Refolding of therapeutic proteins produced in Escherichia coli as inclusion bodies

Overexpression of cloned or synthetic genes in Escherichia coli often results in the formation of insoluble protein inclusion bodies. Within the last decade, specific methods and strategies have been developed for preparing active recombinant proteins from these inclusion bodies. Usually, the inclusion bodies can be separated easily from other cell components by centrifugation, solubilized by denaturants such as guanidine hydrochloride (Gdn-HCl) or urea, and then renatured through a refolding process such as dilution or dialysis. Recent improvements in renaturation procedures have included the inhibition of aggregation during refolding by application of low molecular weight additives and matrix-bound renaturation. These methods have made it possible to obtain high yields of biologically active proteins by taking into account process parameters such as protein concentration, redox conditions, temperature, pH, and ionic strength.     

The refolding, purification, and activity analysis of a rice Bowman-Birk inhibitor expressed in Escherichia coli

A putative rice trypsin/chymotrypsin inhibitor of the Bowman-Birk family, RBBI-8 of about 20 kDa, was expressed in Escherichia coli as a fusion protein bearing an N-terminal (His)6 purification tag. The expressed recombinant protein, rRBBI-8, is insoluble and accumulates as inclusion bodies. The insoluble protein was solubilized in 8 M urea under reducing environment and then refolded into its active conformation under optimized redox conditions. Strategies used to optimize yield and efficiency include selecting the redox system, increasing protein concentration during refolding by adding the denatured protein in a stepwise way, utilizing additives to prevent aggregation, and selecting buffer-exchanging conditions. A Ni-chelate affinity column was then employed to purify the renatured protein. rRBBI-8 shows strong inhibitory activity against trypsin and it can slightly inhibit chymotrypsin. In this study, a refolding and purification system was set up for this cysteine-rich recombinant protein expressed in a prokaryotic system.     

Renaturation of Escherichia coli-derived recombinant human macrophage colony-stimulating factor.

Recombinant human macrophage colony-stimulating factor (rhM-CSF), a homodimeric, disulfide bonded protein, was expressed in Escherichia coli in the form of inclusion bodies. Reduced and denatured rhM-CSF monomers were refolded in the presence of a thiol mixture (reduced and oxidized glutathione) and a low concentration of denaturing agent (urea or guanidinium chloride). Refolding was monitored by nonreducing gel electrophoresis and recovery of bioactivity. The effects of denaturant type and concentration, protein concentration, concentration of thiol/disulfide reagents, temperature, and presence of impurities on the kinetics of rhM-CSF renaturation were investigated. Low denaturant concentrations (<0.5 M urea) and high protein concentrations (>0.4 mg/ml) in the refolding mixture resulted in increased formation of aggregates, although aggregation was never significant even when refolding was carried out at room temperature. Higher protein concentration resulted in higher rates but did not lead to increased yields, due to the formation of unwanted aggregates. Experiments conducted at room temperature resulted in slightly higher rates than those conducted at 4 degrees C. Although the initial renaturation rate for solubilized inclusion body protein without purification was higher than that of the reversed-phase purified reduced denatured rhM-CSF, the final renaturation yield was much higher for the purified material. A maximum refolding yield of 95% was obtained for the purified material at the following refolding conditions: 0.5 M urea, 50 mM Tris, 1.25 mM DTT, 2 mM GSH, 2 mM GSSG, 22 degrees C, pH 8, [protein] = 0.13 mg/ml.     

