Application of biochemical engineering principles to develop a recovery process for protein inclusion bodies.
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Biomedical subjects
Publications and source records attributed to P Dunnill.
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Nucleic acids, lipid, and colloidal particulate material can be selectively flocculated from a yeast cell homogenate by the cationic polymer polyethyleneimine (PEI). Flocculation can occur from a crude homogenate, a homogenate clarified centrifugally, or by the prior use of sodium tetraborate (borax). Flocculation from a homogenate previously clarified by the use of borax is best suited for large-scale operation. The supernatant obtained following centrifugation is effectively free of nucleic acid, lipid, and particulate material with essentially 100% soluble enzyme recovery. Enzyme specific activity increases by approximately 45% compared to a zero PEI control.
Results presented here show that loss of progesterone 11 alpha-hydroxylase activity in Rhizopus nigricans in aqueous-organic two-liquid phase and cosolvent systems correlates well with the concentration of solvent in the cell membranes. Rhizopus nigricans is shown to retain full 11 alpha-hydroxylase activity at saturating aqueous phase concentrations of hexane and the higher primary alcohols. This reflects their inability to attain a critical concentration in the cell membranes. The relationship between our own findings and the previously described correlation of the logarithm of the partition coefficient with activity retention is explained and design parameters are proposed that may be used to select solvents for future biocatalytic systems.
Some of the biochemical engineering issues that arise when the purification of proteins is scaled up are examined. The first question addressed is the quantity of various proteins likely to be required. Consideration is given to the order in which isolation procedures may be applied and to the selective removal on a large scale of non-proteinaceous materials. Some general problems such as the effect of mechanical forces on proteins and their complexes and aggregates are examined, together with ways of enhancing the properties of these aggregates and the methods of recovering them. The manner in which on-line process optimization can be achieved during pilot plant trials is discussed and the paper concludes with a summary of new scientific developments to which the biochemical engineer will need to respond.
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Ni powders coated by deposition of TiO2 or controlled oxidation to NiO develop substantial resistance to corrosion. Chymotrypsin immobilized to these coated Ni supports shows very high stability of activity on storage. Chymotrypsin immobilized by adsorption and glutaraldehyde crosslinking was fairly rapidly eluted under operational conditions in the presence of substrate. If 3-aminopropyltriethoxysilane (APS) was used to produce a covalent linkage, desorption of enzyme still occurred because of relatively unstable bonding of the silane to the oxide surface. A more stable attachment was produced by joining together many silane links with a layer of polyglutaraldehyde. The mechanism of action of APS as a coupling agent under these conditions is discussed. gamma-Fe2O3, and particularly a Mn-Zn ferrite, are suitable magnetic support materials available with smaller particle sizes. Particles below 1 mum give the expected higher specific activities of immobilized enzymes.
Yeast alcohol dehydrogenase (ADH) solutions (approximately 1 mg/ml, pH 7) were sheared in a coaxial cylindrical viscometer. This was fitted with a lid sealing the contents from the atmosphere and preventing evaporation. At 30 degrees C after a total of 5 hr intermittent shearing at 683 sec-1 no losses of activity were observed. No losses were found after 5 hr continuous shearing and in a no-shear control. At 40 degrees C and 683 sec-1 there were only small activity losses in 5 hr. Shearing at 3440 sec-1 no measurable losses of activity were found with a 1.03 mg/ml solution in 5 hr at 30 degrees C, a 1.03 mg/ml solution in 8 hr at 5 degrees C, and with a 3.89 mg/ml solution in 3 hr at 5 degrees C. In all these cases, however, a white precipitate formed that was not observed in zero shear control experiments. The sheared 3.89 mg/ml solution was clarified by centrifugation. It was shown that there were no ADH aggregates in the supernatant and that the precipitate was less than 2% of the original protein. At 30 degrees C under adverse pH conditions (pH 8.8) there was no significant difference in activity losses of an approximately 1 mg/ml solution sheared at 65 and 744 sec-1. An approximately 0.5 mg/ml ADH solution, pH 7, was agitated in a small reactor with no free air-liquid interface. Peak shear rates near the impeller were estimated to be about 9000 sec-1. Only a small decrease in specific activity was observed until over 15 hr total running at 5 degrees C.
