Biosynthesis of synthons in two-liquid-phase media

The Pseudomonas oleovorans alkane hydroxylase and xylene oxygenase from Pseudomonas putida are versatile mono-oxygenases for stereo- and regioselective oxidation of aliphatic and aromatic hydrocarbons. Pseudomonas oleovorans and alkanol dehydrogenase deficient mutants of Pseudomonas have previously been used to produce alkanols from various alkanes and optically active epoxides from alkenes. Similarly, P. putida strains have been used to produce aromatic alcohols, aromatic acids, and optically active styrene oxides. A limitation in the use of Pseudomonas strains for bioconversions is that these strains can degrade some of the products formed. To counter this problem, we have constructed Escherichia coli recombinants, which contain the alk genes from the OCT plasmid of P. oleovorans [E. coli HB101 (pGEc47)] and the xylMA genes from the TOL plasmid of P. putida mt-2 [E. coli HB101 (pGB63)], encoding alkane hydroxylase and xylene oxygenase, respectively. Escherichia coli HB101 (pGEc47) was used to produce octanoic acid from n-octane and E. coli HB101 (pBG63) was put to use for the oxidation of styrene to styrene oxide in two-liquid phase biocatalysis at high cell densities. The alk(+) recombinant strain E. coli HB101 (pGEc47) was grown to 40 g/L cell dry mass in the presence of n-octane, which was converted to octanoic acid by the alkane oxidation system, the product accumulating in the aqueous phase. The xyl(+) recombinant E. coli HB101 (pBG63) was grown to a cell density of 26 g/L cell dry mass in the presence of around 7% (v/v) n-dodecane, which contained 2% (v/v) styrene. The recombinant E. coli (xyl(+)) converted styrene to (S)-(+)-styrene oxide at high enantiomeric excess (94% ee) and this compound partitioned almost exclusively into the organic phase. Using these high-cell-density two-liquid-phase cultures, the products accumulated rapidly, yielding high concentrations of products (50 mM octanoic acid and 90 mM styrene oxide) in the respective phases. (c) 1996 John Wiley & Sons, Inc.     

Bioconversions of aliphatic compounds by Pseudomonas oleovorans in multiphase bioreactors: background and economic potential.

Pseudomonas oleovorans can grow on linear alkanes and alkenes in the hexane to dodecane range by virtue of enzymes encoded by the alk genes. By introducing selected alk genes into Pseudomonas strains and by supplying alkanes in the growth medium as a bulk liquid phase, specific alkane oxidation products can be accumulated in the alkane phase. We review the genetics and enzymology of the alk system and the potential of bioconversions in two-liquid-phase bioreactors, and suggest that such systems might eventually allow the biotechnological production of intermediate value compounds.     

Effects of methanol concentration on expression levels of recombinant protein in fed-batch cultures of Pichia methanolica

The methylotrophic yeast Pichia methanolica can be used to express recombinant genes at high levels under the control of the methanol-inducible alcohol oxidase (AUG1) promoter. Methanol concentrations during the induction phase directly affect cellular growth and protein yield. Various methanol concentrations controlled by an on-line monitoring and control system were investigated in mixed glucose/methanol fed-batch cultures of P. methanolica expressing the human transferrin N-lobe protein. The PMAD18 P. methanolica strain utilized is a knock-out for the chromosomal AUG1 gene locus, resulting in a slow methanol utilization phenotype. Maximum growth of 100 g of dry cell weight per liter of culture was observed in cultures grown at 1.0% (v/v) methanol concentration. Maximum recombinant gene expression was observed for cultures controlled at 0.7% (v/v) methanol concentration, resulting in maximum volumetric production of 450 mg of transferrin per liter after 72 h of elapsed fermentation time.     

Heat shock gene expression in continuous cultures of Escherichia coli.

Temperature inducible systems for the controlled expression of recombinant genes are finding increasing industrial applications. These involve either short or long term exposure of the process culture to superoptimum temperatures. It is well known that bacteria respond to a sudden increase in their environmental temperature with an immediate transient increase in the synthesis rates of specific heat shock proteins. The use of continuous flow processes for the production of recombinant proteins would allow higher productivity and smaller scale bioreactors. However, the induction patterns of heat shock proteins in continuous culture after defined heat shocks are not well defined despite a large amount of information which is now available concerning heat shock protein induction in batch cultures. An overview of this information is presented to enable a better understanding of the response in continuous cultures. The latter was investigated by monitoring the transient expression of a representative heat shock gene, htpG, in E. coli in continuous culture. The relative magnitude of the response was found to be both temperature and exposure time dependent, but growth rate independent. Changing medium composition resulted in both different steady and transient state expression levels.     

