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Method Article
This protocol details an enhanced method for synthesizing high yields of recombinant proteins from a Streptomyces venezuelae cell-free transcription-translation (TX-TL) system.
Streptomyces spp. are a major source of clinical antibiotics and industrial chemicals. Streptomyces venezuelae ATCC 10712 is a fast-growing strain and a natural producer of chloramphenicol, jadomycin, and pikromycin, which makes it an attractive candidate as a next-generation synthetic biology chassis. Therefore, genetic tools that accelerate the development of S. venezuelae ATCC 10712, as well as other Streptomyces spp. models, are highly desirable for natural product engineering and discovery. To this end, a dedicated S. venezuelae ATCC 10712 cell-free system is provided in this protocol to enable high-yield heterologous expression of high G+C (%) genes. This protocol is suitable for small-scale (10-100 μL) batch reactions in either 96-well or 384-well plate format, while reactions are potentially scalable. The cell-free system is robust and can achieve high yields (~5-10 μM) for a range of recombinant proteins in a minimal setup. This work also incorporates a broad plasmid toolset for real-time measurement of mRNA and protein synthesis, as well as in-gel fluorescence staining of tagged proteins. This protocol can also be integrated with high-throughput gene expression characterization workflows or the study of enzyme pathways from high G+C (%) genes present in Actinomycetes genomes.
Cell-free transcription-translation (TX-TL) systems provide an ideal prototyping platform for synthetic biology to implement rapid design-build-test-learn cycles, the conceptual engineering framework for synthetic biology1. In addition, there is growing interest in TX-TL systems for high-value recombinant protein production in an open-reaction environment2, for example, to incorporate non-standard amino acids in antibody-drug conjugates3. Specifically, TX-TL requires a cell extract, plasmid or linear DNA, and an energy solution to catalyze protein synthesis in batch or semicontinuous reactions. While Escherichia coli TX-TL is the dominant cell-free system, a number of emerging non-model TX-TL systems have attracted attention for different applications4,5,6,7,8. Key advantages of TX-TL include flexible scalability (nanoliter to liter scale)9,10, strong reproducibility, and automated workflows8,11,12. In particular, automation of TX-TL permits the accelerated characterization of genetic parts and regulatory elements8,12,13.
In terms of reaction setup, TX-TL requires both primary and secondary energy sources, as well as amino acids, cofactors, additives, and a template DNA sequence. Nucleotide triphosphates (NTPs) provide the primary energy source to drive initial mRNA (ATP, GTP, CTP, and UTP) and protein synthesis (only ATP and GTP). To increase TX-TL yields, NTPs are regenerated through the catabolism of a secondary energy source, such as maltose14, maltodextrin15, glucose14, 3-phosphoglycerate (3-PGA)16, phosphoenolpyruvate17, and L-glutamate18. This inherent metabolic activity is surprisingly versatile, yet poorly studied, especially in emerging TX-TL systems. Each energy source has distinct properties and advantages in terms of ATP yield, chemical stability, and cost, which is an important consideration for scaled-up TX-TL reactions. So far, current protocols for E. coli TX-TL have reached up to 4.0 mg/mL (~157 µM) for the model green fluorescent protein (GFP), using a blend of 3-PGA (30 mM), maltodextrin (60 mM), and D-ribose (30 mM) as the secondary energy source19.
Recently, there has been a rising interest in studying secondary metabolite biosynthetic pathways in TX-TL systems20,21,22. Specifically, Actinobacteria are a major source of secondary metabolites, including antibiotics and agricultural chemicals23,24. Their genomes are enriched with so-called biosynthetic gene clusters (BGCs), which encode enzymatic pathways for secondary metabolite biosynthesis. For the study of Actinobacteria genetic parts and biosynthetic pathways, a range of Streptomyces-based TX-TL systems have recently been developed5,6,25,26. These specialized Streptomyces TX-TL systems are potentially beneficial for the following reasons: [1] provision of a native protein folding environment for enzymes from Streptomyces spp.26; [2] access to an optimal tRNA pool for high G+C (%) gene expression; [3] active primary metabolism, which potentially can be hijacked for the supply of biosynthetic precursors; and [4] provision of enzymes, precursors, or cofactors from secondary metabolism present in the native cell extract. Hence, a high-yield S.venezuelae TX-TL toolkit has recently been established to harness these unique capabilities5.
