A novel LED‐based 2D‐fluorescence spectroscopy system for in‐line bioprocess monitoring of Chinese hamster ovary cell cultivations—Part II

This study was performed in order to evaluate a new LED‐based 2D‐fluorescence spectrometer for in‐line bioprocess monitoring of Chinese hamster ovary (CHO) cell culture processes. The new spectrometer used selected excitation wavelengths of 280, 365, and 455 nm to collect spectral data from six 10‐L fed‐batch processes. The technique provides data on various fluorescent compounds from the cultivation medium as well as from cell metabolism. In addition, scattered light offers information about the cultivation status. Multivariate data analysis tools were applied to analyze the large data sets of the collected fluorescence spectra. First, principal component analysis was used to accomplish an overview of all spectral data from all six CHO cultivations. Partial least square regression models were developed to correlate 2D‐fluorescence spectral data with selected critical process variables as offline reference values. A separate independent fed‐batch process was used for model validation and prediction. An almost continuous in‐line bioprocess monitoring was realized because 2D‐fluorescence spectra were collected every 10 min during the whole cultivation. The new 2D‐fluorescence device demonstrates the significant potential for accurate prediction of the total cell count, viable cell count, and the cell viability. The results strongly indicated that the technique is particularly capable to distinguish between different cell statuses inside the bioreactor. In addition, spectral data provided information about the lactate metabolism shift and cellular respiration during the cultivation process. Overall, the 2D‐fluorescence device is a highly sensitive tool for process analytical technology applications in mammalian cell cultures.     

Replication methods and tools in high-throughput cultivation processes - recognizing potential variations of growth and product formation by on-line monitoring

Background  

High-throughput cultivations in microtiter plates are the method of choice to express proteins from recombinant clone libraries. Such processes typically include several steps, whereby some of them are linked by replication steps: transformation, plating, colony picking, preculture, main culture and induction. In this study, the effects of conventional replication methods and replication tools (8-channel pipette, 96-pin replicators: steel replicator with fixed or spring-loaded pins, plastic replicator with fixed pins) on growth kinetics of Escherichia coli SCS1 pQE-30 pSE111 were observed. Growth was monitored with the BioLector, an on-line monitoring technique for microtiter plates. Furthermore, the influence of these effects on product formation of Escherichia coli pRhotHi-2-EcFbFP was investigated. Finally, a high-throughput cultivation process was simulated with Corynebacterium glutamicum pEKEx2-phoD-GFP, beginning at the colony picking step.     

Validation of a high-throughput fermentation system based on online monitoring of biomass and fluorescence in continuously shaken microtiter plates

Background  

An advanced version of a recently reported high-throughput fermentation system with online measurement, called BioLector, and its validation is presented. The technology combines high-throughput screening and high-information content by applying online monitoring of scattered light and fluorescence intensities in continuously shaken microtiter plates. Various examples in calibration of the optical measurements, clone and media screening and promoter characterization are given.     

Soft sensor based on 2D‐fluorescence and process data enabling real‐time estimation of biomass in Escherichia coli cultivations

In bioprocesses, specific process responses such as the biomass cannot typically be measured directly on‐line, since analytical sampling is associated with unavoidable time delays. Accessing those responses in real‐time is essential for Quality by Design and process analytical technology concepts. Soft sensors overcome these limitations by indirectly measuring the variables of interest using a previously derived model and actual process data in real time. In this study, a biomass soft sensor based on 2D‐fluorescence data and process data, was developed for a comprehensive study with a 20‐L experimental design, for Escherichia coli fed‐batch cultivations. A multivariate adaptive regression splines algorithm was applied to 2D‐fluorescence spectra and process data, to estimate the biomass concentration at any time during the process. Prediction errors of 4.9% (0.99 g/L) for validation and 3.8% (0.69 g/L) for new data (external validation), were obtained. Using principal component and parallel factor analyses on the 2D‐fluorescence data, two potential chemical compounds were identified and directly linked to cell metabolism. The same wavelength pairs were also important predictors for the regression‐model performance. Overall, the proposed soft sensor is a valuable tool for monitoring the process performance on‐line, enabling Quality by Design.     

