Abstract:Pseudomonas putida is recognized as a very promising strain for industrial application due to its high redox capacity and frequently observed tolerance towards organic solvents. In this research, we studied the metabolic and transcriptional response of P. putida KT2440 exposed to large-scale heterogeneous mixing conditions in the form of repeated glucose shortage. Cellular responses were mimicked in an experimental setup comprising a stirred tank reactor and a connected plug flow reactor. We deciphered that a … Show more
“…Pseudomonas putida has become a desirable target organism for the production of industrial products due to several attributes of its native physiology ( Ankenbauer et al., 2020 ). P. putida has a naturally diverse catabolism, with the capacity to metabolize aliphatic, aromatic and heterocyclic compounds in addition to glucose ( Schmid et al., 2001 ), lending to the potential to metabolize carbon from complex feedstocks for commercial chemical production.…”
The development of
Pseudomonas
strains for industrial production of fuels and chemicals will require the integration of heterologous genes and pathways into the chromosome. Finding the most appropriate integration site to maximize strain performance is an essential part of the strain design process. We characterized seven chromosomal loci in
Pseudomonas putida
KT2440 for integration of a fluorescent protein expression construct. Insertion in five of the loci did not affect growth rate, but fluorescence varied by up to 27-fold. Three sites displaying a diversity of phenotypes with the fluorescent reporter were also chosen for the integration of a gene encoding a muconate importer. Depending on the integration locus, expression of the importer varied by approximately 3-fold and produced significant phenotypic differences. This work demonstrates the impact of the integration location on host viability, gene expression, and overall strain performance.
“…Pseudomonas putida has become a desirable target organism for the production of industrial products due to several attributes of its native physiology ( Ankenbauer et al., 2020 ). P. putida has a naturally diverse catabolism, with the capacity to metabolize aliphatic, aromatic and heterocyclic compounds in addition to glucose ( Schmid et al., 2001 ), lending to the potential to metabolize carbon from complex feedstocks for commercial chemical production.…”
The development of
Pseudomonas
strains for industrial production of fuels and chemicals will require the integration of heterologous genes and pathways into the chromosome. Finding the most appropriate integration site to maximize strain performance is an essential part of the strain design process. We characterized seven chromosomal loci in
Pseudomonas putida
KT2440 for integration of a fluorescent protein expression construct. Insertion in five of the loci did not affect growth rate, but fluorescence varied by up to 27-fold. Three sites displaying a diversity of phenotypes with the fluorescent reporter were also chosen for the integration of a gene encoding a muconate importer. Depending on the integration locus, expression of the importer varied by approximately 3-fold and produced significant phenotypic differences. This work demonstrates the impact of the integration location on host viability, gene expression, and overall strain performance.
“…During HAA production with 1.25 kg, about twice the mass of foamed liquid was separated compared to RL production. As a generally higher foaming capability for RLs was determined previously [ 20 , 47 ], it is assumed that other components in the culture broth promote foam formation. Mainly cells, lysed cells, and secreted proteins are known to increase the foaming of a culture broth [ 34 , 73 ].…”
Section: Resultsmentioning
confidence: 94%
“…Such installations cannot avoid inhomogeneities in the reactor headspace and external pipelines. Here, again, P. putida stands out as a robust microbial cell factory, e.g., capable of enduring glucose limitations and temperature variations [ 47 , 48 ].…”
The production of biosurfactants is often hampered by excessive foaming in the bioreactor, impacting system scale-up and downstream processing. Foam fractionation was proposed to tackle this challenge by combining in situ product removal with a pre-purification step. In previous studies, foam fractionation was coupled to bioreactor operation, hence it was operated at suboptimal parameters. Here, we use an external fractionation column to decouple biosurfactant production from foam fractionation, enabling continuous surfactant separation, which is especially suited for system scale-up. As a subsequent product recovery step, continuous foam adsorption was integrated into the process. The configuration is evaluated for rhamnolipid (RL) or 3-(3-hydroxyalkanoyloxy)alkanoic acid (HAA, i.e., RL precursor) production by recombinant non-pathogenic Pseudomonas putida KT2440. Surfactant concentrations of 7.5 gRL/L and 2.0 gHAA/L were obtained in the fractionated foam. 4.7 g RLs and 2.8 g HAAs could be separated in the 2-stage recovery process within 36 h from a 2 L culture volume. With a culture volume scale-up to 9 L, 16 g RLs were adsorbed, and the space-time yield (STY) increased by 31% to 0.21 gRL/L·h. We demonstrate a well-performing process design for biosurfactant production and recovery as a contribution to a vital bioeconomy.
“…The basic technical setup has been characterized previously (Löffler et al, 2016;Simen et al, 2017). Minor modifications to the original setup have been made and are described elsewhere (Ankenbauer et al, 2020).…”
In large-scale fed-batch production processes, microbes are exposed to heterogeneous substrate availability caused by long mixing times. Escherichia coli, the most common industrial host for recombinant protein production, reacts by recurring accumulation of the alarmone ppGpp and energetically wasteful transcriptional strategies. Here, we compare the regulatory responses of the stringent response mutant strain E. coli SR and its parent strain E. coli MG1655 to repeated nutrient starvation in a two-compartment scale-down reactor. Our data show that E. coli SR can withstand these stress conditions without a ppGpp-mediated stress response maintaining fully functional ammonium uptake and biomass formation. Furthermore, E. coli SR exhibited a substantially reduced short-term transcriptional response compared to E. coli MG1655 (less than half as many differentially expressed genes). E. coli SR proceeded adaptation via more general SOS response pathways by initiating negative regulation of transcription, translation and cell division. Our results show that locally induced stress responses propagating through the bioreactor do not result in cyclical induction and repression of genes in E. coli SR, but in a reduced and coordinated response, which makes it potentially suitable for large-scale production processes.
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