Thesis (Ph. D.)--Institute of Paper Chemistry, 1980. / Bibliography: leaves 100-107.

Polyketide biosynthesis is a field that has had tremendous advances in the past 50 years. The understanding of the mechanisms is updated as investigations delve into domain interactions of these microbial natural products. Although numerous polyketides are known, similarities in the sequence of product generation can be used as templates for further exploration of enzymatic activity. The focus of studies recently has been towards developing protocols to manipulate the natural products resulting in medicinally important manufactured products. This investigation examined the mechanism of the acyl carrier protein (ACP) module involved in biosynthesis. / text

Copper metallothionein (Cu-MT) was extracted from the induced biomass of Aspergillus niger. The crude extract (FI), obtained by cell homogenization, was partially purified by heat treatment (FII) and ultrafiltration (FIII). Further purification of the Cu-MT extract by affinity chromatography resulted in three major fractions, FIVa, FIVb and FIVc, of which fraction FIVc was considered to be the Cu-MT extract fraction. Fraction FIVc was re-chromatography on affinity chromatography and the eluted fraction showed a single peak (FIVc'). Spectrophotometric analysis of fraction FIVc' demonstrated a maximum absorption peak at 268 nm. Native and denatured electrophoretic analysis of fraction FIVc ' showed the presence of a single band with an estimated molecular weight of 9.5 and 10.0 kDa, respectively. Inhibition of mushroom tyrosinase (PPO) by the Cu-MT extracts was investigated, using selected phenolic substrates, including catechin, chlorogenic acid, catechol, 4-methylcatechol, caffeic acid, L-3,4-dihydroxyphenylalanine, 3,4-dihydroxyphenylacetic acid, 3-( p-hydroxyphenyl) propionic acid, p-hydroxyphenylpyruvic acid, p- and m-cresol. The results showed that the inhibitory effect of the Cu-MT extract increased with the degree of purification. The results revealed that the Cu-MT extracts were effective inhibitors of PPO activity and the best inhibitory effect was demonstrated with catechin as substrate; however, PPO activity was not inhibited by the Cu-MT extract when p-hydroxyphenylpyruvic acid and p- and m-cresol were used as substrates. The results also showed that the Cu-MT extracts exhibited different types of inhibition, including mixed, competitive and uncompetitive on PPO activity. In addition, the experimental findings indicated that the nature and degree of enzymatic inhibitions by the Cu-MT extracts were dependent upon the structural nature of the substrates as well as the methods including, spectrophotometer and polarograph, used for the detection of enzyme

Two natural enzymatic browning inhibitors, copper-metallothionein (Cu-MT) and polyphenol esterase (PPE), were obtained from A. niger and investigated. Reflectance measurements, expressed as L (lightness variable) and a (red to green degree of color) were used to compare, over extended periods of time, the relative inhibitory effectiveness of Cu-MT and PPE to those observed with the use of selected chemicals including ascorbic acid (AA), citric acid (CA), ethylenediaminetetraacetic acid (EDTA), sodium bisulfite (NaHSO3) and 4-hexylresorcinol (4HR), in the prevention of browning on the cut surfaces of selected food products such as apple and potato slices as well as freshly prepared apple juice. Treatment of each food product required an optimum concentration of the selected inhibitor for the inhibition of browning. (Abstract shortened by UMI.)

Energy utilization is a determining factor for the standards of living around the world, and the current primary source of energy is fossil fuels. A potential source of liquid fuels that could ease the strain caused by diminishing petroleum resources is bioethanol. Effective exploitation of biomass materials requires a pretreatment to disrupt the lignin and cellulose matrix. The pretreatment utilized for this research was oxygen delignification, which is a standard process stage in the production of bleached chemical pulp. The model substrate utilized as a feedstock for bioethanol was recovered fibre. An analysis of the substrates digestibility resulted in a hexose yield of approximately 23%, which justified the need for an effective pretreatment. An experimental design was performed to optimize the delignification conditions by performing experiments over a range of temperature, caustic loadings, and reaction times. Equations were developed that outline the dependence of various response parameters on the experimental variables. An empirical model that can predict sugar concentrations from enzymatic hydrolysis based on the Kappa number, enzyme loading, and initial fibre concentration was also developed. A study of hydrolysis feeding regimes for untreated recovered fibre (87 Kappa), pretreated recovered fibre (17 Kappa), and bleached pulp (6 Kappa) showed that the batch feeding regime offers reduced complexity and high sugar yields for lower Kappa substrates. In order to evaluate the possibility of lignin recovery, the pH of delignification liquor was reduced by the addition of CO₂ and H₂SO₄, resulting in up to 25% lignin yield. An experiment that looked at effect of post-delignification fibre washing on downstream hydrolysis found that a washing efficiency of approximately 90% is required in order to achieve a hexose sugar yield of 85%.