Glucose-containing polymer rings enable fed-batch operation in microtiter plates with parallel online measurement of scattered light,fluorescence, dissolved oxygen tension,and pH

Bioprocesses operated in batch mode can induce adverse effects like overflow metabolism, substrate inhibition, osmotic inhibition, oxygen limitation, and catabolite repression. To avoid these adverse effects, fed-batch is the predominant operation mode in industrial production. Nevertheless, screening for optimal production strains is usually performed in microtiter plates and shake flasks operated in batch mode without any online monitoring. Recently, a polymer-based controlled-release fed-batch microtiter plate with stable glucose release characteristics was described. In this study, a glucose-containing polymer matrix was used to manufacture polymer rings that were placed at the bottom of a 48-well microtiter plate. Thereby, the liquid content of the well became accessible for optical measurement by the BioLector device. Reflections caused by the polymer ring were minimized by adjusting the scattered-light measurement position. Influences on the measurement of the dissolved oxygen tension and pH could be avoided by choosing appropriate polymer-ring geometries. These adjustments enabled parallel online measurement of scattered light, fluorescence, dissolved oxygen tension, and pH of Escherichia coli BL21 (DE3) fed-batch cultivations. The online monitoring and fed-batch operation capabilities of the fed-batch microtiter plate presented in this study finds optimal application in screenings and initial process development.     

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 industry and academic research, there is an increasing demand for flexible automated microfermentation platforms with advanced sensing technology. However, up to now, conventional platforms cannot generate continuous data in high-throughput cultivations, in particular for monitoring biomass and fluorescent proteins. Furthermore, microfermentation platforms are needed that can easily combine cost-effective, disposable microbioreactors with downstream processing and analytical assays.

Results

To meet this demand, a novel automated microfermentation platform consisting of a BioLector and a liquid-handling robot (Robo-Lector) was sucessfully built and tested. The BioLector provides a cultivation system that is able to permanently monitor microbial growth and the fluorescence of reporter proteins under defined conditions in microtiter plates. Three examplary methods were programed on the Robo-Lector platform to study in detail high-throughput cultivation processes and especially recombinant protein expression. The host/vector system E. coli BL21(DE3) pRhotHi-2-EcFbFP, expressing the fluorescence protein EcFbFP, was hereby investigated. With the method 'induction profiling' it was possible to conduct 96 different induction experiments (varying inducer concentrations from 0 to 1.5 mM IPTG at 8 different induction times) simultaneously in an automated way. The method 'biomass-specific induction' allowed to automatically induce cultures with different growth kinetics in a microtiter plate at the same biomass concentration, which resulted in a relative standard deviation of the EcFbFP production of only ± 7%. The third method 'biomass-specific replication' enabled to generate equal initial biomass concentrations in main cultures from precultures with different growth kinetics. This was realized by automatically transferring an appropiate inoculum volume from the different preculture microtiter wells to respective wells of the main culture plate, where subsequently similar growth kinetics could be obtained.

Conclusion

The Robo-Lector generates extensive kinetic data in high-throughput cultivations, particularly for biomass and fluorescence protein formation. Based on the non-invasive on-line-monitoring signals, actions of the liquid-handling robot can easily be triggered. This interaction between the robot and the BioLector (Robo-Lector) combines high-content data generation with systematic high-throughput experimentation in an automated fashion, offering new possibilities to study biological production systems. The presented platform uses a standard liquid-handling workstation with widespread automation possibilities. Thus, high-throughput cultivations can now be combined with small-scale downstream processing techniques and analytical assays. Ultimately, this novel versatile platform can accelerate and intensify research and development in the field of systems biology as well as modelling and bioprocess optimization.     

Application of principal component analysis and self-organizing map to the analysis of 2D fluorescence spectra and the monitoring of fermentation processes

2D fluorescence sensors produce a great deal of spectral data during fermentation processes, which can be analyzed using a variety of statistical techniques. Principal component analysis (PCA) and a self-organizing map (SOM) were used to analyze these 2D fluorescence spectra and to extract useful information from them. PCA resulted in scores and loadings that were visualized in the score-loading plots and used to monitor various fermentation processes with recombinantEscherichia coli andSaccharomyces cerevisiae. The SOM was found to be a useful and interpretative method of classifying the entire gamut of 2D fluorescence spectra and of selecting some significant combinations of excitation and emission wavelengths. The results, including the normalized weights and variances, indicated that the SOM network is capable of being used to interpret the fermentation processes monitored by a 2D fluorescence sensor.     