Streptomyces venezuelae is an emerging host for synthetic biology with a rich history in industrial biotechnology5,27,28,29 and as a model system for studying cell division and genetic regulation in Actinobacteria30,31,32. The main type strain, S. venezuelae ATCC 10712, has a relatively large genome of 8.22 Mb with 72.5% G+C content (%) (Accession number: CP029197), which encodes 7377 coding sequences, 21 rRNAs, 67 tRNAs, and 30 biosynthetic gene clusters27. In synthetic biology, S. venezuelae ATCC 10712 is an attractive chassis for the heterologous expression of biosynthetic pathways. Unlike most other Streptomyces stains, it provides several key advantages, including a rapid doubling time (~40 min), an extensive range of genetic and experimental tools5,28, lack of mycelial clumping, and sporulation in liquid media28,33. Several studies have also demonstrated the use of S. venezuelae for heterologous production of a diverse array of secondary metabolites, including polyketides, ribosomal and nonribosomal peptides34,35,36,37,38. These combined features make this strain an attractive microbial host for synthetic biology and metabolic engineering applications. While S. venezuelae is not the dominant Streptomyces model for heterologous gene expression, with further developments, it is primed for broader use within natural product discovery.
This manuscript presents a detailed protocol (Figure 1) for a high-yield S. venezuelae TX-TL system, which has been updated from the original previously-published protocol26. In this work, the energy solution and reaction conditions have been optimized to increase protein yield up to 260 μg/mL for the mScarlet-I reporter protein in a 4 h, 10 μL batch reaction, using a standard plasmid, pTU1-A-SP44-mScarlet-I. This plasmid has been specifically designed to enable various methods of detecting protein expression. The protocol is also streamlined, while the energy system has been optimized to reduce the complexity and cost of setting up cell-free reactions without compromising the yield. Along with the optimized TX-TL system, a library of genetic parts has been developed for fine-tuning gene expression and as fluorescent tools for monitoring TX-TL in real time, thereby creating a versatile platform for prototyping gene expression and natural product biosynthetic pathways from Streptomyces spp. and related Actinobacteria.
In this work, the recommended standard plasmid (pTU1-A-SP44-mScarlet-I) can be used to establish the S. venezuelae TX-TL workflow in a new laboratory and is available on AddGene (see Supplemental Table S1). pTU1-A-SP44-mScarlet-I provides the user with the flexibility to study other open-reading frames (ORFs). The mScarlet-I ORF is codon-optimized for S. venezuelae gene expression. The SP44 promoter is a strong constitutive promoter that is highly active in both E. coli and Streptomyces spp.39. The plasmid has two unique restriction enzyme sites (NdeI, BamHI) to allow the sub-cloning of new ORFs in-frame with a joint C-terminal FLAG-tag and fluorescein arsenical hairpin (FlAsH) binder tag system. Alternatively, both tags can be removed with the inclusion of a stop codon after sub-cloning a new gene. With this base vector, the high-yield expression of a range of proteins has been demonstrated, namely proteins from the oxytetracycline biosynthesis pathway and an uncharacterized nonribosomal peptide synthetase (NRPS) from Streptomyces rimosus (Figure 2). In terms of mRNA detection, the pTU1-A-SP44-mScarlet-I standard plasmid contains a dBroccoli aptamer (in the 3'-untranslated region) for detection with the 3,5-difluoro-4-hydroxybenzylidene imidazolinone (DFHBI) probe. For increased flexibility, a toolset of EcoFlex40-compatible MoClo parts has also been made available on AddGene, including an EcoFlex-compatible Streptomyces shuttle vector (pSF1C-A-RFP/pSF2C-A-RFP) and a range of pTU1-A-SP44 variant plasmids expressing superfolder green fluorescence protein (sfGFP), mScarlet-I, mVenus-I, and β-glucuronidase (GUS). In particular, the pSF1C-A plasmid is derived from pAV-gapdh28 and is cured of BsaI/BsmBI sites for MoClo assembly. pSF1C-A-RFP/pSF2C-A-RFP is equivalent to pTU1-A-RFP/pTU2-A-RFP from EcoFlex40 but contains additional functionality for conjugation and chromosomal integration in Streptomyces spp. using the phiC31 integrase system28.
