The present study was aimed at extending our knowledge of the antioxidative properties of the milk protein products, whey protein isolate (WPI) and sodium caseinate (NaCas), in oil-in-water (O/W) emulsions rich in polyunsaturated fatty acids (PUFAs). In particular, the objective was to contribute to our understanding of the compositional and processing factors that influence the oxidative stability of protein-stabilised O/W emulsions. Linoleic acid (approximately 60 %) was used as the lipid for the oil phase (10.6 %). The emulsion samples were usually incubated at 50 °C to accelerate lipid oxidation. Lipid oxidation indicators were lipid hydroperoxides and headspace hexanal, determined by solid phase microextraction (SPME) combined with gas chromatography (GC). WPI- or NaCas-stabilised emulsions were prepared using a wide range of protein concentrations (0.5, 1.0, 2.0, 3.0, 4.0, 7.0 or 10.0 %) at two droplet sizes (d32 = 0.31 and 0.65 µm). In general, higher lipid oxidation levels were found for the larger droplet size. Increasing protein concentration led to a decrease in the lipid oxidation rate. The greatest decrease in lipid hydroperoxide levels (values after 4 h) occurred at up to 4.0 % protein concentration. The greatest decrease in hexanal levels (values after 24 h) occurred at up to 4.0 % protein concentration in WPI emulsions (0.31 µm). The hexanal levels were more independent of the protein concentration in the other emulsion types. The hexanal level decreased at protein concentrations > 4.0 % in NaCas emulsions (0.31 and 0.65 µm) and at protein concentrations > 7.0 % in WPI emulsions (0.65 µm). The difference between lipid hydroperoxide generation in emulsions with small and large droplet sizes decreased with increasing protein concentration. This effect was more pronounced in NaCas emulsions. In general, NaCas was a better inhibitor of lipid oxidation than WPI, but WPI appeared to be the better antioxidant at some droplet size/protein concentration combinations. The protein in the continuous phase, i.e. the unadsorbed protein, played an important role in lipid oxidation. In principal, the lipid hydroperoxide and hexanal levels showed the same development over the continuous phase protein concentration as over the protein concentration in WPI and NaCas emulsions (d32 = 0.31 µm). A low NaCas level in the continuous phase already led to a relatively low hexanal level, whereas a higher WPI level was required. When NaCas solution was added to a WPI emulsion or WPI solution was added to a NaCas emulsion, a synergistic antioxidative effect was observed. The high molecular weight fractions (molecular weight = 12000-14000) of WPI and NaCas contained pro-oxidative metal ions that contributed to lipid oxidation in the emulsions. An enrichment of NaCas emulsions with the low molecular weight fraction of NaCas (with a molecular weight = 12000-14000) notably inhibited lipid oxidation. An enrichment of WPI emulsions with the low molecular weight fraction of WPI (with a molecular weight = 12000-14000) also seemed to inhibit lipid oxidation, but the effect was not significant. The protein solutions were enriched with these fractions before emulsion preparation. Pure WPI solution or mixed WPI/NaCas (1:1, weight/weight) solution with 1.12 or 2.24 % protein concentration was heated at 84 °C for up to 40 min, cooled and then used to prepare emulsions. Lipid oxidation was generally not affected by the heat treatment or the degree of whey protein denaturation. However, at the lower WPI concentration, more hexanal was produced for the longer heating times (20, 30 and 40 min) and this appeared to be connected with the physical instability of the emulsions. Greater oxidative stability was found at the higher protein concentration and when the proteins were mixed, pointing to a possible synergistic antioxidative effect of WPI and NaCas. The addition of the free radical source 2,2’-azobis(2-amidinopropane) dihydrochloride (AAPH) greatly increased the oxygen uptake and the generation of lipid hydroperoxides in the emulsions. The oxidative stability increased with increasing protein concentration (1.0, 4.0 and 7.0 %). NaCas had a greater antioxidative effect than WPI. The inhibition of oxygen uptake appeared to be largely influenced by the free-radical-scavenging activity of the system, determined by the protein type and the protein concentration, as the radicals were produced linearly over time and oxygen was consumed linearly over time. It can therefore be concluded that free-radical-scavenging activity represents a major antioxidative mechanism of the milk proteins. Oxygen was consumed much faster in emulsions than in protein solutions when the same level of AAPH was incorporated. In a WPI (1.0 % protein) emulsion, much lower levels of protein hydroperoxides than of lipid hydroperoxides developed. This pointed to a much greater reactivity of linoleic acid than of the milk proteins with oxygen. In contrast, the exposure of WPI to oxidising linoleic acid in an emulsion (1.0 % protein) or to AAPH in aqueous solution led to oxidative damage of the whey proteins, indicated by the loss of amino acids. The loss of specific amino acids was different for proteins in the continuous phase or cream phase of an emulsion or in WPI solution. The present study confirms the antioxidative potential of WPI and NaCas and gives new insights into their functionality as oxidative stabilisers in O/W emulsions.

