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Biomedical subjects

N J Titchener-Hooker

Publications and source records attributed to N J Titchener-Hooker.

9 recordsLinked to original sources
PubMed2000

The use of rapid on-line monitoring of products and contaminants from within an expanded bed to control separations exhibiting fast breakthrough characteristics and to maximize productivity.

Conventional control of expanded-bed adsorption (EBA), like that of packed-bed chromatography, is based upon off-line measurements of the column eluant. The relatively high-void volumes in EBA systems means that this approach can lead to significant performance losses caused by the inability to achieve tight control of breakthrough. This problem is made worse if the product has a fast breakthrough characteristic or if it is necessary to operate to low levels of product loss. In this article we examine the utility of constant on-line monitoring from within the expanded bed using stopped-flow analysis (SFA) to provide data for the control of the expanded-bed operation. A modified Streamline 50 column with side ports that enable sampling along the expanded axis of the bed was used. Comparisons between off-line and on-line measurements are presented, showing how the advanced monitoring method can lead to better control and to an analysis of breakthrough development within the bed. The expanded bed was used to purify alcohol dehydrogenase from homogenized suspensions of bakers' yeast. Accurate control of breakthrough to 10% of the target enzyme was achieved using a SFA control system with a response time of 40 seconds. On-line data compared well to assays carried out off-line on the outlet stream for both the product enzyme (ADH), total protein, RNA, and cell debris levels (via UV 650 nm). This information was used to generate a series of graphs with which to track the EBA process in real-time. Results showed that bed utilization was not linear along the bed axis so that, for example, 60% of ADH is bound in the bottom 33% of the column during loading.

Alcohol Dehydrogenase↗
PubMed2000

Experimental measurement of particle size distribution and voidage in an expanded bed adsorption system.

This paper presents an experimental analysis of matrix bead size distribution and voidage variations with axial height in an expanded bed adsorption system. Use of a specially constructed expanded bed with side ports has enabled sampling from within the expanded bed along the vertical axis. Particles removed from within the bed were measured for their size distributions. Residence time distribution studies were used to estimate bed voidage. Measurements of axial and radial particle size distributions and axial voidage distribution have been made at different flow rates. Particle size was found to be radially constant, indicating constant stratification in the column. The particle size was found to decrease with increasing axial height. Voidage increased with axial height from a settled bed value of 0.39 to approaching unity for high liquid velocities and increased at a constant axial position with increased flowrate. This information provides key insight into bed stability and data for the improved modeling of this important unit operation.

Adsorption↗
PubMed1999

Visualizing integrated bioprocess designs through "windows of operation".

This paper demonstrates a simple graphical approach for the design and analysis of a bioprocess flowsheet in which process interactions are significant. Results are presented showing how the feasible space for operation can be simulated and used both to address key design and operating decisions and to identify suitable trade-offs between operating variables, such as fermentation growth rate and disruption conditions, in order to achieve prespecified levels of process performance. Using verified models to describe the production and isolation of an intracellular protein alcohol dehydrogenase (ADH) in yeast as a test bed, a series of so-called "windows of operation" are developed at growth rates in the range of 0.06-0.28 h(-1) and for a range of overall process specifications. The effects of altering the process design performance specification as defined by the level of cell debris removal and the overall process productivity on the size and position of the feasible space were investigated to demonstrate the sensitivity of the flowsheet to changes in process objectives. Using the approach it has been possible to visualise the processing trade-offs required to increase performance in terms of the level of cell debris removal by 50% and the overall process productivity by 400% from a defined base level. The approach provides a convenient tool when designing integrated bioprocesses by enabling process options to be compared visually and can help in achieving better process designs and accelerating process development for the biological process industry.

Alcohol Dehydrogenase↗
PubMed1999

Immobilised metal ion affinity chromatography purification of alcohol dehydrogenase from baker's yeast using an expanded bed adsorption system.

