On-line monitoring of IPTG induction for recombinant protein production using an automatic pH control signal

The response of IPTG induction was investigated through the monitoring of the alkali consumption rate and buffer capacity during the cultivation of recombinantE. coli BL21(DE3) harboring the plasmid pRSET-LacZ under the control oflac promoter. The rate of alkali consumption increased along with cell growth, but declined suddenly after approximately 0.2 h of IPTG induction. The buffer capacity also declined after 0.9 h of IPTG induction. The profile of buffer capacity seems to correlate with the level of acetate production. The IPTG response was monitored only when introduced into the mid-exponential phase of bacterial cell growth. The minimum concentration of IPTG for induction, which was found out to be 0.1 mM, can also be monitored on-line andin-situ. Therefore, the on-line monitoring of alkali consumption rate and buffer capacity can be an indicator of the metabolic shift initiated by IPTG supplement, as well as for the physiological state of cell growth.     

Synthesis of recombinant human interleukin-2 via controlled feed of lactose-complex media in fed-batch cultures of Escherichia coli BL21(DE3)[pT7-G3IL2]

Using lactose as an inducer, recombinant human interleukin-2 (rhIL-2) was synthesized with an N-terminus fusion partner, G3 (three tandem-arranged glucagon peptides) in fed-batch cultures at high cell concentration (60–90 g l^–1) of Escherichia coli BL21(DE3) [pT7-G3IL2]. With batch additions of lactose (4 × 13.5 g), the fusion rhIL-2 was synthesized up to 9.3 g l^–1. However, if all the lactose (54 g) was added at once to the culture, synthesized fusion rhIL-2 decreased to 5.4 g l^–1 with a decreased cell growth rate. A statistical optimization of the production medium containing glucose, yeast extract, and lactose led to fusion rhIL-2 being produced at > 9 g l^–1.     

Optimization of an extracellular zinc-metalloprotease (SVP2) expression in Escherichia coli BL21 (DE3) using response surface methodology

In this work, SVP2 from Salinivibrio proteolyticus strain AF-2004, a zinc metalloprotease with suitable biotechnological applications, was cloned for expression at high levels in Escherichia coli with the intention of changing culture conditions to generate a stable extracellular enzyme extract. The complete ORF of SVP2 gene was heterologously expressed in E. coli BL21 (DE3) by using pQE-80L expression vector system. In initial step, the effect of seven factors include: incubation temperature, peptone and yeast extract concentration, cell density (OD600) before induction, inducer (IPTG) concentration, induction time, and Ca(2+) ion concentrations on extracellular recombinant SVP2 expression and stability were investigated. The primary results revealed that the IPTG concentration, Ca(2+) ion concentration and induction time are the most important effectors on protease secretion by recombinant E. coli BL21. Central composite design experiment in the following showed that the maximum protease activity (522 U/ml) was achieved in 0.0089 mM IPTG for 24h at 30 °C, an OD600 of 2, 0.5% of peptone and yeast extract, and a Ca(2+) ion concentration of 1.3 mM. The results exhibited that the minimum level of IPTG concentration along with high cell density and medium level of Ca(2+) with prolonged induction time provided the best culture condition for maximum extracellular production of heterologous protease SVP2 in E. coli expression system.     

Production of recombinant bacteriocin divercin V41 by high cell density <Emphasis Type="Italic">Escherichia coli</Emphasis> batch and fed-batch cultures

To increase the yield of heterologous production of the class II bacteriocin DvnRV41 with Escherichia coli Origami (DE3) (pLysS/pCR03), induction of bacteriocin gene expression was optimized by varying the inducer isopropyl beta-D-thiogalactopyranoside (IPTG) concentration (0-2 mM), and controlled batch and fed-batch cultures were tested on a 2-L scale. A concentration of 0.5 mM IPTG was found to be optimal for cell growth and bacteriocin production. Shake flask cultivation of E. coli Origami (DE3) (pLysS/pCR03) gave biomass and bacteriocin yields of 1.54 +/- 0.06 g cdw/l and 18 +/- 1 mg DvnRV41/l, respectively. Biomass (2.70 +/- 0.06 and 6.8 +/- 0.6 g cdw/l, respectively) and bacteriocin yields (30 and 74 mg DvnRV41 per liter, respectively) were both increased with batch and fed-batch compared to shake flask cultures. Bacteriocin yields reported in this study are among the highest published for other heterologous expression systems in shake flasks.     