The present study was aimed at extending our knowledge of the antioxidative properties of the milk protein products, whey protein isolate (WPI) and sodium caseinate (NaCas), in oil-in-water (O/W) emulsions rich in polyunsaturated fatty acids (PUFAs). In particular, the objective was to contribute to our understanding of the compositional and processing factors that influence the oxidative stability of protein-stabilised O/W emulsions. Linoleic acid (approximately 60 %) was used as the lipid for the oil phase (10.6 %). The emulsion samples were usually incubated at 50 °C to accelerate lipid oxidation. Lipid oxidation indicators were lipid hydroperoxides and headspace hexanal, determined by solid phase microextraction (SPME) combined with gas chromatography (GC). WPI- or NaCas-stabilised emulsions were prepared using a wide range of protein concentrations (0.5, 1.0, 2.0, 3.0, 4.0, 7.0 or 10.0 %) at two droplet sizes (d32 = 0.31 and 0.65 µm). In general, higher lipid oxidation levels were found for the larger droplet size. Increasing protein concentration led to a decrease in the lipid oxidation rate. The greatest decrease in lipid hydroperoxide levels (values after 4 h) occurred at up to 4.0 % protein concentration. The greatest decrease in hexanal levels (values after 24 h) occurred at up to 4.0 % protein concentration in WPI emulsions (0.31 µm). The hexanal levels were more independent of the protein concentration in the other emulsion types. The hexanal level decreased at protein concentrations > 4.0 % in NaCas emulsions (0.31 and 0.65 µm) and at protein concentrations > 7.0 % in WPI emulsions (0.65 µm). The difference between lipid hydroperoxide generation in emulsions with small and large droplet sizes decreased with increasing protein concentration. This effect was more pronounced in NaCas emulsions. In general, NaCas was a better inhibitor of lipid oxidation than WPI, but WPI appeared to be the better antioxidant at some droplet size/protein concentration combinations. The protein in the continuous phase, i.e. the unadsorbed protein, played an important role in lipid oxidation. In principal, the lipid hydroperoxide and hexanal levels showed the same development over the continuous phase protein concentration as over the protein concentration in WPI and NaCas emulsions (d32 = 0.31 µm). A low NaCas level in the continuous phase already led to a relatively low hexanal level, whereas a higher WPI level was required. When NaCas solution was added to a WPI emulsion or WPI solution was added to a NaCas emulsion, a synergistic antioxidative effect was observed. The high molecular weight fractions (molecular weight = 12000-14000) of WPI and NaCas contained pro-oxidative metal ions that contributed to lipid oxidation in the emulsions. An enrichment of NaCas emulsions with the low molecular weight fraction of NaCas (with a molecular weight = 12000-14000) notably inhibited lipid oxidation. An enrichment of WPI emulsions with the low molecular weight fraction of WPI (with a molecular weight = 12000-14000) also seemed to inhibit lipid oxidation, but the effect was not significant. The protein solutions were enriched with these fractions before emulsion preparation. Pure WPI solution or mixed WPI/NaCas (1:1, weight/weight) solution with 1.12 or 2.24 % protein concentration was heated at 84 °C for up to 40 min, cooled and then used to prepare emulsions. Lipid oxidation was generally not affected by the heat treatment or the degree of whey protein denaturation. However, at the lower WPI concentration, more hexanal was produced for the longer heating times (20, 30 and 40 min) and this appeared to be connected with the physical instability of the emulsions. Greater oxidative stability was found at the higher protein concentration and when the proteins were mixed, pointing to a possible synergistic antioxidative effect of WPI and NaCas. The addition of the free radical source 2,2’-azobis(2-amidinopropane) dihydrochloride (AAPH) greatly increased the oxygen uptake and the generation of lipid hydroperoxides in the emulsions. The oxidative stability increased with increasing protein concentration (1.0, 4.0 and 7.0 %). NaCas had a greater antioxidative effect than WPI. The inhibition of oxygen uptake appeared to be largely influenced by the free-radical-scavenging activity of the system, determined by the protein type and the protein concentration, as the radicals were produced linearly over time and oxygen was consumed linearly over time. It can therefore be concluded that free-radical-scavenging activity represents a major antioxidative mechanism of the milk proteins. Oxygen was consumed much faster in emulsions than in protein solutions when the same level of AAPH was incorporated. In a WPI (1.0 % protein) emulsion, much lower levels of protein hydroperoxides than of lipid hydroperoxides developed. This pointed to a much greater reactivity of linoleic acid than of the milk proteins with oxygen. In contrast, the exposure of WPI to oxidising linoleic acid in an emulsion (1.0 % protein) or to AAPH in aqueous solution led to oxidative damage of the whey proteins, indicated by the loss of amino acids. The loss of specific amino acids was different for proteins in the continuous phase or cream phase of an emulsion or in WPI solution. The present study confirms the antioxidative potential of WPI and NaCas and gives new insights into their functionality as oxidative stabilisers in O/W emulsions.

