Integrated bioprocessing in Saccharomyces cerevisiae using green fluorescent protein as a fusion partner

Rational design of a tripartite fusion protein of heparinase I enables one-step affinity purification and real-time activity detection

Enzymatic degradation of heparin has great potential as an ecological and specific way to produce low molecular weight heparin. However, the commercial use of heparinase I (HepA), one of the most important heparin lyases, has been hampered by low productivity and poor thermostability. Fusion with green fluorescent protein (GFP) or maltose-binding protein (MBP) has shown potential in facilitating the industrial use of HepA. Thus, tripartite fusion of GFP, MBP and HepA would be a promising approach. Therefore, in the present study, the tripartite fusion strategy was systematically studied, mainly focusing on the fusion order and the linker sequence, to obtain a fusion protein offering one-step purification and real-time detection of HepA activity by fluorescence as well as high HepA activity and thermostability. Our results show that fusion order is important for MBP binding affinity and HepA activity, while the linker sequences at domain junctions have significant effects on protein expression level, HepA activity and thermostability as well as GFP fluorescence. The best tripartite fusion was identified as MBP-(EAAAK)(3)-GFP-(GGGGS)(3)-HepA, which shows potential to facilitate the production of HepA and its application in industrial preparation of low molecular weight heparin.

Scale-up from microtiter plate to laboratory fermenter: evaluation by online monitoring techniques of growth and protein expression in Escherichia coli and Hansenula polymorpha fermentations

BACKGROUND

In the past decade, an enormous number of new bioprocesses have evolved in the biotechnology industry. These bioprocesses have to be developed fast and at a maximum productivity. Up to now, only few microbioreactors were developed to fulfill these demands and to facilitate sample processing. One predominant reaction platform is the shaken microtiter plate (MTP), which provides high-throughput at minimal expenses in time, money and work effort. By taking advantage of this simple and efficient microbioreactor array, a new online monitoring technique for biomass and fluorescence, called BioLector, has been recently developed. The combination of high-throughput and high information content makes the BioLector a very powerful tool in bioprocess development. Nevertheless, the scalabilty of results from the micro-scale to laboratory or even larger scales is very important for short development times. Therefore, engineering parameters regarding the reactor design and its operation conditions play an important role even on a micro-scale. In order to evaluate the scale-up from a microtiter plate scale (200 microL) to a stirred tank fermenter scale (1.4 L), two standard microbial expression systems, Escherichia coli and Hansenula polymorpha, were fermented in parallel at both scales and compared with regard to the biomass and protein formation.

RESULTS

Volumetric mass transfer coefficients (kLa) ranging from 100 to 350 1/h were obtained in 96-well microtiter plates. Even with a suboptimal mass transfer condition in the microtiter plate compared to the stirred tank fermenter (kLa = 370-600 1/h), identical growth and protein expression kinetics were attained in bacteria and yeast fermentations. The bioprocess kinetics were evaluated by optical online measurements of biomass and protein concentrations exhibiting the same fermentation times and maximum signal deviations below 10% between the scales. In the experiments, the widely applied green fluorescent protein (GFP) served as an online reporter of protein expression for both strains.

CONCLUSIONS

The successful 7000-fold scale-up from a shaken microtiter plate to a stirred tank fermenter was demonstrated in parallel fermentations for standard microbial expression systems. This confirms that the very economical and time efficient platform of microtiter plates can be very easily scaled up to larger stirred tank fermenters under defined engineering conditions. New online monitoring techniques for microtiter plates, such as the BioLector, provide even more real-time kinetic data from fermentations than ever before and at an affordable price. This paves the way for a better understanding of the bioprocess and a more rational process design.

The mouse sphingomyelin synthase 1 (SMS1) gene is alternatively spliced to yield multiple transcripts and proteins

Sphingomyelin synthase 1 (SMS1) is a recently identified 413-residue protein that plays a critical role in sphingolipid metabolism by catalyzing the conversion of ceramide and phosphatidylcholine to sphingomyelin and diacylglycerol (DAG). We have previously reported the isolation of a mouse SMS1 encoding cDNA that contains a unique 5' UTR sequence. Three other mouse SMS1 cDNAs that differed in their 5' and 3' non-coding sequences were present in GenBank. In order to ascertain the origin of the unique 5' and 3' UTR sequences, we analyzed the structure of the mouse SMS1 gene. Analysis of the four different SMS1 cDNA sequences and of the corresponding mouse genomic fragment revealed that the SMS1 gene consists of 16 exons that are alternatively spliced to produce 4 different mRNAs (SMS1alpha1, SMS1alpha2, SMS1beta and SMS1gamma) and 3 different proteins (SMS1alpha, SMS1beta and SMS1gamma). RT-PCR was used to demonstrate that all four SMS1 cDNAs represent expressed transcripts that show distinctly different tissue distributions. Transcripts for SMS1alpha1, SMS1alpha2 and SMS1beta were found to increase in response to the pro-apoptotic effects of TNF-alpha. Finally, using a yeast-based assay, we confirmed that SMS1alpha prevents the growth inhibitory effects of Bax but SMS1beta neither prevents nor enhances the effects of Bax or of SMS1alpha. Taken together these results demonstrate the complexity of SMS1 gene structure, expression and function.