液胶色谱柱复性在低分子量尿激酶原突变体（DscuPA—32K）中的应用

将构建一种具溶栓和抗栓以重功能尿激酶原突变体（DscuPA-32K)基因,在大肠杆菌中进行表达。由于DscuPA-32K分子较大并且表达量较高,目的的性质基本以包涵体的形式存在。包涵体中的蛋白质是无活性的蛋白质,为了获得有活性的蛋白质,就需要对包涵体进行变性及复性。尝试了一种新的凝胶色谱柱复性方法,并通过柱复性方法与常规的稀释复性方法进行了比较,发现柱复性方法明显优于稀释复性方法,具有成本低,效率高,并对目的的蛋白质（DscuPA-32K)进行了初步纯化等优点,尤其对酶这一类容易失活降解的蛋白质进行复性时,很值得进行推广应用。     

Production of the recombinant human bone morphogenetic protein-2 in Escherichia coli and testing of its biological activity in vitro and in vivo

Bone morphogenetic protein-2 (rhBMP-2) represents the osteoinductive protein factor which plays a dominant role in growth and regeneration of a bone tissue. In clinical practice the bone grafting materials on the basis of rhBMP-2 are widely applied; the Russian analogues of similar materials are not produced. The fragment of the bmp2gene coding for a mature protein was cloned in Escherichia coli. The effective overproducing strain of rhBMP-2 was created on a basis of the E. coli BL21 (DE3). The rhBMP-2 production was about 25% of total cell protein. The biologically active dimeric form of rhBMP-2 was obtained by isolation and purification of protein from inclusion bodies with subsequent refolding. The rhBMP-2 sample with more than 80% of the dimeric form was obtained, which is able to interact with specific antibodies to BMP-2. Biological activity of the received rhBMP-2 samples was shown in the in vitro experiments by induction of alkaline phosphatase synthesis in C2C12 and C3H10T1/2 cell cultures. On model of the ectopic osteogenesis it was shown that received rhBMP-2 possesses biological activity in vivo, causing tissue calcification in the place of an injection. The protein activity in vivo depends on way of protein introduction and characteristics of protein sample: rhBMP-2 may be introduced in an acid or basic buffer solution, with or without the carrier. The offered method of rhBMP-2 isolation and purification results in increasing common protein yield as well as the maintenance of biologically active dimeric form in comparison with the analogues described in the literature.     

Optimized procedure for expression and renaturation of recombinant human bone morphogenetic protein-2 at high protein concentrations

A prokaryotic expression system has been used to produce recombinant human bone morphogenetic protein-2 (rhBMP-2). However, low rhBMP-2 yields and protein loss during purification and renaturation are the hurdles in the clinical application. Previous studies have indicated that variables such as temperature, host cell, salt concentration, and culture time affect the final rhBMP-2 yield. The optimization of these conditions in an Escherichia coli culture yielded 28.258 mg of rhBMP-2 per liter of culture. To reduce rhBMP-2 loss during purification and renaturation, we performed purification before renaturation in the prokaryotic expression system instead of using the traditional renaturation-before-purification approach. rhBMP-2 was separated on a Sephacryl S-300 HR column and eluted from a DEAE-Sepharose Fast Flow column. The collected protein was refolded by dialysis with urea buffer, which was followed by dialysis with ultrapure water. The purified rhBMP-2 dimer significantly increased alkaline phosphatase (ALP) activity and osteogenic activity in the femoral muscle and showed the same level of bone-forming activity as natural BMP-2. This optimized procedure for expression and renaturation of rhBMP-2 has potential clinical applications.     

Effect of operating variables on the yield of recombinant trypsinogen for a pulse-fed dilution-refolding reactor.