Oxidation plays an important role in the basic processes of life, such as the production of energy and phagocytosis employed by the immune system. However, when an imbalance between oxidants and antioxidants exists in vivo, oxidation can become uncontrolled and result in diseases such as arthritis, cancer, artherosclerosis, and Alzheimer’s Disease. Dietary antioxidants including polyphenolic compounds, proteins, and peptides have been identified as being physiologically functional foods capable of contributing to the restoration of this oxidant-antioxidant balance. The objective of this study was to explore the production of antioxidant soy peptides from a commercially available soy protein isolate (SPI) by enzymatic hydrolysis in a process similar to that occurring in the human digestive tract. In this study Archer-Daniels Midland SPI PRO-FAM 974 was used as a raw material for the production of antioxidant soy peptides. The digestion consisted of enzymatic digestion of the SPI (3.12 wt %) with pepsin (37ºC, pH 1.5) and/or pancreatin (40ºC, pH 7.8) either individually or sequentially. The enzyme concentration and digestion time for each enzyme was optimized using a 2^4 factorial experimental design to produce the greatest concentration of peptides quantified in PheGly equivalents by the OPA assay. A maximum peptide concentration of approximately 65 mM PheGly equivalents was achieved in the follow-up digests resulting from this factorial design model, using pepsin (0.15 g/L, 15 minutes) and pancreatin (4.5 g/L, 120 minutes) sequentially to digest the SPI. Fractionation of the peptides by sequential dead-end membrane ultrafiltration with molecular weight cut-offs (MWCO) of 3 kDa and 1 kDa was performed to produce peptide fractions with increased antioxidant capacity. The permeate flux as a function of time was fit to empirical models, revealing that the membrane fouling resulting in the permeate flux decline is largely reversible and most likely the result of cake filtration. Antioxidant capacity was quantified by the DPPH, FCR, and ORAC assays to determine the electron-donating and proton-donating capacities of the soy peptides. The electron-donating DPPH assay was not suitable to quantify the antioxidant capacity of the soy peptides due to poor peptide solubility in the assay media and sensitivity. The electron-donating FCR assay and the proton-donating ORAC assay were used to distinguish between the ultrafiltration and digestion conditions employed to produce the soy peptides and the antioxidant capacity was quantified in equivalence to the standard antioxidant Trolox. The soy peptide fraction with the greatest antioxidant capacity was produced by enzymatic digestion with pancreatin (4.5 g/L, 120 minutes) alone and had a molecular weight cut-off of between 3 kDa and 1 kDa. This fraction had an equivalent antioxidant capacity of approximately 190 mg Trolox/g sample in the ORAC assay and approximately 180 mg Trolox/g sample in the FCR assay. A preliminary linear model for the optimum digestion and ultrafiltration conditions for the production of antioxidant peptides with the greatest ORAC antioxidant capacity was also developed. The model includes a positive pancreatin digestion time term and a negative pepsin digestion time term. No ultrafiltration terms were found to be significant in this preliminary model, but a large constant term persisted. In conclusion, the enzymatic digestion of commercially available SPI with pancreatin and fractionated by ultrafiltration successfully produced a soy peptide fraction with increased antioxidant capacity.

A crude enzyme extract (FI) of polyphenol esterase (PPE), obtained from the microbial culture of Aspergillus niger, was partially purified by ammonium sulfate precipitation. The partially purified fraction (FII) was subjected to further purification by ion-exchange chromatography, which resulted in five separated fractions, FIIIa, FIIIb, FIIIc, FIIId and FIIIe), where FIIIa showed the highest PPE activity towards chlorogenic acid, as substrate. The biocatalysis of the PPE with a wide range of mono- and diphenols, as substrates, was shown to inhibit mushroom tyrosinase (PPO) activity. Fraction FIIIa exhibited an inhibitory effect, measured spectrophotometrically, on PPO activity with the monophenols, including 4-hydroxyphenylpyruvic acid and m- and p-cresols and the diphenols, including chlorogenic acid, catechin, 3,4-dihydroxyphenylacetic acid (DHPAA), L-3,4-dihydroxyphenylalanine (L-DOPA), 4-methylcatechol, catechol and caffeic acid; however, using the polarographic method, the inhibition of PPO activity by PPE biocatalysis occurred with the diphenols but not with the monophenols. The selected enzymatic fraction FIIIa was further purified, using size-exclusion chromatography, which resulted in three fractions FIVa, FIVb and FIVc. Although fraction FIVc contained the highest PPE activity, it showed a lack of enzyme stability. Fraction FIIIa was therefore, subjected to further purification by hydrophobic interaction chromatography thereby yielding fractions FVa, FVb, FVc, FVd, FVe, FVf and FVg, where fraction FVc showed the highest PPE activity. The denatured electrophoretic analysis of fraction FVc showed the presence of one major band, with a molecular weight of 60 kDa. The successive purification of PPE resulted in a marked increase in the inactivation of PPO activity with diphenols, as demonstrated by both the lower I50 and inhibition dissociation constant (Ki) values. The purified fraction FVc was shown to exhibit, spectrophotometrically, a competitive and un

