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The "push-to-low" approach for optimization of high-density perfusion cultures of animal cells.

High product titer is considered a strategic advantage of fed-batch over perfusion cultivation mode. The titer difference has been experimentally demonstrated and reported in the literature. However, the related theoretical aspects and strategies for optimization of perfusion processes with respect to their fed-batch counterparts have not been thoroughly explored. The present paper introduces a unified framework for comparison of fed-batch and perfusion cultures, and proposes directions for improvement of the latter. The comparison is based on the concept of "equivalent specific perfusion rate", a variable that conveniently bridges various cultivation modes. The analysis shows that development of economically competitive perfusion processes for production of stable proteins depends on our ability to dramatically reduce the dilution rate while keeping high cell density, i.e., operating at low specific perfusion rates. Under these conditions, titer increases significantly, approaching the range of fed-batch titers. However, as dilution rate is decreased, a limit is reached below which performance declines due to poor growth and viability, specific productivity, or product instability. To overcome these limitations, a strategy referred to as "push-to-low" optimization has been developed. This approach involves an iterative stepwise decrease of the specific perfusion rate, and is most suitable for production of stable proteins where increased residence time does not compromise apparent specific productivity or product quality. The push-to-low approach was successfully applied to the production of monoclonal antibody against tumor necrosis factor (TNF). The experimental results followed closely the theoretical prediction, providing a multifold increase in titer. Despite the medium improvement, reduction of the specific growth rate along with increased apoptosis was observed at low specific perfusion rates. This phenomenon could not be explained with limitation or inhibition by the known nutrients and metabolites. Even further improvement would be possible if the cause of apoptosis were understood. In general, a strategic target in the optimization of perfusion processes should be the decrease of the cell-specific perfusion rate to below 0.05 nL/cell/day, resulting in high, batch-like titers. The potential for high titer, combined with high volumetric productivity, stable performance over many months, and superior product/harvest quality, make perfusion processes an attractive alternative to fed-batch production, even in the case of stable proteins.

Animals↗

[Study on aqueous extraction process for preparation of yuxianling granules].

OBJECTIVE: To optimize the aqueous extraction process for preparation of Yuxianling Granules in order to provide a basis for industrial-scale produce. METHODS: The amount of extract and the content of ferulic acid were used as indexes of the extraction process for Yuxianling Granules. The aqueous extract optimum condition of preparation was selected by orthogonal experimental design. RESULTS: The optimum extraction condition was adding ten, eight times amount of water into crude drug, soaking for 30 min, decocting for 1.5 h, 1.0 h. Both the content of ferulic acid and the amount of extract were the highest. CONCLUSION: The above extraction process gave the most rational, feasible and satisfactory results.

Coumaric Acids↗

Process analysis of fluidized bed granulation.

This study assesses the fluidized bed granulation process for the optimization of a model formulation using in-line near-infrared (NIR) spectroscopy for moisture determination. The granulation process was analyzed using an automated granulator and optimization of the verapamil hydrochloride formulation was performed using a mixture design. The NIR setup with a fixed wavelength detector was applied for moisture measurement. Information from other process measurements, temperature difference between process inlet air and granules (T(diff)), and water content of process air (AH), was also analyzed. The application of in-line NIR provided information related to the amount of water throughout the whole granulation process. This information combined with trend charts of T(diff) and AH enabled the analysis of the different process phases. By this means, we can obtain in-line documentation from all the steps of the processing. The choice of the excipient affected the nature of the solid-water interactions; this resulted in varying process times. NIR moisture measurement combined with temperature and humidity measurements provides a tool for the control of water during fluid bed granulation.

Excipients↗

Optimizing release from peptide hormone secretory nerve terminals.

Secretion of the peptide neurohormones oxytocin and vasopressin from terminals of magnocellular neurones in the mammalian neurohypophysis is elicited by conduction of depolarizing action potentials into terminal membranes, inducing opening of voltage-sensitive Ca2+ channels, entry of Ca2+ from the extracellular space and a rise in cytoplasmic Ca2+ concentration. The amount of peptide released per action potential is not immutable. In particular, the patterns in which action potentials are generated at the cell somata of the two types of neurone each appear exquisitely suited to optimize the release process at the terminal by utilizing a frequency-facilitation mechanism and by minimizing a mechanism of fatigue in the release process. The different properties of oxytocin and vasopressin neurones are of important physiological significance. The secretory terminals are also a site of receptor-mediated influences of neuromodulators which can greatly alter release efficiency. The mechanisms underlying facilitation and fatigue are not clearly understood. The evidence suggests that processes both prior to depolarization of the terminals (propagation and form of the action potentials) and directly at the terminals (frequency/pattern-dependent Ca2+ entry and channel openings) are involved. Transient activity-related increases in extracellular K+ concentration may be involved at both sites. Two types of neuromodulation have been partly characterized. Kappa-Opioid receptors in secretory terminal membranes directly modulate depolarization-evoked peptide release probably via interactions with Ca2+ channels. beta-Adrenergic receptors localized on neurohypophyseal astroglial cells mediate more subtle effects of noradrenaline. In the more chronic situation the neurohypophyseal astroglia alter their morphological relationships with neurosecretory elements and the basal lamina at release sites, changes which may also serve to optimize the secretory process.

