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。     

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.     

重组人干扰素α-2b在大肠杆菌中分泌表达

人干扰素α-2b原始基因在重组原核工程菌中表达量偏低,所以我们在不改变干扰素原有氨基酸组成的前提下,根据大肠杆菌密码子偏爱性使用定向突变技术对huIFNα-2b基因进行点突变。将大肠杆菌STⅡ信号肽基因与突变后huIFNα-2b基因融合并于信号肽5′端和huIFNα-2b基因3′端引入合适的酶切位点。融合基因克隆至载体pCSE,pET-22b和pPAK4L中,此3种载体分别含有组成型启动子、T7启动子和phoA启动子。融合基因在载体pCSE中表达量很低,其中约有50%的目标蛋白能够成功实现分泌。在E.coliBL21中,pET-22b经过IPTG诱导可以实现huIFNα-2b的高表达,但STⅡ信号肽不能被有效切除。含有phoA启动子的载体pPAK4L其在E.coliW3110中可以实现huIFNα-2b较高水平的分泌表达,经过低磷诱导其表达量最高可至20μg/mL(A550)菌液,约有30%的目标蛋白质信号肽能够被成功切除并分泌到胞间质中。     

Development and characterization of an oxygen-dependent inducible promoter system, the modified nar promoter in a mutant Escherichia coli

A nar promoter system (a modified nar promoter in a mutant host Escherichia coli (pMW618/W3110narL(-))), which is maximally induced under microaerobic conditions, was developed and characterized through batch and fed-batch culture to see whether the modified nar promoter can be used as an oxygen-dependent inducible promoter in the absence of nitrate ion. The modified nar promoter (pMW618) derived by mutations at -10 and -35 regions of the wild-type nar promoter does not require nitrate ion for the full induction, while a mutant host E. coli, W3110narL(-), does not express nitrate-dependent regulatory protein, NARL, from the host chromosome. In this study, it was found from fed-batch culture that the specific beta-galactosidase activity expressed from the lacZ gene fused to the modified nar promoter in the absence of nitrate ion was maximal when E. coli was grown under aerobic conditions (dissolved oxygen (DO) at 80%) to absorbance at 600 nm (OD(600)) of 35, and then the modified nar promoter was induced by lowering DO to 1-2% with alternating microaerobic and aerobic conditions. The maximal specific beta-galactosidase activity became 58,000 Miller at OD(600) of 160 with an induction ratio of 20. On the basis of these results, we conclude that the modified nar promoter system (pMW618/W3110narL(-)), requiring only reduction of DO for the full induction, provides a convenient and effective high-level expression system under conditions of fed-batch culture.     

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.     

Comparison between Escherichia coli K-12 strains W3110 and MG1655 and wild-type E. coli B as platforms for xylitol production

Escherichia coli W3110 was previously engineered to produce xylitol from a mixture of glucose plus xylose by expressing xylose reductase (CbXR) and deleting xylulokinase (DeltaxylB), combined with either plasmid-based expression of a xylose transporter (XylE or XylFGH) (Khankal et al., J Biotechnol, 2008) or replacing the native crp gene with a mutant (crp*) that alleviates glucose repression of xylose transport (Cirino et al., Biotechnol Bioeng 95:1167-1176, 2006). In this study, E. coli K-12 strains W3110 and MG1655 and wild-type E. coli B were compared as platforms for xylitol production from glucose-xylose mixtures using these same strategies. The engineered strains were compared in fed-batch fermentations and as non-growing resting cells. Expression of CRP* in the E. coli B strains tested was unable to enhance xylose uptake in the presence of glucose. Xylitol production was similar for the (crp*, DeltaxylB)-derivatives of W3110 and MG1655 expressing CbXR (average specific productivities of 0.43 g xylitol g cdw(-1 )h(-1) in fed-batch fermentation). In contrast, results varied substantially between different DeltaxylB-derivative strains co-expressing either XylE or XylFGH. The differences in genetic background between these host strains can therefore profoundly influence metabolic engineering strategies.     

Production of penicillin acylase by a recombinant Escherichia coli using cheese whey as substrate and inducer

Cheese whey (CW) is the major subproduct from cheese manufacturing and it is considered as a waste pollutant since its high content of lactose. In this work a fermentation process for the production of penicillin acylase (PA) by a recombinant Escherichia coli and using CW as unique carbon source and inducer was developed. A design factorial 3(2) was used to evaluate the influence of independent variables (dissolved oxygen and CW concentration) on the ability of E. coli W3110/pPA102 to produce PA. Maximum specific PA activity of 781 U g(-1) was attained at 5 g L(-1) of CW and 3% dissolved oxygen. The results showed that CW can be used successfully as unique carbon source and inducer for the production of recombinant proteins using constructions driven by the lac promoter and this way reducing the discharges of that pollutant to the environment.     