The present study was aimed at extending our knowledge of the antioxidative properties of the milk protein products, whey protein isolate (WPI) and sodium caseinate (NaCas), in oil-in-water (O/W) emulsions rich in polyunsaturated fatty acids (PUFAs). In particular, the objective was to contribute to our understanding of the compositional and processing factors that influence the oxidative stability of protein-stabilised O/W emulsions. Linoleic acid (approximately 60 %) was used as the lipid for the oil phase (10.6 %). The emulsion samples were usually incubated at 50 °C to accelerate lipid oxidation. Lipid oxidation indicators were lipid hydroperoxides and headspace hexanal, determined by solid phase microextraction (SPME) combined with gas chromatography (GC). WPI- or NaCas-stabilised emulsions were prepared using a wide range of protein concentrations (0.5, 1.0, 2.0, 3.0, 4.0, 7.0 or 10.0 %) at two droplet sizes (d32 = 0.31 and 0.65 µm). In general, higher lipid oxidation levels were found for the larger droplet size. Increasing protein concentration led to a decrease in the lipid oxidation rate. The greatest decrease in lipid hydroperoxide levels (values after 4 h) occurred at up to 4.0 % protein concentration. The greatest decrease in hexanal levels (values after 24 h) occurred at up to 4.0 % protein concentration in WPI emulsions (0.31 µm). The hexanal levels were more independent of the protein concentration in the other emulsion types. The hexanal level decreased at protein concentrations > 4.0 % in NaCas emulsions (0.31 and 0.65 µm) and at protein concentrations > 7.0 % in WPI emulsions (0.65 µm). The difference between lipid hydroperoxide generation in emulsions with small and large droplet sizes decreased with increasing protein concentration. This effect was more pronounced in NaCas emulsions. In general, NaCas was a better inhibitor of lipid oxidation than WPI, but WPI appeared to be the better antioxidant at some droplet size/protein concentration combinations. The protein in the continuous phase, i.e. the unadsorbed protein, played an important role in lipid oxidation. In principal, the lipid hydroperoxide and hexanal levels showed the same development over the continuous phase protein concentration as over the protein concentration in WPI and NaCas emulsions (d32 = 0.31 µm). A low NaCas level in the continuous phase already led to a relatively low hexanal level, whereas a higher WPI level was required. When NaCas solution was added to a WPI emulsion or WPI solution was added to a NaCas emulsion, a synergistic antioxidative effect was observed. The high molecular weight fractions (molecular weight = 12000-14000) of WPI and NaCas contained pro-oxidative metal ions that contributed to lipid oxidation in the emulsions. An enrichment of NaCas emulsions with the low molecular weight fraction of NaCas (with a molecular weight = 12000-14000) notably inhibited lipid oxidation. An enrichment of WPI emulsions with the low molecular weight fraction of WPI (with a molecular weight = 12000-14000) also seemed to inhibit lipid oxidation, but the effect was not significant. The protein solutions were enriched with these fractions before emulsion preparation. Pure WPI solution or mixed WPI/NaCas (1:1, weight/weight) solution with 1.12 or 2.24 % protein concentration was heated at 84 °C for up to 40 min, cooled and then used to prepare emulsions. Lipid oxidation was generally not affected by the heat treatment or the degree of whey protein denaturation. However, at the lower WPI concentration, more hexanal was produced for the longer heating times (20, 30 and 40 min) and this appeared to be connected with the physical instability of the emulsions. Greater oxidative stability was found at the higher protein concentration and when the proteins were mixed, pointing to a possible synergistic antioxidative effect of WPI and NaCas. The addition of the free radical source 2,2’-azobis(2-amidinopropane) dihydrochloride (AAPH) greatly increased the oxygen uptake and the generation of lipid hydroperoxides in the emulsions. The oxidative stability increased with increasing protein concentration (1.0, 4.0 and 7.0 %). NaCas had a greater antioxidative effect than WPI. The inhibition of oxygen uptake appeared to be largely influenced by the free-radical-scavenging activity of the system, determined by the protein type and the protein concentration, as the radicals were produced linearly over time and oxygen was consumed linearly over time. It can therefore be concluded that free-radical-scavenging activity represents a major antioxidative mechanism of the milk proteins. Oxygen was consumed much faster in emulsions than in protein solutions when the same level of AAPH was incorporated. In a WPI (1.0 % protein) emulsion, much lower levels of protein hydroperoxides than of lipid hydroperoxides developed. This pointed to a much greater reactivity of linoleic acid than of the milk proteins with oxygen. In contrast, the exposure of WPI to oxidising linoleic acid in an emulsion (1.0 % protein) or to AAPH in aqueous solution led to oxidative damage of the whey proteins, indicated by the loss of amino acids. The loss of specific amino acids was different for proteins in the continuous phase or cream phase of an emulsion or in WPI solution. The present study confirms the antioxidative potential of WPI and NaCas and gives new insights into their functionality as oxidative stabilisers in O/W emulsions.

