Online measurement of the respiratory activity in shake flasks enables the identification of cultivation phases and patterns indicating recombinant protein production in various Escherichia coli host strains

Escherichia coli is commonly used for recombinant protein production with many available host strains. Screening experiments are often performed in batch mode using shake flasks and evaluating only the final product concentration. This conventional approach carries the risk of missing the best strain due to limited monitoring capabilities. Thus, this study focuses on investigating the general suitability of online respiration measurement for selecting expression hosts for heterologous protein production. The oxygen transfer rate (OTR) for different T7‐RNA polymerase‐dependent Escherichia coli expression strains was compared under inducing and noninducing conditions. As model enzymes, a lipase A from Bacillus subtilis (BSLA) and a 3‐hydroxybutyryl‐CoA dehydrogenase from Thermus thermophilus (HBD) were chosen. Four strains were compared during expression of both enzymes in autoinduction medium. Additionally, four strains were compared during expression of the BSLA with IPTG induction. It was found that the metabolic burden during recombinant protein production induces a phase of constant OTR, while undisturbed cell growth with no or little product formation is indicated by an exponential increase. This pattern is independent of the host strain, expressed enzyme, and induction method. Furthermore, the OTR gives information about carbon source consumption, biomass formation, and the transition from production to noninduced second growth phase, thereby ensuring a fair comparison of different strains. In conclusion, online monitoring of the respiration activity is suited to qualitatively identify, if a recombinant protein is produced by a strain or not. Furthermore, laborious offline sampling is avoided. Thus, the technique is easier and faster compared to conventional approaches. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:315–327, 2018     

Simple defined autoinduction medium for high-level recombinant protein production using T7-based Escherichia coli expression systems

Protein production under the control of lac operon regulatory elements using autoinduction is based on diauxic growth of Escherichia coli on lactose after consumption of more preferred carbon substrates. A novel simple and cost-effective defined autoinduction medium using a mixture of glucose, glycerol, and lactose as carbon substrate and NH₄⁺ as sole nitrogen source without any supplementation of amino acids and vitamins was developed for T7-based E. coli expression systems. This medium was successfully employed in 96-well microtiter plates, test tubes, shake flasks, and 15-L bioreactor cultivations for production of different types of proteins achieving an average yield of 500 mg L⁻¹ product. Cell-specific protein concentrations and solubility were similar as during conventional isopropyl β-d-1-thiogalactopyranoside induction using Luria-Bertani broth. However, the final yield of target proteins was about four times higher, as a higher final biomass was achieved using this novel defined autoinduction broth.     

基因重组大肠杆菌表达HrpNEcc蛋白的发酵条件及诱导条件优化

对已构建好的表达HrpNEcc蛋白的工程菌BL21(DE3)/pET30a(+)hrpN Ecc的摇瓶发酵条件及乳糖诱导进行优化, 通过在7L发酵罐中放大发酵实验,以期提高蛋白产量并降低生产成本。在摇瓶中优化的发酵及诱导条件是：5% 的接种量,TB培养基,菌体培养至对数生长前期,添加3g/L外源诱导剂乳糖时,HrpNEcc蛋白产量可达417.60mg/L,比不添加乳糖时提高了36.73%,比用IPTG诱导时提高了16.85%。7L发酵罐中发酵,获得菌体湿重达到57.24g/L（WCW）,可溶性HrpNEcc蛋白产量占细胞总蛋白的50.2%,为3.29 g/L。     

Effect of amino acid supplement on cell yield and gene product in Escherichia coli harboring plasmid

Escherichia coli harboring a recombinant plasmid was cultivated in fed-batch culture to enhance production of a gene product. Expression of the leucine gene from Thermus thermophilus in the recombinant plasmid was examined by the assay of beta-isopropylmalate dehydrogenase activity at 75 degrees C. When E. coli was cultivated in medium without leucine, biomass concentration reached 15 g/L and the specific activity became 0.082 U/mg protein. When leucine was fed in the medium throughout cultivation, although biomass concentration reached 63 g/L, the specific activity decreased to 0.016 U/mg protein. When E. coli was cultivated in medium containing 1 g leucine/L, the specific activity remained virtually constant (about 0.13 U/mg protein) and biomass concentration reached 32 g dry cells/L. In these cultivations, growth yields of several amino acids and glucose were examined. When leucine was not added to the medium, growth yields except for histidine were lowest. When leucine was fed throughout the cultivation, growth yields of glucose and tryptophan were highest. The pH-stat was useful for feeding amino acids.     