The baffled microtiter plate: Increased oxygen transfer and improved online monitoring in small scale fermentations

Most experiments in screening and process development are performed in shaken bioreactors. Today, microtiter plates are the preferred vessels for small‐scale microbial cultivations in high throughput, even though they have never been optimized for this purpose. To interpret the experimental results correctly and to obtain a base for a meaningful scale‐up, sufficient oxygen supply to the culture liquid is crucial. For shaken bioreactors this problem can generally be addressed by the introduction of baffles. Therefore, the focus of this study is to investigate how baffling and the well geometry affect the maximum oxygen transfer capacity (OTR_max) in microtiter plates. On a 48‐well plate scale, 30 different cross‐section geometries of a well were studied. It could be shown that the introduction of baffles into the common circular cylinder of a microtiter plate well doubles the maximum oxygen transfer capacity, resulting in values above 100 mmol/L/h (k_La > 600 1/h). To also guarantee a high volume for microbial cultivation, it is important to maximize the filling volume, applicable during orbital shaking. Additionally, the liquid height at the well bottom was examined, which is a decisive parameter for online‐monitoring systems such as the BioLector. This technology performs fiber‐optical measurements through the well bottom, therefore requires a constant liquid height at all shaking frequencies. Ultimately, a six‐petal flower‐shaped well geometry was shown to be the optimal solution taking into account all aforementioned criteria. With its favorable culture conditions and the possibility for unrestricted online monitoring, this novel microtiter plate is an efficient tool to gain meaningful results for interpreting and scaling‐up experiments in clone screening and bioprocess development. Biotechnol. Bioeng. 2009;103: 1118–1128. © 2009 Wiley Periodicals, Inc.     

An integrated high throughput strategy to screen mutants of Paenibacillus polymyxa with high polymyxin E-productivity

An integrated high-throughput screening (HTS) strategy was developed to screen large numbers of polymyxin E-producing mutants of Paenibacillus polymyxa. Various types of mutants were transferred onto the surfaces of solidified agar in 96-well microtiter plates, and then inoculated to 96-deep-well microtiter plates for micro-cultivation. The culture conditions were optimized for the production of polymyxin E. The supernatants from the micro-culture plates were transferred to 96-well bioassay microtiter plates containing Escherichia coli JM109 for high-throughput bioassay. By using this high-throughput screening (HTS) procedure, one best producer P. polymyxa PE 5.808 was identified from a large NTG mutated library with about 5,000 isolates. The volumetric productivity of polymyxin E of P. polymyxa PE 5.808 was 1,200 μg/ml in shake flasks, about 140% improvement compared with that of the wild type strain.     

Microfluidic biolector—microfluidic bioprocess control in microtiter plates

In industrial‐scale biotechnological processes, the active control of the pH‐value combined with the controlled feeding of substrate solutions (fed‐batch) is the standard strategy to cultivate both prokaryotic and eukaryotic cells. On the contrary, for small‐scale cultivations, much simpler batch experiments with no process control are performed. This lack of process control often hinders researchers to scale‐up and scale‐down fermentation experiments, because the microbial metabolism and thereby the growth and production kinetics drastically changes depending on the cultivation strategy applied. While small‐scale batches are typically performed highly parallel and in high throughput, large‐scale cultivations demand sophisticated equipment for process control which is in most cases costly and difficult to handle. Currently, there is no technical system on the market that realizes simple process control in high throughput. The novel concept of a microfermentation system described in this work combines a fiber‐optic online‐monitoring device for microtiter plates (MTPs)—the BioLector technology—together with microfluidic control of cultivation processes in volumes below 1 mL. In the microfluidic chip, a micropump is integrated to realize distinct substrate flow rates during fed‐batch cultivation in microscale. Hence, a cultivation system with several distinct advantages could be established: (1) high information output on a microscale; (2) many experiments can be performed in parallel and be automated using MTPs; (3) this system is user‐friendly and can easily be transferred to a disposable single‐use system. This article elucidates this new concept and illustrates applications in fermentations of Escherichia coli under pH‐controlled and fed‐batch conditions in shaken MTPs. Biotechnol. Bioeng. 2010;107: 497–505. © 2010 Wiley Periodicals, Inc.     

