Production of poly(3-hydroxybutyric acid) by recombinantEscherichia colistrains: genetic and fermentation studies

1995 ◽  
Vol 41 (13) ◽  
pp. 207-215 ◽  
Author(s):  
Sang Yup Lee ◽  
Ho Nam Chang
Keyword(s):  
Escherichia Coli ◽  
Nitrogen Sources ◽  
Defined Medium ◽  
Hydroxybutyric Acid ◽  
Fed Batch ◽  
E Coli ◽  
Polyhydroxyalkanoic Acid ◽  
High Copy Number Plasmid ◽  
Ph Stat ◽  
The Cost

A number of Escherichia coli strains including K12, B, W, XL1-Blue, DH5α, HB101, JM109, and C600 were transformed with the stable high-copy-number plasmid pSYL105 containing the Alcaligenes eutrophus polyhydroxyalkanoic acid biosynthesis genes, and were subsequently compared for their ability to synthesize and accumulate poly(3-hydroxybutyric acid) (PHB). The rate of PHB synthesis, the extent of PHB accumulation, and PHB yield from glucose varied considerably from one strain to another. Strains XL1-Blue and B harboring pSYL105 synthesized PHB at the highest rate to a final concentration of ca. 7 g/L in complex medium containing 20 g glucose/L. With an aim to reduce the cost of the medium, the effect on PHB accumulation of supplementing a defined medium with complex nitrogen sources was examined. A PHB concentration of 81 g/L could be obtained in 41 h from a pH-stat fed-batch culture of XL1-Blue(pSYL105) in a semidefined medium. When the availability of acetyl-CoA was increased by supplementing the medium with complex nitrogen sources, amino acids, or oleic acid, PHB synthesis by recombinant E. coli was enhanced.Key words: polyhydroxyalkanoic acid, poly(3-hydroxybutyric acid), fed batch, Escherichia coli.

scholarly journals Production of Poly(3-Hydroxybutyrate) by Fed-Batch Culture of Recombinant Escherichia coliwith a Highly Concentrated Whey Solution

2000 ◽  
Vol 66 (8) ◽  
pp. 3624-3627 ◽  
Author(s):  
Woo Suk Ahn ◽  
Si Jae Park ◽  
Sang Yup Lee
Keyword(s):  
Escherichia Coli ◽  
Batch Culture ◽  
Fed Batch ◽  
Batch Cultures ◽  
E Coli ◽  
Alcaligenes Latus ◽  
Stable Plasmid ◽  
Ph Stat ◽  
Fed Batch Culture

ABSTRACT Fermentation strategies for the production of poly(3-hydroxybutyrate) (PHB) from whey by recombinantEscherichia coli strain CGSC 4401 harboring theAlcaligenes latus polyhydroxyalkanoate (PHA) biosynthesis genes were developed. The pH-stat fed-batch cultures of E. coli CGSC 4401 harboring pJC4, a stable plasmid containing theA. latus PHA biosynthesis genes, were carried out with a concentrated whey solution containing 280 g of lactose equivalent per liter. Final cell and PHB concentrations of 119.5 and 96.2 g/liter, respectively, were obtained in 37.5 h, which resulted in PHB productivity of 2.57 g/liter/h.

scholarly journals Metabolic engineering of Escherichia coli W for isobutanol production on chemically defined medium and cheese whey as alternative raw material

2020 ◽  
Vol 47 (12) ◽  
pp. 1117-1132
Author(s):  
Katharina Novak ◽  
Juliane Baar ◽  
Philipp Freitag ◽  
Stefan Pflügl
Keyword(s):  
Escherichia Coli ◽  
Cheese Whey ◽  
Strain Improvement ◽  
Defined Medium ◽  
Raw Material ◽  
Efficient Production ◽  
Substrate Uptake ◽  
Chemically Defined Medium ◽  
E Coli ◽  
Plasmid Library

AbstractThe aim of this study was to establish isobutanol production on chemically defined medium in Escherichia coli. By individually expressing each gene of the pathway, we constructed a plasmid library for isobutanol production. Strain screening on chemically defined medium showed successful production in the robust E. coli W strain, and expression vector IB 4 was selected as the most promising construct due to its high isobutanol yields and efficient substrate uptake. The investigation of different aeration strategies in combination with strain improvement and the implementation of a pulsed fed-batch were key for the development of an efficient production process. E. coli W ΔldhA ΔadhE Δpta ΔfrdA enabled aerobic isobutanol production at 38% of the theoretical maximum. Use of cheese whey as raw material resulted in longer process stability, which allowed production of 20 g l−1 isobutanol. Demonstrating isobutanol production on both chemically defined medium and a residual waste stream, this study provides valuable information for further development of industrially relevant isobutanol production processes.