Cloning and expression of the beta-D-phosphogalactoside galactohydrolase gene of Lactobacillus casei in Escherichia coli K-12.

Lactose metabolism in Lactobacillus casei 64H is associated with the presence of plasmid pLZ64. This plasmid determines both phosphoenolpyruvate-dependent phosphotransferase uptake of lactose and beta-D-phosphogalactoside galactohydrolase. A shotgun clone bank of chimeric plasmids containing restriction enzyme digest fragments of pLZ64 DNA was constructed in Escherichia coli K-12. One clone contained the gene coding for beta-D-phosphogalactoside galactohydrolase on a 7.9-kilobase PstI fragment cloned into the vector pBR322 in E. coli strain chi 1849. The beta-D-phosphogalactoside galactohydrolase enzyme isolated from E. coli showed no difference from that isolated from L. casei, and specific activity of beta-D-phosphogalactoside galactohydrolase was stimulated 1.8-fold in E. coli by growth in media containing beta-galactosides. A restriction map of the recombinant plasmid was compiled, and with that information, a series of subclones was constructed. From an analysis of the proteins produced by minicells prepared from transformant E. coli cells containing each of the recombinant subclone plasmids, it was found that the gene for the 56-kilodalton beta-D-phosphogalactoside galactohydrolase was transcribed from an L. casei-derived promoter. The gene for a second protein product (43 kilodaltons) was transcribed in the opposite direction, presumably under the control of a promoter in pBR322. The relationship of this second product to the lactose metabolism genes of L. casei is at present unknown.     

Enhancement of extracellular bispecific anti‐MUC1 nanobody expression in E. coli BL21 (DE3) by optimization of temperature and carbon sources through an autoinduction condition

Escherichia coli is one of the most suitable hosts for production of antibodies and antibody fragments. Antibody fragment secretion to the culture medium improves product purity in cell culture and diminishes downstream costs. In this study, E. coli strain BL21 (DE3) harboring gene encoding bispecific anti‐MUC1 nanobody was selected, and the autoinduction methodology for expression of bispecific anti‐MUC1 nanobody was investigated. Due to the replacement of IPTG by lactose as inducer, less impurity and toxicity in the final product were observed. To increase both intracellular and extracellular nanobody production, initially, the experiments were performed for the key factors including temperature and duration of protein expression. The highest amount of nanobody was produced after 21 h at 33°C. The effect of different carbon sources, glycerol, glucose, lactose, and glycine as a medium additive at optimum temperature and time were also assessed by using response surface methodology. The optimized concentrations of carbon sources were obtained as 0.75% (w/v), 0.03% (w/v), 0.1% (w/v), and 0.75% (w/v) for glycerol, glucose, lactose, and glycine, respectively. Finally, the production of nanobody in 2 L fermenter under the optimized autoinduction conditions was evaluated. The results show that the total titer of 87.66 µg/mL anti‐MUC1 nanobody, which is approximately seven times more than the total titer of nanobody produced in LB culture medium, is 12.23 µg/L .     

乳糖诱导的重组人血管内皮抑素(rhEndostatin)蛋白的表达

研究用乳糖替代IPTG作为诱导剂进行重组蛋白的表达,观察乳糖对乳糖操纵子调控的基因工程菌发酵及重组血管内皮抑素表达的影响,从而选取最佳诱导表达条件。以重组人血管内皮抑素表达工程菌pETrhEN/BL21(DE3)作为研究对象,分别用IPTG和乳糖作为诱导剂,在摇瓶中进行表达实验。并对重组蛋白质表达量进行分析。然后在5 L发酵罐中进行验证。在摇瓶培养条件下,乳糖浓度大于0.5 g/L即可以诱导目的蛋白的表达。乳糖浓度1 g/L时诱导目的蛋白表达量与1 mmol/L的IPTG相当,当乳糖浓度为10 g/L,目的蛋白表达量达到最大。在发酵罐培养条件下,补料4 h后葡萄糖浓度基本耗尽,此时开始加入乳糖。诱导后1 h,即有重组蛋白表达,在诱导后4 h达到高峰(占菌体可溶性蛋白的56%),与此同时,诱导后5 h菌体浓度也达到最高值。在以乳糖操纵子为调控手段的工程菌表达系统中,可以使用乳糖作为诱导剂,诱导应在葡萄糖消耗完后进行。     

