide surfactin synthesized by Bacillus subtilis displays one interesting biosurfactant. Many studies report on the outstanding physico-chemical characteristics and add on benefits such as antimicrobial properties. Hence, surfactin has the potential to be used in a variety of industrial sectors. Nevertheless, processes ensuring both robustness and high titers are rare, especially as conventional aerobic bioreactor cultivations share one major disadvantage, namely excessive foaming. To approach industrial processes, different methods are applied, which can be categorized in three practices. These are (1) media and process parameter optimization, (2) strain engineering, and (3) investigating novel process strategies. For the latter category, the anaerobic growth by nitrate respiration poses an interesting foam-free alternative. In this sense, the anaerobic cultivation of B. subtilis to produce surfactin coupled with the three afore mentioned practices was addressed in this thesis targeting at a foam-free surfactin production process. In the 1st publication, the genome reduced strain B. subtilis IIG-Bs20-5-1, a derivative of the laboratory strain 168 able to synthesize surfactin, was evaluated with respect to its suitability as surfactin producer at various temperatures under both aerobic and anaerobic conditions. It was hypothesized that a deletion of 10% of the genome, e.g., non-essential genes synthesizing prophages or the antibiotic bacilysin, saves metabolic resources and hence results in increased surfactin titers. Strains B. subtilis JABs24, a 168 derivative able to synthesize surfactin but without genome reduction, and the surfactin producer B. subtilis DSM 10T served for comparison. Although strain IIG-Bs20-5-1 was superior regarding specific growth rate µ and biomass yield YX/S, the strain was inferior with respect to surfactin titers, product related yields YP/S and YP/X, and specific productivity q. Indeed, compared to others in literature described strains, B. subtilis JABs24 was emphasized as promising target strain for further process development, reaching high surfactin titers of 1147 mg/L aerobically and 296 mg/L anaerobically as well as exceptionally high product yields YP/X under anaerobic conditions. Accordingly, iterative process optimization was hypothesized to improve anaerobically achieved surfactin titers. However, several aspects to consider of anaerobic growth of B. subtilis by nitrate respiration were described in the 2nd publication. Amongst others, increasing ammonium concentrations, resulting from nitrate reduction to ammonium via nitrite, were shown to have no impact on growth of strain JABs24, but surfactin titers and expression of nitrate reductase promoter PnarG were reduced. Nitrite was shown to peak within the first hours of cultivation and concentrations up to 10 mmol/L resulted in prolonged lag-phases. Moreover, acetate accumulated drastically during the time course of cultivation independent of glucose availability, thus decreasing the glucose flux into biomass. Acetate additionally influenced both specific growth rate µ and PnarG expression negatively. Concluding, the general feasibility of anaerobic fed-batch cultivations to synthesize surfactin was shown, but several aspects must be addressed in future works to make this strategy an equated process with aerobic cultivations. In the 3rd publication, a self-inducible surfactin synthesis process was presented where expression of the surfactin operon in B. subtilis JABs24 was induced under oxygen limited conditions. The native promoter of the srfA operon PsrfA was replaced by anaerobically inducible nitrate reductase promoter PnarG and nitrite reductase promoter PnasD. Shake flask cultivations with varying oxygen availabilities demonstrated that both PnarG and PnasD can serve as auto-inducible promoters. At high oxygen availability, surfactin was not produced in the promoter exchange strains. At lowest oxygen availability, the strain carrying PnarG reached lower surfactin titers than the native JABs24 strain, although expression levels of PnarG and PsrfA were similar. However, strain B. subtilis MG14 with PsrfA::PnasD reached 1.4-fold higher surfactin titers with 696 mg/L and an exceptionally high YP/X of 1.007 g/g with overall lower foam levels. Though, bioreactor cultivations have illustrated that the anaerobic induction must be performed slowly as to avoid cell lysis, resulting in so-defined aerobic-anaerobic switch processes. With further appropriate process optimization, a simple and robust surfactin production process with highly reduced or even no foam formation can be achieved employing strain B. subtilis MG14.
Surfactin shows relatively low antimicrobial activity against Bacillus subtilis and other bacterial model organisms in the absence of synergistic metabolites
(2022) Lilge, Lars; Ersig, Nadine; Hubel, Philipp; Aschern, Moritz; Pillai, Evelina; Klausmann, Peter; Pfannstiel, Jens; Henkel, Marius; Morabbi Heravi, Kambiz; Hausmann, Rudolf
Surfactin is described as a powerful biosurfactant and is natively produced by Bacillus subtilis in notable quantities. Among other industrially relevant characteristics, antimicrobial properties have been attributed to surfactin-producing Bacillus isolates. To investigate this property, stress approaches were carried out with biotechnologically established strains of Corynebacterium glutamicum, Bacillus subtilis, Escherichia coli and Pseudomonas putida with the highest possible amounts of surfactin. Contrary to the popular opinion, the highest growth-reducing effects were detectable in B. subtilis and E. coli after surfactin treatment of 100 g/L with 35 and 33%, respectively, while P. putida showed no growth-specific response. In contrast, other antimicrobial biosurfactants, like rhamnolipids and sophorolipids, showed significantly stronger effects on bacterial growth. Since the addition of high amounts of surfactin in defined mineral salt medium reduced the cell growth of B. subtilis by about 40%, the initial stress response at the protein level was analyzed by mass spectrometry, showing induction of stress proteins under control of alternative sigma factors σB and σW as well as the activation of LiaRS two-component system. Overall, although surfactin is associated with antimicrobial properties, relatively low growth-reducing effects could be demonstrated after the surfactin addition, challenging the general claim of the antimicrobial properties of surfactin.