scholarly journals Alleviation of C⋅C Mismatches in DNA by the Escherichia coli Fpg Protein

2021 ◽  
Vol 12 ◽  
Author(s):  
Almaz Nigatu Tesfahun ◽  
Marina Alexeeva ◽  
Miglė Tomkuvienė ◽  
Aysha Arshad ◽  
Prashanna Guragain ◽  
...  
Keyword(s):  
Escherichia Coli ◽  
Excision Repair ◽  
Dna Lesions ◽  
Base Pairs ◽  
E Coli ◽  
Thymine Glycol ◽  
Base Excision ◽  
The Cost ◽  
Primary Substrate

DNA polymerase III mis-insertion may, where not corrected by its 3′→ 5′ exonuclease or the mismatch repair (MMR) function, result in all possible non-cognate base pairs in DNA generating base substitutions. The most thermodynamically unstable base pair, the cytosine (C)⋅C mismatch, destabilizes adjacent base pairs, is resistant to correction by MMR in Escherichia coli, and its repair mechanism remains elusive. We present here in vitro evidence that C⋅C mismatch can be processed by base excision repair initiated by the E. coli formamidopyrimidine-DNA glycosylase (Fpg) protein. The kcat for C⋅C is, however, 2.5 to 10 times lower than for its primary substrate 8-oxoguanine (oxo8G)⋅C, but approaches those for 5,6-dihydrothymine (dHT)⋅C and thymine glycol (Tg)⋅C. The KM values are all in the same range, which indicates efficient recognition of C⋅C mismatches in DNA. Fpg activity was also exhibited for the thymine (T)⋅T mismatch and for N4- and/or 5-methylated C opposite C or T, Fpg activity being enabled on a broad spectrum of DNA lesions and mismatches by the flexibility of the active site loop. We hypothesize that Fpg plays a role in resolving C⋅C in particular, but also other pyrimidine⋅pyrimidine mismatches, which increases survival at the cost of some mutagenesis.

Co-Expression of Threonine Dehydratase and Acetolactate Synthase in Escherichia Coli for L-Isoleucine Production

2014 ◽  
Vol 989-994 ◽  
pp. 997-1002 ◽  
Author(s):  
Jian Wang ◽  
Jia Kai Sun ◽  
Qing Yang Xu
Keyword(s):  
Escherichia Coli ◽  
Corynebacterium Glutamicum ◽  
Carbon Flux ◽  
Batch Fermentation ◽  
Acetolactate Synthase ◽  
Fed Batch ◽  
Threonine Dehydratase ◽  
E Coli ◽  
Fed Batch Fermentation ◽  
Fermentation Period

Metabolic engineering ofCorynebacterium glutamicumhas sought to divert carbon into L-isoleucine. However, the fermentation period of this strain is long. TheC.glutamicumYILW strain (LeuL, AHVr, SGr, Leu-MEr) was previously derived by repeated compound mutagenesis which could accumulate 20.2 g/L L-isoleucine in a 5-L jar fermentor. Overexpression of the threonine dehydratase gene (ilvA) fromCorynebacterium glutamicumYILW and coexpression of threonine dehydratase and acetolactate synthase (ilvBN) from it were employed to divert carbon flux toward L-isoleucine. The strainE. coliTRFC with the expression ofilvA could accumulate L-isoleucine of 6.8 g/L without accumulation of any L-threonine by fed-batch fermentation in a 5-L jar fermentor. However, the production of L-isoleucine by the strainE.coliTRFC with the co-expression ofilvA andilvBN was decreased by 19.1%, and the production of L-valine was increased by 40% compared with that ofE. coliTRFC with the expression ofilvA.