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。     

IPTG limitation avoids metabolic burden and acetic acid accumulation in induced fed-batch cultures of Escherichia coli M15 under glucose limiting conditions

The most common strategy to produce recombinant proteins using Escherichia coli as expression vector is fed-batch culture, since high cell density cultures strategies have successfully been applied. Several methodologies to limit the specific growth rate in order to control E. coli metabolism have been defined, demonstrating that cultures can be grown under glucose limitation up to high cell densities without accumulation of acetic acid. However, under induction conditions it has been observed that E. coli metabolism is reorganized again and leads to acetic acid accumulation, causing inhibition of cell growth and decreasing protein expression efficiency.We propose a double limitation strategy (glucose and IPTG) for E. coli fed-batch cultures to avoid the deregulation of the metabolism in the induction phase. Reducing the concentration of IPTG while keeping glucose growth limitation, the accumulation of acetic acid decreased. At an IPTG concentration of 0.03 mmol/g DCW no accumulation of acetic acid was observed during the induction phase, in contraposition to what has normally been observed.Although a slight reduction of protein expression rate was observed when applying this double limitation strategy, the bioprocess volumetric productivity was enhanced due to the capability to prolong the induction phase, reaching higher levels of protein production. Another advantage of this strategy is the reduction of media cost due to the lower level of IPTG used.     

High cell density cultivation of <Emphasis Type="Italic">Escherichia coli</Emphasis> with surface anchored transglucosidase for use as whole-cell biocatalyst for α-arbutin synthesis

A fed-batch culture strategy for the production of recombinant Escherichia coli cells anchoring surface-displayed transglucosidase for use as a whole-cell biocatalyst for α-arbutin synthesis was developed. Lactose was used as an inducer of the recombinant protein. In fed-batch cultures, dissolved oxygen was used as the feed indicator for glucose, thus accumulation of glucose and acetate that affected the cell growth and recombinant protein production was avoided. Fed-batch fermentation with lactose induction yielded a biomass of 18 g/L, and the cells possessed very high transglucosylation activity. In the synthesis of α-arbutin by hydroquinone glucosylation, the whole-cell biocatalysts showed a specific activity of 501 nkat/g cell and produced 21 g/L of arbutin, which corresponded to 76% molar conversion. A sixfold increased productivity of whole cell biocatalysts was obtained in the fed-batch culture with lactose induction, as compared to batch culture induced by IPTG.     

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。     

Enhanced production of recombinant streptokinase in Escherichia coli using fed-batch culture

Fed-batch culture strategy is often used for increasing production of heterologous recombinant proteins in Escherichia coli. This study was initiated to investigate the effects of dissolved oxygen concentration (DOC), complex nitrogen sources and pH control agents on cell growth and intracellular expression of streptokinase (SK) in recombinant E. coli BL21(DE3). Increase in DOC set point from 30% to 50% did not affect SK expression in batch culture where as similar increase in fed-batch cultivation led to a significant improvement in SK expression (from 188 to 720 mg l⁻¹). This increase in SK could be correlated with increase in plasmid segregational stability. Supplementation of production medium with yeast extract and tryptone and replacement of liquid ammonia with NaOH as pH control agent further enhanced SK expression without affecting cell growth. Overall, SK concentration of 1120 mg l⁻¹ representing 14-fold increase in SK production on process scale-up from flask to bioreactor scale fed-batch culture is the highest reported concentration of SK to date.     