The inclusion body process route for manufacturing proteins offers distinct process advantages in terms of expression levels and the ease of initial inclusion body recovery. The efficiency of the refolding unit operation, however, does determine the overall economic feasibility of a process. Dilution refolding is the simplest and most extensively used refolding operation, although significant yield losses often occur due mainly to aggregation. Operating variables may have a significant effect on the degree of aggregation, but a systematic study has not been reported. This study investigates the effect of operating variables on the dilution refolding of solubilized r-trypsinogen inclusion bodies in a pulse-fed stirred reactor. Variables investigated were inclusion body washing, stirring speed, feed rate, concentration of solubilized r-trypsinogen, and concentration of urea during solubilization of the inclusion bodies. Additionally, the effect of baffles in the reactor was investigated. The yield of renatured r-trypsinogen varied between 12 +/- 0.2% and 21 +/- 1.0% depending on the specific combination of operating variables employed. It is clear that a suboptimal operating strategy can significantly reduce protein yield. In particular, we note that an increased intensity of mixing adversely affected yield in contrast to previous reports indicating that enhanced dispersion increases yield. We conclude that yield is determined not only by the efficiency of dispersion, but also by the local chemical environment of the protein as it folds, and the rate of change of this environment. This will be controlled by micromixing effects, and hence the intensity of agitation, in a complex manner requiring further characterization.     

Direct refolding of inclusion bodies using reversed micelles

The protein refolding of inclusion bodies was investigated using reversed micelles formed by aerosol OT (AOT). Ribonuclease A (RNase A) was overexpressed in Escherichia coli and used as native inclusion bodies. The enzymatic activity of RNase A was completely regained from the inclusion bodies within 14 h by solubilization in reversed micelles. To further enhance the refolding rate, a molecular chaperone, GroEL, was incorporated into the refolding system. The resultant refolding system including GroEL showed better performance under optimized conditions for the refolding of RNase A inclusion bodies. The refolding rate was considerably improved by the addition of the molecular chaperone, and the refolding step was completed in 1 h. The protein refolding in the GroEL-containing refolding system was strongly dependent on the coexistence of ATP and Mg2+, suggesting that the GroEL hosted in the reversed micelles was biologically active and assisted in the renaturation of the inclusion bodies. The addition of cold acetone to the reversed micellar solution allowed over 90% recovery of the renatured RNase A.     

Refolding and two-step purification by hydrophobic interaction chromatography of recombinant human bone morphogenetic protein-2 from Escherichia coli

To renature the inactive rhBMP-2 which overexpressed in Escherichia coli, post-expression treatments including inclusion bodies solubilization and in vitro refolding were systematically investigated. An optimized refolding process was established from screening and successfully scaled up with yield greater than 70%. Then, hydrophobic interaction chromatography (HIC) was adopted as two consecutive stages to separate the active rhBMP-2 homodimer from refolding mixture. Aiding additive N,N-dimethylformamide (DMF) was found to enhance the resolution of rhBMP-2 homodimer most effectively. The rhBMP-2 homodimer was purified to homogeneity through two HIC separations at different salt contents, the purified rhBMP-2 homodimer was fully bioactive and had equivalent biological activity to rhBMP-2 produced from Chinese hamster ovary cell (CHO). Under the optimal refolding and purification conditions, 80 mg rhBMP-2 homodimer with high purity could be obtained from 1 g wet weight of inclusion bodies. Finally, this efficient refolding and purification procedure was successfully scaled up in the pilot pharmaceutical plant.     

Renaturation of human proinsulin--a study on refolding and conversion to insulin

The production of human proinsulin in Escherichia coli usually leads to the formation of inclusion bodies. As a consequence, the recombinant protein must be isolated, refolded under suitable redox conditions, and enzymatically converted to the biologically active insulin. In this study we describe a detailed in vitro renaturation protocol for human proinsulin that includes native structure formation and the enzymatic conversion to mature insulin. We used a His(8)-Arg-proinsulin that was renatured from the completely reduced and denatured state in the presence of a cysteine/cystine redox couple. The refolding process was completed after 10-30 min and was shown to be strongly dependent on the redox potential and the pH value, but not on the temperature. Refolding yields of 60-70% could be obtained even at high concentrations of denaturant (3M guanidinium-HCl or 4M urea) and protein concentrations of 0.5mg/ml. By stepwise renaturation a concentration of about 6 mg/ml of native proinsulin was achieved. The refolded proinsulin was correctly disulfide-bonded and native and monomeric as shown by RP-HPLC, ELISA, circular dichroism, and analytical gel filtration. Treatment of the renatured proinsulin with trypsin and carboxypeptidase B yielded mature insulin.     