Optimization of Reporter Cells for Expression Profiling in a Microfluidic Device

The emergence of green fluorescence protein (GFP) technologies has enabled non-invasive monitoring of cell function and gene expression. GFP-based expression studies are typically performed in traditional single-dish or multi-well formats to monitor a small number of genes or conditions that do not lend well to scaling, high-throughput analysis, or single-cell measurements. We have recently developed a microfluidic device, the Living Cell Array (LCA), for monitoring GFP-based gene expression in a high-throughput manner. Here, we report the optimization of GFP reporter cell characteristics in this microfluidic device for gene expression profiling. A reporter cell line for the transcription factor NF-kappa B was generated and used as the model cell line. Reporter cells were seeded in the LCA and NF-kappa B activated by addition of the cytokine TNF-alpha . Our studies show that the fluorescence kinetics from the reporter cell line in response to both single and repeated TNF-alpha stimulation in the LCA is similar to that observed in standard tissue culture. In addition, our data also indicate that multiple expression waves can be reliably monitored from a small population of reporter cells. Using reporter cell line subcloning and cell cycle synchronization, we demonstrate that the kinetics and magnitude of induced fluorescence in the reporter cell lines can be further improved to maximize the fluorescence readout from reporter cell lines, thereby improving their applicability to live cell expression profiling. Our studies establish some of the important criteria to be considered when using reporter cell lines for dynamic expression profiling in microfluidic devices.

Secretion and surface display of green fluorescent protein using the yeast Saccharomyces cerevisiae

Green fluorescent protein (GFP) continues to be a very useful tool in biotechnology, but soluble production of GFP and GFP-protein fusions has been difficult. In this study, we have produced yeast-enhanced green fluorescent protein (yEGFP) in Saccharomyces cerevisiae as a soluble, secreted product with a purified level of 6 mg/L. Expression was directed by the inducible GAL1-10 promoter and synthetic prepro leader sequence. The secretion of yEGFP by yeast was strongly dependent on temperature, with 20 degrees C induction being optimal. Use of 2 micro multicopy expression constructs elevated yields over a low-copy CEN-based system by approximately 2-fold. Yeast-enhanced GFP was also expressed as a fusion to the Aga2p mating agglutinin in order to test the secretory processing fidelity of yEGFP-protein fusions. When the cell surface anchoring protein, Aga1p, was co-overexpressed with the Aga2p-yEGFP fusion, the Aga2p-yEGFP protein was tethered to the yeast cell surface. Flow cytometry and fluorescence microscopy analysis indicated that the fusion was displayed on the yeast cell surface at high levels. In the absence of high level Aga1p expression, the Aga2p-yEGFP fusion protein was instead secreted in its entirety with no detectable surface display. These findings reveal that yeast is a suitable host for secretion of GFP and GFP-protein fusions and thus could enable a wide range of biochemistry and biotechnology applications.

In situ measurement of bioluminescence and fluorescence in an integrated microbioreactor

Reporter strains of bacteria that emit light or a fluorescent marker in response to specific conditions in their environment are having a significant impact in many areas of biology, including toxicity assays for environmental pollutants, chemical detection, and gene expression profiling. We have demonstrated methods for in situ measurements of bioluminescence and fluorescence from bacterial cultures grown in 50 microL instrumented microbioreactors. Results from microbioreactors were compared to results obtained from conventional 500 mL batch bioreactors and shake flasks. Experiments were conducted with reporter strains of Escherichia coli in which luxCDABE or gfp was fused to a promoter that was either expressed constitutively, or that responded to oxygen limitation. With these reporter strains, we have demonstrated the ability to obtain information on growth conditions within the microbioreactor. We have also shown that the large aspect ratio of the microbioreactor provides a unique advantage over measurements in larger bioreactors by reducing the inner filter effect in on-line measurements and eliminating the need for error-prone off-line dilutions. In addition, continuous on-line monitoring of genes in real-time, when expanded to include entire reporter libraries, could potentially provide a true dynamic picture of cellular gene expression from which the kinetics of gene expression can be untangled and elucidated.

A critical review of the methods for cleavage of fusion proteins with thrombin and factor Xa

Expression and purification of proteins in recombinant DNA systems is a powerful and widely used technique. Frequently there is the need to express the protein of interest as a fusion protein or chimeric protein. Fusion protein technology is frequently used to attach a "signal" which can be used for subsequent localization of the protein or a "carrier" which can be used to deliver a "therapeutic" such as a radioactive molecule to a specific site. In addition to these applications, fusion protein technology can be employed for several other useful purposes. Of these, the most frequent reason is to provide a 'tag' or 'handle' which will aid in the purification of the protein. Another useful purpose is to improve the expression or folding of the protein of interest. In these latter two situations, it is often necessary to remove the fusion partner before the recombinant protein of interest can be used for further studies. This removal process involves the insertion of a unique amino acid sequence that is susceptible to cleavage by a highly specific protease. Thrombin and factor Xa are the most frequently used proteases for this application. The purpose of this review is to discuss the application of thrombin and factor Xa for the cleavage of fusion proteins. It is emphasized that while these enzymes are quite specific for cleavage at the inserted cleavage site, proteolysis can frequently occur at other site(s) in the protein of interest. It is necessary to characterize the protein of interest after cleavage from the affinity label to assure that there are no changes in the covalent structure of the protein of interest. Examples are presented which describe the proteolysis of the protein of interest by either factor Xa or thrombin.