Yeasts are traditionally used as part of the surface microflora in surface-ripened cheeses, where they contribute positively to the flavour of the cheese. The primary objective of this study was to investigate the potential of three dairy yeasts to provide attributes as adjuncts in anaerobically ripened cheeses. Geotrichum candidum (B9001), Yarrowia lipolytica (B9014) and Candida kefyr (B9006), obtained from the Fonterra Co-operative Group Ltd, Palmerston North, New Zealand, were studied. They showed diverse metabolic activities in laboratory media, which were influenced by the growth conditions. The metabolic activities of special interest were the lipase and proteinase activities and the production of volatile compounds, as these are important for cheese ripening and flavour development. Lipase activity (p-nitrophenyl butyrate assay) and proteinase activity (fluorescein isothiocyanate β-casein assay) were determined in three fractions prepared from yeast cultures and designated as extracellular fraction, washed-cell fraction and intracellular fraction. Lipase activity of G. candidum was detected only in the extracellular fraction and increased five fold when induced by safflower oil in a shake culture (0.16 µM/min/mL supernatant at 24 h). Lipase expression was delayed in static cultures. Y. lipolytica showed lipase activity in extracellular, washed-cell and intracellular fractions under all conditions. Static cultures in both glucose and safflower oil media showed higher lipase activity than shake cultures. The lipase activity of Y. lipolytica was higher in the late stationary phase than in the log phase under all conditions tested. The highest lipase activity was detected in a 192 h static culture grown in safflower oil medium (0.13 µM/min/mg dry cell weight, 0.3 µM/min/mg dry cell weight and 4.29 µM/min/mL supernatant in the intracellular, washed-cell and extracellular fractions respectively). C. kefyr did not show any lipase activity (< 0.03 µM/min/mL culture) under any of the growth conditions tested. Proteinase activity was detected in the intracellular fraction of 72 h shake cultures of G. candidum grown in both glucose medium and safflower oil medium (154 and 122 RFU/min/mg dry cell weight respectively) but was not detected in static cultures. Proteinase activity was absent in the Y. lipolytica cultures under all conditions tested (< 10 RFU/min/mL culture). C kefyr showed low proteinase activity (12-74 RFU/min/mL supernatant) in the extracellular fraction only in shake cultures grown in glucose medium. Volatile compounds of the headspace were sampled and analysed using solid phase microextraction (SPME) and gas chromatography-mass spectrometry (GC-MS). The concentrations of volatile compounds were highest in shake cultures grown in glucose medium for all three yeasts. All yeasts produced several alcohols. Several esters were also detected in the G. candidum and C. kefyr cultures whereas aldehydes were detected only in the G. candidum cultures. G. candidum and Y. lipolytica were selected for cheese production trials because of their active cheese ripening enzymes. These yeasts, grown under different conditions, were added to Cheddar cheese (10 L vat). The yeast adjuncts influenced the cheese ripening by lipolysis [in terms of the production of free fatty acids (FFAs) analysed by gas chromatography-flame ionisation detector (GC-FID)] and the production of volatile compounds (SPME-GC-MS), whereas proteolysis (analysed by size-exclusion high performance liquid chromatography) by yeast enzymes was not obvious. The influence of Y. lipolytica as an anaerobic adjunct to cheese ripening was dependent on the growth conditions used during its propagation in laboratory media. The concentration of total FFAs was very high (37.1 mg/g cheese at 6 months) when a 192 h Y. lipolytica culture grown in safflower oil medium was added to a cheese make, whereas the cultures grown in glucose medium did not have any detectable effect. Addition of G. candidum culture to the cheese curd was more effective than its addition to the cheese milk. Both G. candidum and Y. lipolytica lipase(s) selectively hydrolysed the long-chain unsaturated fatty acids from the milk triglyceride in the cheese environment. Also, Y. lipolytica lipase exhibited some selectivity towards hydrolysis of butyric acid from the milk fat in the cheese. 2-Heptanone, 3-methyl-2-butanone and 2-nonanone were detected (1-10 x 106 relative peak area) only in the cheeses with yeast adjuncts but not in the control cheese. Enhancement of the production of both conjugated linoleic acid (CLA) and ethyl esters in a washed-curd, dry-salted cheese (375 L vat), made with G. candidum, Y. lipolytica, Propionibacterium freudenreichii ssp. shermanii, Lactobacillus fermentum and Lb. rhamnosus, was only partially successful. Higher concentrations of ethyl esters (> five fold; analysed by SPME-GC-MS) were produced in the cheeses made with yeast adjuncts. However, the concentration of total CLA (free plus esterified; analysed by GC-FID) did not increase although a higher concentration of free linoleic acid (> 10 fold), the substrate for CLA synthesis, was produced in the cheeses made with yeast adjuncts. A study of the formation of aromatic volatile compounds by C. kefyr in a medium containing L-phenylalanine (L-phe) showed that the yeast's ability to produce phenyl ethanol, phenyl ethyl acetate and benzaldehydc (analysed by SPME-GC-MS) was enhanced with an increase in the initial L-phe concentration (in the experimental range; analysed by enzymatic assay using phenylalanine ammonia lyase), but the yield was very low (20-27%). The initial concentration of glucose (in the experimental range; analysed by enzymatic assay using Peridochrom glucose reagent) did not affect the production of these aromatic volatile compounds. This study successfully showed that the yeasts G. candidum and Y. lipolytica, when used as anaerobic adjuncts, can influence the ripening and flavour development in Cheddar and washed-curd, dry-salted cheeses. The study also showed the capability of C. kefyr to produce aromatic volatile compounds from amino acid fermentation but the yields need to be increased by further manipulation of the medium components and the culture conditions before this capability can be used commercially.

