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Motivated by the advancement of genomics and accelerated rate of discovery of new proteins, high throughput pipelines have been developed to parallelize traditional approaches for the screening and identification of optimal protein production strategies. Potential variables to be optimized include, but are not limited to, varying expression strains1,2, temperature3,4, media2,3, target variants5, fusion partners6-13, co-expression with chaperones14,15, cytoplasmic or periplasmic expression16-18, and purification buffer components3. By implementing high throughput approaches, many variables or many targets can be tested in parallel with a high level of efficiency, while limiting batch-to-batch variation. In our experience, the strategy also gives good reproducibility upon scale-up using the same culture (temperature, media, aeration, etc.) and purification conditions (same resin, buffers, etc.). Several high throughput platforms have been used in the past decade to identify conditions for soluble protein expression, namely through varying parameters such as fusion partners, expression strains or temperature19-23.
We recently used our high throughput screening approach for the expression of soluble disulfide-rich proteins11. The proteins selected were not only from venomous sources, but also included disulfide-rich enzyme inhibitors from a wide range of species including plants, pigs, cows and humans. The experiment compared the effects of 12 different fusion partners and three different expression strains on the solubility and folding of 28 disulfide-reticulated proteins. We demonstrated that using DsbC as a fusion partner for production in the strain BL21 (DE3) pLysS vastly outproduced (in both yield and number of soluble proteins obtained) any other combination of strain and fusion tested11. The results of this experiment formed the basis for adapting our original general high throughput pipeline (which has been used for the expression screening of a wide range of proteins)22,24 into one more suited for the expression of disulfide-rich targets. Disulfide-rich proteins from animal venoms are of particular interest. Venoms are a complex mixture of bioactive peptides and proteins, with potential value pharmacologically and therapeutically. However, expression of disulfide bond-containing proteins is not trivial. These proteins generally contain between one to seven disulfide bonds, and must be oxidized with the correct disulfide-bonding patterns in order to be active. Currently, the platform is being used for screening the expression of a large number of disulfide-rich animal venom proteins as part of the FP7 European VENOMICS Project (www.venomics.eu) and benchmarking novel protocols for the high throughput expression of thousands of targets. Here, an automated method is provided for high throughput small-scale expression screening and purification (see Figure 1) applied to disulfide-rich animal venom proteins. The strategy for disulfide rich peptides and proteins utilizes a HIS-tag for purification and the redox-active fusion partner, DsbC, creating cleavable HIS-DsbC fusions to the target proteins (see Figure 2).
While the focus of the protocols herein is automation using a liquid handling robot and HTP electrophoresis, these methods are also suitable for a high throughput manual approach, meaning that even laboratories with a basic setup can take advantage of the protocols without any prerequisite for expensive equipment. Manual protocols for the transformation to purification and analysis (not specific to disulfide-rich proteins) have been published elsewhere24 and will not be repeated here. The throughput of the manual procedure (from expression clone, produced by recombinational cloning25, to analysis of soluble protein levels) is 96 (using SDS-PAGE detection) or 384 (4 x 96; using dot blot and SDS-PAGE26) cultures per week (see Figure 1). This can be increased if performed in a semi-automated way (using a liquid handling robot and dot blot26 or HTP electrophoresis, such as with a Caliper GXII LabChip system22 for analysis of results) to up to 1,152 (12 x 96) cultures in parallel over one week, as described herein. Culturing is performed in deep well 24 (DW24) format so that regular shaking incubators can be used in contrast to cultures grown in deep well 96 (DW96) format, which necessitate the use of short orbital high-speed shaking incubators for sufficient aeration (shaking at 800 rpm). The use of auto-induction media27 also simplifies expression, eliminating the manual induction step. Even where laboratories already use pre-defined expression and purification conditions, these can be transferred directly into this HTP system simply to improve efficiency. A detailed schematic of the high throughput screening pipeline for disulfide-rich proteins is provided in Figure 3. The parameters in the pipeline were selected based on extensive screening experiments11,22, which allowed us to choose the most useful conditions for protein production.
Characterization can be performed on tagged proteins purified directly from small-scale expressions in pilot studies where tens of micrograms of sample is sufficient, or for sensitive functional assays and binding assays (for example, low volume HTP patch clamp systems28). The same can even be performed on the untagged targets after cleavage, provided the tag and protease are removed (for example, by reverse phase HPLC). Quality control can also be performed by mass spectrometry (to confirm the expected size and oxidation state) or chromatographic methods (to confirm purity or heterogeneity)29. Sometimes tag cleavage is unnecessary or even undesirable (particularly for poorly soluble proteins30,31), so in this protocol cleavage is optional. Regardless, in all constructs there is a TEV protease cleavage site (ENLYFQ/[G]32) directly preceding the target gene to produce native protein after cleavage (see Figure 2 and Discussion). If cleavage of the fusion tag is desired, cleavage can be tested (on the elution fraction or ‘on column’) at the small scale to analyze efficiency, optimize conditions if required and obtain reliable estimates of yields for subsequent scale-up experiments.
There are two options for the volume of beads used during the affinity purification, depending on the aims and expectations of the experiment. To be able to capture as much protein as possible (to purify for pilot assays or MS, or to extrapolate for scale-up yields) a final volume of 200 µl of resin should be used, allowing detection of soluble protein in the range of 1-100 mg/L culture before saturation of the system (see protocol (A) in Section 8.1). However, if the aim of the experiment is the detection of low amounts of soluble proteins then a final volume of 50 µl of resin is suitable, allowing detection of soluble protein in the range of 0.1-25 mg/L culture (see protocol (B) in Section 8.2).
Production can be scaled up, if required, to obtain milligram quantities of purified targets for further structural and functional studies using the conditions identified for soluble expression. The details of scale-up protocols used at AFMB have been discussed elsewhere22,24.
Further details relevant to the experimental setup, critical steps within the protocol, modifications and trouble-shooting and limitations of the technique are provided in the discussion. Please read the discussion before commencing the experiments.
Throughout the protocols we expect a success rate of 90% at each step (for example, at least 90% of the cultures must grow at any given step). If the success rate of any step in the experiment falls below 90% the samples are discarded and the experiment is repeated for the full collection of constructs. However, this success rate is not applicable to the number of constructs that express as soluble proteins or the proportion of constructs that cleave with 100% efficiency, as this will be highly dependent on the proteins tested.
The specific details for the set-up of the robot worktable are provided for each protocol (also see Figure 4), however they can be adapted as required for alternative worktable set-ups. The robot hardware (Tecan) consists of a 96-multichannel arm (MCA96), robotic manipulator (RoMa) and the 8-channel liquid handling head (LiHa). All steps utilizing the MCA96 can also be performed using the LiHa if an MCA96 is not available, however they will take longer because the LiHa will need to be washed between steps. While the robot is technically not a sterile environment, the inclusion of antibiotics generally ensures that there are not problems with contamination or sterility.