重组α-环糊精葡萄糖基转移酶表达条件的优化及其产物专一性的分析

将来源于Bacillus sp 602 -1的α-环糊精葡萄糖基转移酶(ot-CGT)基因(cgt)插入到表达载体PQE30中,构建重组质粒PQE30/cgt,成功转化宿主菌E coli M15后,得到重组菌株E coli M15 (PQE30/cgt).在IPTG的诱导下得到酶表达的最适条件:TB培养基,0.01 mmol/L IPTG,诱导温度16℃,胞内酶比活力最高可达5 209 U/mL;加入IPTG 24 h后,添加甘氨酸和甘露醇会促使酶向胞外分泌.酶蛋白自诱导表达的适宜条件为在TB培养基中添加乳糖3.0 g/L,葡萄糖1.2 g/L,16℃培养96 h,酶比活力达到8 635 U/mL,明显高于IPTG诱导的效果.通过SDSPAGE验证了上述结论.酶催化转化实验表明:重组酶转化质量分数为1％可溶淀粉24h后,α-环糊精(α-CD)转化率可达38.2％,α和β的峰面积比约为3.4:1,α-CD具有较高的专一性,因此该重组α-CGT酶具有较好的工业化应用前景.     

液化沙雷氏菌磷脂酶A1的克隆表达及乳糖自诱导发酵

为了利用大肠杆菌高效生产重组磷脂酶,克隆了液化沙雷氏菌磷脂酶A1的编码基因pla,分别使用pET-28a(+)和pET-20b(+)载体,实现了磷脂酶A1在大肠杆菌BL21(DE3)中的功能表达.重组菌利用载体pET-28a(+)在原始信号肽的介导下胞外PLA1酶活达40.8 U/mL,占总酶活的91％.重组菌转接至优化后的发酵诱导培养基:蛋白胨10 g/L,酵母粉5g/L,葡萄糖0.8 g/L,乳糖5 g/L,25 mmol/L Na2HPO4,25 mmol/L KH2PO4和1 mmol/L MgSO4;菌体生长6h后,添加7.5 g/L的甘氨酸,37℃恒温发酵24 h,重组菌胞外PLA1酶活达到128.7 U/mL.     

Linear correlation between online capacitance and offline biomass measurement up to high cell densities in Escherichia coli fermentations in a pilot-scale pressurized bioreactor

To yield high concentrations of protein expressed by genetically modified Escherichia coli, it is important that the bacterial strains are cultivated to high cell density in industrial bioprocesses. Since the expressed target protein is mostly accumulated inside the E. coli cells, the cellular product formation can be directly correlated to the bacterial biomass concentration. The typical way to determine this concentration is to sample offline. Such manual sampling, however, wastes time and is not efficient for acquiring direct feedback to control a fedbatch fermentation. An E. coli K12-derived strain was cultivated to high cell density in a pressurized stirred bioreactor on a pilot scale, by detecting biomass concentration online using a capacitance probe. This E. coli strain was grown in pure minimal medium using two carbon sources (glucose and glycerol). By applying exponential feeding profiles corresponding to a constant specific growth rate, the E. coli culture grew under carbon-limited conditions to minimize overflow metabolites. A high linearity was found between capacitance and biomass concentration, whereby up to 85 g/L dry cell weight was measured. To validate the viability of the culture, the oxygen transfer rate (OTR) was determined online, yielding maximum values of 0.69 mol/l/h and 0.98 mol/l/h by using glucose and glycerol as carbon sources, respectively. Consequently, online monitoring of biomass using a capacitance probe provides direct and fast information about the viable E. coli biomass generated under aerobic fermentation conditions at elevated headspace pressures.     