Kinetic modeling of free fatty acid production in Escherichia coli based on continuous cultivation of a plasmid free strain

The microbial production of free fatty acids (FFAs) and reduced derivatives is an attractive process for the renewable production of diesel fuels. Toward this goal, a plasmid-free strain of Escherichia coli was engineered to produce FFAs by integrating three copies of a thioesterase gene from Umbellularia californica (BTE) under the control of an inducible promoter onto the chromosome. In batch culture, the resulting strain produced identical titers to a previously reported strain that expressed the thioesterase from a plasmid. The growth rate, glucose consumption rate, and FFA production rate of this strain were studied in continuous cultivation under carbon limitation. The highest yield of FFA on glucose was observed at a dilution rate of 0.05 h(-1) with the highest specific productivity observed at a dilution rate of 0.2 h(-1). The observed yields under the lowest dilution rate were 15% higher than that observed in batch cultures. An increase in both productivity and yield (≈ 40%) was observed when the composition of the nutrients was altered to shift the culture toward non-carbon limitation. A deterministic model of the production strain has been proposed and indicates that maintenance requirements for this strain are significantly higher than wild-type E. coli.     

Stability of recombinant protein production by Penicillium chrysogenum in prolonged chemostat culture

Abstract A strain (WKW2) of Penicillium chrysogenum transformed with heterologous fungal acetamidase ( amd S) and bacterial β-galactosidase ( lac Z) was grown at a dilution rate of 0.17 h⁻¹ (doubling time of approx. 4.1 h) for 1600 h in a glucose-limited culture. By the end of the experiment the original strain had been almost completely replaced by spontaneous, morphological mutants, but the acetamidase and β-galactosidase activities of the culture were essentially unaltered. Furthermore, when WKW2 and the non-transformed parental strain (NRRL1951) were grown together in glucose- or NH₄⁺-limited chemostat cultures, neither strain had a selective advantage over the other. Thus, heterologous gene expression does not result in NRRL1951 having a selective advantage over WKW2. These results suggest that continuous flow culture systems could be used for efficient (and cost effective) production of recombinant proteins.     

进化代谢选育高渗透压耐受型产琥珀酸大肠杆菌

在以碳酸钠为酸中和剂的大肠杆菌两阶段发酵产琥珀酸的过程中,由于Na+的积累造成发酵体系中渗透压的提高,严重抑制了琥珀酸的产物浓度。为了增强大肠杆菌对渗透压的耐受性,考察了利用进化代谢方法筛选高渗透压耐受型高产琥珀酸大肠杆菌菌株的可行性。进化代谢系统作为一种菌株突变装置,可以使菌体在连续培养条件下以最大的生长速率生长。以NaCl为渗透压调节剂,通过在连续培养装置中逐步提高NaCl浓度使菌体在高渗透压条件下快速生长,最终得到了一株高渗透压耐受型琥珀酸生产菌株Escherichia coli XB4。以碳酸钠为酸中和剂,在7 L发酵罐中利用Escherichia coli XB4进行两阶段发酵,厌氧培养60 h后,琥珀酸产量达到了69.5 g/L,琥珀酸生产速率达到了1.81 g/(L.h),分别比出发菌株提高了18.6%和20%。     

Characterization of the AlkS/P(alkB)-expression system as an efficient tool for the production of recombinant proteins in Escherichia coli fed-batch fermentations

