The scale-down of an industrial disc stack centrifuge

The means are described whereby a disc stack centrifuge may be scaled-down by up to 10-fold of its separation capacity. The centrifuge separation characteristics so measured are suitable for direct scale-up predictions of centrifuge performance where only small volumes of particle suspension are available for study. Such an ability to scale-down is especially important in the processing of biological particles where for example, in the early stage of process development, there is often insufficient fermentation broth for fullscale studies. Scale-down is achieved by the reduction of the number of discs available for separation purposes and by the careful positioning of these discs in the overall disc stack. A combination of dye tracer and particle separation studies are used to optimise the disc stack configuration. The resulting grade efficiency curve is an accurate reflection of the curve for the full-scale centrifuge especially in the critical design region specifying centrifuge throughput for near complete particle recovery.     

A comparison of two centrifuge techniques for constructing vulnerability curves: insight into the ‘open‐vessel’ artifact

A vulnerability curve (VC) describes the extent of xylem cavitation resistance. Centrifuges have been used to generate VCs for decades via static‐ and flow‐centrifuge methods. Recently, the validity of the centrifuge techniques has been questioned. Researchers have hypothesized that the centrifuge techniques might yield unreliable VCs due to the open‐vessel artifact. However, other researchers reject this hypothesis. The focus of the dispute is centered on whether exponential VCs are more reliable when the static‐centrifuge method is used rather than the flow‐centrifuge method. To further test the reliability of the centrifuge technique, two centrifuges were manufactured to simulate the static‐ and flow‐centrifuge methods. VCs of three species with open vessels of known lengths were constructed using the two centrifuges. The results showed that both centrifuge techniques produced invalid VCs for Robinia because the water flow through stems under mild tension in centrifuges led to an increasing loss of water conductivity. In addition, the injection of water in the flow‐centrifuge exacerbated the loss of water conductivity. However, both centrifuge techniques yielded reliable VCs for Prunus, regardless of the presence of open vessels in the tested samples. We conclude that centrifuge techniques can be used in species with open vessels only when the centrifuge produces a VC that matches the bench‐dehydration VC.     

Centrifuge Modeling of Cadmium Migration in Saturated and Unsaturated Soils

Researchers recently have come to recognize that geotechnical centrifuge can provide a powerful experimental tool for investigating the flow and transport of inorganic contaminants in soils. Inert, non-adsorptive inorganic compounds (e.g., sodium ions) rather than adsorptive heavy metals are often used as the chemical for the investigation of pollutant transport behavior in most centrifuge modeling. To overcome the shortcomings of this approach, centrifuge tests for the study of one-dimensional pollutant migration in both saturated and unsaturated soils were designed using an adsorptive pollutant (i.e., cadmium) and conducted at two centrifugal accelerations. In this study, the concentration profile of adsorptive cadmium along the depth of soil, the moisture content varying with the soil depth and the transport behavior of the cadmium in soils were investigated. The centrifuge results show that the cadmium concentration profiles are found to be similar for the centrifuge models performed at 15 g and 20 g and the one-dimensional moisture movement in the unsaturated soil can be reproducible. The validity of centrifuge modeling of adsorptive pollutants might be affected by the g-level that, in turn, determines the centrifuge testing time and affects the sorption equilibrium.     

The total containment of a batch-type zonal centrifuge.

A batch-type zonal centrifuge has been modified and totally contained for use with biologically hazardous materials. A sealed cabinet encloses the centrifuge and the ancilliary equipment. It is operated with a flow of filtered air when the zonal system is on, decontaminated with ethylene oxide, and maintained at a negative pressure throughout. The centrifuge subsystems can be drained, flushed, and decontaminated with ethylene oxide before an engineer services the machine. The sample handling system within the cabinet is remotely controlled.     

Aquatic animals and use of centrifuge in space experiments]

There are some experiments which do not need a centrifuge apparatus in space, however, for other space experiments the use of centrifuge is indispensable as the control. The characteristics of these two types of space experiments are explained. Generally, the more quantitatively the phenomenon is analyzed, the greater the need of centrifuge apparatus becomes. The centrifuge in space can realize various gravity values ranging from 0 to 1 G, and this will extend the present biology to a more universal biology.     