Animals↗

Applications of process analytical technology to crystallization processes.

Crystallizations of pharmaceutical active ingredients, particularly those that posses multiple polymorphic forms, are among the most critical and least understood pharmaceutical manufacturing processes. Many process and product failures can be traced to a poor understanding and control of crystallization processes. The Food and Drug Administration's process analytical technology (PAT) initiative is a collaborative effort with industry to introduce new and efficient manufacturing technologies into the pharmaceutical industry. PAT's are systems for design, analysis, and control of manufacturing processes. They aim to assure high quality through timely measurements of critical quality and performance attributes of raw materials, in-process materials, and final products. Implementation of PAT involves scientifically based process design and optimization, appropriate sensor technologies, statistical and information tools (chemometrics), and feedback process control strategies working together to produce quality products. This review introduces the concept of PAT and discusses its application to crystallization processes through review of several case studies. A variety of in situ analytical methods combined with chemometric tools for analysis of multivariate process information provide a basis for future improvements in modeling, simulation, and control of crystallization processes.

Amino Acids↗

Evaluation and prediction of stereoisomerizations in comprehensive two-dimensional chromatography.

Conformational and configurational changes such as isomerizations, epimerizations, diastereomerizations and, enantiomerizations are important for the investigation of a large variety of processes ranging from protein folding to the stereostability of drugs. Under optimized conditions, these processes lead to an elution profile characterized by a plateau formation between the two interconverting species in chromatographic separations in a certain temperature range. By temperature-dependent measurements and subsequent computer simulation of the experimental chromatograms, the forward and backward rate constants k1 and k(-1), the Gibb's energy DeltaG++, activation enthalpy DeltaH++, and entropy DeltaS++ can be obtained. Due to its high efficiency two-dimensional chromatography is able to resolve the time-dependent distribution of the two species in the second dimension, thereby yielding the precise ratio of stereoisomers. An algorithm for the simulation and evaluation of two-dimensional chromatographic experiments has been developed, based on the theoretical plate model, which allows the determination of rate constants and barriers of isomerization, epimerization, and enantiomerization processes from two-dimensional chromatographic experiments. In the present article a detailed description of the extended theoretical plate model required for the simulation, the methods available, and examples for the evaluation of complex experimental data and the prediction of the separation conditions to observe isomerization, epimerizations, and enantiomerizations in two-dimensional chromatography are given.

Journal Article↗

Studies on the Processivity of Maize DNA Polymerase 2, an [alpha]-Type Enzyme.

This paper describes studies on the processivity of an [alpha]-type DNA polymerase from maize (Zea mays L.) embryonic axes, designated as DNA polymerase 2. Using poly(dA)/oligo(dT) as template, DNA polymerase 2 has a processivity of 18 ([plus or minus]5) nucleotides incorporated, a value much lower than that found for wheat [alpha]-type DNA polymerase (P. Laquel, S. Litvak, M. Castroviejo [1993] Plant Physiol 102: 107-114). Conditions that maximally stimulate enzyme activity, such as 100 mM KCl and 12 mM Mg2+, are strongly inhibitory of processivity and cause the enzyme to become distributive under these conditions. Optimal concentrations for processivity are 10 mM KCl and 1 to 2 mM Mg2+. Both enzyme activity and processivity were found to be similar at different Mn2+ concentrations. Both DNA polymerase 2 activity and processivity are greatly reduced by spermine and N-ethylmaleimide. A distinguishing feature of processivity in DNA polymerase 2 was the response to ATP, which not only stimulated processivity by more than 2-fold, but also produced a distinctive pattern in which the enzyme seemed to pause every 10 nucleotides, reaching a value of 40 to 50 nucleotides incorporated. This pattern was observed in some, but not all, heparin-Sepharose fractions with enzyme activity, suggesting the possibility of different DNA polymerase 2 complexes.