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Chymotrypsin has been immobilized to several nonporous magnetic materials. Nickel particles were considered to be most suitable as immobilized enzyme supports. Chymotrypsin immobilized to nonporous magnetic supports was not fouled significantly by either whole milk or clarified yeast homogenate. AE-cellulose-chymotrypsin was rapidly fouled by both these materials and chymotrypsin immobilized to acrylic-based ion exchangers was slowly fouled. Immobilized enzyme activity was found to be inversely proportional to particle diameter for nonporous rock magnetic particles. Immobilization by adsorption and then glutaraldehyde crosslinking was used to produce controlled amounts of chymotrypsin on the particles. Esterolytic activity increased with enzyme loading but caseinolytic activity did not increase. Chymotrypsin is inhibited by metal ions from the magnetic supports. It is partially protected by use of a preliminary protein coating and may be reactivated by incubation with EDTA or BSA.
Protein solubility can be adequately represented by the classical Cohn equation for the salting-out of alcohol dehydrogenase and fumarase from clarified yeast homogenate with ammonium sulfate. However, the constant beta in this equation is a function of the contacting procedure employed. The kinetics of continuous salting-out were similar for alcohol dehydrogenase and fumarase. The overall rate equation for precipitation had a variable order which was high initially, up to 3.1, but approached unity on completion of precipitation. This was followed by a partial resolution stage which was first order with respect to the concentration driving force. Precipitate particle size was estimated as 0.5 to 5 mum with continuous flow precipitation producing the largest particles.
The production of cholesterol oxidase by 3 liter batch cultures of Nocardia rhodocrous growing on a glycerol/yeast extract medium was investigated. Cholesterol was shown to be a good inducer of the enzyme. The optimum time for cholesterol addition and the quantity to be added were determined, resulting in a 15-fold yield increase. Cholesterol oxidase synthesis was influenced by the dissolved oxygen tension. Maximum cholesterol oxidase production was obtained at 30-40% air saturation. The effect of growth conditions on the extraction of cholesterol oxidase by Triton X-100 was investigated. The scale-up of the fermentation to 800 liters in a pilot-plant fermenter is described.
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1. Alcohol dehydrogenase (EC 1.1.1.1.) has been immobilised to aminoethyl-cellulose by glutaraldehyde, to DEAE-cellulose by an s-triazine derivative and to agarose using CNBr. Lactate dehydrogenase has been immobilised to the latter two supports. 2. Their use for affinity chromatography of NAD was compared and alcohol dehydrogenase immobilised to CNBr-activated agarose chosen for detailed study due to the efficient coupling of applied enzyme and the specific nature of binding. 3. The efficiency of coupling of alcohol dehydrogenase dropped from 94.5 to 72.2% when the applied load was increased from 18 to 54 mg/g activated agarose. Activity relative to free enzyme fell from 21 to 11%. The binding of NAD was maximal between pH 5.5 and 6. With the lowest loading of enzyme, NAD binding fell from 450 to 320 mug/g support when the linear flow rate was increased from 0.84 to 3.95 cm/min. 4. NAD was completely separated from a mixture with ATP, ADP and AMP. Separation from NMN and hydrolysed RNA and DNA was evidently possible. Immobilised alcohol dehydrogenase used for 34 binding experiments over a period of weeks maintained 60% of its original enzyme activity. 5. The method was applied to yeast NAD following mechanical disruption of yeast, clarification and either ultrafiltration or hollow-fibre dialysis to permit separate purification of macromolecules and nucleotides.
The synthesis of beta-galactosidase by an E. coli constitutive mutant was examined in a chemostat using glucose-, glycerol-, succinate- or N-limited growth media. Except for glucose-grown bacteria, the steady-state intracellular level of beta-galactosidase was maximal at dilution rates between 0-2 and 0-3 h-1. At higher dilution rates enzyme synthesis was reduced by catabolite repression, which could be relieved by the addition of cyclic AMP. With a catabolite-resistant mutant (UV5c), no decrease in enzyme level at high dilution rates were observed. All mutants examined were constitutive and gave decreased enzyme levels at low dilution rates, with the exception of lac-/F'lac UV5c mutants where the enzyme levels rose at low dilution rates. Hyper-producing mutants were isolated but were unstable. A constitutive mutant growing on glycerol-limited media was considered the most suitable for large-scale production of beta-galactosidase in a chemostat.
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