The availability of suitable, well-characterized, and robust expression systems remains an essential requirement for successful metabolic engineering and recombinant protein production. We investigated the suitability of the Pseudomonas putida GPo1-derived AlkS/P(alkB) expression system in strictly aqueous cultures. By applying the apolar inducer dicyclopropylketone (DCPK) to express green fluorescent protein (GFP) from this system in Escherichia coli and analyzing the resulting cultures on single-cell level by flow cytometry, we found that this expression system gives rise to a homogeneous population of cells, even though the overall system is expected to have a positive feed-back element in the expression of the regulatory gene alkS. Overexpressing E. coli's serine hydroxymethyltransferase gene glyA, we showed that the system was already fully turned on at inducer concentrations as low as 0.005% (v/v). This allows efficient mass production of recombinant enzymes even though DCPK concentrations decreased from 0.05% to 0.01% over the course of a fully aerated cultivation in aqueous medium. Therefore, we elaborated the optimum induction procedure for production of the biocatalytically promising serine hydroxymethyltransferase and found volumetric and specific productivity to increase with specific growth rate in glucose-limited fed-batch cultures. Acetate excretion as a result of recombinant protein production could be avoided in an optimized fermentation protocol by switching earlier to a linear feed. This protocol resulted in a production of a final cell dry weight (CDW) concentration of 52 g/L, producing recombinant GlyA with a maximum specific activity of 6.3 U/mg total protein.     

Stabilization of pet operon plasmids and ethanol production in Escherichia coli strains lacking lactate dehydrogenase and pyruvate formate-lyase activities.

In the last decade, a major goal of research in biofuels has been to metabolically engineer microorganisms to ferment multiple sugars from biomass or agricultural wastes to fuel ethanol. Escherichia coli strains genetically engineered to contain the pet operon (Zymomonas mobilis pyruvate decarboxylase and alcohol dehydrogenase B genes) produce high levels of ethanol. Strains carrying the pet operon in plasmid (e.g., E. coli B/pLOI297) or in chromosomal (e.g., E. coli KO11) sites require antibiotics in the media to maintain genetic stability and high ethanol productivity. To overcome this requirement, we used the conditionally lethal E. coli strain FMJ39, which carries mutations for lactate dehydrogenase and pyruvate formate lyase and grows aerobically but is incapable of anaerobic growth unless these mutations are complemented. E. coli FBR1 and FBR2 were created by transforming E. coli FMJ39 with the pet operon plasmids pLOI295 and pLOI297, respectively. Both strains were capable of anaerobic growth and displayed no apparent pet plasmid losses after 60 generations in serially transferred (nine times) anaerobic batch cultures. In contrast, similar aerobic cultures rapidly lost plasmids. In high-cell-density batch fermentations, 3.8% (wt/vol) ethanol (strain FBR1) and 4.4% (wt/vol) ethanol (strain FBR2) were made from 10% glucose. Anaerobic, glucose-limited continuous cultures of strain FBR2 grown for 20 days (51 generations; 23 with tetracycline and then 28 after tetracycline removal) showed no loss of antibiotic resistance. Anaerobic, serially transferred batch cultures and high-density fermentations were inoculated with cells taken at 57 generations from the previous continuous culture. Both cultures continued to produce high levels of ethanol in the absence of tetracycline. The genetic stability conferred by selective pressure for pet-containing cells without requirement for antibiotics suggests potential commercial suitability for E. coli FBR1 and FBR2.     

Production of D-p-hydroxyphenylglycine by N-carbamoyl-D-amino acid amidohydrolase-overproducing Escherichia coli strains.

The N-carbamoyl-D-amino acid amidohydrolase (D-carbamoylase) gene from Agrobacterium radiobacter NRRL B11291 has been successfully cloned and expressed in Escherichia coli. Subcloning of the D-carbamoylase gene into different types of vectors and backgrounds of E. coli strains showed that the optimal expression level of D-carbamoylase was achieved in a ColE1-derived plasmid with a 150-fold increase in specific enzyme activity compared to that in a pSC101-derived plasmid. In addition, the recombinant plasmids were very stable in the E. coli strain ATCC11303 but not in JCL1258 tested here. Employing the recombinant E. coli strain DH5alpha/pAH61 for D-p-hydroxyphenylglycine production showed that the cell was capable of transforming N-carbamoyl-D-hydroxylphenylglycine to D-p-hydroxyphenylglycine with a molar conversion yield of 100% and a production rate of 1.9 g/(L h). In comparison with A. radiobacter NRRL B11291, this productivity approximates a 55-fold increase in D-hydroxyphenylglycine production. This result suggests the potential application of recombinant E. coli strains for the transformation reaction.     

Contamination of a high-cell-density continuous bioreactor

Continuous fermentations were carried out with a recombinant flocculent Saccharomyces cerevisiae strain in an airlift bioreactor. Once operating under steady state at a dilution rate of 0.45 h(-1), the bioreactor was contaminated with Escherichia coli cells. The faster growing E. coli strain was washed out of the bioreactor and the recombinant, slower growing flocculating S. cerevisiae strain remained as the only species detected in the bioreactor. Flocculation, besides allowing for the realization of high-cell-density systems with corresponding unusual high productivity, may be used as a selective property for controlling some contamination problems associated with prolonged continuous operation.     