The biosynthesis of Aflatoxin B1 (AFB1) has been the subject of conflicting speculation and numerous reviews. The currently accepted scheme for the aflatoxin pathway is based on data obtained from feeding studies using isotopically labelled precursors. In these studies the conversion of possible intermediate metabolites to AFBl by mutants of Aspergillus parasiticus illustrated their role as biogenetic precursors. Currently there is now agreement on the identity of most of the intermediate Illetabolites involved in the biosynthesis of AFB1. However, there is a lack of clarity on the details of AFB1 biosynthesis including the conversion of sterigmatocystin (ST) to AFB1 via the metabolite O-methylsterigmatocystin (OMST). There is no clear cut evidence of the metabolic role of OMST, i.e., either it is a compulsory intermediate or a shunt metabolite and hence part of a metabolic grid. In order to investigate this step in AFBl biosynthesis, ST was isolated from surface cultures of A. versicolor (M1101) and purified by silica gel column chromatography and repeated recrystallisation. Sterigmatocystin was characterised by thin layer chromatography (t.1.c.), low resolution mass spectrometry (M.S) and nuclear magnetic resonance spectroscopy (N.M.R). A series of seven derivatives of the free hydroxyl group of ST were synthesised by known chemical reactions, purified by silica gel column chromatography and characterised by high resolution mass spectrometry and proton nuclear magnetic resonance spectroscopy. A high pressure liquid chromatography (HPLC) method was developed using a fluorescence detector. The optimum parameters for the separation of the four major aflatoxins, namely AFBl, AFB2, AFGl and AFG2, using trifluoroacetic acid as the derivatising reagent, were obtained for a reversed phase Prodigy C18 column with a mobile phase of water: acetonitrile: isopropanol: acetic acid (8: 1: 0.5: 0.5, v/v). Feeding studies, using whole cells of A. parasiticus (WhI-11-105), showed that ST and the ST derivatives were converted to AFB1. A time courser study for the conversion of ST and selected ST derivatives to AFB1 indicated a decrease in the rate of conversion in the order: a-propyl sterigmatocystin (OPROST) > a-ethyl sterigmatocystin > a-methylsterigmatocystin > Sterigmatocystin> a-benzoyl sterigmatocystin (OBzST). It was apparent that the "enzyme" responsible for the conversion of the derivatives to AFB1 did not display a high degree of substrate specificity, since it was unable to recognize the difference between the various alkyl groups, either as ether or ester functional groups. An HPLC method was developed using a diode array detector. The optimum parameters for the separation of aflatoxin metabolites and the synthesised derivatives were obtained for a reversed phase Lichrosphere RP-I8 column with a 30 minute gradient elution program with water and acetonitrile as the mobile phase. Crude cell-free extracts were prepared by lyophilisation of the mycelia of A. parasiticus (Whl-11l-105) with phosphate buffer. The temperature and pH for the conversion of ST to AFB1, were found to be optimum at 28°C and 7.2, respectively. The addition of SAM (1.5 mM) and NADPH (1.5 mM) increased the conversion of ST to AFBl from 11.21 % to 27.10 %. A time course study with ST, OMST and OPROST showed that the rate of conversion to AFBl was close to linear for an incubation time of up to 60 minutes. Approximation of the reaction rate indicated a decrease in the order: OMST > ST > OPROST. This indicated that the time course reaction using whole cells was in part a measure of membrane permeability rather than substrate specificity. Molecular exclusion chromatography was used to separate enzymatic protein from primary and secondary metabolites, small biomolecules and indigenous co-factors (MW < 10 000) and the partially purified "enzyme" was concentrated by dialysis against solid sucrose. The "enzyme" was subjected to non-denaturing polyacrylamide gel electrophoresis and was found to be made of sub-units ranging from 58 kDa to over 200 kDa. Enzymatic investigations with ST, as substrate, indicated that OMST is a compulsory intermediate in the biosynthesis of AFBl. Also, enzymatic investigations of selected ST derivatives showed that the partially purified "enzyme" displayed relative specificity for these substrates, viz., OMST, OPROST and OBzST. Three xanthones, namely, 1-hydroxy-,6-dimethylxanthone, I-methoxy-3,6-dimethylxanthone and l-acetyl-3,6-dimethylxanthone were synthesised, purified and characterised spectroscopically. Whole cell studies of A. parasiticus (CMI 91019b) and A. parasiticus (Wh1-11-105) showed that these xanthones inhibited AFBl production to varying extents. Kinetic studies of cell-free extracts revealed that the 1-methoxy-3,6-dimethylxanthone derivative was a non-competitive inhibitor. The Michaelis Menten constant (Km) of approximately 5.60 uM (for OMST) was determined for a cell-free reaction at pH 7.2 and 28 QC. A Clark oxygen electrode was used to carry out oxygen consumption studies in a partially purified "enzyme" preparation. A calibration system was designed and the enzymatic conversion of OMST to AFB1 and NADPH consumption were monitored by HPLC and UV spectroscopy, respectively. From the results of these enzymatic reactions, the following stoichiometric relationship was determined: 2 mole oxygen consumed = 1 mole NADPH consumed = 1 mole AFB1 produced A tentative mechanism is discussed for the conversion of OMST to AFB1 which utilizes a monooxygenase and a dioxygenase. / Thesis (Ph.D.)-University of Natal, Durban, 1996.