Bacterial growth properties at low optical densities

A method for accurate quantification of growth rate and yield of bacterial populations at low densities was developed with a modified version of a stepwise linear model for fitting growth curves based on optical density measurements, and adapted to measurements at low optical densities in 96-well microtiter plates. The method can be used for rapid and precise estimates of growth rate and yield, based on optical density measurements of large numbers of cultures of Escherichia coli. E. coli B lines were serially propagated at low glucose concentration during a long-term evolution experiment. Growth rate and yield of populations sampled from each of 12 lines that evolved for 20,000 generations under these conditions and two ancestral clones was measured. Populations were grown at three different glucose concentrations. Consistent with earlier findings, statistical analysis showed that both exponential growth rate and yield per unit of glucose differed significantly between the three glucose concentrations tested. Significant adaptation of the evolved populations to the nutrient conditions in which they evolved for 20,000 generations was observed. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

Characterisation of operation conditions and online monitoring of physiological culture parameters in shaken 24-well microtiter plates

A new online monitoring technique to measure the physiological parameters, dissolved oxygen (DO) and pH of microbial cultures in continuously shaken 24-well microtiter plates (MTP) is introduced. The new technology is based on immobilised fluorophores at the bottom of standard 24-well MTPs. The sensor MTP is installed in a sensor dish reader, which can be fixed on an orbital shaker. This approach allows real online measurements of physiological parameters during continuous shaking of cultures without interrupting mixing and mass transfer like currently available technologies do. The oxygen transfer conditions at one constant shaking frequency (250 1/min) and diameter (25 mm) was examined with the chemical sulphite oxidation method. Varied filling volumes (600–1,200 μL) of Escherichia coli cultures demonstrated the importance of sufficient oxygen transfer to the culture. Cultures with higher filling volumes were subjected to an oxygen limitation, which influenced the cell metabolism and prolongated the cultivation time. The effects could be clearly monitored by online DO and pH measurements. A further study of different media in an E. coli fermentation elucidated the different growth behaviour in response to the medium composition. The MTP fermentations correlated very well with parallel fermentations in shake flasks. The new technique gives valuable new insights into biological processes at a very small scale, thus enabling parallel experimentation and shorter development times in bioprocessing.     

96-well microtiter plates for biofouling simulation in biomedical settings

Microtiter plates with 96 wells are routinely used in biofilm research mainly because they enable high-throughput assays. These platforms are used in a variety of conditions ranging from static to dynamic operation using different shaking frequencies and orbital diameters. The main goals of this work were to assess the influence of nutrient concentration and flow conditions on biofilm formation by Escherichia coli in microtiter plates and to define the operational conditions to be used in order to simulate relevant biomedical scenarios. Assays were performed in static mode and in incubators with distinct orbital diameters using different concentrations of glucose, peptone and yeast extract. Computational fluid dynamics (CFD) was used to simulate the flow inside the wells for shaking frequencies ranging from 50 to 200?rpm and orbital diameters from 25 to 100?mm. Higher glucose concentrations enhanced adhesion of E. coli in the first 24?h, but variation in peptone and yeast extract concentration had no significant impact on biofilm formation. Numerical simulations indicate that 96-well microtiter plates can be used to simulate a variety of biomedical scenarios if the operating conditions are carefully set.     