Evaluation of a single-use disk stack centrifuge for improved efficiency and sustainability at 1000 L GMP manufacturing scale

Direct depth filtration is an established technology for single-use harvest operation. Advantages of direct depth filtration include familiarity with depth filtration in downstream processes and simplicity of the operation. Drawbacks include low capacity, large footprint, labor-intensive set-up, high water use, and high waste in the form of discarded filters. Single-use centrifugation is emerging as an alternative to depth filtration for the single-use harvest step. Within the single-use centrifugation space, disc stack centrifugation represents the newest entrant. In this study, we evaluated the performance of the GEA kytero single-use disc stack centrifuge to clarify two monoclonal antibody-producing cell culture fluids. The separation performance of the GEA kytero centrifuge varied between the two cell culture fluids, with differences in centrate turbidity and centrate filterability measured. A comparison was then performed to determine resource savings, compared to direct two-stage depth filtration, when using a GEA kytero centrifuge to harvest a 1000 L bioreactor. The analysis concluded that replacement of the first stage of depth filters with a GEA kytero centrifuge has the potential to decrease the required second stage depth filtration area by up to 80%. The decrease in depth filter area resulting from the use of the GEA kytero would result in a decrease in the harvest step footprint, a decrease in buffer volume required to prime and rinse depth filters, and a decrease in the volume of plastic waste. An economic comparison of the GEA kytero single-use centrifuge against a direct depth filtration step found that for a 1000 L harvest step, the GEA kytero centrifuge may reduce costs by up to 20% compared with two-stage direct depth filtration.     

Control and optimization of apheresis procedures in a COBE 2997 cell separator

To obtain more efficient operation of a COBE Model 2997 clinical cell separator using either a Single Stage II (SS II) or a Dual Stage separation chamber, modifications were made to allow complete computer control. Product cell density was detected using an optical sensor and controlled by automatic feedback through a microcomputer interface. Control was accomplished by automatically adjusting the red blood cell (RBC) and plasma product flow rates using a proportional-integral (PI) algorithm. Results show that, using either chamber, the product cell density can be maintained at a preselected value for extended periods of time without operator intervention. This system allowed investigation of optimal operating regions for plateletpheresis and leukapheresis procedures. The effects of centrifuge rpm and controller set point on centrifuge operation were investigated using a second order factorial experimental design. Theoretical significance of model parameters was assessed with the aid of a hindered settling model and simple reasoning about the interface position relative to the collection port. The results suggest that, in either chamber, the optimum operating region for plateletpheresis procedures occurs at moderate controller set points and high centrifuge rpm. The resultant operating efficiency and product purity values are approximately 63 percent and 0.65 respectively in the SS II chamber and approximately 70 percent and 0.70 respectively in the Dual Chamber. In the SS II, the optimum operating region for leukapheresis procedures occurred at high controller set point values for any centrifuge rpm above 1200 with an operating efficiency near 100 percent. However, in the Dual Chamber, the optimum operating region for leukapheresis procedures occurred at high controller set points and high centrifuge rpm's, again providing an operating efficiency near 100 percent.     

The use of laboratory centrifugation studies to predict performance of industrial machines: studies of shear-insensitive and shear-sensitive materials

A method for using a bench-top centrifuge is described in order to mimic the recovery performance of an industrial-scale centrifuge, in this case a continuous-flow disc stack separator. Recovery performance was determined for polyvinyl acetate particles and for biological process streams of yeast cell debris and protein precipitates. Recovery of polyvinyl acetate particles was found to be well predicted for these robust particles. The laboratory centrifugation scale-down technique again predicted the performance of the disc stack centrifuge for the recovery of yeast cell debris particles although there was some suggestion of over-prediction at high levels of debris recovery due to the nature of any cell debris aggregates present. The laboratory centrifuge scale-down technique also proved to be an important investigative probe into the extent of shear-induced breakup of shear-sensitive protein precipitate aggregates during recovery in continuous high speed centrifuges. Such breakup can lead to over 10-fold reduction in separator capacity.     

Modeling industrial centrifugation of mammalian cell culture using a capillary based scale-down system

Continuous-flow centrifugation is widely utilized as the primary clarification step in the recovery of biopharmaceuticals from cell culture. However, it is a challenging operation to develop and characterize due to the lack of easy to use, small-scale, systems that can be used to model industrial processes. As a result, pilot-scale continuous centrifugation is typically employed to model large-scale systems requiring a significant amount of resources. In an effort to reduce resource requirements and create a system which is easy to construct and utilize, a capillary shear device, capable of producing energy dissipation rates equivalent to those present in the feed zones of industrial disk stack centrifuges, was developed and evaluated. When coupled to a bench-top, batch centrifuge, the capillary device reduced centrate turbidity prediction error from 37% to 4% compared to using a bench-top centrifuge alone. Laboratory-scale parameters that are analogous to those routinely varied during industrial-scale continuous centrifugation were identified and evaluated for their utility in emulating disk stack centrifuge performance. The resulting relationships enable bench-scale process modeling of continuous disk stack centrifuges using an easily constructed, scalable, capillary shear device coupled to a typical bench-top centrifuge.     