Production of recombinant β-galactosidase in bioreactors by fed-batch culture using DO-stat and linear control

β-Galactosidase enzymes continue to play an important role in food and pharmaceutical industries. These enzymes hydrolyze lactose in its constituent monosaccharides, glucose and galactose. The industrial use of enzymes presents an increase in process costs reflecting in higher final product value. An alternative to enhance processes’ productivity and yield would be the use of recombinant enzymes and their large-scale fed-batch production. The overexpression of recombinant β-galactosidase from Kluyveromyces sp. was carried out in 2-L bioreactors using Escherichia coli strain BL21 (DE3) as host. Effect of induction time on recombinant enzyme expression was studied by adding 1?mM isopropyl thiogalactoside (IPTG) at 12?h, 18?h and 24?h of cultivation. Glucose feeding strategies were compared employing feedback-controlled DO-stat and ascendant linear pump feeding in bioreactor fed-batch cultivations. Linear feeding strategy with IPTG addition at 18?h of cultivation resulted in approximately 20?g/L and 17,745?U/L of biomass and β-galactosidase activity, respectively. On the other hand, although the feedback-controlled DO-stat feeding strategy induced at 12?h of cultivation led to lower final biomass of 18?g/L, it presented an approximately 2.5 increase in enzymatic activity, resulting in 42,367?U/L, and most importantly it led to the most prominent specific enzymatic activity of approximately 40?U/mg_protein. Comparing to previous results, these results suggest that the DO-stat feeding is a promising strategy for recombinant β-galactosidase enzyme production.     

argE基因在大肠杆菌中的表达优化

N-乙酰鸟氨酸脱酰基酶可在重组菌BL21（DE3）-pET22b-argE中表达。首先确定了该酶的细胞表达定位,再研究了诱导温度、诱导剂种类及浓度、诱导起始菌体密度、诱导时间等因素对重组菌生长及目的蛋白表达活性的影响。结果表明,IPTG和乳糖皆可诱导目的蛋白表达,乳糖的诱导效果优于IPTG。在诱导起始0D600为0．46时加入15g／L乳糖,20℃诱导18h最适于目的蛋白的活性表达。表达条件优化后,酶活从1．68U／mL提高至282．99U／mL,约为原来的168倍。     

Influences of yeast extract on specific cellular yield of Ovine growth hormone during fed-batch fermentation of E. coli

In most cases of E. coli high cell density fermentation process, maximizing cell concentration helps in increasing the volumetric productivity of recombinant proteins usually at the cost of lower specific cellular protein yield. In this report, we describe a process for maintaining the specific cellular yield of Ovine growth hormone (oGH) from E. coli by optimal feeding of yeast extract during high cell density fermentation process. Recombinant oGH was produced as inclusion bodies in Escherichia coli. Specific cellular yield of recombinant oGH was maintained by feeding yeast extract along with glucose during fed-batch fermentation. Glucose to yeast extract ratio of 0.75 was found to be optimum for maintaining the specific cellular oGH yield of 66 mg/g of E. coli cells. Continuous feeding of yeast extract along with glucose helped in reducing acetic acid secretion and promoted higher cell growth during fed-batch fermentation. High cell growth of E. coli and high specific yield of recombinant oGH thus helped in achieving high volumetric productivity of the expressed protein. A maximum of 2 g/l of ovine growth hormone was expressed as inclusion bodies in 12 h of fed-batch fermentation.     