瑞氏木霉表达黑曲霉葡萄糖氧化酶

利用高表达分泌纤维素酶的真菌瑞氏木霉表达重组的黑曲霉葡萄糖氧化酶。在大肠杆菌DH5α中构建瑞氏木霉纤维素酶CBHI启动子和CBHI信号肽基因黑曲霉葡萄糖氧化酶基因瑞氏木霉纤维素酶CBHI终止子构巢曲霉的甘油醛3磷酸脱氢酶启动子大肠杆菌抗潮霉素B磷酸转移酶基因构巢曲霉色氨酸C终止子pUC19(命名为pCBHGOD)质粒,线性化后用瑞氏木霉纤维素酶CBHI启动子和CBHI信号肽基因黑曲霉葡萄糖氧化酶基因瑞氏木霉纤维素酶CBHI终止子构巢曲霉的甘油醛3磷酸脱氢酶启动子大肠杆菌抗潮霉素B磷酸转移酶基因构巢曲霉色氨酸C终止子(命名为CBHGOD)核酸片段转化瑞氏木霉QM9414原生质体。用PCR扩增方法筛选出同源重组葡萄糖氧化酶基因的瑞士木霉突变株。用麦杆诱导瑞氏木霉突变株,生产黑曲霉葡萄糖氧化酶,Westernblot分析重组的葡萄糖氧化酶分子量与Sigma公司的天然黑曲霉葡萄糖氧化酶一致,生产的重组酶活性25umL,相当于Sigma公司葡萄糖氧化酶标准品的产量为0.5gL。瑞氏木霉可用于生产黑曲霉葡萄糖氧化酶。     

大肠杆菌抗氟乙酸变株的选育及应用

In the cultivation of gene engineered strain of Escherichia coli on glucose medium, excretion and accumulation of acetic acid inhibit not only cell growth but also the the expression of heterologous protein. It is obvious that the desirable host strain maintaining acetate at a low level is one of the approaches to increase the production of recombinant protein. The present article deals with the selection of mutants of E.coli DP19, DP8, which grow on the medium containing pyruvate as the sole carbon…     

Optimizing the expression of a monoclonal antibody fragment under the transcriptional control of the Escherichia coli lac promoter

The expression of a monoclonal antibody Fab fragment in Escherichia coli strain RB791/pComb3, induced with either lactose or isopropyl-beta-D-thiogalactoside (IPTG), was compared to determine if lactose might provide an inexpensive alternative to induction with IPTG. Induction of Fab expression imposed a metabolic load on the recombinant cells, resulting in lower final cell yields compared to the non-induced controls. An IPTG concentration of 0.05 mM was sufficient to achieve maximal expression of soluble Fab protein when inducing in the early-, mid-, or late-log phases of batch cultures grown using either glucose or glycerol as a carbon source. The largest overall yield of Fab fragments when using 0.05 mM IPTG was achieved by increasing the final yield of cells through glycerol feeding following induction in late-log phase. Lactose was as effective as IPTG for inducing Fab expression in E. coli RB791/pComb3. The greatest overall level of Fab expression was found when cells grown on glycerol were induced with 2 g/L lactose in late-log phase. Since the cost of 0.05 mM of IPTG is significantly greater than the cost of 2 g/L lactose, lactose provides an inexpensive alternative to IPTG for inducing the expression of Fab fragments, and possibly other recombinant proteins, from the E. coli lac promoter.     

Temperature-induced production of recombinant human insulin in high-cell density cultures of recombinant Escherichia coli

The construction of expression vectors encoding either the human insulin A- or B-chains fused to a synthetic peptide and the temperature-induced expression of the recombinant genes in Escherichia coli are reported. Using this two-chain approach we also describe the separate isolation of the insulin A- and B-chains from inclusion bodies and their subsequent assembly into native human insulin. The production of the insulin fusion proteins were carried out in high-cell density fed-batch cultures using a synthetic medium with glucose as sole carbon and energy source. The expression of the recombinant genes by temperature-shift in high-cell density cultures of recombinant E. coli resulted in product yields of grams per litre of culture broth, e.g. 4.5 g of insulin B-chain fusion protein per litre of culture broth. This translates into an expression yield of about 800 mg of the insulin B-chain per litre of culture. Under similar cultivation conditions the expression yield of the insulin A-chain corresponds to approximately 600 mg per litre of culture. The metabolic burden imposed on the recombinant cells during temperature-induced production of insulin fusion proteins in high-cell density cultures is reflected in an increased respiratory activity and a reduction of the biomass yield coefficient with respect to glucose.     