Equalizing growth in high‐throughput small scale cultivations via precultures operated in fed‐batch mode

An often underestimated problem when working with different clones in microtiter plates and shake flask screenings is the non‐parallel and non‐equal growth of batch cultures. These growth differences are caused by variances of individual clones regarding initial biomass concentration, lag‐phase or specific growth rate. Problems arising from unequal growth kinetics are different induction points in expression studies or uneven cultivation periods at the time of harvest. Screening for the best producing clones of a library under comparable conditions is thus often impractical or even impossible. A new approach to circumvent the problem of unequal growth kinetics of main cultures is the application of fed‐batch mode in precultures in microtiter plates and shake flasks. Fed‐batch operation in precultures is realized through a slow‐release system for glucose. After differently growing cultures turn to glucose‐limited growth, they all consume the same amount of glucose due to the fixed feed profile of glucose provided by the slow‐release system. This leads to equalized growth. Inherent advantages of this method are that it is easy to use and requires no additional equipment like pumps. This new technique for growth equalization in high‐throughput cultivations is simulated and verified experimentally. The growth of distinctly inoculated precultures in microtiter plates and shake flasks could be equalized for different microorganisms such as Escherichia coli and Hansenula polymorpha. Biotechnol. Bioeng. 2009;103: 1095–1102. © 2009 Wiley Periodicals, Inc.     

On-line fluorescence profile of aerobic sludge digestion

An online fluorometer designed for following intracellular NAD(P)H was used to monitor aerobic sludge digestion experiments. The fluorescence showed an initial rise to a high plateau, a sharp decline after staying at the plateau for 20-60 h, and a trailing very slow decrease. The characteristic fluorescence profile was shown to result mainly from the solids-associated fluorescence, after ruling out other factors such as pH, temperature, and supernatant fluorescence. The fluorescence profile was, however, not a mere result of the decreasing solids concentration. The varying sludge viability and population composition (e.g., the decay of heterotrophs and the increasing fraction of nitrifiers) played important roles. The fluorescence profile correlated well with the profile of the viable heterotrophic cell number concentration evaluated with TSB-agar plates. The initial increase of the number concentration was attributed to the growth of multiple small bacteria from the lysate of each large microorganism, which was demonstrated in the experiments with baker's yeast as the starting culture for digestion. The fluorescence profiles observed in the yeast experiments were similar to those in the sludge experiments. Responding to glucose additions and the switch from aerobic to anaerobic conditions, the yeast systems showed typical step increases of fluorescence as expected from the change of NAD(P)H level associated with heterotrophic metabolism. However, no such fluorescence responses were detectable in the sludge digestion systems. NAD(P)H were thus uncertain to be responsible for the online fluorescence observed. Nonetheless, the initial fluorescence plateau corresponded to the period of rapid digestion and, for the plant studied, the EPA regulation criteria of VSS reduction >38% and/or SOUR <1.5 mg of O(2) (g of TS)(-)(1) h(-)(1) were satisfied at the end of the plateau. The online fluorescence provides an effective means of monitoring the aerobic sludge digestion process.     

Increased product formation induced by a directed secondary substrate limitation in a batch Hansenula polymorpha culture

By the use of directed limitations of secondary substrates, the metabolic flux should be deflected from biomass production to product formation. In order to study the impact of directed limitations caused by various secondary substrates on the growth and product formation of the methylotrophic yeast Hansenula polymorpha, the cultivation systems respiration activity monitoring system (RAMOS) and BioLector were used in parallel. While the RAMOS device allows the online monitoring of the oxygen transfer rate in shake flasks, the BioLector enables in microtiter plates the monitoring of scattered light and the fluorescence intensity of the green fluorescent protein (GFP). Secondary substrate limitations of phosphate, potassium, and magnesium were analyzed in batch fermentations. The sole carbon source was either 10 g/L glucose or 10 g/L glycerol. The expression of the GFP gene is controlled by the FMD promoter (formate dehydrogenase). In batch cultures with glucose as carbon source, a directed limitation of phosphate increased the GFP production 1.87-fold, compared to phosphate unlimited conditions. Under potassium-limited conditions with glycerol as sole carbon source, the GFP production was 1.41-fold higher compared to unlimited conditions. A limitation of the substrate magnesium resulted in a 1.22-fold increase GFP formation in the case of glycerol as carbon source.     