Co-expression of bacterial hemoglobin overrides high glucose-induced repression of foreign protein expression in Escherichia coli W3110

Co-expression of Vitreoscilla hemoglobin (VHb) can enhance production of foreign proteins in several microorganisms, including Escherichia coli. Production of foreign proteins [green fluorescent protein (GFP) and organophosphorous hydrolase (OPH)] has been examined in two typical industrial E. coli strains, W3110 (a K12 derivative) and BL21 (a B derivative). In particular, we investigated the effects of VHb co-expression and media glucose concentration on target protein production. We employed the nar O(2)-dependent promoter for self-tuning of VHb expression based on the natural changes in dissolved O(2) levels over the duration of culture. Foreign protein production in strain BL21 was decreased by a high glucose concentration but co-expression of VHb had no effect on this. In contrast, co-expression of VHb in strain W3110 overrode the glucose-induced repression and resulted in steady expression of foreign proteins.     

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.     

基于rhaSR嵌合操纵子的构建及其在大肠杆菌中表达的研究

通过PCR等重组DNA技术,构建了含rhaSR启动子表达调控元件、RhaR基因、报告基因gst(谷胱甘肽-S-转移酶)的两个嵌合操纵子,并插入大肠杆菌表达载体pALEX中构成pALEX-PR1和pALEX-PR2。其中pALEX-PR2的RhaR基因上游为原有的SD序列,而pALEX-PR1的RhaR基因上游则插入了增强的SD序列。把这两个重组表达质粒分别转入大肠杆菌BL21(DE3)中,报告基因gst能够在L-鼠李糖诱导下表达,其表达量是非诱导条件下的4～5倍,且pALEX-PR1的表达量是pALEX-PR2的3.14倍。以上结果表明,gst的表达既受L-鼠李糖诱导,同时又受RhaR的正调控。SDS-PAGE结果显示,GST占大肠杆菌培养物总可溶蛋白的5.41%(W/W),平均1L培养物可获得3.0mg纯化的GST。酶活性分析表明,所构建的嵌合操纵子表达的GST保持了正确的构型且具有很高的活性。     

Enhanced production of plasmid DNA by engineered Escherichia coli strains

Escherichia coli strains VH33 (PTS? GalP? strain displaying a strongly reduced overflow metabolism) and VH34 (additionally lacking the pyruvate kinase A) were evaluated for the production of a plasmid DNA (pDNA) vaccine. The parent (W3110) and mutant strains were cultured using 10 g of glucose/L. While the specific growth rates of the three strains were similar, they presented differences in the accumulation of acetate. W3110 accumulated up to 4 g/L of acetate, VH33 produced 1.4 g/L, and VH34 only 0.78 g/L. VH33 and VH34 produced 76% and 300% more pDNA than W3110. Moreover, VH34 demanded 33% less oxygen than VH33 and W3110, which can be advantageous for large-scale applications.     

High‐level conversion of L‐lysine into 5‐aminovalerate that can be used for nylon 6,5 synthesis

L ‐Lysine is a potential feedstock for the production of bio‐based precursors for engineering plastics. In this study, we developed a microbial process for high‐level conversion of L ‐lysine into 5‐aminovalerate (5AVA) that can be used as a monomer in nylon 6,5 synthesis. Recombinant Escherichia coli WL3110 strain expressing Pseudomonas putida delta‐aminovaleramidase (DavA) and lysine 2‐monooxygenase (DavB) was grown to high density in fed‐batch culture and used as a whole cell catalyst. High‐density E. coli WL3110 expressing DavAB, grown to an optical density at 600 nm (OD₆₀₀) of 30, yielded 36.51 g/L 5AVA from 60 g/L L ‐lysine in 24 h. Doubling the cell density of E. coli WL3110 improved the conversion yield to 47.96 g/L 5AVA from 60 g/L of L ‐lysine in 24 h. 5AVA production was further improved by doubling the L ‐lysine concentration from 60 to 120 g/L. The highest 5AVA titer (90.59 g/L; molar yield 0.942) was obtained from 120 g/L L ‐lysine by E. coli WL3110 cells grown to OD₆₀₀ of 60. Finally, nylon 6,5 was synthesized by bulk polymerization of ?‐caprolactam and δ‐valerolactam prepared from microbially synthesized 5AVA. The hybrid system demonstrated here has promising possibilities for application in the development of industrial bio‐nylon production processes.     

L-lyxose metabolism employs the L-rhamnose pathway in mutant cells of Escherichia coli adapted to grow on L-lyxose.