Journal Article↗

A novel approach to data processing of the QT interval response in the conscious telemetered beagle dog.

INTRODUCTION: Drug-induced QT interval prolongation may lead to ventricular arrhythmias. The aim of the study was to optimize QT interval data processing to quantify drug-induced QT interval prolongation in the telemetry instrumented conscious dog model. METHODS: The test substances cisapride, dofetilide, haloperidol, and terfenadine and corresponding vehicles were given to male and female beagle dogs during two consecutive 90-min intravenous infusions. Cardiovascular parameters were recorded for 24 h and exposure to the drugs was measured. The delayed response in the QT interval after an abrupt change in heart rate was investigated. Eight mathematical models to describe the QT interval-heart rate relationship were compared and different sets of covariates were used to quantify the drug-induced effect on the QT interval. RESULTS: After an abrupt decrease in heart rate, a 75% adaptation of the QT interval was reached after 54+/-9 s. A linear model was preferred to correct the drug-induced effect on the QT interval for heart rate, vehicle effect, serial correlation, plasma concentration and time of day. All test substances significantly prolonged the QT interval. DISCUSSION: To optimize the processing of QT interval data, the delay in QT interval response after an abrupt change in heart rate should be considered. The QT interval-heart rate relationship and vehicle response were individual-specific and corrections were therefore made individually. When estimating the drug-induced effect on the QT interval it is considered advantageous to use plasma concentration as a covariate, as well as adjusting for vehicle effect and serial correlation in measurements. The conscious dog model detected significant increases in the QT interval for all test substances investigated.

Algorithms↗

[Clinical pathways in psychiatry and psychotherapy].

BACKGROUND: Implementing evidence-based clinical guidelines by means of clinical pathways is one of the key elements of continuous quality management at the University Hospital of Marburg. This paper explains how clinical pathways for suicidal ideation and suicide attempts were developed. METHODS: Based upon a review of existing guidelines and literature, optimal standards of care were defined. Step-by-step analysis of the process of care and results of a questionnaire were used to describe the actual processes. A problem-orientated comparison of the actual and the optimal process of care was the basis for developing these pathways. A consensus was achieved with all persons involved in the respective process of care taking into consideration local resources as well as barriers. The most important decisions and interventions were defined and presented as a patient-oriented process. RESULTS: The lack of explicit "how to do it"-recommendations of the guidelines for the entire care processes required specific, locally tailored adaptations. Potentials for improvement were identified in the following areas: transfer of patients, consultation, information and coordination within the team, and diagnosis of suicide risk. The pathways include care-oriented algorithms, checklists and assignments of responsibility. CONCLUSIONS: The development of clinical pathways as part of quality management and transsectoral integrated care in psychiatry and psychotherapy is feasible. The concept presented incorporates the potential of increasing transparency, efficiency and efficacy of care, and of improving satisfaction of those involved. It offers psychiatric hospitals the chance to guarantee optimal quality of care in face of increasing workload and costs.

Critical Pathways↗

Magnetic resonance imaging. Part I--physical principles.

Magnetic resonance (MR) imaging is the most complex imaging technology available to clinicians. Whereas most imaging technologies depict differences in one, or occasionally two, tissue characteristics, MR imaging has five tissue variables-spin density, T(1) and T(2) relaxation times and flow and spectral shifts-from which to construct its images. These variables can be combined in various ways by selecting pulse sequences and pulse times to emphasize any desired combination of tissue characteristics in the image. This selection is determined by the user of the MR system before imaging data are collected. If the selection is not optimal, the imaging process must be repeated at a cost of time and resources. The optimal selection of MR imaging procedures and the proper interpretation of the resultant images require a thorough understanding of the basic principles of MR imaging. Included in this understanding should be at least the rudiments of how an MR imaging signal is produced and why it decays with time; the significance of relaxation constants; the principles of scanning methods such as saturation recovery, inversion recovery and spin echo; how data obtained by these methods are used to form an image, and how the imaging data are complied by multi-slice and volumetric processes. In selecting an MR imaging unit, information about different magnet designs (resistive, superconductive and permanent) is useful. Although no bioeffects are thought to be associated with an MR imaging examination, some knowledge of the attempts to identify bioeffects is helpful in alleviating concern in patients.

Humans↗

Human chymotrypsinogen B production with Pichia pastoris by integrated development of fermentation and downstream processing. Part 1. Fermentation.