The objective of this study was to investigate the effects of preheat treatments on fouling by fresh whole milk (FWM), recombined whole milk (RCB) and reconstituted whole milk (Recon) in the high-temperature heater of indirect UHT plants. Various preheat treatments prior to evaporation during milk powder manufacture were applied to skim milk powder (SMP, 75 °C 2 s, 85 °C, 155 s and 95 °C, 155 s) and whole milk powder (WMP, 95 °C, 33 s). These preheat treatments were so-called “evaporator preheat treatments”. Skim milk powder (SMP) and whole milk powder (WMP) were derived from the same original batch of pasteurised FWM to remove the effects of the variation in milk composition between different milk batches. These SMPs were recombined with anhydrous milk fat and water to prepare RCB, and WMPs were reconstituted with water to prepare Recon. Then, (homogenized) FWM, RCB and Recon were subjected to various preheat treatments (75 °C, 11 s, 85 °C, 147 s and 95 °C, 147 s) prior to UHT processing. These preheat treatments were so-called “UHT preheat treatments”. Temperature difference (hot water inlet temperature – milk outlet temperature) was taken as a measure of the extent of fouling in the high-temperature heater. The slope of the linear regression of temperature difference versus time (for two hours of UHT processing) was taken as fouling rate (°C/h). Increasing both evaporator and UHT preheat treatments resulted in increasing fouling rate and total deposit weight for all three whole milk types for several milk batches. In the case of FWM, there was no reduction in fouling rate with increasing UHT preheat treatment whether FWM was homogenized then preheated, preheated then homogenized or not homogenized at all. These findings, which are wholly consistent and well replicated, are in apparent conflict with the results of most previous comparable studies. Possible reasons for this are explained. Further investigations of the effects of homogenization relating to the role of whey protein on the surface of the fat globules showed that whey protein associated with the membrane covering the surface of fat globules for homogenized then preheated FWM, RCB and Recon and that association increased with increasing heating process stage. The increasing association of whey protein with the milk fat globules membrane with increasing severity of heating process stage became faster when preheat treatment was more severe: the association of whey protein plateaued on intermediate temperature heating when the milks were preheated at 75°C, 11 s and on preheating when the milks were preheated at 95°C, 147 s. In the case of FWM, the thickness of the membrane covering the surface of fat globules for homogenized then preheated FWM, which increased with the severity of heating process stage, was greater than the thickness of the membrane in preheated then homogenized FWM. Preheating then homogenization resulted in the greater interfacial spreading of small molecules on the surface of fat globules, i.e. whey protein or small molecules from the disintegration of casein micelles during preheating. Possible basic mechanisms for UHT fouling in the high-temperature heater include: the reduction in the solubility of calcium phosphate and the deposition of protein as fat-bound protein and non-fat-bound protein. When non-fat-bound protein in milk plasma deposited, it could be a carrier for the deposition of mineral, such as, the precipitate of calcium phosphate in the casein micelles or the deposition of complexes between whey protein and casein micelles.

Made available in DSpace on 2014-11-10T11:09:48Z (GMT). No. of bitstreams: 0 Previous issue date: 2013-08-23Bitstream added on 2014-11-10T11:58:01Z : No. of bitstreams: 1 000786749_20150920.pdf: 227688 bytes, checksum: c800c0192a1f81b1c24ac20d93cf4f4c (MD5) Bitstreams deleted on 2015-09-21T13:18:45Z: 000786749_20150920.pdf,. Added 1 bitstream(s) on 2015-09-21T13:19:48Z : No. of bitstreams: 1 000786749.pdf: 1032630 bytes, checksum: 9ff7c0ae2515a60572247ae468fd531f (MD5) / Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES) / Peptidases são enzimas responsáveis por realizar a clivagem de ligações peptídicas de outras proteínas e peptídeos. Essas enzimas apresentam grande importância, pois são utilizadas em vários segmentos industriais, desde a indústria alimentícia até mesmo no processamento de couro e pele e formulações de medicamentos. Uma das principais aplicações das peptidases é nos laticínios, na produção de queijo, que inicialmente envolve a coagulação das caseínas do leite pela ação de enzimas proteolíticas coagulantes, sendo a renina a principal delas. Enzimas microbianas coagulantes de leite são peptidases aspárticas que catalisam a coagulação do leite, substituindo o coalho de vitelo. Em trabalhos anteriores foi isolado o fungo termofílico Thermomucor indicae-seudaticae N31 que produziu em fermentação em estado sólido (FES), uma peptidase com capacidade de hidrolisar a κ-caseína do leite e produzir coágulo de boa qualidade. Entretanto, sua caracterização funcional e especificidade de ação ainda não estão claras. Assim, neste estudo, deu-se continuidade à investigação de estrutura e ação desta enzima coagulante. Foi realizado o monitoramento da hidrólise enzimática da caseína por cromatografia líquida de alta eficiência, foi feita análise da especificidade primária da peptidase utilizando substrato de fluorescência da série Abz-LSFMAIQ-EDDnp e foi determinada a sequência primária da proteína por espectrometria de massas. O monitoramento da hidrólise enzimática da caseína por cromatografia líquida de alta eficiência mostrou que o perfil do extrato bruto de Thermomucor indicae-seudaticae N31 apresenta alta similaridade com as enzimas comerciais das marcas Bela-Vista e Chr-Hansen obtidas dos fungos Rhizomucor miehei e Aspergillus niger, respectivamente. A análise de especificidade primária da peptidase demonstrou alta especificidade e afinidade pelo substrato sintético. A determinação