Quasi-continuous combined scattered light and fluorescence measurements: a novel measurement technique for shaken microtiter plates

A novel quasi-continuous on-line measuring technique for shaken microtiter plates is presented. Light scattering as well as intracellular and/or protein fluorescence (e.g. NADH, YFP) is measured during the shaking procedure, thus allowing a process monitoring of 96 different simultaneous cultures in a microtiter plate. In contrast to existing measurement techniques, the shaking process does not have to be stopped to take the measurements, thus avoiding the corresponding interruption of the cultures' oxygen supply and any unpredictable effects on the cultures. Experiments were conducted with E. coli in LB, TB, and MOPS minimal medium and V. natriegens in modified LB and TB media. Intensity curves of scattered light and NADH fluorescence were used to distinguish different lag phases, growth velocities, or inoculation densities. Data from this new method corresponded well to the off-line measured optical densities and to the oxygen transfer rates of cultures run in simultaneously conducted shake flask experiments at equivalent oxygen transfer capacities. With the aid of yellow fluorescence protein fused to interleukin-6 the optimal induction time of an expressing E. coli strain could be determined by on-line monitoring of product formation. Thus, this measuring technique enables the researcher to evaluate and to discriminate different cultures on a screening level and to improve screening conditions, process development and scale-up.     

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 μL) 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.     

A fluorescence study of Tn10-encoded Tet repressor

Steady-state fluorescence quenching and time-resolved measurements have been performed to resolve the fluorescence contributions of the two tryptophan residues, W43 and W75, in the subunit of the homodimer of the Tet repressor fromEscherichia coli. The W43 residue is localized within the helix-turn-helix structural domain, which is responsible for sequence-specific binding of the Tet repressor to thetet operator. The W75 residue is in the protein matrix near the tetracycline-binding site. The assignment of the two residues has been confirmed by use of single-tryptophan mutants carrying either W43 or W75. The FQRS (fluorescence-quenching-resolved-spectra) method has been used to decompose the total emission spectrum of the wild-type protein into spectral components. The resolved spectra have maxima of fluorescence at 349 and 324 nm for the W43 and W75 residues, respectively. The maxima of the resolved spectra are in excellent agreement with those found using single-tryptophan-containing mutants. The fluorescence decay properties of the wild type as well as of both mutants of Tet repressor have been characterized by carrying out a multitemperature study. The decays of the wild-type Tet repressor and W43-containing mutant can be described as being of double-exponential type. The W75 mutant decay can be described by a Gaussian continuous distribution centered at 5.0 nsec with a bandwidth equal to 1.34 nsec. The quenching experiments have shown the presence of two classes of W43 emission. One of the components, exposed to solvent, has a maximum of fluorescence emission at 355 nm, with the second one at about 334 nm. The red-emitting component can be characterized by bimolecular-quenching rate constant,k _q equal to 2.6×10⁹, 2.8×10⁹, and 2.0×10⁹ M^–1 sec^–1 for acrylamide, iodide, and succinimide, respectively. The bluer component is unquenchable by any of the quenchers used. The W75 residue of the Tet repressor has quenching rate constant equal to 0.85×10⁹ and 0.28 × 10⁹ M^–1 sec^–1 for acrylamide and succinimide, respectively. These values indicate that the W75 is not deeply buried within the protein matrix. Our results indicate that the Tet repressor can exist in its ground state in two distinct conformational states which differ in the microenvironment of the W43 residue.Abbreviations FQRS fluorescence-quenching-resolved spectra - HTH helix-turn-helix motif - TetR tetracycline repressor fromE. coli - WT wild-type TetR - W43 single point mutant with phenyloalanine substituted for tryptophan at position 75 in both subunits - W75 single point mutant with phenyloalanine substituted for tryptophan at position 43 in both subunits     

On-line process monitoring and chemometric modeling with 2D fluorescence spectra obtained in recombinant E. coli fermentations

2D spectrofluorometry produces a large volume of spectral data during fermentation processes with recombinant E. coli, which can be analyzed using chemometric methods such as principal component analysis (PCA), principal component regression (PCR) and partial least square regression (PLS). An analysis of the spectral data by PCA results in scores and loadings that are not only visualized in the score-loading plots but are also used to monitor the fermentation processes on-line. The score plots provided useful qualitative information on four fermentation processes for the production of extracellular 5-aminolevulinic acid (ALA). Two chemometric models (PCR and PLS) were used to examine the correlation between the 2D fluorescence spectra and a few parameters of the fermentation processes. The results showed that PLS had slightly better calibration and prediction performance than PCR.