Master of Science / Food Science Institute / J. Scott Smith / Heterocyclic amines (HCAs) are cancer causing compounds formed during the cooking of meat. Previous studies show that incorporating antioxidant spices into meat as well as marinating meat with antioxidant spices reduces formation of HCAs. The purpose of this study was to determine if commercially available spices applied to the surface of meat could effectively reduce HCA formation. Two commercially available spice blends and one blend of spices with known quantities of antioxidant spices were sprinkled onto the surface of beef just prior to pan-frying. The quantities of spices used were based on the amounts customarily consumed in typical Western cooking. The results of direct application were then compared to marinating with the same types and amounts of spices. The antioxidant potential of the spices was analyzed using DPPH and total phenolics methods. Results indicated that the spices would be effective antioxidants. Low recovery rates and problems during the extraction process made results inconclusive, but suggest that further research may find that applying spices directly to the surface of meat in consumer acceptable quantities may be as effective as marinating at reducing the formation of HCAs.

The Canadian livestock industry generates 150 million tonnes of manure annually and the majority of this manure is land applied. This practice allows the manure nutrients to be recycled to the soil crop system while improving soil fertility. However, land application of manure has the potential to negatively impact soil, water, and air quality if not managed properly. Microbial processes transform the manure nutrients into forms that are susceptible to leaching or volatilization. Balancing the nutrient loss dynamics from fertilized soil is very difficult because the nutrient transformations are affected by the soil environment such as air and water content, pH, and labile carbon content. All of these soil environmental factors can be influenced by manure application practices such as application rate, timing, and manure placement. Knowledge of how these management practices affect the soil environment can help producers make management decisions that reduce the likelihood of soil, water, and air contamination from manure application.<p> Very few data exist on how manure application practices affect odour emissions after spreading. Therefore, the efficiency of subsurface application in reducing odours from manure spreading for both solid and liquid manure was assessed. Flux chambers and dynamic dilution olfactometry were used to measure odour emissions from five livestock manure species applied at three application rates using surface and subsurface application methods. The results indicated that odour concentrations from injected plots were up to 66% (37% on average) lower than concentrations from broadcast applications. Injection seemed to have a larger impact on reducing odours from solid manure than liquid manure, mainly due to efficient manure coverage from solid manure injection. Odours measured immediately after solid manure applications were also 37% lower than from liquid manure applications. In general, odours from both manure types increased with higher application rates, but there was little difference in the odours among low, mid, and high application rates. The specific odour rate (odour emission rate per kg N applied) decreased with application rate due to the reduced surface area available for volatilization of compounds with higher application rates. Based on these results, injection of manure is an effective way to reduce the odour emissions immediately after spreading, particularly for solid manure. However, other factors associated with manure injection, such as the increased power requirement and soil disturbance must be considered when evaluating the overall impact of manure injection versus surface application.<p> The odour data collected in this study described how management practices affected odours immediately after spreading. Knowledge of how these practices affect the emission rate trend over time is required to apply dispersion models to optimize the minimum separation distances for manure spreading activities. The model parameters for an existing volatilization model were determined from field and literature data and the resulting model allowed the effects of application mode (surface vs. subsurface) and manure type (liquid vs. solid) on odour emissions for 48 hours after application to be simulated. The effects of injection depth and a coverage factor on emissions were also simulated. The modeled peak fluxes from liquid manure applications were higher than those for solid manure applications, but the extended duration of odour emissions from solid manure resulted in higher cumulative losses from solid manure applications. While the application rate had no effect on the initial odour flux, higher application rates resulted in higher peak fluxes, higher overall emissions, and longer odour durations for both manure types and application methods. Modest injection depths were shown to reduce odours from both liquid and solid manure applications compared to surface spreading. The percent reductions in cumulative odours due to injection were estimated assuming typical coverage factors. The general predictions of the model developed in this study agree reasonably well with odour emission rate trends reported in literature. Future work should focus on better estimation of the model parameters and the variation of effective diffusivity with time and soil conditions.