Design of a recombinant Escherichia coli for producing l-phenylalanine from glycerol

A recombinant Escherichia coli was engineered to produce the commercially important amino acid L: -phenylalanine (L: -Phe) using glycerol as the carbon source. Compared to the conventionally used glucose and sucrose, glycerol is a less expensive carbon source. As phenylalanine dehydrogenase (PheDH) activity is involved in the last step of L: -Phe synthesis in E. coli, a phenylalanine dehydrogenase gene (phedh) from the thermotolerant Bacillus lentus was cloned into pRSFDuet-1 (pPheDH) and expressed in E. coli BL21(DE3). The resulting clone had a limited ability to produce L: -Phe from glycerol, possibly because of a poor glycerol uptake by the cell, or an inability to excrete L: -Phe, or both. Therefore, yddG gene encoding an aromatic amino acid exporter and glpF gene encoding a glycerol transport facilitator were coexpressed with the phedh in a reengineered E. coli. In a glycerol medium, the maximum L: -Phe production rates of the clones pPY (phedh and yddG genes) and pPYF (phedh, yddG and glpF genes) were 1.4- and 1.8-fold higher than the maximum production rate of the pPheDH clone. The better producing pPYF clone was further evaluated in a 5?l stirred-tank fermenter (37?°C, an aeration rate of 1 vvm, an agitation speed of 400?rpm). In the fermenter, the maximum concentration of L: -Phe (366?mg/l) was achieved in a much shorter period compared to in the shake flasks. In the latter, the highest titer of L: -Phe was only 76?% of the maximum value attained in the fermenter.     

Molecular characterization of autoinduction of bioluminescence in the Microtox indicator strain Vibrio fischeri ATCC 49387

Repeated attempts to clone the luxI from Vibrio fischeri ATCC 49387 failed to produce a clone carrying a functional LuxI. Sequence data from the clones revealed the presence of a polymorphism when compared with previously published luxI sequences, prompting further characterization of bioluminescence regulation in V. fischeri ATCC 49387. Further investigation of V. fischeri ATCC 49387 revealed that its LuxI protein lacks detectable LuxI activity due to the presence of a glutamine residue at position 125 in the deduced amino acid sequence. Specific bioluminescence in V. fischeri ATCC 49387 increases with increasing cell density, indicative of a typical autoinduction response. However, conditioned medium from this strain does not induce bioluminescence in an ATCC 49387 luxR-plux-based acyl homoserine lactone reporter strain, but does induce bioluminescence in ATCC 49387. It has been previously shown that a V. fischeri MJ-1 luxI mutant exhibits autoinduction of bioluminescence through N-octanoyl-L-homoserine lactone, the product of the AinS autoinducer synthase. However, a bioreporter based on luxR-plux from V. fischeri ATCC 49387 responded poorly to conditioned medium from V. fischeri ATCC 49387 and also responded poorly to authentic N-octanoyl-DL-homoserine lactone. A similar MJ-1-based bioreporter showed significant induction under the same conditions. A putative ainS gene cloned from ATCC 49387, unlike luxI from ATCC 49387, expresses V. fischeri autoinducer synthase activity in Escherichia coli. This study suggests that a regulatory mechanism independent of LuxR and LuxI but possibly involving AinS is responsible for the control of autoinduction of bioluminescence in V. fischeri ATCC 49387.     

Batch and fed-batch cultivation for excretive production of human epidermal growth factor (hEGF) with recombinant E. Coli K12 system

Batch and fed-batch production of recombinant human epidermal growth factor (hEGF) was studied in an E. coli secretary expression system. By using MMBL medium containing 5 g/L glucose, controlling the temperature at 32 degrees C and maintaining the dissolved oxgen level over 20% saturation, a high yield of hEGF (32 mg/L) was obtained after an 18 hr batch cultivation with 0.2 mM IPTG induction at mid-log phase. Three different glucose feeding strategies were employed to further improve hEGF productivity in a bench top fermentor. Compared with the batch results, hEGF yield was improved up to 25.5% or 28.1%, respectively by intermittent or pH-stat glucose feeding, and up to 150% improvement of hEGF production was achieved by constant feeding of 200 g/L glucose solution at a rate of 0.11 mL/min. The effects of further combined feeding with other medium components and inducer on hEGF yield were also examined in the benchtop fermentor. This work is very helpful to further improve the productivity of extracellular hEGF in the recombinant E. coli system.     