Based on an integrated approach of genetic engineering, fermentation process development, and downstream processing, a fermentative chymotrypsinogen B production process using recombinant Pichia pastoris is presented. Making use of the P. pastoris AOX1-promotor, the demand for methanol as the single carbon source as well as an inducer of protein secretion enforced the use of an optimized feeding strategy by help of on-line analysis and an advanced controller algorithm. By using an experimental system of six parallel sparged column bioreactors, proteolytic product degradation could be minimized while also optimizing starting conditions for the following downstream processing. This optimization of process conditions resulted in the production of authentic chymotrypsinogen at a final concentration level of 480 mg.L(-)(1) in the whole broth and a biomass concentration of 150 g.L(-)(1) cell dry weight, thus comprising a space-time yield of 5.2 mg.L(-)(1).h(-)(1). Alternatively to the high cell density fermentation approach, a continuous fermentation process was developed to study the effects of reduced cell density toward oxygen demand, cooling energy, and biomass separation. This development led to a process with a highly increased space-time yield of 25 mg.L(-)(1).h(-)(1) while reducing the cell dry weight concentration from 150 g.L(-)(1) in fed-batch to 65 g.L(-)(1) in continuous cultivation.

Chymotrypsinogen↗

Designing relational models of collaborative integrative medicine that support healing processes.

The concept of optimal healing environments (OHE) includes a variety of elements that require exploration, definition, measurement, and interpretation. One key element is the relationships between healer and patient/client and between healers themselves. These complexities mean that models of OHE that include relationship dynamics as resources in the healing processes need information to help planning, execution and measurement. This paper examines aspects of a proposed model of optimal healing that utilizes relational dynamics as central to healing processes. The dynamics of relationships between healers and clients are critical to the effectiveness of healing as a process of transformation. Conscious examination of healers' emotional availability in relationship-centered care may be important in determining primary roles in delivering care.

Attitude of Health Personnel↗

Study of process variables in industrial acetic fermentation by a continuous pilot fermentor and response surfaces.

The modeling and optimization of industrial processes requires an intensive study of the factors involved. In this work, a continuous pilot system for studying the industrial process of acetic fermentation is developed. A Doehlert design is applied to the five variables involved in the pilot process. This experimental design allows reduction of the experimental burden and the maximum amount of information to be obtained, studying the factors at different levels depending on their significance. The experimental system provides a robust measure of the specific growth rate and the rates of substrates consumption and acetic acid production, related to the flow of effluent stream evaluated in the steady state. The results demonstrate the growth-associated kinetics of substrates and product, and the yield factors are calculated with low values of variances for the coefficients, i.e., within the range 1-11%. The specific growth rate suits the quadratic model proposed. The response surfaces generated by the model are applied to explain the behavior of the bacterial growth and, therefore, the effects of the process variables studied over the acetic acid production. Very low levels of ethanol or oxygen make the acetification rate decrease, and a saturation effect with high levels of ethanol or oxygen is also deduced. The effects of the aeration rate, agitation, and overpressure suggest a kind of inhibition of the acetic acid production caused by the oxygen that has not been practically studied before. The temperature strengthens the inhibitory effect of the ethanol and the oxygen. The conclusions of this work consolidate the structure of a hybrid model for the acetic fermentation.

Acetates↗

Optimization of activation conditions of Rhodobacter sphaeroides in hydrogen generation process.

AIMS: To examine the effects of the culture age, illuminance intensity and changes in these parameters during activation on hydrogen generation process carried out by purple nonsulfur Rhodobacter sphaeroides bacteria. METHODS AND RESULTS: The following parameters were determined in all experiments: the amount of hydrogen evolved (measured using gas chromatography), biomass increase as dry mass, pH values and consumption of organic substance as chemical oxygen demand (COD). The medium used in the process of activation and hydrogen generation contained malic acid (15 mmol) and sodium glutamate (2 mmol). The optimum age of bacteria was 12-24 h and the best intensity of illuminance was found to be 5 cd sr m-2 on activation and 9 cd sr m-2 on hydrogen generation. These conditions provided hydrogen evolution of 1.39 l l-1 of the medium with the highest specific hydrogen production of 0.146 l H2 l-1 medium h-1 g-1 inoculum. An increase in the illuminance intensity resulted in a slight inhibition of the process. CONCLUSIONS: The activation stage of bacteria has a significant effect on the parameters of hydrogen photogeneration. The optimization of the activation stages allowed a shortening of the time of hydrogen generation and of the period after which hydrogen evolution starts. SIGNIFICANCE AND IMPACT OF THE STUDY: An innovative method of bacteria activation before the initiation of the hydrogen generation process has been used to optimize this process. The shortening of the process duration as well as the twice higher hydrogen yield can help in the designing of other systems (including also those operating under solar irradiation) in which R. sphaeroides bacteria are to be applied.