Alcohol dehydrogenase (ADH) from solutions of homogenised packed bakers' yeast has been successfully purified using immobilised metal-ion affinity chromatography in an expanded bed. Method scouting carried out using pure ADH solutions loaded onto 5-ml HiTrap columns charged with Zn2+, Ni2+ and Cu2+ and eluted using 0-50 mM EDTA gradient found that charging with Zn2+ gave the highest recovery and the lowest EDTA concentration required for elution. These results were used to develop a protocol for the expanded bed system and further tested using clarified yeast homogenate loaded onto XK16/20 packed beds (approximately 30 ml) packed with Chelating Sepharose FastFlow matrix in order to determine the optimum elution conditions using EDTA. The ADH was found to elute at 5 mM EDTA and the dynamic and total binding capacities of Streamline chelating for ADH were found to be 235 U/ml and 1075 U/ml matrix, respectively. Expanded bed work based on a step EDTA elution protocol demonstrated that ADH could be successfully eluted from unclarified homogenised bakers' yeast diluted to 10 mg/ml total protein content with a recovery of 80-100% that was maintained over five consecutive runs with a vigorous clean-in-place procedure between each run.

Adsorption↗
PubMed1998

Time course of SDS-alkaline lysis of recombinant bacterial cells for plasmid release.

SDS-alkaline lysis of recombinant Escherichia coli cell suspensions was carried out in a coaxial cylinder rheometer, and the data were used to establish the time course of lysis reaction. The results of the experiments showed that cell lysis reaction time depended on cell strain but was unaffected by plasmid size and plasmid copy number. The high molecular weight globular proteins and chromosomal DNA were denatured, and the resulting changes in rheometric measurements characterised the denaturation time.

Escherichia coli↗
PubMedDate not supplied

Selective flocculation and precipitation for the improvement of virus-like particle recovery from yeast homogenate.

The purification of an intracellular product from a complex mixture of contaminants after cell disruption is a common problem in processes downstream of fermentation systems. This is particularly challenging for the recovery of particulate (80 nm in diameter) multimeric protein products, named virus-like particles (VLPs), from cell debris and other intracellular components. Selective flocculation for debris removal followed by selective precipitation of the target protein can be used as a preclarification step to aid purification. In this paper, selective borax flocculation of cell debris in yeast homogenate, followed by selective poly(ethylene glycol) precipitation of VLPs are defined with a view to demonstrating their potential in aiding the initial clarification stages of the purification sequence. The translation from laboratory scale to pilot scale operation is addressed, demonstrating the challenge of scale-up of solid-liquid separation stages for biological particle processing.

Borates↗
PubMedDate not supplied

A tool for modeling strategic decisions in cell culture manufacturing.

The development of a prototype tool for modeling manufacturing in a biopharmaceutical plant is discussed. A hierarchical approach to modeling a manufacturing process has been adopted to confer maximum user flexibility. The use of this framework for assessing the impact of manufacturing decisions on strategic technical and business indicators is demonstrated via a case study. In the case study, which takes the example of a mammalian cell culture process delivering a therapeutic for clinical trials, the dynamic modeling tool indicates how manufacturing options affect the demands on resources and the associated manufacturing costs. The example illustrates how the decision-support software can be used by biopharmaceutical companies to investigate the effects of working toward different strategic goals on the cost-effectiveness of the process, prior to committing to a particular option.

Biotechnology↗
PubMedDate not supplied

A study of process interactions between cell disruption and debris clarification stages in the recovery of yeast intracellular products.

The effects of varying the levels of cell disruption achieved by high-pressure homogenization upon subsequent centrifugal separation of cell debris have been defined by measuring sedimentation velocity distributions of the cell debris. Using this data together with particle size distributions, a computer-based model of a disk stack centrifuge has been used to predict the efficiency of centrifugal separation. These predictions have been compared with both laboratory scale and pilot plant scale experimental results. A similar sedimentation velocity technique has been used to characterize the properties of the flocs formed by addition of poly(ethylene imine) to a borax-clarified homogenate supernatant. The variations of floc settling properties with respect to polymer concentration are defined.

Biotechnology↗