Utilization of chymotrypsin as a sole carbon and (or) nitrogen source by Escherichia coli

1992 ◽  
Vol 38 (4) ◽  
pp. 290-295 ◽  
Author(s):  
Arthur S. Brecher ◽  
Timothy A. Moehlman ◽  
William D. Hann
Keyword(s):  
Escherichia Coli ◽  
Carbon Source ◽  
Nitrogen Source ◽  
Degradation Products ◽  
Defined Medium ◽  
Host Protein ◽  
Mammalian Host ◽  
Sole Nitrogen Source ◽  
E Coli ◽  
Nitrogen Nutrients

α-Chymotrypsin serves as a sole carbon source, sole nitrogen source, and as sole carbon plus nitrogen source for wild-type Escherichia coli in a totally defined medium. Hence, a mammalian host for E. coli may supply the necessary carbon and nitrogen nutrients for the microorganism. Growth is most rapid when chymotrypsin is a sole nitrogen source,and least rapid with chymotrypsin as a carbon source. The approximate doubling times for E. coli utilizing chymotrypsin as a nitrogen source, carbon plus nitrogen source, and carbon source are 1.6, 4.6, and 11.3 h, respectively. The activity of the residual enzyme in the culture supernates falls off asymptotically over the course of time, as followed by cleavage of glutaryl-L-phenylalanine-p-nitroanilide. Chymotrypsin hydrolyzes succinyl-L-ala-L-ala-L-ala-p-nitroanilide, the elastase substrate, to some extent. Peptidases do not appear to be secreted that hydrolyze such model substrates as benzoyl-DL-arginine-p-nitroanilide, the tryptic and cathepsin B substrate, L-leucine-p-nitroanilide, the leucine aminopeptidase substrate, or L-lysine-p-nitroanilide, the aminopeptidase B substrate. Growth of E. coli is generally directly related to the loss of chymotryptic activity in the medium. Hence, autolysis of chymotrypsin, i.e., self-degradation, is an important factor for the availability of degradation products of the enzyme to the bacterium for growth purposes. Accordingly, the degradation of a host protein by autolysis presents an opportunity for E. coli to survive during periods of host nutritional crisis by utilization of the degradation peptides that are produced during autolysis. Key words: chymotrypsin, Escherichia coli, growth, nutrition, peptide source.

scholarly journals Roles of Glutamate Synthase, gltBD, and gltF in Nitrogen Metabolism of Escherichia coli and Klebsiella aerogenes

2001 ◽  
Vol 183 (22) ◽  
pp. 6607-6619 ◽  
Author(s):  
Thomas J. Goss ◽  
Ana Perez-Matos ◽  
Robert A. Bender
Keyword(s):  
Escherichia Coli ◽  
Nitrogen Metabolism ◽  
Glutamate Synthase ◽  
Nitrogen Sources ◽  
Enteric Bacteria ◽  
The Other ◽  
Klebsiella Aerogenes ◽  
E Coli ◽  
Glutamine Synthesis ◽  
Subsequent Failure

ABSTRACT Mutants of Escherichia coli and Klebsiella aerogenes that are deficient in glutamate synthase (glutamate-oxoglutarate amidotransferase [GOGAT]) activity have difficulty growing with nitrogen sources other than ammonia. Two models have been proposed to account for this inability to grow. One model postulated an imbalance between glutamine synthesis and glutamine degradation that led to a repression of the Ntr system and the subsequent failure to activate transcription of genes required for the use of alternative nitrogen sources. The other model postulated that mutations in gltB or gltD (which encode the subunits of GOGAT) were polar on a downstream gene,gltF, which is necessary for proper activation of gene expression by the Ntr system. The data reported here show that thegltF model is incorrect for three reasons: first, a nonpolar gltB and a polar gltD mutation of K. aerogenes both show the same phenotype; second,K. aerogenes and several other enteric bacteria lack a gene homologous to gltF; and third, mutants of E. coli whose gltF gene has been deleted show no defect in nitrogen metabolism. The argument that accumulated glutamine represses the Ntr system in gltB or gltDmutants is also incorrect, because these mutants can derepress the Ntr system normally so long as sufficient glutamate is supplied. Thus, we conclude that gltB or gltD mutants grow slowly on many poor nitrogen sources because they are starved for glutamate. Much of the glutamate formed by catabolism of alternative nitrogen sources is converted to glutamine, which cannot be efficiently converted to glutamate in the absence of GOGAT activity. Finally, GOGAT-deficient E. coli cells growing with glutamine as the sole nitrogen source increase their synthesis of the other glutamate-forming enzyme, glutamate dehydrogenase, severalfold, but this is still insufficient to allow rapid growth under these conditions.