do ... / Peptidase enzymes are responsible for catalyze the cleavage of peptide bonds of other proteins. These enzymes present great importance, therefore, are used in several industrial segments, since the food industry even in the processing of leather and formulations of medicinal products. One major application of peptidases is in the dairy industry for cheese production, which initially involves clotting of milk caseins by the action of coagulant proteolytic enzymes being rennin the main one. Microbial rennet-like milk-clotting enzymes are aspartic proteinases that catalyze milk coagulation, substituting calf rennet. In previous study it was isolated a thermophilic fungus Thermomucor indicae-seudaticae N31 that produced on Solid State Fermentation (SSF), a peptidase with capacity to hydrolyses the k-casein of milk and produce good quality curd. However its functional characterization and specificity of action is not clear yet. Thus, in this study we continued the investigation of structure and action of this enzyme coagulant. Was carried out the monitoring of enzymatic hydrolysis of casein by high performance liquid chromatography-reverse phase, was analyzed the specificity of primary peptidase using substrate of fluorescence resonance energy transfer (FRET) peptide series Abz-LSFMAIQ-EDDnp and determined the primary sequence of the protein by mass spectrometry. Monitoring the enzymatic hydrolysis of casein by high performance liquid chromatography-reverse phase showed that the crude extract Thermomucor indicae-seudaticae N31 shows high similarity with commercial enzymes brands Bela-Vista and Chr-Hansen obtained from fungi Rhizomucor miehei and Aspergillus niger, respectively. The analysis of primary peptidase specificity demonstrated high specificity and affinity for the synthetic substrate. The determination of the cleavage site showed 46% hydrolysis of the bond between the amino acids phenylalanine and methionine and 54% between alanine ...

Orientador: Roberto da Silva / Banca: Hamilton Cabral / Banca: Gustavo Orlando Bonilla Rodríguez / Resumo: Peptidases são enzimas responsáveis por realizar a clivagem de ligações peptídicas de outras proteínas e peptídeos. Essas enzimas apresentam grande importância, pois são utilizadas em vários segmentos industriais, desde a indústria alimentícia até mesmo no processamento de couro e pele e formulações de medicamentos. Uma das principais aplicações das peptidases é nos laticínios, na produção de queijo, que inicialmente envolve a coagulação das caseínas do leite pela ação de enzimas proteolíticas coagulantes, sendo a renina a principal delas. Enzimas microbianas coagulantes de leite são peptidases aspárticas que catalisam a coagulação do leite, substituindo o coalho de vitelo. Em trabalhos anteriores foi isolado o fungo termofílico Thermomucor indicae-seudaticae N31 que produziu em fermentação em estado sólido (FES), uma peptidase com capacidade de hidrolisar a κ-caseína do leite e produzir coágulo de boa qualidade. Entretanto, sua caracterização funcional e especificidade de ação ainda não estão claras. Assim, neste estudo, deu-se continuidade à investigação de estrutura e ação desta enzima coagulante. Foi realizado o monitoramento da hidrólise enzimática da caseína por cromatografia líquida de alta eficiência, foi feita análise da especificidade primária da peptidase utilizando substrato de fluorescência da série Abz-LSFMAIQ-EDDnp e foi determinada a sequência primária da proteína por espectrometria de massas. O monitoramento da hidrólise enzimática da caseína por cromatografia líquida de alta eficiência mostrou que o perfil do extrato bruto de Thermomucor indicae-seudaticae N31 apresenta alta similaridade com as enzimas comerciais das marcas Bela-Vista e Chr-Hansen obtidas dos fungos Rhizomucor miehei e Aspergillus niger, respectivamente. A análise de especificidade primária da peptidase demonstrou alta especificidade e afinidade pelo substrato sintético. A determinação do ... / Abstract: Peptidase enzymes are responsible for catalyze the cleavage of peptide bonds of other proteins. These enzymes present great importance, therefore, are used in several industrial segments, since the food industry even in the processing of leather and formulations of medicinal products. One major application of peptidases is in the dairy industry for cheese production, which initially involves clotting of milk caseins by the action of coagulant proteolytic enzymes being rennin the main one. Microbial rennet-like milk-clotting enzymes are aspartic proteinases that catalyze milk coagulation, substituting calf rennet. In previous study it was isolated a thermophilic fungus Thermomucor indicae-seudaticae N31 that produced on Solid State Fermentation (SSF), a peptidase with capacity to hydrolyses the k-casein of milk and produce good quality curd. However its functional characterization and specificity of action is not clear yet. Thus, in this study we continued the investigation of structure and action of this enzyme coagulant. Was carried out the monitoring of enzymatic hydrolysis of casein by high performance liquid chromatography-reverse phase, was analyzed the specificity of primary peptidase using substrate of fluorescence resonance energy transfer (FRET) peptide series Abz-LSFMAIQ-EDDnp and determined the primary sequence of the protein by mass spectrometry. Monitoring the enzymatic hydrolysis of casein by high performance liquid chromatography-reverse phase showed that the crude extract Thermomucor indicae-seudaticae N31 shows high similarity with commercial enzymes brands Bela-Vista and Chr-Hansen obtained from fungi Rhizomucor miehei and Aspergillus niger, respectively. The analysis of primary peptidase specificity demonstrated high specificity and affinity for the synthetic substrate. The determination of the cleavage site showed 46% hydrolysis of the bond between the amino acids phenylalanine and methionine and 54% between alanine ... / Mestre