乳糖诱导木聚糖酶基因在大肠杆菌中的可溶性表达

以构建好的大肠杆菌工程菌BL21(DE3)/xylanase为研究对象,研究了以IPTG和乳糖作为诱导剂时重组蛋白的表达规律。在摇瓶发酵条件下研究了诱导剂浓度、诱导时机、诱导培养时间和诱导培养温度对目标蛋白表达的影响。实验结果表明,乳糖作为诱导剂时,重组菌产酶活力33.9 U/mg略高于IPTG作为诱导剂时重组菌产酶活力28.10 U/mg,这为乳糖作为诱导剂应用于重组大肠杆菌生产木聚糖酶提供了参考依据。     

High-level production of recombinant human IFN-α2a with co-expression of tRNAArg(AGG/AGA) in high-cell-density cultures ofEscherichia coli

The co-expression of theargU gene in a double-vector expression system of recombinantEscherichia coli BL21(DE3)[pET-IFN2a+pAC-argU] significantly enhanced the production level of recombinant human interferon-α2a (rhIFN-α2a) in high cell density cultures compared to a recombinantE coli culture containing only the single expression vector, pET-IFN2a. The dry cell mass concentration increased to almost 100 g/L, and more than 4 g/L of rhIFN-α2a was accumulated in the culture broth. Evidently, the synthesis of rhIFN-α2a was strongly dependent on the pre-induction growth rate and more efficient at a higher specific growth rate. The additional supply of tRNA^Arg(AGG/AGA) enhanced the expression level of the rhIFN-α2a gene in the early stage of the post-induction phase, yet thereafter the specific production rate of rhIFN-α2a rapidly decreased due to severe segregational instability of plasmid vector pET-IFN2a. It would appear that the plasmid instability, which only occurred to pET-IFN2a in the double vector system, was related to the effect of translational stress due to the overexpression of rhIFN-α2a.     

重组大肠杆菌产Streptomyces sp. FA1来源木聚糖酶的摇瓶发酵优化

为了实现来源于Streptomyces sp. FA1的木聚糖酶的高效胞外分泌表达,对E.coli BL21(DE3)/pET20b(+)/coe/xynA基因工程菌的发酵产酶诱导条件进行优化,获得最优的诱导条件为25 ℃发酵6 h后添加终浓度为0.4 mmol/L的IPTG。在此基础上对发酵培养基进一步优化,得到最优培养基成分为:甘油11 g/L,酵母粉24 g/L,蛋白胨8 g/L,磷酸盐浓度89 mmol/L,镁离子4 mmol/L。最终酶活达到780.2 U/ml,为未优化前的2.2倍,是目前大肠杆菌摇瓶发酵产木聚糖酶的最高表达水平,为实现该酶的工业化生产奠定基础。     

乳糖代替IPTG诱导己糖激酶在大肠杆菌中的表达

构建了己糖激酶GLK高效表达的工程菌株BL21(DE3)/pET-glk,考察了乳糖代替IPTC诱导己糖激酶GLK在大肠杆菌BL21(DE3)中表达的可行性.实验结果表明,工程菌对数生长中期(OD<,600>约为1.0)添加终浓度为10 g/L的乳糖于25℃的条件下诱导6 h能获得最大量的目的蛋白和菌体量,目的蛋白表达...     

抗菌肽Adenoregulin基因工程菌培养条件的优化及分批发酵研究

denoregulin（ADR）是来源于南美树蛙Phyllomedusa bicolor皮肤的含有33个氨基酸的抗菌肽,在非极性环境中形成α_螺旋型结构,具有抗菌活性强、抗菌谱广的特点。将ADR基因克隆于pET32a载体上,转化大肠杆菌BL21(DE3),对这一工程菌株的培养条件进行了优化。通过正交试验,考察诱导时机、诱导剂量和诱导时间三个因素的不同水平对蛋白表达的影响,结果发现诱导时机的影响尤为显著,考察了9种不同培养基对表达量的影响,发现培养基中加入葡萄糖对目标蛋白的稳定表达起了重要的作用,确定最佳培养条件为：培养基为2×YT+0.5%葡萄糖,诱导时机为OD600=0.9左右,诱导剂IPTG加入的终浓度为0.1mmol/L,诱导时间为4h。采用前期恒pH、后期指数流加的策略进行工程菌BL21(DE3)/pET32a-adr的高密度培养,在整个流加过程中,通过控制葡萄糖的加入量,将菌株的比生长速率控制在015h^-1,乙酸浓度也被控制在较低的水平(<2g/L),但是质粒丢失严重,在发酵结束时,约有40%的大肠杆菌中不带质粒,这导致了目标蛋白的表达量下降严重,但是表达的目标蛋白90%以上为可溶性形式。表达的融合蛋白无抑菌活性,而裂解后得到的ADR单体具有明显的抑菌活性。     