Improved penicillin amidase production using a genetically engineered mutant of Escherichia coli ATCC 11105

Penicillin G amidase (PGA) is a key enzyme for the industrial production of penicillin G derivatives used in therapeutics. Escherichia coli ATCC 11105 is the more commonly used strain for PGA production. To improve enzyme yield, we constructed various recombinant E. coli HB101 and ATCC 11105 strains. For each strain, PGA production was determined for various concentrations of glucose and phenylacetic and (PAA) in the medium. The E. coli strain, G271, was identified as the best performer (800 U NIPAB/L). This strain was obtained as follows: an E. coli ATCC 11105 mutant (E. coli G133) was first selected based on a low negative effect of glucose on PGA production. This mutant was then transformed with a pBR322 derivative containing the PGA gene. Various experiments were made to try to understand the reason for the high productivity of E. coli G271. The host strain, E. coli G133, was found to be mutated in one (or more) gene(s) whose product(s) act(s) in trans on the PGA gene expression. Its growth is not inhibited by high glucose concentration in the medium. Interestingly, whereas glucose still exerts some negative effect on the PGA production by E. coli G133, PGA production by its transformant (E. coli G271) is stimulated by glucose. The reason for this stimulation is discussed. Transformation of E. coli G133 with a pBR322 derivative containing the Hindlll fragment of the PGA gene, showed that the performance of E. coli G271 depends both upon the host strain properties and the plasmid structure. Study of the production by the less efficient E. coli HB101 derivatives brought some light on the mechanism of regulation of the PGA gene. (c) 1993 John Wiley & Sons, Inc.     

High-level expression of a soluble functional antimicrobial peptide, human beta-defensin 2, in Escherichia coli

In this work, taking human beta-defensin-2 (HBD2) as a demonstrative molecule, the strategies for high efficient production of functional human beta-defensins in E. coli were studied. Fusion mature HBD2 (TrxA-mHBD2) showed high solubility and productivity without the need for lowering the cultivation temperature. The solubility of target fusion protein could attain 81.3% even at 37 degrees C with a volumetric productivity as high as 235 mg/L in a rich medium MBL at the same temperature and reached 346 mg/L at 28 degrees C. The His-Tag in the fusion protein enabled the application of affinity chromatography separation to obtain high purity of the overexpressed recombinant fusion protein. After digestion by enterokinase, purification via cationic exchange chromatography, and desalting by ultrafiltration, mature HBD2 product was obtained with a purity of 95% in an overall recovery of 29.2%. The antimicrobial activity of the recombinant mature HBD2 and the influence factors were tested using E. coli K12D31 as a sensitive strain.     

Cost-effective production of recombinant human interleukin 24 by lactose induction and a two-step denaturing and one-step refolding method

Recombinant human interleukin 24 (rhIL24) is a member of the interleukin 10 (IL10) family of cytokines with novel therapeutic properties. Human IL24 possesses three N glycosylation sites and a disulfide bridge. The cost and composition of culture media is critical for commercial-scale production of recombinant proteins in E. coli. Addition of yeast extract and glucose to medium enhances rhIL24 production, and the use of lactose instead of IPTG for induction drops the cost and decreases toxicity. In addition, a two-step denaturing and one-step refolding (2DR) strategy improves rhIL24 production. The 2DR strategy replaces a more conventional approach for protein solubilization and refolding. LC–MS/MS provides definitive identification and quantitative information on rhIL24. Single-step purified rhIL24 displayed biological activity on HepG2 hepatocellular carcinoma cells, but no effect on L02 cells. Proliferation analysis suggests that rhIL24 may have potential use as a medication. In the present study, we developed a simple process for producing quality product with high purity. The expression and purification of rhIL24 described here may be a step towards inexpensive large-scale production.