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S L Mistry

Publications and source records attributed to S L Mistry.

3 recordsLinked to original sources

Phase separation rates of aqueous two-phase systems: correlation with system properties.

The kinetics of phase separation in aqueous two-phase systems have been investigated as a function of the physical properties of the system. Two distinct situations for the settling velocities were found, one in which the light, organic-rich (PEG) phase is continuous and the other in which the heavier, salt-rich (phosphate) phase is continuous. The settling rate of a particular system is a crucial parameter for equipment design, and it was studied as a function of measured viscosity and density of each of the phases as well as the interfacial tension between the phases. Interfacial tension increases with increasing tie line length. A correlation that describes the rate of phase separation was investigated. This correlation, which is a function of the system parameters mentioned above, described the behavior of the system successfully. Different values of the parameters in the correlation were fitted for bottom-phase-continuous and top-phase-continuous systems. These parameters showed that density and viscosity play a role in the rate of separation in both top continuous- and bottom continuous-phase regions but are more dominant in the continuous top-phase region. The composition of the two-phase system was characterized by the tie line length. The rate of separation increased with increasing tie line length in both cases but at a faster rate when the bottom (less viscous) phase was the continuous phase. These results show that working in a continuous bottom-phase region is advantageous to ensure fast separation.

Models, Chemical↗

Separation and purification of recombinant proteins from Escherichia coli with aqueous two-phase systems.

The partition of the protein thaumatin in the presence of Escherichia coli contaminant proteins has been studied. Extraction of thaumatin was followed by back-extraction of the product into a new phosphate phase and also back extraction combined with recycle of the top polyethylene glycol (PEG) phase. When partitioned in the absence or presence of insoluble cell debris (whole cell homogenate) little effect on the partitioning of thaumatin or the soluble E. coli protein was observed. A back extraction step that allowed for dilution of the NaCl was successful in extracting thaumatin back into a heavy phosphate phase. The PEG top phase was recycled to the first extraction stage. The stability ratio (tie-line length) had an effect on the average partition coefficient (Kapp) of E. coli soluble proteins in PEG-phosphate systems but in PEG sulphate systems Kapp was independent of this ratio. An increase in NaCl resulted in an increase in Kapp but this was always below 1. A mathematical model that describes the continuous steady-state operation of extraction and back extraction has been developed; it is based on steady state mass balances of the main components and phase equilibrium data and was successfully used to simulate the extraction and back extraction processes.

Bacterial Proteins↗

Mathematical modelling and simulation of aqueous two-phase continuous protein extraction.

A mathematical model has been developed to describe the continuous, steady-state operation of an aqueous two-phase system for protein extraction. The model is based on steady-state mass balances of the main components and phase equilibrium data. Experimental data on the separation of thaumatin from contaminant proteins of an homogenate of E. coli in a PEG4000/Phosphate system was used. The data shows the effect of the presence and absence of NaCl which was used to carry out the extraction of thaumatin into the PEG phase and back into the PO4(-3) phase. Simulation results showing the sensitivity to key process parameters, and the effect of process variables on performance are presented and discussed. The model can be used to predict performance and thus 'robustness' of process conditions as well as predict protein recovery yield and purity. This model can also be used to implement a suitable control strategy to maintain process stability.

Bacterial Proteins↗