Made available in DSpace on 2014-08-20T13:32:51Z (GMT). No. of bitstreams: 1 ficha_de_caroline_borges_biotecnologia.pdf: 7018 bytes, checksum: b335f912cae89a687603fa35c4e44d7d (MD5) Previous issue date: 2007-10-16 / Xanthan yield and physical and chemical characteristics can be improved by modification in culture conditions, as well as, by post-fermentation treatments in order to obtain a xanthan with the required characteristics. The aim of this work was to study the operational conditions in xanthan production by Xanthomonas arborícola pv pruni strains 106 and 115 to be used in oilwell drilling fluids. The influence of thermal treatment applied to the fermentation broth was evaluated in the xanthan produced by strain 106 in a range of pH and stirrer speed. The thermal treatment decreased the yield between 5.8 and 14%, nevertheless, was observed increase of aqueous solution and fermentation broth viscosities. The aggregation of xanthan molecules caused by thermal treatment and determined by increase of molar mass was dependent on the sodium content. As a result, a correlation between molar mass and xanthan solution viscosity can be observed. The fermentation broth sterilization was adopted for experiment in which a pre-selection of production medium in orbital shaker was performed for subsequent pH, production medium and stirrer speed study in fermentor by strains 106 and 115. Xanthan production and viscosity was dependent on the strain of X. arborícola pv pruni and on the operational condition used. The production medium B showed the best balance of yield and viscosity results, in orbital shaker, as well as in fermentor. The best results for both strains were obtained at pH 7, 600 rpm and 66 h of fermentation. The two strains showed potential for xanthan production. In an evaluation study of, physical and chemical characteristics, the xanthan produced by strain 115 was compared to the characteristics of the commercial xanthans, Roeper and Kelzan. The former is for application in food, pharmeceutical products and cosmetics and the latter for application in oilwell drilling fluids. The results were within the literature specified patterns, except by the low piruvate content of xanthan produced by strain 115, low monovalent salt content of Roeper sample and high divalent salt content of both commercial samples. The xanthans produced by X. arborícola pv pruni were evaluated as viscosifying fluid for use in oilwell drilling, in comparison to Duo Vis, Kelzan and Xanvis commercial brands. As a whole, the results obtained in this study show that the commercial polymers are more efficient when used in aqueous solution, since these polymers contain high salt concentrations. Xanthans produced by patovar pruni, Xc 106 600 and Xc 115 600, as having low salt concentration, they show potential for application in oilwell drilling fluid, when a salt solution was used, similar to the conditions of marine exploration. / O rendimento e as características físicas e químicas da xantana podem ser melhorados através das modificações nas condições de cultivo, assim como, por tratamentos empregados após a fermentação, para a obtenção de uma xantana com características desejadas para o fim que se propõe. O trabalho objetivou estudar as condições operacionais de produção de xantana por Xanthomonas arboricola pv pruni cepas 106 e 115 para aplicação em fluidos de perfuração de poços de petróleo. A influência do tratamento térmico aplicado no caldo fermentado foi avaliada na xantana produzida pela cepa 106 em diferentes condições de pH e velocidade de agitação. O tratamento térmico reduziu o rendimento entre 5,8 e 14%, entretanto, foi observado o aumento da viscosidade da solução aquosa e do caldo fermentado. A agregação de moléculas de xantana provocada pelo tratamento térmico, e comprovada pelo aumento da massa molar foi dependente da concentração de sódio. Como resultado pode ser observada relação entre a massa molar e a viscosidade da solução de xantana. A esterilização do caldo fermentado foi adotada para o experimento posterior, em que foi realizada uma pré-seleção de meios de produção, em agitador incubador, para posterior estudo de pH, meio de produção e velocidade de agitação em fermentador pelas cepas 106 e 115. A produção e a viscosidade das xantanas sintetizadas foram dependentes da cepa de X. arboricola pv pruni e das condições operacionais. O meio de produção B apresentou o melhor equilíbrio entre produção e viscosidade, em agitador incubador, assim como no fermentador. Os melhores resultados para ambas as cepas foram obtidos em pH 7, 600 rpm e 66 h de fermentação. As duas cepas apresentaram potencial para serem utilizadas na produção de xantana. No estudo da avaliação das características físicas e químicas, a xantana produzida pela cepa 115 foi comparada as características das xantanas comerciais, Roeper e Kelzan. A primeira, para aplicação em alimentos, produtos farmacêuticos e cosméticos e a segunda, para aplicação em fluido de perfuração de poços de petróleo. Os resultados apresentaram-se dentro dos padrões especificados pela literatura, exceto pelo baixo conteúdo de piruvato da xantana produzida pela cepa 115, baixo conteúdo de sais monovalentes da amostra Roeper e alto conteúdo de sais divalentes das duas amostras comerciais. As xantanas produzidas por X. arboricola pv pruni foram avaliadas como viscosificante de fluido para aplicação na perfuração de poços de petróleo, comparando-as com amostras comerciais: Duo Vis, Kelzan e Xanvis. De uma forma geral, os resultados obtidos neste estudo mostram que os polímeros comerciais apresentaram maior eficiência quando preparados em solução aquosa, pois estes polímeros continham alta concentração de sais. Já as xantanas produzidas pelo patovar pruni, Xc 106 600 e Xc 115 600, por apresentarem baixa concentração de sais, apresentaram potencial para aplicação em fluido de perfuração de poços de petróleo, quando preparados em solução salina, condição semelhante a utilizada na exploração marítima.

