Replacement of the glucose phosphotransferase transport system by galactose permease reduces acetate accumulation and improves process performance of Escherichia coli for recombinant protein production without impairment of growth rate

Acetate accumulation under aerobic conditions is a common problem in Escherichia coli cultures, as it causes a reduction in both growth rate and recombinant protein productivity. In this study, the effect of replacing the glucose phosphotransferase transport system (PTS) with an alternate glucose transport activity on growth kinetics, acetate accumulation and production of two model recombinant proteins, was determined. Strain VH32 is a W3110 derivative with an inactive PTS. The promoter region of the chromosomal galactose permease gene galP of VH32 was replaced by the strong trc promoter. The resulting strain, VH32GalP+ acquired the capacity to utilize glucose as a carbon source. Strains W3110 and VH32GalP+ were transformed for the production of recombinant TrpLE-proinsulin accumulated as inclusion bodies (W3110-PI and VH32GalP+-PI) and for production of soluble intracellular green fluorescent protein (W3110-pV21 and VH32GalP+-pV21). W3110-pV21 and VH32GalP+-pV21 were grown in batch cultures. Maximum recombinant protein concentration, as determined from fluorescence, was almost four-fold higher in VH32GalP+-pV21, relative to W3110-pV21. Maximum acetate concentration reached 2.8 g/L for W3110-pV21 cultures, whereas a maximum of 0.39 g/L accumulated in VH32GalP+-pV21. W3110-PI and VH32GalP+-PI were grown in batch and fed-batch cultures. Compared to W3110-PI, the engineered strain maintained similar production and growth rate capabilities while reducing acetate accumulation. Specific glucose consumption rate was lower and product yield on glucose was higher in VH32GalP+-PI fed-batch cultures. Altogether, strains with the engineered glucose uptake system showed improved process performance parameters for recombinant protein production over the wild-type strain.     

Utility of an Escherichia coli strain engineered in the substrate uptake system for improved culture performance at high glucose and cell concentrations: an alternative to fed-batch cultures

Overflow metabolism is an undesirable characteristic of aerobic cultures of Escherichia coli. It results from elevated glucose consumption rates that cause a high substrate conversion to acetate, severely affecting cell physiology and bioprocess performance. Such phenomenon typically occurs in batch cultures under high glucose concentration. Fed-batch culture, where glucose uptake rate is controlled by external addition of glucose, is the classical bioprocessing alternative to prevent overflow metabolism. Despite its wide-spread use, fed-batch mode presents drawbacks that could be overcome by simpler batch cultures at high initial glucose concentration, only if overflow metabolism is effectively prevented. In this study, an E. coli strain (VH32) lacking the phosphoenolpyruvate: carbohydrate phosphotransferase system (PTS) with a modified glucose transport system was cultured at glucose concentrations of up to 100 g/L in batch mode, while expressing the recombinant green fluorescence protein (GFP). At the highest glucose concentration tested, acetate accumulated to a maximum of 13.6 g/L for the parental strain (W3110), whereas a maximum concentration of only 2 g/L was observed for VH32. Consequently, high cell and GFP concentrations of 52 and 8.2 g/L, respectively, were achieved in VH32 cultures at 100 g/L of glucose. In contrast, maximum biomass and GFP in W3110 cultures only reached 65 and 48%, respectively, of the values attained by the engineered strain. A comparison of this culture strategy against traditional fed-batch culture of W3110 is presented. This study shows that high cell and recombinant protein concentrations are attainable in simple batch cultures by circumventing overflow metabolism through metabolic engineering. This represents a novel and valuable alternative to classical bioprocessing approaches.     

