His-tag purification, dialysis, and activation are employed to increase yields of soluble, active matrix metalloproteinase-3 catalytic domain protein expression in bacteria. Protein fractions are analyzed via SDS-PAGE gels.
方法文章
* These authors contributed equally
His-tag purification, dialysis, and activation are employed to increase yields of soluble, active matrix metalloproteinase-3 catalytic domain protein expression in bacteria. Protein fractions are analyzed via SDS-PAGE gels.
Matrix metalloproteinases (MMPs) belong to the family of metzincin proteases with central roles in extracellular matrix (ECM) degradation and remodeling, as well as interactions with several growth factors and cytokines. Overexpression of specific MMPs is responsible in several diseases such as cancer, neurodegenerative diseases, and cardiovascular disease. MMPs have been the center of attention recently as targets to develop therapeutics that can treat diseases correlated to MMP overexpression.
To study the MMP mechanism in solution, more facile and robust recombinant protein expression and purification methods are needed for the production of active, soluble MMPs. However, the catalytic domain of most MMPs cannot be expressed in Escherichia coli (E. coli) in soluble form due to lack of posttranslational machinery, whereas mammalian expression systems are usually costly and have lower yields. MMP inclusion bodies must undergo the tedious and laborious process of extensive purification and refolding, significantly reducing the yield of MMPs in native conformation. This paper presents a protocol using Rosetta2(DE3)pLysS (hereafter referred to as R2DP) cells to produce matrix metalloproteinase-3 catalytic domain (MMP-3cd), which contains an N-terminal His-tag followed by pro-domain (Hisx6-pro-MMP-3cd) for use in affinity purification. R2DP cells enhance the expression of eukaryotic proteins through a chloramphenicol-resistant plasmid containing codons normally rare in bacterial expression systems. Compared to the traditional cell line of choice for recombinant protein expression, BL21(DE3), purification using this new strain improved the yield of purified Hisx6-pro-MMP-3cd. Upon activation and desalting, the pro domain is cleaved along with the N-terminal His-tag, providing active MMP-3cd for immediate use in countless in vitro applications. This method does not require expensive equipment or complex fusion proteins and describes rapid production of recombinant human MMPs in bacteria.
Most complex eukaryotic proteins undergo elaborate posttranslational modifications after expression, requiring highly assisted protein folding and co-factors to be functional1. Producing large amounts of soluble human protein in a bacterial host remains a significant challenge due to high costs and the lack of robust expression and purification methods, even for smaller-scale laboratory experiments2,3. MMPs, human endopeptidases with large molecular weight, are usually expressed as insoluble inclusion bodies when expressed in E. coli. Extraction of soluble human MMPs often leads to a laborious, time-consuming solubilization and refolding process4.
MMPs have critical roles in both physiological and pathogenic processes. Human MMPs are a family of 23 zinc endopeptidases, categorized by structure and substrate specificity, and differentially expressed in spite of a highly conserved catalytic domain5,6. MMPs are secreted as inactive zymogens, regulated via posttranslational activation and their endogenous inhibitors, tissue inhibitors of metalloproteinases (TIMPs)7,8,9,10. Though initially recognized for their role in ECM turnover, MMPs have also been implicated in development, morphogenesis, tissue repair, and remodeling8. Dysregulation of MMPs has been notably linked to cancer along with neurodegenerative, cardiovascular, and fibrotic diseases, among other illnesses5,7.
The development of robust large-scale MMP production methods is critical to ensure the success of future studies of MMP mechanisms through biochemical and cell-based assays. Various MMPs have been previously expressed in bacteria11, including Hisx6-tagged MMPs, without altering MMP activity12,13,14,15. However, these methods include tedious, long steps that might be difficult to replicate.