Biomass↗

Optimal design of protein production plants with time and size factor process models.

In this work we propose an optimization model for the design of a biotechnological multiproduct batch plant. A first level of detail posynomial model is constructed for each unit, as well as decisions regarding the structural optimization of the plant. A particular feature of this model is that it contains composite units in which semicontinuous items operate on the material contained by batch items. This occurs in the purification steps, in particular with the microfilters operating between retentate and permeate vessels, and with the homogenizer and ultrafilters operating on the material contained in a batch holding vessel. Also, the unit models rely on batch operating time expressions that depend on both the batch size and the size of semicontinuous items. The model takes into account all of the available options to increase the efficiency of the batch plant design: unit duplication in-phase and out-of-phase and intermediate storage tanks. The resulting mathematical model for the minimization of the plant capital cost is a mixed integer non-linear program (MINLP), which is solved to global optimality with an implementation of the outer approximation/ equality relaxation/ augmented penalty (OA/ER/AP) method. A plant that produces four recombinant proteins in eight processing stages is used to illustrate the proposed approach. An interesting feature of this example is that it represents an attempt to standardize a plant for the production of both therapeutic and nontherapeutic proteins; the model applied is generic and can thus be applied to any such modular plant. Results indicate that the best solution in terms of minimal capital cost contains no units in parallel and with intermediate storage tank allocation.

Algorithms↗

Process parameter shifting: Part I. Effect of DOT, pH, and temperature on the performance of Epo-Fc expressing CHO cells cultivated in controlled batch bioreactors.

The impact of process environment changes on process performance is one of the most crucial process safety issues when cultivating mammalian cells in a bioreactor. In contrast, directed shifting of process parameters can also be used as an optimization tool providing higher cell and product yields. Compared to other strategies that also aim on the regulation of cell growth and protein expression process parameter shifts can be easily performed without reagent addition or even genetic modification of the host cell line. However, a successful application of changing process conditions implies a profound understanding of the provoked physiological changes within the cells. In a systematic approach we varied the dissolved oxygen tension (DOT), pH, and temperature of CHO cultures in controlled bioreactors and investigated the impact on growth, productivity, metabolism, product quality and cell cycle distribution using a recombinant CHO cell line expressing the highly glycosylated fusion protein Epo-Fc. We found the reduction of cultivation temperature and the reduction of (external) pH to exert the most significant effects on process performance by mainly reducing cell growth and metabolism. With respect to the cell line used we identified a set of parameters capable of affecting cell proliferation in favor of an increased specific productivity and total product yield. The well directed alteration of the process environment has emerged as a tool adequate for further process optimization applying a biphasic cultivation strategy.

Animals↗

Optimization of serum-free fermentation processes for antibody production.

Serum free fermentation procedures of cell cultures have got a wide application in production of biochemicals. But, cells cultured in serum free media in general are more sensitive to changes in culture condition, especially to nutrient limitation. There are no substances from serum which can support the cells when conditions are changing. In this study special attention is directed to amino acid utilization of mouse hybridoma in batch, chemostat and perfusion fermentations. Detailed data are presented which show the considerable difference of amino acid consumption rates in different fermentation modes. Already, in batch mode there are differences of the two investigated mouse hybridoma cell lines, although they are derived from the same myeloma line. In chemostat running at a dilution rate representing maximal growth rate most of the consumption rates are significant higher than in batch. On the other hand, in perfusion mode the rates are lower than in batch. This indicates clearly the different conditions of the fermentation modes. Therefore, it is necessary to develop serum free processes under the desired production conditions. An accurate analysis of the process is strongly recommended.

Amino Acids↗

Fundamental bottlenecks in the application of continuous bioprocesses.

Continuous culture is applied mainly as a research tool and much less as a production process. Fundamental bottlenecks in continuous culture are discussed to help shed light on this apparent contradiction. Based on a discussion of technical, process related, and economic/market bottlenecks it is concluded that the often mentioned productivity argument in favor of continuous processing is much too simple. The optimal choice of a process mode is determined by a full understanding of the equipment and production plant factors and of the economic/market factors. Very often the resulting choice will be the fed batch and/or the cell retention process mode which is characterized by low growth rates. Therefore more research towards product formation at low growth rates (less than 0.05 h-1) is needed.

Beer↗