<p> Greenhouse gas (GHG) emissions from agricultural activities such as land application of livestock manure cannot be ignored when assessing overall emissions from anthropogenic sources. Like odour emissions, the magnitude of the GHG emissions will be influenced by management practices such as manure placement during land application. The GHG fluxes resulting from the surface and subsurface application of liquid and solid manure were also compared within 24 hours of application using a static chamber and gas chromatography. The results showed that carbon dioxide equivalent (CO2-e) fluxes were approximately three times higher from the injected plots than the surface plots for both solid and liquid manure. The elevated CO2-e fluxes were mainly due to a pronounced increase in N2O fluxes which was likely caused by increased denitrification rates. The CO2-e fluxes from the liquid manure applications were also approximately three times higher than the CO2-e fluxes from the solid manure applications, probably due to higher levels of ammonium available for nitrification and subsequent denitrification. The CH4 fluxes were generally low and the treatments had no effect. The measured specific fluxes (total flux per kg N applied) remained relatively constant with application rate, indicating that, in this study, GHG emissions from manure applications were approximately proportional to the amount of land applied manure.<p> While the data from this study showed that manure type and placement influenced short-term nitrous oxide (N2O) emissions, manure management practices (particularly slurry injection or solid manure incorporation) have the potential to influence long-term emissions by changing the magnitude and pattern of the nitrogen cycle in the soil-plant system. Management practices also impact the magnitude of other nitrogen losses (ammonia volatilization, nitrate leaching) which affect indirect N2O emissions. A model that simulates the environmental conditions and nutrient transformations after manure application may allow a more reliable prediction of the effect of management practices on total GHG emissions. Numerous process-based models have been used to estimate N2O emissions as influenced by agricultural practices in Canada. However, these models do not account for enhanced denitrification that potentially exists after slurry injection or manure incorporation, resulting in an underestimation of N2O emissions. A simple mass balance of nitrogen after application to land showed that enhanced denitrification can increase total N2O-N emissions by a factor of 5. By accounting for the increased microbial activity, slower oxygen diffusion and higher water filled pore space that exists after manure injection, models may better estimate N2O emissions from manure application practices.

The Canadian livestock industry generates 150 million tonnes of manure annually and the majority of this manure is land applied. This practice allows the manure nutrients to be recycled to the soil crop system while improving soil fertility. However, land application of manure has the potential to negatively impact soil, water, and air quality if not managed properly. Microbial processes transform the manure nutrients into forms that are susceptible to leaching or volatilization. Balancing the nutrient loss dynamics from fertilized soil is very difficult because the nutrient transformations are affected by the soil environment such as air and water content, pH, and labile carbon content. All of these soil environmental factors can be influenced by manure application practices such as application rate, timing, and manure placement. Knowledge of how these management practices affect the soil environment can help producers make management decisions that reduce the likelihood of soil, water, and air contamination from manure application.<p> Very few data exist on how manure application practices affect odour emissions after spreading. Therefore, the efficiency of subsurface application in reducing odours from manure spreading for both solid and liquid manure was assessed. Flux chambers and dynamic dilution olfactometry were used to measure odour emissions from five livestock manure species applied at three application rates using surface and subsurface application methods. The results indicated that odour concentrations from injected plots were up to 66% (37% on average) lower than concentrations from broadcast applications. Injection seemed to have a larger impact on reducing odours from solid manure than liquid manure, mainly due to efficient manure coverage from solid manure injection. Odours measured immediately after solid manure applications were also 37% lower than from liquid manure applications. In general, odours from both manure types increased with higher application rates, but there was little difference in the odours among low, mid, and high application rates. The specific odour rate (odour emission rate per kg N applied) decreased with application rate due to the reduced surface area available for volatilization of compounds with higher application rates. Based on these results, injection of manure is an effective way to reduce the odour emissions immediately after spreading, particularly for solid manure. However, other factors associated with manure injection, such as the increased power requirement and soil disturbance must be considered when evaluating the overall impact of manure injection versus surface application.