Mammalian cells can also be used to express many different human proteins while ensuring the proper posttranslational modifications16. Although the mammalian expression system is an ideal choice to produce recombinant human proteins with proper post-translational modifications, the main disadvantages of this method are initial low yields, costly growth media and reagents, long timelines to reach stable expression lines, and risk of contamination with other species such as fungi or bacteria2,11. Moreover, MMP production in mammalian cell lines yields impurities from associated cellular proteins such as TIMPs or fibronectins11. Unlike the slow cell growth observed in mammalian cells, the bacterial expression system offers large-scale protein production in a short period along with simpler media and growth requirements. However, due to the lack of other associated cellular proteins (i.e., TIMPs) in bacterial expression systems, active MMPs at higher concentrations are subject to degradation through autoproteolysis, resulting in poor MMP yield17.
This paper describes a detailed method for bacterial expression, purification, and activation of recombinant Hisx6-pro-MMP-3cd using E. coli as an expression host due to its affordability, simplicity, and success in producing higher yields of MMPs2,3,18. Since E. coli lacks the protein folding machinery and posttranslational processing required for recombinant MMPs and other complex proteins, many E. coli strains have been engineered to overcome these limitations, making E. coli a more suitable host for expression of recombinant human MMP-3cd,19,20. For instance, the R2DP strain used in this study enhances eukaryotic expression by supplying a chloramphenicol-resistant plasmid containing codons rarely used in E. coli.
As described in this protocol, after overexpression of relatively pure inclusion bodies from the pET-3a vector (Figure 1) in R2DP cells, Hisx6-pro-MMP-3 catalytic domain (MMP-3cd) proteins are extracted and denatured4. Hisx6-pro-MMP-3cd3,19 was purified using affinity tag chromatography. Upon refolding and dialysis, the pro-MMP-3cd (zymogen) was activated by 4-aminophenylmercuric acetate (APMA), and SDS-PAGE analysis is used to evaluate yields and the need for further purification5,21. This protocol describes expression, purification, and activation of soluble MMP-3cd as an example. However, it may be also used as a guide for expression of other MMPs and human proteases with similar expression, and activation mechanisms (Figure 2). For other proteins other than MMP-3cd, the reader is advised to determine optimal buffer compositions and methods for their target protein before attempting this protocol.

Figure 1: Plasmid map of the pET-3a-Hisx6-pro-MMP-3cd plasmid. The pET-3a vector includes an ampicillin resistance gene. An N-terminal Hisx6-tag sequence is cloned into the pET-3a-based vector, including pro-MMP-3cd, to yield the pET-3a-Hisx6-pro-MMP-3cd construct under control of T7 promoter between BamHI and NdeI restriction sites. Please click here to view a larger version of this figure.

Figure 2: Bacterial expression of pro-MMP-3cd, purification, refolding, and activation. 1.1: pET-3a-Hisx6-pro-MMP-3cd plasmid was transformed into BL21(DE3) or R2DP Cells. 1.2: Pro-MMP-3cd protein expression was induced using IPTG. 1.3: Chemical lysis and sonication are used to extract Hisx6-pro-MMP-3cd proteins that are mainly insoluble and found in the inclusion bodies. Urea was used to denature and solubilize protein from inclusion bodies. 2.1. Denatured Hisx6-pro-MMP-3cd protein was purified via affinity chromatography purification. 3. The eluted Hisx6-pro-MMP-3cd was slowly refolded during dialysis through gradual removal of urea from the buffer. 4. Finally, refolded MMP-3cd protein was activated using APMA by removing the N-terminal pro-peptide domain. APMA is later removed from the solution through desalting. The numbers correspond to protocol sections describing these steps. Abbreviations: MMP-3cd = Matrix metalloproteinase-3 catalytic domain; APMA = 4-aminophenylmercuric acetate. Please click here to view a larger version of this figure.
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1. MMP expression
2. MMP purification and refolding
3. Protein refolding
NOTE: For smaller volumes, dialysis cassettes can be used at a lower risk of sample loss. Dialysis tubing is required if larger volumes are used (see the Table of Materials).