Consequences of phosphoenolpyruvate:sugar phosphotranferase system and pyruvate kinase isozymes inactivation in central carbon metabolism flux distribution in Escherichia coli

ABSTRACT: BACKGROUND: In Escherichia coli phosphoenolpyruvate (PEP) is a key central metabolism intermediate that participates in glucose transport, as precursor in several biosynthetic pathways and it is involved in allosteric regulation of glycolytic enzymes. In this work we generated W3110 derivative strains that lack the main PEP consumers PEP:sugar phosphotransferase system (PTS-) and pyruvate kinase isozymes PykA and PykF (PTS- pykA- and PTS- pykF -). To characterize the effects of these modifications on cell physiology, carbon flux distribution and aromatics production capacity were determined. RESULTS: When compared to reference strain W3110, strain VH33 (PTS-) displayed lower specific rates for growth, glucose consumption and acetate production as well as a higher biomass yield from glucose. These phenotypic effects were even more pronounced by the additional inactivation of PykA or PykF. Carbon flux analysis revealed that PTS inactivation causes a redirection of metabolic flux towards biomass formation. A cycle involving PEP carboxylase (Ppc) and PEP carboxykinase (Pck) was detected in all strains. In strains W3110, VH33 (PTS-) and VH35 (PTS-, pykF-), the net flux in this cycle was inversely correlated with the specific rate of glucose consumption and inactivation of Pck in these strains caused a reduction in growth rate. In the PTS- background, inactivation of PykA caused a reduction in Ppc and Pck cycling as well as a reduction in flux to TCA, whereas inactivation of PykF caused an increase in anaplerotic flux from PEP to OAA and an increased flux to TCA. The wild-type and mutant strains were modified to overproduce L-phenylalanine. In resting cells experiments, compared to reference strain, a 10, 4 and 7-fold higher aromatics yields from glucose were observed as consequence of PTS, PTS PykA and PTS PykF inactivation. CONCLUSIONS: Metabolic flux analysis performed on strains lacking the main activities generating pyruvate from PEP revealed the high degree of flexibility to perturbations of the central metabolic network in E. coli. The observed responses to reduced glucose uptake and PEP to pyruvate rate of conversion caused by PTS, PykA and PykF inactivation included flux rerouting in several central metabolism nodes towards anabolic biosynthetic reactions, thus compensating for carbon limitation in these mutant strains. The detected cycle involving Ppc and Pck was found to be required for maintaining the specific growth and glucose consumption rates in all studied strains. Strains VH33 (PTS-), VH34 (PTS- pykA-) and VH35 (PTS- pykF-) have useful properties for biotechnological processes, such as increased PEP availability and high biomass yields from glucose, making them useful for the production of aromatic compounds or recombinant proteins.     

Engineering E. coli for improved microaerobic pDNA production

Escherichia coli strains W3110 and BL21 were engineered for the production of plasmid DNA (pDNA) under aerobic and transitions to microaerobic conditions. The gene coding for recombinase A (recA) was deleted in both strains. In addition, the Vitreoscilla hemoglobin (VHb) gene (vgb) was chromosomally inserted and constitutively expressed in each E. coli recA mutant and wild type. The recA inactivation increased the supercoiled pDNA fraction (SCF) in both strains, while VHb expression improved the pDNA production in W3110, but not in BL21. Therefore, a codon-optimized version of vgb was inserted in strain BL21recA⁻, which, together with W3110recA⁻vgb⁺, was tested in cultures with shifts from aerobic to oxygen-limited regimes. VHb expression lowered the accumulation of fermentative by-products in both strains. VHb-expressing cells displayed higher oxidative activity as indicated by the Redox Sensor Green fluorescence, which was more intense in BL21 than in W3110. Furthermore, VHb expression did not change pDNA production in W3110, but decreased it in BL21. These results are useful for understanding the physiological effects of VHb expression in two industrially relevant E. coli strains, and for the selection of a host for pDNA production.

     

Expression of galP and glk in a Escherichia coli PTS mutant restores glucose transport and increases glycolytic flux to fermentation products