<p> The odour data collected in this study described how management practices affected odours immediately after spreading. Knowledge of how these practices affect the emission rate trend over time is required to apply dispersion models to optimize the minimum separation distances for manure spreading activities. The model parameters for an existing volatilization model were determined from field and literature data and the resulting model allowed the effects of application mode (surface vs. subsurface) and manure type (liquid vs. solid) on odour emissions for 48 hours after application to be simulated. The effects of injection depth and a coverage factor on emissions were also simulated. The modeled peak fluxes from liquid manure applications were higher than those for solid manure applications, but the extended duration of odour emissions from solid manure resulted in higher cumulative losses from solid manure applications. While the application rate had no effect on the initial odour flux, higher application rates resulted in higher peak fluxes, higher overall emissions, and longer odour durations for both manure types and application methods. Modest injection depths were shown to reduce odours from both liquid and solid manure applications compared to surface spreading. The percent reductions in cumulative odours due to injection were estimated assuming typical coverage factors. The general predictions of the model developed in this study agree reasonably well with odour emission rate trends reported in literature. Future work should focus on better estimation of the model parameters and the variation of effective diffusivity with time and soil conditions.<p> Greenhouse gas (GHG) emissions from agricultural activities such as land application of livestock manure cannot be ignored when assessing overall emissions from anthropogenic sources. Like odour emissions, the magnitude of the GHG emissions will be influenced by management practices such as manure placement during land application. The GHG fluxes resulting from the surface and subsurface application of liquid and solid manure were also compared within 24 hours of application using a static chamber and gas chromatography. The results showed that carbon dioxide equivalent (CO2-e) fluxes were approximately three times higher from the injected plots than the surface plots for both solid and liquid manure. The elevated CO2-e fluxes were mainly due to a pronounced increase in N2O fluxes which was likely caused by increased denitrification rates. The CO2-e fluxes from the liquid manure applications were also approximately three times higher than the CO2-e fluxes from the solid manure applications, probably due to higher levels of ammonium available for nitrification and subsequent denitrification. The CH4 fluxes were generally low and the treatments had no effect. The measured specific fluxes (total flux per kg N applied) remained relatively constant with application rate, indicating that, in this study, GHG emissions from manure applications were approximately proportional to the amount of land applied manure.<p> While the data from this study showed that manure type and placement influenced short-term nitrous oxide (N2O) emissions, manure management practices (particularly slurry injection or solid manure incorporation) have the potential to influence long-term emissions by changing the magnitude and pattern of the nitrogen cycle in the soil-plant system. Management practices also impact the magnitude of other nitrogen losses (ammonia volatilization, nitrate leaching) which affect indirect N2O emissions. A model that simulates the environmental conditions and nutrient transformations after manure application may allow a more reliable prediction of the effect of management practices on total GHG emissions. Numerous process-based models have been used to estimate N2O emissions as influenced by agricultural practices in Canada. However, these models do not account for enhanced denitrification that potentially exists after slurry injection or manure incorporation, resulting in an underestimation of N2O emissions. A simple mass balance of nitrogen after application to land showed that enhanced denitrification can increase total N2O-N emissions by a factor of 5. By accounting for the increased microbial activity, slower oxygen diffusion and higher water filled pore space that exists after manure injection, models may better estimate N2O emissions from manure application practices.