scholarly journals Titration and Conditional Knockdown of the prfB Gene in Escherichia coli: Effects on Growth and Overproduction of the Recombinant Mammalian Selenoprotein Thioredoxin Reductase

2006 ◽  
Vol 73 (2) ◽  
pp. 432-441 ◽  
Author(s):  
Olle Rengby ◽  
Elias S. J. Arnér
Keyword(s):  
Escherichia Coli ◽  
Growth Rate ◽  
Essential Gene ◽  
Thioredoxin Reductase ◽  
Lower Growth ◽  
E Coli ◽  
Native Promoter ◽  
Lower Growth Rate ◽  
The Cost ◽  
Translational Termination

ABSTRACT Release factor 2 (RF2), encoded by the prfB gene in Escherichia coli, catalyzes translational termination at UGA and UAA codons. Termination at UGA competes with selenocysteine (Sec) incorporation at Sec-dedicated UGA codons, and RF2 thereby counteracts expression of selenoproteins. prfB is an essential gene in E. coli and can therefore not be removed in order to increase yield of recombinant selenoproteins. We therefore constructed an E. coli strain with the endogenous chromosomal promoter of prfB replaced with the titratable PBAD promoter. Knockdown of prfB expression gave a bacteriostatic effect, while two- to sevenfold overexpression of RF2 resulted in a slightly lowered growth rate in late exponential phase. In a turbidostatic fermentor system the simultaneous impact of prfB knockdown on growth and recombinant selenoprotein expression was subsequently studied, using production of mammalian thioredoxin reductase as model system. This showed that lowering the levels of RF2 correlated directly with increasing Sec incorporation specificity, while also affecting total selenoprotein yield concomitant with a lower growth rate. This study thus demonstrates that expression of prfB can be titrated through targeted exchange of the native promoter with a PBAD-promoter and that knockdown of RF2 can result in almost full efficiency of Sec incorporation at the cost of lower total selenoprotein yield.

scholarly journals Metabolic Engineering of Escherichia coli for Production of Enantiomerically Pure (R)-(−)-Hydroxycarboxylic Acids

2003 ◽  
Vol 69 (6) ◽  
pp. 3421-3426 ◽  
Author(s):  
Sang Yup Lee ◽  
Young Lee
Keyword(s):  
Escherichia Coli ◽  
Copy Number ◽  
Ralstonia Eutropha ◽  
Enantiomerically Pure ◽  
Pha Depolymerase ◽  
E Coli ◽  
Theoretical Yield ◽  
Hydroxycarboxylic Acids ◽  
Copy Number Plasmid ◽  
High Copy Number Plasmid

ABSTRACT A heterologous metabolism of polyhydroxyalkanoate (PHA) biosynthesis and degradation was established in Escherichia coli by introducing the Ralstonia eutropha PHA biosynthesis operon along with the R. eutropha intracellular PHA depolymerase gene. By with this metabolically engineered E. coli, enantiomerically pure (R)-3-hydroxybutyric acid (R3HB) could be efficiently produced from glucose. By employing a two-plasmid system, developed as the PHA biosynthesis operon on a medium-copy-number plasmid and the PHA depolymerase gene on a high-copy-number plasmid, R3HB could be produced with a yield of 49.5% (85.6% of the maximum theoretical yield) from glucose. By integration of the PHA biosynthesis genes into the chromosome of E. coli and by introducing a plasmid containing the PHA depolymerase gene, R3HB could be produced without plasmid instability in the absence of antibiotics. This strategy can be used for the production of various enantiomerically pure (R)-hydroxycarboxylic acids from renewable resources.

scholarly journals Development of a semi-defined medium for high cell density cultivation of Escherichia coli in shake flasks: Part 1

2016 ◽  
Author(s):  
Wenfa Ng ◽  
Yen-Peng Ting
Keyword(s):  
Escherichia Coli ◽  
Cell Density ◽  
Yeast Extract ◽  
High Cell Density ◽  
Defined Medium ◽  
High Cell ◽  
High Cell Density Cultivation ◽  
E Coli ◽  
Carbon And Nitrogen ◽  
Shake Flasks