Oxidative renaturation of lysozyme at high concentrations

Newly synthesized cloned gene proteins expressed in bacteria frequently accumulate in insoluble aggregates or inclusion bodies. Active protein can be recovered by solubilization of inclusion bodies followed by renaturation of the solubilized (unfolded) protein. The recovery of active protein is highly dependent on the renaturation conditions chosen. The renaturation process is generally conducted at low protein concentrations (0.01-0.2 mg/mL) to avoid aggregation. We have investigated the potential of successfully refolding reduced and denatured hen egg white lysozyme at high concentrations (1 and 5 mg/mL). By varying the composition of the renaturation media, optimum conditions which kinetically favor proper folding over inactivation were found. Solubilizing agents such as guanidinium chloride (GdmCl) and folding aids such as L-arginine present in low concentrations during refolding effectively enhanced renaturation yields by suppressing aggregation resulting in reactivation yields as high as 95%. Quantitatively the kinetic competition between lysozyme folding and aggregation can be described using first-order kinetics for the renaturation reaction and third-order kinetics for the overall aggregation pathway. The rate constants for both reactions have been found to be strongly dependent on denaturant and thiol concentration. This strategy supercedes the necessity to reactivate proteins at low concentrations using large renaturation volumes. The marked increase in volumetric productivity makes this a viable option for recovering biologically active protein efficiently and in high yield in vitro from proteins produced as inclusion bodies within microbial cells. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 221-230, 1997.     

<Emphasis Type="SmallCaps">l</Emphasis>-Arginine Suppresses Aggregation of Recombinant Growth Hormones in Refolding Process from <Emphasis Type="Italic">E. coli</Emphasis> Inclusion Bodies

l-Arginine was used to suppress the aggregation of recombinant mink and porcine growth hormones in the refolding process from E. coli inclusion bodies by solubilization–dilution protocol at high protein concentration and pH 8.0. The influence of l-arginine concentration on the renaturation yield of both proteins was investigated. l-Arginine effectively suppressed the precipitation of growth hormones during dilution, but did not inhibit soluble oligomers formation. The results of mink and porcine growth hormones purification from 4 g of biomass are presented.     

Important parameters affecting efficiency of protein refolding by reversed micelles

Refolding of denatured RNase A as a model of inclusion bodies was performed by reversed micelles formulated with sodium di-2-ethylhexyl sulfosuccinate (AOT) in isooctane. In the novel refolding process, a solid-liquid extraction was utilized as an alternative to the ordinary protein extraction by reversed micelles based on a liquid-liquid extraction. First, the effects of operational parameters such as concentration of AOT, W(o) (= [H(2)O]/[AOT]), and pH were examined on the solubilization of solid denatured proteins into a reversed micellar solution. The solubilization was facilitated by a high AOT concentration, a high W(o) value, and a high pH in water pools. These conditions are favorable for the dispersion of the solid protein aggregates in an organic solvent. Second, the renaturation of the denatured RNase A solubilized into the reversed micellar solution was conducted by addition of glutathione as a redox reagent. A complete renaturation of RNase A was accomplished by adjusting the composition of the redox reagent even at a high protein concentration in which protein aggregation would usually occur in aqueous media. In addition, the renaturation rates were improved by optimizing water content (W(o)) and the pH of water pools in reversed micelles. Finally, the recovery of renatured RNase A from the reversed micellar solution was performed by adding a polar organic solvent such as acetone into the reversed micellar solution. This precipitation method was effective for recovering proteins from reversed micellar media without any significant reduction in enzymatic activity.     