O desempenho de unidades de flotação por ar dissolvido (FAD) depende significativamente do projeto da zona de contato (ZC) dessas unidades, situada na entrada das mesmas e responsável por promover condições adequadas para que ocorram taxas satisfatórias de colisão entre as microbolhas de ar e os flocos formados na etapa antecedente de floculação da água para abastecimento. Os dois principais parâmetros de projeto da ZC são o tempo de detenção hidráulico ou tempo de contato (Tzc) e o gradiente médio de velocidade na ZC (Gzc). A presente dissertação apresenta os resultados de estudo sobre a influência do Tzc e do Gzc na ZC de uma unidade piloto de flotação por ar dissolvido (UPFAD) com escoamento contínuo aplicada ao tratamento de água para abastecimento. Foram utilizados módulos contendo tela metálica em seu interior com malha de #25 mm com diferentes dimensões, de modo a se obterem diferentes valores de Gzc e Tzc. Foram investigadas duas configurações na unidade de FAD (Configurações A e B), nas quais o comprimento (Lzc) e a altura (Hzc) da ZC foram variados, permitindo a alteração do Tzc e mantendo-se controlados os valores de Gzc (com a introdução ou não de diferentes módulos de tela metálica na ZC) e vice versa. Os demais parâmetros do processo de FAD não sofreram variações, tais como taxa de aplicação superficial (TAS) na zona de separação, tempo de floculação, entre outros. Para a configuração A, foram estudadas três alturas diferentes na ZC e para a configuração B, quatro alturas diferentes na ZC, o que acarretou, para cada valor de Gzc variação do Tzc. Para cada configuração da ZC, também foram testados três valores de vazão de recirculação de água saturada com ar de modo a se obterem três diferentes concentrações de ar (A/V) no processo de flotação. Para todos os parâmetros analisados (Turbidez, Cor, Absorbância), as maiores eficiências de remoção foram obtidas nos ensaios realizados com o uso da tela #25 mm tanto na configuração A (TASzc = 136 m/h e G = 6,1 s-1) quanto na configuração B (TASzc = 87 m/h e G = 3,2 s-1). Os resultados permitem concluir que o par de valores (Tzc, Gzc) é mais apropriado para o projeto da zona de contato de unidades FAD do que o par (Tzc, TASzc) usualmente adotado pelos projetistas, sendo que, na faixa de valores investigados a UPFAD apresentou melhor desempenho para o par: Tzc de 41 s e Gzc de 6,1 s-1. / The performance of units dissolved air flotation (DAF) depend significantly of design on the contact zone (CZ) of these units, situated at the entrance thereof and responsible for promoting appropriate conditions to occur satisfactory collision rates between air microbubbles and the flocs formed in the step of flocculation of potable water. The two main design parameters of the CZ are the hydraulic detention time or contact time (Tcz) and the velocity gradient in the CZ (Gcz). This work presents the results of study of the effects of varying the Tcz and Gcz at the contact zone of pilot unit DAF with continuous flow applied to the treatment of potable water. Were used modules containing metal grille with mesh of #25 mm, with different dimensions in order to obtain different values of Gcz and Tcz. Were investigated two configurations in the unit FAD ( configurations A and B) where the length (Lcz) and height (Hcz) of contact zone were varied, allowing the variation of Tzc and keeping the values of Gcz controlled (with the introduction or not of different modules in the metal grille in CZ) and vice versa, without changes in other process variables FAD, such as rate of surface application (TAS) in the separation zone, flocculation time, among others. For the configuration A were studied three different heights in the CZ and in configuration B, four different heights in the CZ, which resulted, for each value of Gcz (relative to the chosen value of Lcz) the variation of Tzc. For each configuration of CZ were also tested three values of recirculation flow of air saturated in order to obtain three different values of concentration in air (A/V) in the flotation process. For all parameters analyzed (turbidity, color, absorbance), the highest efficiencies were obtained in assays performed using the grille #25 mm, both in configuration A (TAScz = 136 m/h and L = 6,1 s-1) and configuration B (TAScz = 87 m/h and G = 3,2 s-1). The results indicate that the pair of values (Tcz, Gcz) is more suitable for project of the CZ of units FAD than the pair (Tcz, TAScz) usually adopted by the designers, and values in the range investigated in UPFAD showed performed better for Tcz of 41 s and Gcz of 6,1 s-1.

Urea is the main nitrogen (N) fertilizer used worldwide, but N losses in the form of ammonia (NH3) is a major problem when this fertilizer is topdressed over crop residues. The treatment of urea with N-(n-butyl) thiophosphoric triamide (NBPT) decreases the activity of urease enzyme and volatilization losses in many crops. However, the amount of straw over the soil in green cane trash blanketing (GCTB) systems affect the effectiveness of NBPT-treated urea in reducing NH3 losses. The hypothesis of this study is that an increase of NBPT concentration in NBPT-treated urea above the commercial concentration adopted nowadays (530 mg kg-1) is necessary to reduce volatilization losses and improve the efficiency of this fertilizer in GCTB systems. The aim of this study was to evaluate, under field conditions, NH3 losses from urea amended with four NBPT concentrations and