High cell density culture of metabolically engineered Escherichia coli for the production of poly(3-hydroxybutyrate) in a defined medium

A recombinant Escherichia coli strain XL1-Blue harboring a stable high-copy-number plasmid pSYL107 containing the Alcaligenes eutrophus polyhydroxyalkanoate biosynthesis genes and the Escherichia coli ftsZ gene was employed for the production of poly(3-hydroxybutyrate) (PHB) by fed-batch culture in a defined medium. Suppression of filamentation by overexpressing the cell division protein FtsZ allowed production of PHB to a high concentration (77 g/L) with high productivity (2 g/L/h) in a defined medium, which was not possible with the recombinant E. coli that underwent filamentation. Further optimization of fed-batch culture condition resulted in PHB concentration of 104 g/L in a defined medium, which was the highest value reported to date by employing recombinant E. coli.     

过量表达苹果酸脱氢酶对大肠杆菌NZN111产丁二酸的影响

大肠杆菌NZN111是敲除了乳酸脱氢酶的编码基因 (ldhA) 和丙酮酸-甲酸裂解酶的编码基因 (pflB) 的工程菌,厌氧条件下由于辅酶NAD(H) 的不平衡导致其丧失了代谢葡萄糖的能力。构建了苹果酸脱氢酶的重组菌大肠杆菌NZN111/pTrc99a-mdh,在厌氧摇瓶发酵过程中通过0.3 mmol/L的IPTG诱导后重组菌的苹果酸脱氢酶 (Malate dehydrogenase,MDH) 酶活较出发菌株提高了14.8倍,NADH/NAD+的比例从0.64下降到0.26,同时NAD+和NADH浓度分别     

Scale-up of recombinant Opc protein production in Escherichia coli for a meningococcal vaccine

Opc is an outer membrane protein from Neisseria meningitidis present in meningococcal vaccine preparations. The opc gene, codifying for this protein, was cloned in to Escherichia coli and the Opc protein was expressed under the control of a tryptophan promoter. The recombinant strain was grown in batch cultures. Opc was expressed as inclusion bodies at about 32% of the total cellular protein. We examined the scale-up culture conditions for the production of the recombinant Opc. The scale-up process was performed from 1.5 l to 50 l culture, using first, the constant power per unit of volume (P/V) as main scaling criteria, and then the oxygen mass transfer coefficient (K(L)a) scaling criteria to adjust the optimal aeration conditions. A final productivity of 52 mgl(-1)h(-1) was obtained at the 50l culture scale compared with the 49 mgl(-1)h(-1) productivity at 1.5l laboratory scale.     

Foreign protein expression from S phase specific promoters in continuous cultures of recombinant CHO cells

Foreign protein expression from the commonly used SV40 promoter has been found to be primarily during the S-phase of the cell cycle. Simple mathematical models with this cell cycle phase dependent expression of foreign protein suggest that the specific production rate will be proportional to the cell growth rate, which is particularly disadvantageous in high cell density fed-batch or perfusion bioreactors. In this study we investigate this predicted relationship between the production rate and growth rate by culturing recombinant CHO cells in a continuous suspension bioreactor. One CHO cell line, GS-26, has been stably transfected with the plasmid pSVgal, which contains the E. coli lac Z gene under the control of the SV40 promoter. This GS-26 cell line was grown in suspension cultures over a range of specific growth rates in batch and continuous modes. The intracellular -galactosidase activity was assayed using a standard spectrophotometric method after breaking the cells open and releasing the enzyme. A strong growth associated relationship is found between the intracellular -galactosidase content and the specific growth rate in batch and continuous cultures, as predicted.     