Soybean production and consumption has increased in recent decades. However, trypsin inhibitor activity and “beany” flavour are two drawbacks limiting the utilization of soybean. In the present study, micronization, ethanol washing, and enzymatic hydrolysis (alone or in combination) were used to treat soybean. Micronization at 100 °C and 135 °C decreased the activity of both trypsin inhibitors (53% and 80% respectively), and lipoxygenase (51% and 99%, respectively). Ethanol increased the trypsin inhibitor activity while alcalase hydrolysis decreased its activity. Different treatment combinations affected trypsin inhibitor activity, with micronization having a major influence. “Beany” flavour related volatiles (hexanal, (E)- 2-hexenal, 1-hexanol, heptanal, (E)-2-octenal, (E)-2-nonenal, (E,E)-2,4-nonadienal, 2,4-decadienal, (E,E)-2,4-decadienal, 1-octen-3-ol, 2-pentylfuran and 3-octen-2-one) were significantly decreased with micronization. Ethanol effects varied with different volatiles. Soybean micronized at 135°C and washed with 65% ethanol was recommended for soybean processing due to its low trypsin inhibitor activity and low “beany” related volatile content.

Pseudo-lignin, which can be broadly defined as aromatic material that yields a positive acid-insoluble (Klason) lignin value, has been reported to generate from biomass polysaccharides during dilute acid pretreatment (DAP). To investigate the fundamental chemistry of pseudo-lignin, a series of state-to-art analytical techniques including GPC, FT-IR and ¹³C NMR were applied to characterize pseudo-lignin extracted from poplar α-cellulose and holocellulose after DAP. The results showed that pseudo-lignin is polymeric (Mn ~ 1000 g/mol; Mw ~ 5000 g/mol) and consists of carbonyl, carboxylic, aromatic, methoxy and aliphatic structures, which can be produced from both dilute acid-treated cellulose and hemicellulose. During DAP, the hydrolysis of polysaccharides, which leads to some release of monosaccharides, and their subsequent dehydration reactions to form furfural and 5-hydromethylfurfural (HMF) takes place. Further rearrangements of furfural and/or HMF can produce aromatic compounds, which undergo further polymerization and/or polycondensation reactions to form pseudo-lignin. More importantly, pseudo-lignin was revealed to bind with cellulase enzymes unproductively and significantly retard enzymatic conversion of cellulose. As compared to native lignin after DAP, the inhibition effect arise from pseudo-lignin is much stronger, which clearly indicates pseudo-lignin formation should be avoided during DAP. Process optimization study indicated that addition of dimethyl sulfoxide (DMSO) to the DAP reaction medium can effectively increase sugar recovery and reduce pseudo-lignin formation, even under high-severity pretreatment conditions. The pseudo-lignin suppression property of DMSO has been attributed to the preferential arrangement of DMSO in the vicinity of the C1 carbon of the HMF molecule, thereby protecting HMF from further reactions to form pseudo-lignin.