applied over sugarcane straw. Six field trials were carried out across the State of São Paulo, the main sugarcane-cropped area in Brazil. It was adopted the randomized block experimental design with four replications. The treatments consisted of urea amended with the NBPT concentrations 0, 530, 850, 1500 and 2000 mg kg-1, ammonium nitrate and a control treatment (without N fertilizer). The NH3 volatilization was measured through an enclosure semi-static collector system containing two polyethylene foam discs treated with orthophosphoric acid and glycerol. The foam discs were collected and replaced at 2, 4, 6, 8, 10, 12, 16, 20, 25 and 30 days after the fertilizer application (DAF). The N trapped into the foams was extracted using deionized water and the N concentration determined by Flow Injection Analysis (FIA). Boltzmann sigmoidal models were fitted to cumulative losses of NH3 along the days. Cumulative losses between locals were compared by Tukey HSD and the effect of NBPT concentrations were tested by regression analyses (P<0.05). There was a significant effect of local and environmental conditions on amount of NH3 losses. NBPT was less effective in reducing NH3 losses under high temperatures and thick straw layer, probably because of the high urease activity and the early inhibitor degradation. The increase on NBPT concentration on urea above 530 mg kg-1 not only delayed the time of maximum rate of loss (Tmax), but also reduced cumulative NH3 losses. The two higher NBPT concentrations promoted an average delay of six days from untreated urea Tmax. Linear reduction of NH3 emissions occurred up to the NBPT concentration of 1000 mg kg-1 that reduced 43% of NH3 losses as compared to urea. Any increment in NBPT concentration above this range did not reflect in substantial reduction of NH3 losses. Increase NBPT concentration showed potential in reducing NH3 volatilization losses under GCTB sugarcane, however, further research is necessary to evaluate the impact of NH3 savings on sugarcane yield and the economic feasibility of this technology. / A ureia é o principal fertilizante nitrogenado utilizado em todo o mundo, porém, perdas de nitrogênio (N) na forma de amônia (NH3) são um importante problema associado ao uso desse fertilizante. O tratamento da ureia com N-(n-butil) tiofosfórico triamida (NBPT) reduz a atividade da enzima urease e a volatilização de NH3 em muitos cultivos. Entretanto, a quantidade de palha sobre o solo em sistemas de cultivo da cana-de-açúcar colhida sem queima (CCSQ) afeta a eficiência do tratamento da ureia com NBPT em reduzir as perdas de NH3. A hipótese deste estudo é que é necessário aumentar a concentração de NBPT na ureia acima da atual concentração comercial (530 mg kg-1) para reduzir as perdas por volatilização, de modo a viabilizar o uso de ureia tratada com NBPT em sistemas de CCSQ. O objetivo desse estudo foi avaliar, em condições de campo, as perdas de NH3 de ureia tratada com quatro concentrações de NBPT e aplicada sobre a palhada de cana-de-açúcar. Seis experimentos de campo foram conduzidos no Estado de São Paulo, principal área cultivada com cana-de-açúcar no Brasil. Foi utilizado delineamento aleatorizado em blocos com quatro repetições. Os tratamentos consistiram em ureia tratada com NBPT nas concentrações 0, 530, 850, 1500 e 2000 mg kg-1, nitrato de amônio e um tratamento controle (sem adubação nitrogenada). A volatilização e NH3 foi mensurada através de sistema coletor semiestático fechado, contendo dois discos de espuma de polietileno embebidos com solução de ácido ortofosfórico e glicerina. Os discos de espuma foram coletados e substituídos aos 2, 4, 6, 8, 10, 12, 16, 20, 25 e 30 dias após a aplicação dos fertilizantes (DAF). O N retido nas espumas foi extraído usando água deionizada e a concentração de N determinada por Análise por Injeção em Fluxo (FIA). Modelos sigmoides de Boltzmann foram ajustados para as perdas cumulativas de NH3 ao longo dos dias. As médias das perdas acumuladas entre locais foram comparadas usando teste de Tukey e o efeito das concentrações de NBPT foi testado por análise de regressão (P<0,05). Houve forte influência do local e das condições ambientais nas perdas de NH3. O NBPT foi menos eficiente reduzir as perdas de NH3 em condições de alta temperatura e grossa camada de palha, provavelmente devido à alta atividade de urease e à degradação prematura do inibidor. O aumento na concentração de NBPT na ureia acima de 530 mg kg-1 não apenas retardou o pico de máxima taxa de perda diária (Tmax), mas também reduziu as perdas acumuladas de NH3. As duas maiores concentrações de NBPT promoveram um retardamento médio de seis dias em relação ao Tmax da ureia. Uma redução linear nas emissões de NH3 foi verificada até a dose de 1000 mg kg-1 de NBPT, que levou a uma redução de 43% nas perdas em comparação à ureia não tratada. Incrementos na concentração de NBPT acima desse valor não se refletiram em redução substancial das perdas de NH3. Aumentar a concentração de NBPT na ureia demonstrou potencial em reduzir as perdas e NH3 por volatilização em sistemas de CCSQ, entretanto são necessárias mais pesquisas avaliando o impacto do N preservado no sistema sobre a produtividade da cana-de-açúcar e a viabilidade econômica dessa tecnologia.