The first stage of the protocol involves the growth of the S. venezuelae ATCC 10712 or a closely related strain, cell harvest at mid-exponential phase, cell wash steps, and equilibration in S30A and S30B buffers. This stage requires three days, and the time for cell growth can be used to prepare the remaining components as described below. The harvested cells are then lysed by sonication, clarified, and undergo a run-off reaction. At this final stage of preparation, the cell extracts can be prepared for long-term storage at -80 °C to minimize loss of activity. For the assembly of TX-TL reactions using this protocol, a Streptomyces Master Mix (SMM) is presented, with the option of a Minimal Energy Solution format (MES) that gives comparable yields. Further, it is recommended to streak a fresh culture of S. venezuelae ATCC 10712 from a -80 °C glycerol stock onto a GYM agar plate and incubate at 28 °C for at least 48-72 h until single colonies are visible. Only fresh cultures should be used for the following steps.
NOTE: See Table 1 and Table 2 for recipes for GYM medium and agar plate and S30A and S30B wash buffers.
1. Preparation of solutions and general guidance
2. Preparation of S. venezuelae ATCC 10712 cells
3. Cell lysis by sonication to obtain the crude cell extract
NOTE: At this stage, the user can choose to disrupt the cells by sonication either in 1 mL fractions (option 1) or as a larger cell suspension (5 mL) in a 50 mL tube (option 2). Both options have been detailed below to ensure reproducibility, as the final volume of the cell suspension can change due to the loss of cells during previous harvesting and wash steps. A new user should attempt option 2.1 first to establish the protocol.
4. Cell extract clarification and run-off reaction
5. Preparation of plasmid DNA template
6. Preparation of the Streptomyces Master Mix (SMM) solution
7. Setting up a standard S. venezuelae TX-TL reaction
This detailed protocol is provided as an example to help the user establish a Streptomyces TX-TL system based on the S. venezuelae ATCC 10712 model strain (Figure 1). The user may seek to study other Streptomyces strains; however, the growth/harvesting stages of other strains with longer doubling times or distinct growth preferences will need to be custom-optimized to achieve peak results. For the representative result, the mScarlet-I fluorescent protein from ...
In this manuscript, a high-yield S. venezuelae TX-TL protocol has been described with detailed steps that are straightforward to conduct for both experienced and new users of TX-TL systems. Several features from existing Streptomyces45 and E. coli TX-TL41 protocols have been removed to establish a minimal, yet high-yield protocol for S. venezuelae TX-TL5,26. The workflow recommend...
The authors declare that they have no competing financial interests.
The authors would like to acknowledge the following research support: EPSRC [EP/K038648/1] for SJM as a PDRA with PSF; Wellcome Trust sponsored ISSF fellowship for SJM with PSF at Imperial College London; Royal Society research grant [RGS\R1\191186]; Wellcome Trust SEED award [217528/Z/19/Z] for SJM at the University of Kent; and Global Challenges Research Fund (GCRF) Ph.D. scholarship for KC at the University of Kent.
Name | Company | Catalog Number | Comments |
2.5 L UltraYield Flask | Thomson | 931136-B | |
3-PGA (>93%) | Sigma | P8877 | |
384 Well Black/Clear Bottom Plate | ThermoFisher | 10692202 | |
Ammonium chloride (98%) | Fluorochem | 44722 | |
ATP, CTP, UTP, GTP (100 mM solution, >99%) | ThermoFisher | R0481 | |
Carbenicillin (contact supplier for purity) | Melford | C46000-25.0 | |
D-(+)-glucose (contact supplier for purity) | Melford | G32040 | |
DFHBI (≥98% - HPLC) | Sigma | SML1627 | |
DTT (contact supplier for purity) | Melford | MB1015 | |
FlAsH-EDT2 (contact supplier for purity) | Santa Cruz Biotech | sc-363644 | |
Glucose-6-phosphate (>98%) | Sigma | G7879 | |
HEPES Free Acid (contact supplier for purity) | Melford | B2001 | |
L-glutamic acid hemimagnesium salt tetrahydrate (>98%) | Sigma | 49605 | |
Magnesium chloride (98%) | Fluorochem | 494356 | |
Malt extract | Sigma | 70167-500G | |
PEG-6000 | Sigma | 807491 | |
Pierce 96-well Microdialysis Plate, 10K MWCO | ThermoFisher | 88260 | |
Poly(vinyl sulfate) potassium salt | Sigma | 271969 | |
Potassium glutamate (>99%) | Sigma | G1149 | |
RTS amino acid sampler | 5 Prime | 2401530 | |
Sodium chloride (99%) | Fluorochem | 94554 | |
Supelclean LC-18 SPE C-18 SPE column (1 g) | Sigma | 505471 | |
Yeast Extract | Melford | Y1333 | |
Equipment | |||
Platereader | BMG | Omega |
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