尖吻蝮蛇毒酸性磷脂酶A_2I的表达及其生化特征

将尖吻蝮蛇毒酸性磷脂酶 Ａ２ Ｉ（ Ａ．ａ Ａ Ｐ Ｌ Ａ２ Ｉ） 的基因克隆至表达载体ｐ Ｂ Ｌ Ｍ Ｖ Ｌ２ , 在大肠杆菌 Ｒ Ｒ１ 中成功表达。表达产物 Ａ．ａ Ａ Ｐ Ｌ Ａ２ Ｉ约占细菌蛋白质总量的３０ ％ , 以包含体的形式存在。纯化包含体后, 将产物变性、复性, 然后用 Ｆ Ｐ Ｌ Ｃ Ｓｕｐｅｒｏｓｅ Ｔ Ｍ１２ 纯化, 产物经过 Ｓ Ｄ Ｓ Ｐ Ａ Ｇ Ｅ 检测只有单一条带。对表达的 Ａ．ａ Ａ Ｐ Ｌ Ａ２ Ｉ进行了酶活性、抑制血小板聚集活性和溶血活性的测定。结果显示, 表达的 Ａ．ａ Ａ Ｐ Ｌ Ａ２ Ｉ的酶活性同变性后复性江浙蝮蛇酸性磷脂酶 Ａ２（ Ａ Ｐ Ｌ Ａ２） 的酶活性相近, 既具有抑制血小板聚集活性也具有溶血活性。最后对磷脂酶 Ａ２（ Ｐ Ｌ Ａ２） 的结构与这些活性的关系进行了讨论     

EXPRESSION AND PURIFICATION OF RECOMBINANT HUMAN BONE MORPHOGENETIC PROTEIN-7 IN Escherichia coli

Bone morphogenetic protein-7 (BMP-7) is a multifunctional cytokine of the transforming growth factor β superfamily, which induces bone formation and plays an important role during bone tissue repair and embryonic development. In this study, human BMP-7 (hBMP-7) cDNA was cloned and expressed in Escherichia coli, and its yield was approximately 30% of the total bacterial protein. After the bacteria were lysed by ultrasonication and repeated washing, inclusion bodies were extracted and dissolved using a high-strength denaturant. The monomer of rhBMP-7 was purified by ion-exchange chromatography, and the purity coefficient was approximately 96%. The protein was renatured with refolding buffers at different pH values. The renatured rhBMP-7 dimer protein in this study increased the alkaline phosphatase activity of NIH3T3 cells. This study may be helpful for the in vitro production and biomedical application of rhBMP-7 protein expressed in an E. coli expression system.     

尖吻蝮蛇毒酸性磷脂酶A_2Ⅱ的表达及其生化特征

将尖吻蝮蛇毒酸性磷酯酶 A2 ( A.a APLA2 )基因克隆至温敏表达载体 p BLMVL2 ,在大肠杆菌 RR1中成功诱导表达 .表达产物 A.a APLA2 约占细菌蛋白质总量 2 5 % ,并以包涵体形式存在 .纯化包涵体后 ,将产物变性、复性 ,然后用 FPLC Superose TM1 2纯化 ,产物经过 SDS- PAGE检测只有单一条带 .对纯化后的表达 A.a APLA2 进行了酶活性、抑制血小板聚集活性和溶血活性的测定 .结果显示 ,A.a APLA2 的酶活性处于变性后复性江浙蝮蛇酸性磷脂酶 A2 和碱性磷脂酶A2 的酶活性之间 ,没有抑制血小板聚集活性 ,只有微弱溶血活性 .最后对 PLA2 的结构与这些活性的关系进行了讨论     

Refolding of protein inclusion bodies directly from E. coli homogenate using expanded bed adsorption chromatography

To avoid the intrinsic problem of aggregation associated with the traditional solution-phase refolding process, we proposed a solid-phase refolding method integrated with the expanded bed adsorption chromatography. The model protein was a fusion protein of recombinant human growth hormone and a glutathione S-transferase fragment. It was demonstrated that the inclusion body proteins in the cell homogenate could be directly refolded with higher yield. To verify the applicability of this method, we have tested with success three types of the starting materials, i.e., rhGH monomer, inclusion bodies containing the fusion protein, and the E. coli cell homogenate. This direct refolding process could reduce the number of the renaturation steps required and allow the refolding at a higher concentration, approximately 2 mg fusion protein per ml resin. This revised version was published online in July 2006 with corrections to the Cover Date.     