In Escherichia coli, the uptake and phosphorylation of glucose is carried out mainly by the phosphotransferase system (PTS). Despite the efficiency of glucose transport by PTS, the required consumption of 1 mol of phosphoenolpyruvate (PEP) for each mol of internalized glucose represents a drawback for some biotechnological applications where PEP is a precursor of the desired product. For this reason, there is considerable interest in the generation of strains that can transport glucose efficiently by a non-PTS mechanism. The purpose of this work was to study the effect of different gene expression levels, of galactose permease (GalP) and glucokinase (Glk), on glucose internalization and phosphorylation in a E. coli PTS(-) strain. The W3110 PTS(-), designated VH32, showed limited growth on glucose with a specific growth rate (mu) of 0.03 h(-1). A low copy plasmid family was constructed containing E. coli galP and glk genes, individually or combined, under the control of a trc-derived promoter set. This plasmid family was used to transform the VH32 strain, each plasmid having different levels of expression of galP and glk. Experiments in minimal medium with glucose showed that expression of only galP under the control of a wild-type trc promoter resulted in a mu of 0.55 h(-1), corresponding to 89% of the mu measured for W3110 (0.62 h(-1)). In contrast, no increase in specific growth rate (mu) was observed in VH32 with a plasmid expressing only glk from the same promoter. Strains transformed with part of the plasmid family, containing both galP and glk genes, showed a mu value similar to that of W3110. Fermentor experiments with the VH32 strain harboring plasmids pv1Glk1GalP, pv4Glk5GalP, and pv5Glk5GalP showed that specific acetate productivity was twofold higher than in W3110. Introduction of plasmid pLOI1594, coding for pyruvate decarboxylase and alcohol dehydrogenase from Zymomonas mobilis, to strain VH32 carrying one of the plasmids with galP and glk caused a twofold increase in ethanol productivity over strain W3110, also containing pLOI1594.     

Effective 5-aminolevulinic acid production via T7 RNA polymerase and RuBisCO equipped Escherichia coli W3110

Chromosome-based engineering is a superior approach for gene integration generating a stable and robust chassis. Therefore, an effective amplifier, T7 RNA polymerase (T7RNAP) from bacteriophage, has been incorporated into Escherichia coli W3110 by site-specific integration. Herein, we performed the 5-aminolevulinic acid (5-ALA) production in four T7RNAP-equipped W3110 strains using recombinant 5-aminolevulinic synthase and further explored the metabolic difference in best strain. The fastest glucose consumption resulted in the highest biomass and the 5-ALA production reached to 5.5 g/L; thus, the least by-product of acetate was shown in RH strain in which T7RNAP was inserted at HK022 phage attack site. Overexpression of phosphoenolpyruvate (PEP) carboxylase would pull PEP to oxaloacetic acid in tricarboxylic acid cycle, leading to energy conservation and even no acetate production, thus, 6.53 g/L of 5-ALA was achieved. Amino acid utilization in RH deciphered the major metabolic flux in α-ketoglutaric acid dominating 5-ALA production. Finally, the ribulose-1,5-bisphosphate carboxylase/oxygenase (RuBisCO) and phosphoribulokinase were expressed for carbon dioxide recycling; a robust and efficient chassis toward low-carbon assimilation and high-level of 5-ALA production up to 11.2 g/L in fed-batch fermentation was established.     

Vitreoscilla hemoglobin expression in engineered Escherichia coli: improved performance in high cell-density batch cultivations

High cell-density cultivations are the preferred system for biomolecules production by Escherichia coli. It has been previously demonstrated that a strain of E. coli with a modified substrate transport system is able to attain high cell densities in batch mode, due to the very low overflow metabolism displayed. The use of elevated amounts of glucose from the beginning of the cultivation, eliminates the existence of substrate gradients due to deficient mixing at large-scale. However, the large amounts of oxygen demanded resulted in microaerobic conditions after some hours of cultivation, even at small-scale. In this work, the effect of expressing the Vitreoscilla hemoglobin (VHb) in the engineered strain during batch cultures using high-glucose concentrations was tested. Together, the expression of VHb and the modified substrate transport system resulted in a 33% increase of biomass production compared to the parental strain (W3110) lacking the VHb in batch cultivations using 25 g/L of glucose. When 50 g/L of glucose were used, expression of VHb in the modified strain led to 11% higher biomass production compared to W3110. The VHb also increased the growth rates of the strains by about 30% in the aerobic phase and more than 200% in the microaerobic phase of batch cultivation.     