<p>  Non-model microorganisms offer a wealth of biotechnological potential that may be leveraged to address a variety of global grand challenges. These include challenges in carrying out complex or altogether new chemistries, discovery and production of bioactive molecules, sustainable production of biochemicals and bioproducts from renewable feedstocks, and improving agricultural practices for responsible management of carbon. Specifically, using renewable plant biomass as a substrate for production of fuels and or chemicals offers a near ubiquitous supply that does not compete with food or petrochemicals. Alternatively, identifying new natural products will be essential to addressing the ever-increasing occurrence of antibiotic resistance. Non-model organisms may provide elegant solutions to many of these challenges, whether by possessing new or more efficient strategies to depolymerize lignocellulose, by encoding enzymes with increased stabilities and or specific activities, or perhaps by containing rich biosynthetic capabilities for production of previously unidentified natural products, among others. Yet efforts to leverage non-model microorganisms for their diverse biotechnological potential remain limited to a variety of often difficult, yet not insurmountable challenges.</p> <p>     In this work, I propose anaerobic gut fungi (Neocallimastigomycota) as a robust microbial system that may be leveraged to efficiently depolymerize crude lignocellulose, increase animal nutrition, or identify novel natural products. To this end, I detail the first chromosomally resolved genome assembly of anaerobic fungi (<em>Piromyces communis </em>var. <em>indianae</em> UH3-1). I investigate the genome organization of this isolate and describe how acquisition of Carbohydrate Active EnZymes (CAZymes) contribute to the robust lignocellulolytic activity of gut fungi. I then detail efforts to build a nascent genetic engineering toolbox for these anaerobic organisms. With the acquisition of the first chromosomally resolved genome assemblies, I identify a basic set of genetic parts needed for a genetic engineering toolkit. I show these parts are functional and detail methods to enable higher throughput testing in vivo. I subsequently detail efforts to construct the first preliminary CRISPR tools for anaerobic fungi as these will be essential to establish precise DNA targeting in future strain engineering efforts. I then describe the role of epigenetics in anaerobic fungi, detailing the extent to which it may be leveraged to control gene expression. Finally, I provide a discussion of this work and describe how it may guide future efforts to domesticate these organisms. Collectively, this work provides the first chromosomally resolved genome assembly as a resource for the community, along with genetic tools and techniques to begin domesticating these non-model organisms. Importantly, this work reveals that despite the challenges associated with anaerobic microbes of relatively high complexity, they are not insurmountable, and thus efforts to domesticate them are feasible.</p>

<p><a href="" target="_blank">Synthetic microbial communities (SynComs) are an important focus in modern microbiology. SynComs are used for studying the dynamics of naturally occurring microbial communities ranging from soil to the human gut. Synthetic refers to the assemblage of some or all the members of these communities in a laboratory setting. SynComs allow for communities difficult to study <i>in situ</i> to be studied in a controlled environment, or they may be used to create beneficial products like biofertilizers. When SynComs are used as products, the focus shifts to optimizing a desired outcome of a culture. For biofertilizers, a high diversity is key to producing a functionally redundant product for stimulating plant growth. Media manipulation is a common approach for inducing community changes in a SynCom. Amino acids (AA) are a media supplement that soil microbes (often the components of biofertilizers) are particularly fond of to support their metabolic activities. This study took a scale-up approach to assess the changes in growth dynamics of a SynCom (Environoc© 401) when supplemented with different concentrations of commercially available AA products from plant and animal sources. Expanding from microplates, to shake flasks, then into a 4L bioreactor, Environoc© 401 cultures were compared for their maximum growth rate, time in lag phase, and final growth (optical density or viable cell density) when supplemented with these AA products at various concentrations. Furthermore, Illumina sequencing of the 16S rRNA gene was used to evaluate community-level changes from these treatments based on taxonomic, alpha (Chao 1 and Shannon indices), and beta diversity (Generalized UniFrac) of shake flask and bioreactor samples. Quantitative PCR was also used to assess the relative change of three select species of the SynCom in each AA treatment. Shake flask data revealed significant changes in the growth dynamics of the SynComs within AA treatment groups. Whether the AA was animal or plant derived, generally as the concentration of AA increased, the maximum growth rate decreased, lag time increased, and final growth readings increased. The best AA supplement and rate according to the growth metrics and <i>Curveball </i>analysis was Stimtide at a 33% supplementation rate. This was compared with the control at the bioreactor scale where it showed higher overall final growth and a higher taxonomic and alpha diversity. The scale-up approach to this study was successful at selecting the best amino acid supplement type and rate despite having less sophisticated control and monitoring compared to larger scales (i.e. the bioreactor). Use of the <i>Curveball</i> modeling program was useful for treatment group selection but did not always predict the outcomes seen in the live cultures. The use of AA as a media supplement can increase growth and diversity of a SynCom, though not all AA supplements or rates affect growth and community dynamics in the same way</a>.</p>