4. Activation
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When running samples on SDS-PAGE, because the protein is expressed in the form of insoluble inclusion bodies, the lysed and sonicated fractions should contain little to no Hisx6-pro-MMP-3cd extract, as the protein has not yet been resolubilized in urea. Figure 3 compares the His-tag purification elution fractions of Hisx6-pro-MMP-3cd from BL21(DE3) cells and R2DP cells. Elution fractions were pooled separately for both BL21(DE3) and R2DP cells before dialysis. Fractions from each step were r...
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The large-scale production of soluble, human, recombinant MMPs remains a challenging task. Mammalian cells can express functional MMPs at high costs and long wait times, whereas E. coli rapidly produce high quantities of MMP inclusion bodies that must be purified and refolded11,16. R2DP cells significantly increase the yield of MMP inclusion bodies, enabling a more cost-effective and productive MMP refolding process. However, E. coli lack the po...
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The authors declare that they have no competing financial interests.
The authors would like to acknowledge Dr. Evette Radisky and Alexandra Hockla at the Mayo Clinic in Jacksonville, Florida, for providing the pET-3a-pro-MMP-3cd plasmid as the template for cloning the Hisx6pro-MMP-3cd gene, and their comments, along with Dr. Paul Hartley from the Nevada Genomics Center at the University of Nevada, Reno, for DNA sequencing. The authors would also like to thank Cassandra Hergenrader for helping with part of protein expression. M.R.-S. would like to thank the NIH-P20 GM103650-COBRE Integrative Neuroscience grant and the UNR R&D mICRO SEED Grant Award.
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| 姓名 | 公司 | 目录编号 | 评论 |
|---|---|---|---|
| 0.22 和微量;m 无菌过滤器 | Sigma Aldrich | SLGP033RS | 用于在纯化前去除蛋白质提取物中的一些污染物,并防止 Ni-NTA 柱堵塞 |
| 1 L 锥形瓶 | Thermo Fisher Scientific | S76106F | n/a |
| 1 L 玻璃瓶 | Thermo Fisher Scientific | 06-414-1D | n/a |
| 1.5 mL 微量离心管 | Thermo Fisher Scientific | 02-682-002 | 不适用 |
| 15 mL 锥形管 | Thermo Fisher Scientific | 339650 | n/a |
| 18 G,1 英寸斜面针 | Amazon | B07S7VBHM2 | 与透析盒结合使用 |
| 2 mL 脱盐柱 | Thermo Fisher Scientific | 89890 | 活化后去除 APMA |