Production of 3-hydroxypropionic acid from glycerol by acid tolerant Escherichia coli

The biological production of 3-hydroxypropionic acid (3-HP) has attracted significant attention because of its industrial importance. The low titer, yield and productivity, all of which are related directly or indirectly to the toxicity of 3-HP, have limited the commercial production of 3-HP. The aim of this study was to identify and select a 3-HP tolerant Escherichia coli strain among nine strains reported to produce various organic acids efficiently at high titer. When transformed with heterologous glycerol dehydratase, reactivase and aldehyde dehydrogenase, all nine E. coli strains produced 3-HP from glycerol but the level of 3-HP production, protein expression and activities of the important enzymes differed significantly according to the strain. Two E. coli strains, W3110 and W, showed higher levels of growth than the others in the presence of 25 g/L 3-HP. In the glycerol fed-batch bioreactor experiments, the recombinant E. coli W produced a high level of 3-HP at 460 ± 10 mM (41.5 ± 1.1 g/L) in 48 h with a yield of 31 % and a productivity of 0.86 ± 0.05 g/L h. In contrast, the recombinant E. coli W3110 produced only 180 ± 8.5 mM 3-HP (15.3 ± 0.8 g/L) in 48 h with a yield and productivity of 26 % and 0.36 ± 0.02 g/L h, respectively. This shows that the tolerance to and the production of 3-HP differ significantly among the well-known, similar strains of E. coli. The titer and productivity obtained with E. coli W were the highest reported thus far for the biological production of 3-HP from glycerol by E. coli.     

Comparison of growth, acetate production, and acetate inhibition of Escherichia coli strains in batch and fed-batch fermentations.

The growth characteristics and acetate production of several Escherichia coli strains were compared by using shake flasks, batch fermentations, and glucose-feedback-controlled fed-batch fermentations to assess the potential of each strain to grow at high cell densities. Of the E. coli strains tested, including JM105, B, W3110, W3100, HB101, DH1, CSH50, MC1060, JRG1046, and JRG1061, strains JM105 and B were found to have the greatest relative biomass accumulation, strain MC1060 accumulated the highest concentrations of acetic acid, and strain B had the highest growth rates under the conditions tested. In glucose-feedback-controlled fed-batch fermentations, strains B and JM105 produced only 2 g of acetate.liter-1 while accumulating up to 30 g of biomass.liter-1. Under identical conditions, strains HB101 and MC1060 accumulated less than 10 g of biomass.liter-1 and strain MC1060 produced 8 g of acetate.liter-1. The addition of various concentrations of sodium acetate to the growth medium resulted in a logarithmic decrease, with respect to acetate concentration, in the growth rates of E. coli JM105, JM105(pOS4201), and JRG1061. These data indicated that the growth of the E. coli strains was likely to be inhibited by the acetate they produced when grown on media containing glucose. A model for the inhibition of growth of E. coli by acetate was derived from these experiments to explain the inhibition of acetate on E. coli strains at neutral pH.     

Comparison of growth, acetate production, and acetate inhibition of Escherichia coli strains in batch and fed-batch fermentations

The growth characteristics and acetate production of several Escherichia coli strains were compared by using shake flasks, batch fermentations, and glucose-feedback-controlled fed-batch fermentations to assess the potential of each strain to grow at high cell densities. Of the E. coli strains tested, including JM105, B, W3110, W3100, HB101, DH1, CSH50, MC1060, JRG1046, and JRG1061, strains JM105 and B were found to have the greatest relative biomass accumulation, strain MC1060 accumulated the highest concentrations of acetic acid, and strain B had the highest growth rates under the conditions tested. In glucose-feedback-controlled fed-batch fermentations, strains B and JM105 produced only 2 g of acetate.liter-1 while accumulating up to 30 g of biomass.liter-1. Under identical conditions, strains HB101 and MC1060 accumulated less than 10 g of biomass.liter-1 and strain MC1060 produced 8 g of acetate.liter-1. The addition of various concentrations of sodium acetate to the growth medium resulted in a logarithmic decrease, with respect to acetate concentration, in the growth rates of E. coli JM105, JM105(pOS4201), and JRG1061. These data indicated that the growth of the E. coli strains was likely to be inhibited by the acetate they produced when grown on media containing glucose. A model for the inhibition of growth of E. coli by acetate was derived from these experiments to explain the inhibition of acetate on E. coli strains at neutral pH.     