尖吻蝮蛇毒碱性磷脂酶A2的表达及其生化特征

将尖吻蝮蛇毒碱性磷脂酶A2 (A .aBPLA2 )基因克隆至温敏表达载体 pBLMVL2 ,在大肠杆菌RR1中成功诱导表达 .表达产物A .aBPLA2 约占细菌蛋白质总量的 2 0 % ,并以包涵体的形式存在 .纯化包涵体后 ,将产物变性、复性 ,然后用FPLCSuperoseTM12纯化 ,产物经过SDS 聚丙烯酰胺凝胶电泳检测只有单一条带 .对纯化后的表达A .aBPLA2 进行了酶活性、抑制血小板聚集活性和溶血活性的测定 .结果显示 ,表达A .aBPLA2的酶活性与变性后复性江浙蝮蛇酸性磷脂酶A2 酶活性相近 ,具有类似变性后复性江浙蝮蛇碱性磷脂酶A2 的溶血活性 ,没有抑制血小板聚集活性 .最后对磷脂酶A2 的结构与这些活性的关系进行了讨论     

Renaturation of recombinant ErmSF and its refolding behavior

ErmSF is one of four gene products responsible for the resistance of Streptomyces fradiae to the autogenous antibiotic, tylosin. It catalyzes the methylation of a single adenine residue (A2058) of 23S rRNA to produce dimethyl adenine from monomethyl adenine or unmodified adenine. This reduces the affinity of macrolide-lincosamide-streptogramin B (MLS) antibiotics for the peptidyltransferase circle and confers resistance to these antibiotics. We earlier cloned ermSF from Streptomyces fradiae, ligated it into pET23b with a T7 promoter and transformed it into E. coli. The transformants were resistant to erythromycin, but most of the expressed protein was present as an inclusion body. In the present work, the protein was extracted from the inclusion bodies, solubilized with 6 M guanidine-HCl, and purified by metal ion (Ni2+) affinity chromatography yielding 171 mg of denatured protein per liter of culture. Renaturation of the protein was achieved by step-wise removal of the guanidine-HCl. Most of the refolded protein appeared to assume the natural conformation, as judged by circular dichroism spectroscopy. The yield of refolded protein increased as the protein concentration in the renaturation medium was lowered, but the activity of the renatured protein tended to increase with protein concentration. The highest yield of renatured protein, 107 mg/L of culture had 55% of the activity of the naturally folded protein. Refolding was also carried out by removing denaturant by a simple two-step dilution-dialysis method. With that method, the yield of the refolded protein was lower and the activity higher than with step-wise refolding. The yields and activities did not seem to be affected by the concentration of denaturant, suggesting that renaturation under the conditions employed occurred spontaneously with a strong tendency to fold to the native state, even though ErmSF contains two domains.     

重组羧肽酶原B的复性方法研究

构建的羧肽酶原B表达质粒在大肠杆菌中获得高表达。但目的蛋白是以包涵体的形式存在。为了获得活性羧肽酶B,必须对其包涵体进行变复性。首先利用稀释复性确定了羧肽酶原B复性的最佳缓冲液;在凝胶过滤复性中,研究了柱长和洗脱流速对羧肽酶原B复性效率的影响;另外对比了稀释复性、透析复性、凝胶层析复性和Ni2 亲合层析法等四种方法对羧肽酶原B的复性效果。结果发现,这4种方法的复性效果有以下顺序:凝胶过滤复性>稀释复性>Ni2 亲合层析>透析复性。