| 2-(N-吗啉代)乙磺酸 (MES) | Thermo Fisher Scientific | AAA1610422 | n/a |
| 250 mL 锥形瓶垫 | Thermo Fisher Scientific | 05-538-53A | 在大容量离心过程中稳定锥形瓶 |
| 250 mL 锥形瓶 | Thermo Fisher Scientific | 05-538-53 | n/a |
| 400 mL 搅拌池 | Sigma Aldrich | UFSC40001 | 再浓缩的体积比离心式过滤装置大得多。Rosetta2(DE3)pLysS 细胞产生大量蛋白质,可能超过离心过滤装置的 15 mL 限 |
| 4-氨基苯基乙酸汞 (APMA) | Sigma Aldrich | A9563-5G | 通过切割前肽 5 mL 注射器激活 MMP-3 |
| Fisher Scientific | NC0829167 | 与透析盒 | |
| 50 mL 锥形管 | Thermo Fisher Scientific | 339650 | 结合使用用于许多纯化步骤中的储存 |
| 50 mL 再浓缩管 | Sigma Aldrich | UFC901024D | 用于透析后重新浓缩蛋白质样品或去除污染物 |
| 琼脂 | Thermo Fisher Scientific | BP1423-500 | 缓冲成分,可在冷却时固化高压灭菌的 LB 培养基 |
| 苄青霉素 | Thermo Fisher Scientific | BP1760-25 | 与 pET3a 载体一起使用的抗生素;用于 100 µLB 培养基中的 g/mL |
| BamHI | NEB | R3136S | 与 pET3a 载体一起使用的限制性内切酶 |
| 氯化钙 (CaCl2) | Thermo Fisher Scientific | 600-30-23 | 钙离子稳定 MMP 结构 |
| 细胞铺展器 | Thermo Fisher Scientific | 50-189-7544 | 可用于在转化 |
| 后将细胞铺展到培养皿中氯霉素 | Thermo Fisher Scientific | 22-055-125GM | 抗生素与 pET3a 载体一起使用;用于 34 µLB 培养基 |
| 透析缓冲液 1 | n/a | n/a | 20 mM Tris-HCl (pH 8.0)、150 mM NaCl、10 mM CaCl2、1 &微量;M ZnCl2,4 M 尿素。 |
| 透析缓冲液 2 | n/a | n/a | 20 mM Tris-HCl (pH 8.0)、150 mM NaCl、10 mM CaCl2、1 &微量;M ZnCl2,2 M 尿素。 |
| 透析缓冲液 3 | n/a | n/a | 20 mM Tris-HCl (pH 8.0)、150 mM NaCl、10 mM CaCl2、1 &微量;M ZnCl2 中。 |
| 透析夹 | Thermo Fisher Scientific | 68011 | 与蛇皮透析管结合使用 |
| 透析管 | Thermo Fisher Scientific | 88243 | 替代透析方法,可容纳更大的样品量,但样品损失风险更高 |
| 消化缓冲液 | NEB | B7204S | 用于消化 pET3a 载体的缓冲液 |
| 一次性比色皿 | Thermo Fisher科学 | 21-200-257 | 用于测量细菌培养物生长和表达过程中的 OD |
| 二硫苏糖醇 (DTT)Thermo | Fisher Scientific | D107125G | 通过减少任何二硫键来帮助蛋白质变性 |
| DNA 组装混合物 | NEB | E2621S | 用于连接 Hisx6-pro-MMP-3cd PCR 产物和消化的 pET3a 载体 |
| DNase I | NEB | M0303S | 核酸内切酶,用于降解以后可能影响蛋白质纯化的不利 DNA 污染物 |
| 乙醇 | Thermo Fisher Scientific | A995-4 | n/a |
| 乙二胺四乙酸 (EDTA) | Thermo Fisher Scientific | J15694-AE | 用于变性。防止氧化和随后形成二硫键 |
| 凝胶回收试剂盒 | Promega | A9281 | 从琼脂糖凝胶中分离和纯化 DNA |
| 甘油 | Thermo Fisher Scientific | G33-500 | 用于制备甘油原液,将其在 -80 ° 下冷冻;C |
| 重力流柱 | BioRad | 7321010 | 用于重组 His 标签蛋白的 Ni-NTA 纯化 |
| 高转化效率细胞 | NEB | C2987 | 高转化效率细胞,将 N 端 His 标签克隆到 pET3a-pro-MMP-3cd 构建 |
| HT 洗脱缓冲液 | n/a | n/a | 20 mM Tris-HCl (pH 8.0)、50 mM NaCl、6 M 尿素、250 mM 咪唑。将 pH 值调节至 7.4 |
| HT 平衡缓冲液 | n/a n | /a | 20 mM Tris-HCl (pH 8.0)、50 mM NaCl、6 M 尿素。将 pH 值调节至 7.4 |