Shikimic acid production by a modified strain of E. coli (W3110.shik1) under phosphate-limited and carbon-limited conditions

Shikimic acid is one of several industrially interesting chiral starting materials formed in the aromatic amino acid pathway of plants and microorganisms. In this study, the physiology of a shikimic acid producing strain of Escherichia coli (derived from W3110) deleted in aroL (shikimic acid kinase II gene), was compared to that of a corresponding control strain (W3110) under carbon- and phosphate-limited conditions. For the shikimic acid producing strain (referred to as W3110.shik1), phosphate limitation resulted in a higher yield of shikimic acid (0.059 +/- 0.012 vs. 0.024 +/- 0.005 c-mol/c-mol) and a lower yield of by-products from the shikimate pathway, when compared to carbon-limited condition. The yield of the by-product 3-dehydroshikimic acid (DHS) decreased from 0.076 +/- 0.028 to 0.022 +/- 0.001 c-mol/c-mol. Several other by-products were only detected under carbon-limited conditions. The latter group included 3-dehydroquinic acid (0.021 +/- 0.021 c-mol/c-mol), quinic acid (0.012 +/- 0.005 c-mol/c-mol), and gallic acid (0.002 +/- 0.001 c-mol/c-mol). For both strains, more acetate was produced under phosphate than the carbon-limited case. Considerable cell lysis was found for both strains but was higher for W3110.shik1, and increased for both strains under phosphate limitation. The advantages of the latter condition in terms of an increased shikimic acid yield was thus counteracted by an increased cell lysis, which may make downstream processing more difficult.     

Comparison of the extracellular proteomes of Escherichia coli B and K-12 strains during high cell density cultivation

Escherichia coli BL21 (DE3) and W3110 strains, belonging to the family B and K-12, respectively, have been most widely employed for recombinant protein production. During the excretory production of recombinant proteins by high cell density cultivation (HCDC) of these strains, other native E. coli proteins were also released. Thus, we analyzed the extracellular proteomes of E. coli BL21 (DE3) and W3110 during HCDC. E. coli BL21 (DE3) released more than twice the amount of protein compared with W3110 during HCDC. A total of 204 protein spots including 83 nonredundant proteins were unambiguously identified by 2-DE and MS. Of these, 32 proteins were conserved in the two strains, while 20 and 33 strain-specific proteins were identified for E. coli BL21 (DE3) and W3110, respectively. More than 70% of identified proteins were found to be of periplasmic origin. The outer membrane proteins, OmpA and OmpF, were most abundant. Two strains showed much different patterns in their released proteins. Also, cell density-dependent variations in the released proteins were observed in both strains. These findings summarized as reference proteome maps will be useful for studying protein release in further detail, and provide new strategies for enhanced excretory production of recombinant proteins.     

High expression of the second lysine decarboxylase gene, ldc, in Escherichia coli WC196 due to the recognition of the stop codon (TAG), at a position which corresponds to the 33th amino acid residue of sigma38, as a serine residue by the amber suppressor, supD

Escherichia coli WC196, which was obtained from the strain W3110 by nitrosoguanidine mutagenesis as an overproducer of lysine, produced approximately twenty times more cadaverine than did W3110, and had a twenty fold higher level of rpoS gene product, sigma38, than in W3110. Both WC196 and W3110 had a stop codon (TAG) in rpoS at position which corresponds to the 33th residue of sigma38 protein. In addition, WC196 but not W3110 had a mutation in the gene encoding Ser-tRNA (SerU), called, supD. Analysis of the amino acid sequence of a sigma38 preparation from WC196 showed that the 33th residue of sigma38 is a serine residue. The deltarpoS deltacadA mutant of E. coli W3110 harboring the plasmid containing rpoS, in which the TAG codon was converted to a TCG codon for serine-33 residue of sigma38, expressed a significant amount of Ldc and accumulated a large amount of sigma38. However, the deltarpoS deltacadA mutant of W3110 with the plasmid containing the intact rpoS from W3110 could synthesize neither sigma38 nor Ldc significantly.     