Urea is the main nitrogen (N) fertilizer used worldwide, but N losses in the form of ammonia (NH3) is a major problem when this fertilizer is topdressed over crop residues. The treatment of urea with N-(n-butyl) thiophosphoric triamide (NBPT) decreases the activity of urease enzyme and volatilization losses in many crops. However, the amount of straw over the soil in green cane trash blanketing (GCTB) systems affect the effectiveness of NBPT-treated urea in reducing NH3 losses. The hypothesis of this study is that an increase of NBPT concentration in NBPT-treated urea above the commercial concentration adopted nowadays (530 mg kg-1) is necessary to reduce volatilization losses and improve the efficiency of this fertilizer in GCTB systems. The aim of this study was to evaluate, under field conditions, NH3 losses from urea amended with four NBPT concentrations and applied over sugarcane straw. Six field trials were carried out across the State of São Paulo, the main sugarcane-cropped area in Brazil. It was adopted the randomized block experimental design with four replications. The treatments consisted of urea amended with the NBPT concentrations 0, 530, 850, 1500 and 2000 mg kg-1, ammonium nitrate and a control treatment (without N fertilizer). The NH3 volatilization was measured through an enclosure semi-static collector system containing two polyethylene foam discs treated with orthophosphoric acid and glycerol. The foam discs were collected and replaced at 2, 4, 6, 8, 10, 12, 16, 20, 25 and 30 days after the fertilizer application (DAF). The N trapped into the foams was extracted using deionized water and the N concentration determined by Flow Injection Analysis (FIA). Boltzmann sigmoidal models were fitted to cumulative losses of NH3 along the days. Cumulative losses between locals were compared by Tukey HSD and the effect of NBPT concentrations were tested by regression analyses (P<0.05). There was a significant effect of local and environmental conditions on amount of NH3 losses. NBPT was less effective in reducing NH3 losses under high temperatures and thick straw layer, probably because of the high urease activity and the early inhibitor degradation. The increase on NBPT concentration on urea above 530 mg kg-1 not only delayed the time of maximum rate of loss (Tmax), but also reduced cumulative NH3 losses. The two higher NBPT concentrations promoted an average delay of six days from untreated urea Tmax. Linear reduction of NH3 emissions occurred up to the NBPT concentration of 1000 mg kg-1 that reduced 43% of NH3 losses as compared to urea. Any increment in NBPT concentration above this range did not reflect in substantial reduction of NH3 losses. Increase NBPT concentration showed potential in reducing NH3 volatilization losses under GCTB sugarcane, however, further research is necessary to evaluate the impact of NH3 savings on sugarcane yield and the economic feasibility of this technology. / A ureia é o principal fertilizante nitrogenado utilizado em todo o mundo, porém, perdas de nitrogênio (N) na forma de amônia (NH3) são um importante problema associado ao uso desse fertilizante. O tratamento da ureia com N-(n-butil) tiofosfórico triamida (NBPT) reduz a atividade da enzima urease e a volatilização de NH3 em muitos cultivos. Entretanto, a quantidade de palha sobre o solo em sistemas de cultivo da cana-de-açúcar colhida sem queima (CCSQ) afeta a eficiência do tratamento da ureia com NBPT em reduzir as perdas de NH3. A hipótese deste estudo é que é necessário aumentar a concentração de NBPT na ureia acima da atual concentração comercial (530 mg kg-1) para reduzir as perdas por volatilização, de modo a viabilizar o uso de ureia tratada com NBPT em sistemas de CCSQ. O objetivo desse estudo foi avaliar, em condições de campo, as perdas de NH3 de ureia tratada com quatro concentrações de NBPT e aplicada sobre a palhada de cana-de-açúcar. Seis experimentos de campo foram conduzidos no Estado de São Paulo, principal área cultivada com cana-de-açúcar no Brasil. Foi utilizado delineamento aleatorizado em blocos com quatro repetições. Os tratamentos consistiram em ureia tratada com NBPT nas concentrações 0, 530, 850, 1500 e 2000 mg kg-1, nitrato de amônio e um tratamento controle (sem adubação nitrogenada). A volatilização e NH3 foi mensurada através de sistema coletor semiestático fechado, contendo dois discos de espuma de polietileno embebidos com solução de ácido ortofosfórico e glicerina. Os discos de espuma foram coletados e substituídos aos 2, 4, 6, 8, 10, 12, 16, 20, 25 e 30 dias após a aplicação dos fertilizantes (DAF). O N retido nas espumas foi extraído usando água deionizada e a concentração de N determinada por Análise por Injeção em Fluxo (FIA). Modelos sigmoides de Boltzmann foram ajustados para as perdas cumulativas de NH3 ao longo dos dias. As médias das perdas acumuladas entre locais foram comparadas usando teste de Tukey e o efeito das concentrações de NBPT foi testado por análise de regressão (P<0,05). Houve forte influência do local e das condições ambientais nas perdas de NH3. O NBPT foi menos eficiente reduzir as perdas de NH3 em condições de alta temperatura e grossa camada de palha, provavelmente devido à alta atividade de urease e à degradação prematura do inibidor. O aumento na concentração de NBPT na ureia acima de 530 mg kg-1 não apenas retardou o pico de máxima taxa de perda diária (Tmax), mas também reduziu as perdas acumuladas de NH3. As duas maiores concentrações de NBPT promoveram um retardamento médio de seis dias em relação ao Tmax da ureia. Uma redução linear nas emissões de NH3 foi verificada até a dose de 1000 mg kg-1 de NBPT, que levou a uma redução de 43% nas perdas em comparação à ureia não tratada. Incrementos na concentração de NBPT acima desse valor não se refletiram em redução substancial das perdas de NH3. Aumentar a concentração de NBPT na ureia demonstrou potencial em reduzir as perdas e NH3 por volatilização em sistemas de CCSQ, entretanto são necessárias mais pesquisas avaliando o impacto do N preservado no sistema sobre a produtividade da cana-de-açúcar e a viabilidade econômica dessa tecnologia.