l-Lactic acid production by Bacillus subtilis MUR1 in continuous culture

A novel UV-induced mutant strain of recombinant Bacillus subtilis MUR1 was used for the production of l-LA in continuous cultures with a variety of culture conditions. The maximal productivity of 17.6 g/L/h was obtained with a l-LA concentration of 44.1 g/L at the dilution rate of 0.4 h⁻¹. The highest concentration of l-LA (77.1 g/L) was produced at the dilution rate of 0.05 h⁻¹. This study showed that the maximum l-LA productivity of B. subtilis MUR1 which can only last for a very short period of time during the exponential phase in fed-batch cultures, can be extended indefinitely at steady state in continuous cultures. l-LA production increased with the increase of yeast extract concentrations in the medium. Moreover, temperature, agitation rate and various glucose concentrations in the feed were compared in continuous cultures. Different nitrogen sources (lysine, glutamine, ammonium sulphate and corn steep liquor) were studied to partly or completely replace yeast extract in the medium, most of them showed positive effects on l-LA production and cell growth. The l-LA productivities from continuous cultures in this study are higher than the productivity of current microbial industrial processes which use Lactobacillus to produce l-LA.     

Medium optimization for the production of recombinant nattokinase by Bacillus subtilis using response surface methodology

Nattokinase is a potent fibrinolytic enzyme with the potential for fighting cardiovascular diseases. Most recently, a new Bacillus subtilis/Escherichia coli (B. subtilis/E. coli) shuttle vector has been developed to achieve stable production of recombinant nattokinase in B. subtilis (Chen; et al. 2007, 23, 808-813). With this developed B. subtilis strain, the design of an optimum but cost-effective medium for high-level production of recombinant nattokinase was attempted by using response surface methodology. On the basis of the Plackett-Burman design, three critical medium components were selected. Subsequently, the optimum combination of selected factors was investigated by the Box-Behnken design. As a result, it gave the predicted maximum production of recombinant nattokinase with 71 500 CU/mL for shake-flask cultures when the concentrations of soybean hydrolysate, potassium phosphate, and calcium chloride in medium were at 6.100, 0.415, and 0.015%, respectively. This was further verified by a duplicated experiment. Moreover, the production scheme based on the optimum medium was scaled up in a fermenter. The batch fermentation of 3 L was carried out by controlling the condition at 37 degrees C and dissolved oxygen reaching 20% of air saturation level while the fermentation pH was initially set at 8.5. Without the need for controlling the broth pH, recombinant nattokinase production with a yield of 77 400 CU/mL (corresponding to 560 mg/L) could be obtained in the culture broth within 24 h. In particular, the recombinant B. subtilis strain was found fully stable at the end of fermentation when grown on the optimum medium. Overall, it indicates the success of this experimental design approach in formulating a simple and cost-effective medium, which provides the developed strain with sufficient nutrient supplements for stable and high-level production of recombinant nattokinase in a fermenter.     

Whole-cell bio-oxidation of n-dodecane using the alkane hydroxylase system of P. putida GPo1 expressed in E. coli

The alkane-1-monoxygenase (alkB) complex of Pseudomonas putida GPo1 has been extensively studied in the past and shown to be capable of oxidising aliphatic C(5)-C(12) alkanes to primary alcohols both in the wild-type organism by growth on C(5)-C(12) alkanes as sole carbon source and in vitro. Despite this, successful n-dodecane oxidation for the production of 1-dodecanol or dodecanoic acid has proven elusive in the past when using alkB-expressing recombinants. This article demonstrates, for the first time in vivo, by using the Escherichia coli GEC137 pGEc47ΔJ strain, that n-dodecane oxidation using this enzyme for the production of primary alcohols and carboxylic acids is feasible and in fact potentially more promising than n-octane oxidation due to lower product and substrate toxicity. Yields are reported of 1-dodecanol of up to 2 g/L(organic) and dodecanoic acid up to 19.7 g/L(organic) in a 2 L stirred tank reactor with 1L aqueous phase and 200 mL of n-dodecane as a second phase. The maximum volumetric rate of combined alcohol and acid production achieved was 1.9 g/L(organic)/h (0.35 g/L(total)/h). The maximum specific activity of combined alcohol and acid production was 7-fold lower on n-dodecane (3.5 μmol/min/g(dcw)) than on n-octane (21 μmol/min/g(dcw)); similar to the 5-fold difference observed between wild-type growth rates using the two respective alkanes as sole carbon source. Despite this, both total volumetric rate and final yield exceeded n-octane oxidation by 3.5-fold under the same conditions, due to the lower toxicity of n-dodecane and its oxidation products to E. coli compared to the 8-carbon equivalents. Substrate access limitations and the overoxidation of 1-dodecanol to dodecanoic acid were identified as the most important limitations to be addressed.