Escherichia coli cannot grow on L-lyxose, a pentose analog of the 6-deoxyhexose L-rhamnose, which supports the growth of this and other enteric bacteria. L-Rhamnose is metabolized in E. coli by a system that consists of a rhamnose permease, rhamnose isomerase, rhamnulose kinase, and rhamnulose-1-phosphate aldolase, which yields the degradation products dihydroxyacetone phosphate and L-lactaldehyde. This aldehyde is oxidized to L-lactate by lactaldehyde dehydrogenase. All enzymes of the rhamnose system were found to be inducible not only by L-rhamnose but also by L-lyxose. L-Lyxose competed with L-rhamnose for the rhamnose transport system, and purified rhamnose isomerase catalyzed the conversion of L-lyxose into L-xylulose. However, rhamnulose kinase did not phosphorylate L-xylulose sufficiently to support the growth of wild-type E. coli on L-lyxose. Mutants able to grow on L-lyxose were analyzed and found to have a mutated rhamnulose kinase which phosphorylated L-xylulose as efficiently as the wild-type enzyme phosphorylated L-rhamnulose. Thus, the mutated kinase, mapped in the rha locus, enabled the growth of the mutant cells on L-lyxose. The glycolaldehyde generated in the cleavage of L-xylulose 1-phosphate by the rhamnulose-1-phosphate aldolase was oxidized by lactaldehyde dehydrogenase to glycolate, a compound normally utilized by E. coli.     

Bioreactor cultivation of Escherichia coli for production of recombinant penicillin G amidase from Alcaligenes faecalis

The penicillin G amidase (PGA) from Alcaligenes faecalis, which has interesting properties for use in combinatorial biochemistry, was produced by recombinant expression in Escherichia coli. The corresponding gene was cloned into a multicopy vector under the strict regulatory control of the rhamnose inducible promoter. Cells were grown in a synthetic minimal medium in a bioreactor (5 l working vol.), and production of PGA was induced by repeated addition of the inducer rhamnose, that served also as a carbon source. The fermentation yield was about 4500 units PGA activity per liter of culture medium.     

Propionate-regulated high-yield protein production in Escherichia coli

A new expression system containing the Salmonella enterica prpBCDE promoter (P(prpB)) responsible for expression of the propionate catabolic genes (prp BCDE) and prpR encoding the positive regulator of this promoter has been developed and tested. The main features of the expression system compared to those based on the bacteriophage T7 promoter are low background expression and high induced expression in Escherichia coli strains BL21, BL21(DE3), MG1655, and W3110. In addition, propionate is an inexpensive, simple-to-use, nontoxic inducer that is attractive for large-scale protein production. Hence, this new system is highly complementary to the widely used T7 promoter-driven expression systems.     

Role of xylose transporters in xylitol production from engineered Escherichia coli

Escherichia coli W3110 was previously engineered to co-utilize glucose and xylose by replacing the wild-type crp gene with a crp* mutant encoding a cAMP-independent CRP variant (Cirino et al., 2006 [Cirino, P.C., Chin, J.W., Ingram, L.O., 2006. Engineering Escherichia coli for xylitol production from glucose-xylose mixtures. Biotechnol. Bioeng. 95, 1167-1176.]). Subsequent deletion of the xylB gene (encoding xylulokinase) and expression of xylose reductase from Candida boidinii (CbXR) resulted in a strain which produces xylitol from glucose-xylose mixtures. In this study we examine the contributions of the native E. coli xylose transporters (the d-xylose/proton symporter XylE and the d-xylose ABC transporter XylFGH) and CRP* to xylitol production in the presence of glucose and xylose. The final batch xylitol titer with strain PC09 (Delta xylB and crp*) is reduced by 40% upon deletion of xylG and by 60% upon deletion of both xyl transporters. Xylitol production by the wild-type strain (W3110) expressing CbXR is not reduced when xylE and xylG are deleted, demonstrating tight regulation of the xylose transporters by CRP and revealing significant secondary xylose transport. Finally, plasmid expression of XylE or XylFGH with CbXR in PC07 (Delta xylB and wild-type crp) growing on glucose results in xylitol titers similar to that achieved with PC09 and provides an alternative strategy to the use of CRP*.     

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.     

Development of anaerobically inducible nar promoter expression vectors for the expression of recombinant proteins in Escherichia coli

Dissolved oxygen (DO)-controlled nar promoter expression vectors were constructed, and their expression efficiency was compared with that of the T7 promoter pET22 expression vector by expressing human growth hormone (hGH), enhanced green fluorescence protein (EGFP), and β-tyrosinase in Escherichia coli cells. The nar promoter expression vector pRBS, which was engineered with a 5′-untranslated region and ribosomal binding site for the T7 promoter, expressed hGH at a rate of up to 32% of the total cellular proteins (TCP) in E. coli W3110narL⁻. The expression level of hGH was further enhanced, up to ∼42% of the TCP, by adding the N-terminal peptide tag of β-galactosidase to hGH, which was comparable to the expression of ∼43% of the TCP in pET-lac:hGH/BL21(DE3). A further engineered expression vector, pRBS(fnr), which coexpressed fumarate/nitrate reductase (fnr), expressed more EGFP than pET22 in BL21(DE3). In addition, recombinant β-tyrosinase was successfully expressed at a rate of up to ∼45% of the TCP in pRBS(fnr) in W3110narL⁻. From these results, the DO-controlled nar promoter system developed in this study can be considered a reliable and cost-effective expression system for protein production, especially in large-scale fermentation, as an alternative to the pET/BL(DE3) system.