Enhanced plasmid DNA production by enzyme-controlled glucose release and an engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

Objectives

To evaluate the combination of a culture medium employing glucoamylase-mediated glucose reléase from a gluco-polysaccharide and an E. coli strain engineered in its glucose transport system for improving plasmid DNA (pDNA) production.

Results

The production of pDNA was tested using E. coli DH5α grown in shake-flasks and the recently developed VH33 Δ(recA deoR)-engineered strain, which utilizes glucose more efficiently than wild type strains. Three glucoamylase concentrations for releasing glucose from the polysaccharide carbon source were used: 1, 2 and 3 U l^?1. Both strains reached similar cell densities ranging from 5 to 8.8 g l^?1 under the different conditions. The highest pDNA yields on biomass (Y_pDNA/X) for both strains were obtained when 3 U enzyme l^?1were used. Under these conditions, 35 ± 3 mgof pDNA l^?1 were produced by DH5α after 24 h of culture. Under the same conditions, the engineered strain produced 66 ± 1 mgpDNAl^?1 after 20 h. pDNA supercoiled fractionswere close to 80 % for both strains.

Conclusions

The pDNA concentration achieved by the engineered E. coli was 89 % higher than that of DH5α. The combination of the engineered strain and enzyme-controlled glucose release is an attractive alternative for pDNA production in shake-flasks.

     

含苏氨酸操纵子重组质粒的构建及其对大肠杆菌L-苏氨酸积累的影响

摘要：【目的】通过分子生物学手段构建重组质粒,将其转入野生型大肠杆菌W3110,分析含苏氨酸操纵子基因的质粒及质粒定点突变解除反馈抑制时,对L-苏氨酸积累的影响。【方法】以W3110染色体DNA为模板,PCR扩增苏氨酸操纵子基因,即启动子THrLp、编码前导肽基因thrL以及thrA、thrB、thrC基因,通过重叠延伸PCR的方法对thrA基因定点突变,解除苏氨酸对它的反馈抑制,构建出重组表达质粒WYE112和WYE134,5 L发酵实验测定L-苏氨酸的产量。【结果】经5 L发酵罐发酵产酸实验,W3110的L-苏氨酸产量为0.036 ± 0.004 g/L,携带含苏氨酸操纵子质粒的W3110菌株L-苏氨酸产量为2.590 ± 0.115 g/L,质粒上thrA解除反馈抑制后,L-苏氨酸的产量增加到9.223 ± 1.279 g/L。【结论】过表达苏氨酸操纵子基因可以使L-苏氨酸积累,进一步解除thrA基因的反馈抑制,可以增强L-苏氨酸积累的效果,为L-苏氨酸工程菌改造的进一步研究奠定了基础。     

Engineering Escherichia coli to improve culture performance and reduce formation of by-products during recombinant protein production under transient intermittent anaerobic conditions

Three E. coli strains, named VAL22, VAL23, and VAL24, were engineered at the level of mixed-acid fermentation pathways to improve culture performance under transient anaerobic conditions. VAL22 is a single mutant with an inactivated poxB gene that codes for pyruvate oxidase which converts pyruvate to acetate. VAL23 is a double mutant unable to produce lactate and formate due to deletions of the ldhA and pflB genes that code for lactate dehydrogenase and pyruvate-formate lyase, respectively. VAL24 is a triple mutant with ldhA and pflB deleted and poxB inactivated. Engineered strains were cultured under oscillating dissolved oxygen tension (DOT) in a scale-down system, to simulate gradients occurring in large-scale bioreactors. Kinetic and stoichiometric parameters of constant (10%) and oscillating DOT cultures of the engineered strains were compared with those of the parental strain, W3110. All strains expressed recombinant green fluorescent protein (GFP) as a protein model. Mutant strains showed improved specific growth rate, reduced by-product formation, and reduced specific glucose uptake rate compared to the parental strain, when cultured under oscillating DOT. In particular, lactate and formate production was abolished and acetate accumulation was reduced by 9-12%s. VAL24 showed the best performance, as specific growth and GFP production rates, and maximum GFP concentration were not affected by DOT gradients and were at least twofold higher than those of W3110 under constant DOT. Under oscillating DOT, VAL24 wasted about 40% less carbon into fermentation by-products than W3110. It was demonstrated that, although E. coli responds rapidly to DOT fluctuations by deviating to fermentative metabolism, such pathways can be eliminated as they are not necessary for bacterial survival during the short circulation times typical of large-scale cultures. The approach shown here opens new possibilities for designing metabolically engineered strains, with reduced sensitivity to DOT gradients and improved performance under typical conditions of large-scale cultures.     