Single-Molecule Assay for Proteolytic Susceptibility: Force-Induced Collagen Destabilization

Force plays a key role in regulating dynamics of biomolecular structure and interactions, yet techniques are lacking to manipulate and continuously read out this response with high throughput. We present an enzymatic assay for force-dependent accessibility of structure that makes use of a wireless mini-radio centrifuge force microscope to provide a real-time readout of kinetics. The microscope is designed for ease of use, fits in a standard centrifuge bucket, and offers high-throughput, video-rate readout of individual proteolytic cleavage events. Proteolysis measurements on thousands of tethered collagen molecules show a load-enhanced trypsin sensitivity, indicating destabilization of the triple helix.     

A methodology for centrifuge selection for the separation of high solids density cell broths by visualisation of performance using windows of operation

Expression systems capable of growing to high cell densities are now readily available and are popular due to the benefits of increased product concentration. However, such high solids density cultures pose a major challenge for bioprocess engineers as choosing the right separation equipment and operating it at optimal conditions is crucial for efficient recovery. This study proposes a methodology for the rapid determination of suitable operating conditions for the centrifugal recovery of high cell density fermentation broths. An ultra scale-down (USD) approach for the prediction of clarification and dewatering levels achieved in a range of typical high-speed centrifuges is presented. Together with a visualisation tool, a Window of Operation, this provides for the rapid analysis of separation performance and evaluation of the available operating conditions, as an aid in the selection of the centrifuge equipment most appropriate for a given process duty. A case study examining centrifuge selection for the processing of a high cell density Pichia pastoris culture demonstrates the method. The study examines semi-continuous disc-stack centrifuges and batch-operated machines such as multi-chamber bowls and Carr Powerfuges. Performance is assessed based on the variables of clarification, dewatering and product yield. Inclusion of limits imposed by the centrifuge type and design, and operation itself, serve to constrain the process and to define the Windows of Operation. The insight gained from the case study provides a useful indication of the utility of the methodology presented and illustrates the challenges of centrifuge selection for the demanding case of high solids concentration feed streams.     

Physiological response of pilots to the load of lower body negative pressure

The Czech Air-Force prepares an introduction of a new generation of aircraft with high maneuvering possibilities. The possibility of making full use of the aircraft flight properties assumes sufficient pilot's +Gz tolerance and also its improvement during the new flight training system. The optimal method to achieve this purpose is the human centrifuge utilization. For the Czech Republic, the building or the renting of a human centrifuge for the pilot's selection is unfortunately very expensive. In our institute we are interested in the analysis of the possibilities of the lower body negative pressure (LBNP) technique for the basic pilot's selection with low level of +Gz tolerance, using the examination of the orthostatic cardiovascular reactions of the pilot's organism.     

A simple method for the extraction of soil solution by high speed centrifugation

Summary A simple technique for extracting samples of soil solution by high speed centrifugation is described. The method uses inexpensive commerically available centrifuge tubes requiring only slight modification. Aspects of the method are discussed together with an example of its application.     

离心机训练对大鼠脑及其它组织IL-6和TNFα基因表达水平的影响

为了解离心机训练前后大鼠脑及心、肺、肾和小肠组织中IL 6和TNFα基因表达水平的变化 ,对雄性SD大鼠进行动物离心机训练 ,刺激值从 + 7Gz～ + 12Gz ,每天增加 + 0 5Gz ,第 12d重复 + 12Gz刺激 ,第 13d离心机训练后 ,断头处死 ,取心、脑、肺、肾和小肠组织 ,分别提取mRNA并定量 .用地高辛标记IL 6和TNFαcDNA作为探针 ,进行狭缝杂交 ,杂交结果通过光密度扫描定量后 ,进行统计学处理 .离心机训练不同时间 ,比较大鼠各组织IL 6和TNFα基因表达水平的变化 .结果显示随着训练时间的延长 ,表达水平均有所差异 .提示训练对大鼠脑及其它主要组织IL 6和TNFα基因表达水平有影响 ,这种影响可能与机体对加速度作用的习服有关     

Large-scale perfusion culture process for suspended mammalian cells that uses a centrifuge with multiple settling zones

A high-cell-density perfusion culture process, using a novel centrifuge, was developed. The centrifuge has spiral multiple settling zones to separate cells from culture medium. Because of the multiple zones, the separation area can be efficiently increased without enlarging the diameter of the centrifuge. The centrifuge used in this study had a separation capacity of 2600 ml culture medium min^–1 at 100g of the centrifugal force. A new cell separation and withdrawal method was also developed. The cells separated in the centrifuge can be withdrawn easily from the centrifuge with no cell clogging by feeding a liquid carrier such as a perfluorocarbon into the centrifuge and pushing the cells out with the liquid carrier. By this culture process, monoclonal antibodies were produced with mouse-human hybridoma X87X at a cell density of about 8 × 10⁶ cells ml^–1 for 25 days. This centrifuge culture shows promise as a large-scale perfusion culture process.     