Batch and Fed-Batch Cultivation for Excretive Production of Human Epidermal Growth Factor (hEGF) with Recombinant E. Coli K12 System

Abstract

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°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.     

Down regulation of gyrase A gene expression in E. coli by antisense ribozymes using RT-PCR

Nucleic acid-based gene interference technologies represent promising strategies for specific inhibition of mRNA sequences of choice. Recently, small interfering RNAs have been implicated in inducing endogenous RNase of the RNA-induced silencing complex in the RNA interference pathway to inhibit gene expression and growth of several human viruses. We report down regulation of gene expression of E. coli gyrase A, an essential gene for DNA supercoiling and antibiotic susceptibility in BL21 (DE3) strain of E. coli, using Ribonuclease P based external guide sequence (EGS) technique. EGS directed against gyrase A gene that was cloned into pUC vector, which contains the ampicillin (Amp) resistance gene. The recombinant plasmid pT7EGyrA was transformed into BL21 (DE3) and inductions were performed using IPTG. RT-PCR experiment was done to investigate the down regulation of gyrase A gene. RT-PCR results demonstrated a significant decrease of gyrase A gene after 18 h of induction of the transformants. These experiments showed that the down regulation of the gene was seen after 18 h of induction than earlier hours of induction with IPTG suggesting inhibition of gyrase A gene with profound effect on cell viability. These results demonstrate the utility of EGS RNAs in gene therapy applications, by inhibiting the expression of essential proteins.     

Optimizing recombinant protein expression via automated induction profiling in microtiter plates at different temperatures

Background

Escherichia coli (E. coli) is the most abundant expression host for recombinant proteins. The production efficiency is dependent on a multitude of parameters. Therefore, high-throughput applications have become an increasingly frequent technique to investigate the main factors. Within this study, the effects of temperature, induction time and inducer concentration on the metabolic state and the product formation were extensively examined. Induction profiling of E. coli Tuner(DE3) pRhotHi-2-EcFbFP was performed in 48-well Flowerplates and standard 96-well plates using a robotic platform. In parallel shake flask cultivations, the respiration activity of the microorganisms was analyzed. Therefore, two online-monitoring systems were applied: the BioLector for microtiter plates and the RAMOS-device for shake flasks. The impact of different induction conditions on biomass and product formation as well as on the oxygen transfer rate was surveyed.

Results

Different optimal induction conditions were obtained for temperatures of 28, 30, 34, and 37 °C. The best inducer concentrations were determined to be between 0.05 and 0.1 mM IPTG for all investigated temperatures. This is 10–20 times lower than conventional guidelines suggest. The induction time was less relevant when the correct inducer concentration was chosen. Furthermore, there was a stronger impact on growth and respiration activity at higher temperatures. This indicated a higher metabolic burden. Therefore, lower IPTG concentrations were advantageous at elevated temperatures. Very similar results were obtained in standard 96-well plates.

Conclusion

Two online-monitoring systems were successfully used to investigate the optimal induction conditions for the E. coli Tuner(DE3) pRhotHi-2-EcFbFP strain (lacY deletion mutant) at four different temperatures. The experimental effort was reduced to a minimum by integrating a liquid handling robot. To reach the maximum product formation, a detailed induction analysis was necessary. Whenever the cultivation temperature was changed, the induction conditions have to be adapted. Due to the experimental options provided by the BioLector technology, it was found that the higher the cultivation temperature, the lower the inducer concentration that has to be applied.