A rapid screening procedure to identify mini-Tn10 insertion mutants of Escherichia coli K-12 with altered adhesion properties

Abstract A rapid screening procedure was developed for detection of Escherichia coli mutants with altered adhesion abilities using polystyrene 96-well microtiter plates as attachment surfaces. During this assay, bacterial strains grew and adhered simultaneously, and attached cells were measured after crystal violet staining. Starting with a total of 7000 W3110::Tn10 insertion mutants of E. coli K-12 W3110, 50 adhesion-deficient mutants were isolated which showed less than 40% attachment, and 22 mutants were found with an attachment of 40–75%. Motility assays were performed on these 72 mutants, and 34 displayed altered motility.     

Two-Level factorial screening of new plasmid/strain combinations for prodution of recombinant-DNA products

This article treats the basic problem of selection of experimental conditions for microbiological experiments for evaluation of newly isolated bacterial strains, mutants, or plasmid/strain combinations. For this purpose shake flask experiments in a 2(10-4)confounded factorial design at resolution IV with four blocks of 16 flasks were used. The design was used for testing of two new strain/plasmid combinations (E. coli MT 102/403-SD2 and W 3110/403-SD2) i.e., both strains with the same plasmid 403-SD2. Both strains were integrated in the design, so both strains were tested with nine factors (temperature, aeration, glucose, initial pH, pH regulation, reduced aeration, chloramphenicol, acetate, and glycerol). With both strains the interaction between initial pH and reduced aeration had a significant influence on the yield of the recombinant-DNA product nuclease. There was more than a factor of 10 between lowest and highest yield of product. In this interactive system the strains reacted differently. MT 102/403-SD2 had highest yields at high initial pH (8.4) and no reduction in aeration, whereas W 3110/403-SD2 had highest yields of nuclease at low initial pH (7.4) and reduced aeration (rubber stopper inserted after cultivation for 12 h). These data (and previous work) clearly demonstrate that it is impossible to suggest a simple set of experimental conditions for testing of new plasmid/strain combinations. It is clear that the exclusive application of a standardized growth technique e.g., LB-medium at 37 degrees C at an unspecified and uncontrolled aeration level, may lead to wrong conclusions on properties and potentials of now plasmid/strain combinations and may lead to rejection of useful strains or plasmids.     

Lipid production by yeasts grown on crude glycerol from biodiesel industry

The main carbon source used for growth by four yeast strains (Yarrowia lipolytica CCMA 0357, Y. lipolytica CCMA 0242, Wickerhamomyces anomalus CCMA 0358, and Cryptococcus humicola CCMA 0346) and their lipid production were evaluated, using different concentrations of crude and pure glycerol and glucose. Whereas crude glycerol (100?g/L) was the main carbon source used by Y. lipolytica CCMA 0357 (nearly 15?g/L consumed at 120?hr) and W. anomalus CCMA 0358 (nearly 45.10?g/L consumed at 48?hr), pure glycerol (150?g/L) was the main one used by C. humicola CCMA 0346 (nearly 130?g/L consumed). On the other hand, Y. lipolytica CCMA 0242 used glucose (100?g/L) as its main source of carbon (nearly 96.48?g/L consumed). Y. lipolytica CCMA 0357 demonstrated the highest lipid production [about 70% (wt/wt)], forming palmitic (45.73% of fatty acid composition), stearic (16.43%), palmitoleic (13.29%), linolenic (10.77%), heptadecanoic (4.07%), and linoleic (14.14%) acids. Linoleic acid, an essential fatty acid, was produced by all four yeast strains but in varying degrees, representing 70.42% of the fatty acid profile of lipids produced by C. humicola CCMA 0346.