| HT 再生缓冲液 | n/a | n/a | 20 mM MES,0.1 M NaCl。将 pH 值调节至 5.0 |
| HT 洗涤缓冲液 | n/a | n/a | 20 mM Tris-HCl (pH 8.0)、50 mM NaCl、6 M 尿素、25 mM 咪唑。将 pH 值调节至 7.4 |
| 盐酸 (HCl) | Thermo Fisher Scientific | A144C-212 | 用于 pH 缓冲液 |
| 咪唑 | Thermo Fisher Scientific | AAA1022122 | 模拟组氨酸侧基。用于将非特异性结合蛋白与 his 标记的靶蛋白 |
| 分离 包涵体缓冲液 | n/a | n/a | 20 mM Tris-HCl (pH 8.0)、1 mM EDTA、100 mM NaCl、5 mM DTT、2% v/v Triton X 100、0.5 M 尿素。将 pH 值调节至 8.0 |
| 异丙基-szlig;-D-硫代吡喃半乳糖苷 (IPTG) | Thermo Fisher Scientific | FERR0392 | 一种在 pET3a 中诱导靶基因表达的试剂。制备 0.5 mL 1 M 等分试样,过滤、消毒并储存在 -20 °C 中;C |
| LB Amp CamR media | n/a n | /a | 倒入可消毒的 1 L 瓶子或 1 L 烧瓶中。对于 1 L,加入 25 g LB 肉汤。通过高压灭菌灭菌。冷却至 50 °C 以下;C、加入氨苄青霉素至100 &微量;g/mL 和氯霉素至 34 &微量;g/mL |
| LB Amp CamR 板 | n/a | n/a | 倒入无菌培养皿中。倒入直至培养皿盖完全覆盖。1 L 培养基可产生 40-60 个板。1 L 培养基:25 g LB 肉汤,16 g 琼脂。通过高压灭菌灭菌。冷却至 50 °C 以下;C、加入氨苄青霉素至100 &微量;g/mL 和氯霉素至 34 &微量;g/mL |
| LB 肉汤 | Thermo Fisher Scientific | BP1426-2 | 与胰蛋白胨、酵母提取物和氯化钠 |
| 裂解缓冲液 | n/a | n/a | 预混 50 mM Tris-HCl (pH 8.0)、1 mM EDTA、100 mM NaCl、0.133 g/mL 溶菌酶、0.49% v/v Triton X-100。将 pH 值调节至 8.0 |
| 溶菌酶 | MP 生物医学195303 | 用于蛋白质提取。裂解细菌细胞壁的酶 | |
| 小量制备试剂盒 | Promega | A1330 | 中提取 pET3a-pro-MMP-3cd 构建 |
| ,与 pET3a 载体 | |||
| Ni-NTA 树脂 | Thermo Fisher Scientific | PI88221 | 一起使用用于结合重组 his 标签蛋白。这种强烈的相互作用可以用更高浓度的咪唑 |
| 非离子表面活性剂 | Thermo Fisher Scientific | PI28316 | Storage 去污剂来代替,以防止 MMP 聚集。最大限度地减少 MMP 表面疏水残基与水分子之间的相互作用,而不会破坏催化活性。 |
| PCR 混合物 | NEB | M0492S | 一种 PCR 试剂,用于将 N 端 his 标签插入 pET3a-pro-MMP-3cd 载体 |
| pET 质粒 | Addgene | n/a | pET3a 载体提供氨苄青霉素抗性、靶基因的诱导表达以及使用 T7 引物进行测序 |
| 培养皿 | VWR | 25384-342 | 用于在 LB 琼脂培养基上接种转化体 |
| R2DP 细胞 | Novagen | 714033 | BL21 衍生物,真核蛋白表达增强。含有在大肠杆菌中发现罕见的密码子的 tRNA,SOC |
| 生长培养基 | NEB | B9020S | 非选择性生长培养基,用于转化过程中的快速生长 |
| 氯化钠 (NaCl) | Thermo Fisher Scientific | BP358-1 | 用于缓冲液,有助于蛋白质稳定性 |
| Thermo | Fisher Scientific | PI89905 | 用于蛋白质提取的去污剂。裂解细胞壁 |
| 增溶缓冲液 | n/a | n/a | 20 mM Tris-HCl (pH 8.0)、50 mM NaCl、10 mM DTT、6 M 尿素。将 pH 值调节至 8.0 |
| Tris 碱 | Thermo Fisher Scientific | BP152-1 | 常用缓冲液,用于生理 pH 值范围。温度敏感型 |
| Triton X-100 | Thermo Fisher Scientific | M1122980101 | 用于细胞裂解的去污剂 |
| 尿素 | Thermo Fisher Scientific | AAJ75826A7 | 第一种用于破坏蛋白质二级结构的离液剂 |
| 氯化锌 (ZnCl2) | Thermo Fisher Scientific | AAA162810E | 稳定 MMP 结构。锌离子存在于 MMP-3 的催化位点 |
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