Toward effects of hydrophobicity on biosurfactant production by Bacillus subtilis isolates from crude-oil-exposed environments
(2024) Hashemi, Seyedeh Zahra; Fooladi, Jamshid; Vahidinasab, Maliheh; Hubel, Philipp; Pfannstiel, Jens; Pillai, Evelina; Hrenn, Holger; Hausmann, Rudolf; Lilge, Lars
Background: Due to their structural features, biosurfactants reveal promising physicochemical properties, making them interesting for various applications in different fields, such as the food, cosmetics, agriculture, and bioremediation sectors. In particular, the bioproduction of surfactin, one of the most potent microbially synthesized biosurfactant molecules, is of great interest. However, since the wild-type productivities are comparably low, stimulatory environmental conditions have to be identified for improved bioproduction This study aims to find a correlation between the hydrophobicity and production of the biosurfactant surfactin by B. subtilis isolates from crude-oil-contaminated soil and water. Methods: The surfactin production yield was characterized in adapted batch cultivations using high-performance thin-layer liquid chromatography (HPTLC). Defined hydrophobic environmental conditions were achieved by supplementation with hexadecane or polystyrene beads, and the effects on biosurfactant production were measured. Adaptations at the protein level were analyzed using mass spectrometry measurements. Results: The correlation between hydrophobicity and surfactin production was characterized using Bacillus subtilis strains ZH1 and P7 isolated from crude-oil-contaminated soil and water. Since these isolates show the biodegradation of crude oil and hexadecane as hydrophobic substrates, respectively, a first-time approach, using polystyrene beads, was applied to provide a hydrophobic environment. Interestingly, contrary to popular opinion, reduced biosurfactant production was determined. Using mass spectrometric approaches, the physiological effects of co-cultivation and the cellular response at the protein level were investigated, resulting in altered quantities of stress proteins and proteins involved in the carbon metabolism counter to polystyrene beads. Conclusions: Contrary to common opinion, increasing hydrophobicity does not have a stimulating effect, and even reduces the effect on the bioproduction of surfactin as the main biosurfactant using selected B. subtilis strains.
Utilizing process waters from conversion processes based on regenerative resources for microbial production of platform chemicals
(2024) Merkel, Manuel; Hausmann, Rudolf
A future bioeconomy relying on biotechnological production processes makes it necessary to find a replacement for sugars as microbial carbon source to prevent ethically questionable competition with the food and feed sector. An attractive alternative is acetic acid, as it is inexpensive, available in high quantities and utilized equally well as glucose by some bacteria. Still, the application of acetic acid as sole carbon source in bioproduction processes offers several challenges. In its protonated form acetic acid leads to medium acidification, when applied in high concentrations, while as salt it leads to salinization causing osmotic stress for the production organisms. As such, established process strategies are difficult to apply with acetic acid, making specialized strategies necessary for production processes. Therefore, an efficient fed-batch strategy was developed and is presented in the 1st publication utilizing acetic acid as sole carbon source for production of itaconic acid with a genetically modified strain C. glutamicum ICDR453C (pEKEx2-malEcadopt). An earlier published pH-coupled feeding strategy for addition of glacial acetic acid was adapted to obtain the nitrogen limited conditions necessary for itaconic acid production. It was found that the consumption of ammonia at high carbon to nitrogen ratios of the feeds, which was necessary to achieve nitrogen limited conditions, caused acidification of the medium. This countered the increase of pH-value caused by acetic acid consumption and led to early acetate depletion. Thus, an additional DO-coupled feeding of sodium acetate was started once acetic acid in the medium was depleted. Sodium acetate did not directly effect the pH-value, but its consumption again led to an increase of the pH-value and continuation of the pH-coupled feeding. With this combined strategy an itaconic acid production process was developed with separate growth and production phases. In the end a titer of 29.2 g/L and a volumetric productivity of 0.63 g L−1h−1 were achieved. These were comparable to bacterial production processes using glucose as sole carbon source, with the only drawback being a lower yield. Still, the results demonstrated that C. glutamicum is suited as production organism on acetate as alternative carbon source. Another challenge is, that biobased acetic acid, for example produced by thermochemical conversion of lignocellulose, is often available only in dilute concentrations up to 50 g/L or in complex solutions containing potentially harmful substances. Therefore, conventional fed-batch processes are not applicable, because of strong dilution of the product and accumulation of inhibitors. Perfusion bioreactors can be a solution to these problems. They allow application of dilute substrate concentrations, as the bacteria are retained in the reactor. Furthermore, the continuous flow through the system prevents accumulation of inhibitors. Thus, the 2nd publication presented a newly developed, lab scale perfusion bioreactor, that was manufactured via 3D-printing using the fused filament fabrication method. Hydrophilic flat sheet membranes in the main bioreactor module were used for cell retention. A circulation flow was applied for diffusive oxygen supply via an oxygen transfer module that contained hydrophobic membranes and for temperature control via a heat exchanger module. The bioreactor system was characterized regarding oxygen transfer rates and mixing time. Finally, a proof-of-concept cultivation with C. glutamicum ATCC13032 on glucose utilizing a dilute feed solution resulted in 18.4 g/L biomass after 53 h of cultivation and a maximum specific growth rate of 0.34 1/h. Until the end of the process no membrane blockage occurred. This showed that the reactor system was suited for bacterial cultivation as well as for application of dilute substrates. To sum it up, it was shown that acetic acid can be efficiently used as alternative carbon source for bioproduction with C. glutamicum as model organism. Still, in case of itaconic acid production further genetic modifications are necessary in future works to increase the product yield. Regarding process strategies for utilization of biobased acetic acid in dilute solutions, a new 3D-printed perfusion bioreactor was successfully developed, and its function proven. Future works can focus on the application of the perfusion system for production processes and evaluate its suitability for bioprocesses with sustainably produced acetic acid