Sufficient quantities of cells of consistent characteristics are needed for studying biological processes (at the population level) in many areas of applied microbiology. However, generating the requisite biomass by cell culture is usually the rate-limiting step of a project given the relatively low biomass yield of many commercial culture media in shake flasks. This work reports the formulation of a semi-defined medium that enabled aerobic high cell density cultivation of Escherichia coli DH5α (ATCC 53868) in shake flasks. The formulated medium (FM) comprises: a buffer system (K2HPO4: 12.54 g/L and KH2PO4: 2.31 g/L); vitamins and trace elements (yeast extract: 12.0 g/L); salts (NaCl: 5.0 g/L and MgSO4: 0.24 g/L); and carbon and nitrogen sources (D-Glucose: 6.0 g/L and NH4Cl: 1.5 g/L). Notable characteristics of this medium are: high buffer capacity (89 mM phosphate), 1:1 molar ratio between D-Glucose and NH4Cl, and yeast extract providing trace elements and a secondary source of carbon and nitrogen. Preliminary data revealed that an OD600nm of 9 was attained after 24 hours of cultivation at 37 oC, with glucose and NH4Cl as the main nutrients. At 48 hours, the OD600nm reached a maximum value of 11 with yeast extract providing the necessary nutrients for cell growth and biomass formation. The broth’s pH varied between 5.5 and 7.8 during cultivation. For comparison, the maximum OD600nm of E. coli grown in three commonly used complex media: Nutrient Broth, LB Lennox, and Tryptic Soy Broth (TSB) were 1.4, 3.2 and 9.2, respectively, under identical culture conditions. Finally, FM maintained the viability of a larger population of cells for three days - compared to a population collapse observed in TSB after one day. Collectively, the present findings suggested that the formulated medium might find use as a high cell density aerobic growth medium for E. coli in shake flasks. Part 2 of this work describes improvements in medium performance - specifically, higher cell yield as well as a shorter diauxic lag phase and total culture period – achieved through a small reduction in D-Glucose and NH4Cl concentrations in the medium composition. An abstract preprint of Part 2 is available at https://peerj.com/preprints/117/

scholarly journals Development of a semi-defined medium for high cell density cultivation of Escherichia coli in shake flasks: Part 1

2017 ◽  
Author(s):  
Wenfa Ng
Keyword(s):  
Escherichia Coli ◽  
Cell Density ◽  
Yeast Extract ◽  
High Cell Density ◽  
Defined Medium ◽  
High Cell ◽  
High Cell Density Cultivation ◽  
E Coli ◽  
Carbon And Nitrogen ◽  
Shake Flasks

Sufficient quantities of cells of consistent characteristics are needed for studying biologicalprocesses (at the population level ) in many areas of applied microbiology. However, generating the requisite biomass by cell culture is usually the rate-limiting step of a project given the relatively low biomass yield of many commercial culture media in shake flask culture systems. This work reports the formulation of a semi-defined medium that enabled aerobic high cell density cultivation of Escherichia coli DH5α (ATCC 53868) in shake flasks. The formulated medium (FM) comprises: a buffer system (K2HPO4 : 12.54 g/L and KH2 PO4 : 2.31 g/L); vitamins and trace elements (yeast extract: 12.0 g/L); salts (NaCl: 5.0 g/L and MgSO4 : 0.24 g/L); and carbon and nitrogen sources (D-Glucose: 6.0 g/L and NH4Cl: 1.5 g/L). Notable characteristics of this medium are: high buffer capacity (89 mM phosphate), 1:1 molar ratio between D-Glucose and NH4Cl, and yeast extract providing trace elements and a secondary source of carbon and nitrogen. Preliminary data revealed an OD 600nm of 9 after 24 hours of cultivation at 37 oC, presumably with glucose and NH4Cl as the main nutrients. At 48 hours, an OD 600nm of 11 was attained with yeast extract providing the necessary nutrients for cell growth and biomass formation. The broth’s pH varied between 5.5 and 7.8 during cultivation. On the other hand, the maximum OD 600nm of E. coli grown in three commonly used complex media: Nutrient Broth, LB Lennox, and Tryptic Soy Broth (TSB) were 1.4, 3.2 and 9.2, respectively, under identical culture conditions. Finally, FM maintained the viability of a larger population of cells for three days, compared to a population collapse in TSB broth after one day. Collectively, the results suggested that the formulated medium might find use as a high cell density aerobic growth medium for E. coli in shake flasks. Part 2 of this work describes improvements in medium performance ; specifically, higher cell yield as well as a shorter diauxic lag phase and total culture period achieved through a small reduction in D-Glucose and NH4Cl concentrations in the medium composition. An abstract preprint of Part 2 is available at https://peerj.com/preprints/117/

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