Cycle-powered short radius (1.9M) centrifuge: exercise vs. passive acceleration

A human-powered short-arm centrifuge is described. This centrifuge could be used during spaceflight to provide +Gz acceleration while subjects performed exercise, thus supplying two forms of weightlessness countermeasures. Results from a study of cardiovascular responses while using the centrifuge are presented.     

Effects of gravitropic stress on the development of the primary root of lentil seedlings grown in space

Root growth and cell differentiation were analysed in lentil seedlings grown (1) in microgravity (F microg), (2) on the 1 x g centrifuge (F1 x g), (3) in microgravity and placed on the 1 x g centrifuge for 4 h [F(microg + 1 x g)], (4) on the 1 x g centrifuge and placed in microgravity for 4 h [F(1 x g + microg)]. In microgravity, there were strong oscillations of the root tip, even when the seedlings were grown first on the 1 x g centrifuge [F(1 x g + microg)]. In the [F(microg + 1 x g)] sample, the roots grown in microgravity were oblique with respect to the 1 x g acceleration when the seedlings were placed on the centrifuge. They were therefore gravistimulated. However, root length was similar in the 4 samples after 29 h of growth and growth rate of the root was the same between 25 h and 29 h although it appeared to be slightly greater in the [F(microg + 1 x g)] sample. Cell elongation was analysed as a function of the distance from the root cap junction. Cell length was similar in the seedlings grown in microgravity or on the 1 x g centrifuge. The transfer from the 1 x g centrifuge to microgravity [F(1 x g + microg)] did not modify cell elongation in the roots. Cell length in the roots which were grown in microgravity and gravistimulated [F(microg + 1 x g)] was different from that observed in microgravity but this was only due to gravistimulation. Thus, gravity does not have an effect on cell elongation when the roots are strictly oriented in the vertical position but it does as soon as the root tip deviates from this orientation.     

Vulnerability curves by centrifugation: is there an open vessel artefact,and are ‘r’ shaped curves necessarily invalid?

Vulnerability curves using the 'Cavitron' centrifuge rotor yield anomalous results when vessels extend from the end of the stem segment to the centre ('open-to-centre' vessels). Curves showing a decline in conductivity at modest xylem pressures ('r' shaped) have been attributed to this artefact. We determined whether the original centrifugal method with its different rotor is influenced by open-to-centre vessels. Increasing the proportion of open-to-centre vessels by shortening stems had no substantial effect in four species. Nor was there more embolism at the segment end versus centre as seen in the Cavitron. The dehydration method yielded an 'r' shaped curve in Quercus gambelii that was similar to centrifuged stems with 86% open-to-centre vessels. Both 'r' and 's' (sigmoidal) curves from Cercocarpus intricatus were consistent with each other, differing only in whether native embolism had been removed. An 'r' shaped centrifuge curve in Olea europaea was indistinguishable from the loss of conductivity caused by forcing air directly across vessel end-walls. We conclude that centrifuge curves on long-vesselled material are not always prone to the open vessel artefact when the original rotor design is used, and 'r' shaped curves are not necessarily artefacts. Nevertheless, confirming curves with native embolism and dehydration data is recommended.     

Feasibility Study of Using Centrifuge for Investigating LNAPL Migration in Unsaturated Soils

Centrifuge modeling appears potentially useful for studying geo-environmental problems such as pollutant migration in subsurface systems. In this study, the “modeling of models” technique was used to validate the feasibility of using a geotechnical centrifuge to model the transport behavior of light non-aqueous phase liquids (LNAPLs) in unsaturated soils. All the experiments were conducted to simulate a gasoline spill from a leaking underground storage tank (UST) and the subsequent subsurface migration of the gasoline. When the gravity in the centrifuge reached the desired g-level, the gasoline was released from the UST and then it migrated in the unsaturated soil corresponding to a prototype time equivalent of one year. After the centrifuge tests, soil samples were collected using sampling tubes and the concentrations of individual constituent in the LNAPL were directly measured by means of gas chromatograph analysis. Results obtained from the centrifuge tests at different g-levels show that similar migration patterns are found for LNAPL transport in unsaturated porous media. The location of the peak concentration and the behavior of lateral spreading can be adequately described. In addition, centrifuge test data show that the migration pattern of LNAPLs is related to the soil type and the physical properties of individual constituents in the LNAPLs.     

A simple, rapid, aseptic method for filling micropipettes by centrifugation

A centrifugation method for sterilizing, storing, and filling micropipettes is described. Each micropipette is held in a centrifuge tube by a rubber stopper which clamps the butt end of the micropipette. The pipettes are sterilized and aseptically stored. A pipette is filled by injecting solution into the butt end of the micropipette. The micropipette is returned to a suspended position in the centrifuge tube and the liquid is rapidly forced into the micropipette tip by centrifugation. The technique is simpler and more rapid than presently used centrifugation methods.