O desempenho de unidades de flotação por ar dissolvido (FAD) depende significativamente do projeto da zona de contato (ZC) dessas unidades, situada na entrada das mesmas e responsável por promover condições adequadas para que ocorram taxas satisfatórias de colisão entre as microbolhas de ar e os flocos formados na etapa antecedente de floculação da água para abastecimento. Os dois principais parâmetros de projeto da ZC são o tempo de detenção hidráulico ou tempo de contato (Tzc) e o gradiente médio de velocidade na ZC (Gzc). A presente dissertação apresenta os resultados de estudo sobre a influência do Tzc e do Gzc na ZC de uma unidade piloto de flotação por ar dissolvido (UPFAD) com escoamento contínuo aplicada ao tratamento de água para abastecimento. Foram utilizados módulos contendo tela metálica em seu interior com malha de #25 mm com diferentes dimensões, de modo a se obterem diferentes valores de Gzc e Tzc. Foram investigadas duas configurações na unidade de FAD (Configurações A e B), nas quais o comprimento (Lzc) e a altura (Hzc) da ZC foram variados, permitindo a alteração do Tzc e mantendo-se controlados os valores de Gzc (com a introdução ou não de diferentes módulos de tela metálica na ZC) e vice versa. Os demais parâmetros do processo de FAD não sofreram variações, tais como taxa de aplicação superficial (TAS) na zona de separação, tempo de floculação, entre outros. Para a configuração A, foram estudadas três alturas diferentes na ZC e para a configuração B, quatro alturas diferentes na ZC, o que acarretou, para cada valor de Gzc variação do Tzc. Para cada configuração da ZC, também foram testados três valores de vazão de recirculação de água saturada com ar de modo a se obterem três diferentes concentrações de ar (A/V) no processo de flotação. Para todos os parâmetros analisados (Turbidez, Cor, Absorbância), as maiores eficiências de remoção foram obtidas nos ensaios realizados com o uso da tela #25 mm tanto na configuração A (TASzc = 136 m/h e G = 6,1 s-1) quanto na configuração B (TASzc = 87 m/h e G = 3,2 s-1). Os resultados permitem concluir que o par de valores (Tzc, Gzc) é mais apropriado para o projeto da zona de contato de unidades FAD do que o par (Tzc, TASzc) usualmente adotado pelos projetistas, sendo que, na faixa de valores investigados a UPFAD apresentou melhor desempenho para o par: Tzc de 41 s e Gzc de 6,1 s-1. / The performance of units dissolved air flotation (DAF) depend significantly of design on the contact zone (CZ) of these units, situated at the entrance thereof and responsible for promoting appropriate conditions to occur satisfactory collision rates between air microbubbles and the flocs formed in the step of flocculation of potable water. The two main design parameters of the CZ are the hydraulic detention time or contact time (Tcz) and the velocity gradient in the CZ (Gcz). This work presents the results of study of the effects of varying the Tcz and Gcz at the contact zone of pilot unit DAF with continuous flow applied to the treatment of potable water. Were used modules containing metal grille with mesh of #25 mm, with different dimensions in order to obtain different values of Gcz and Tcz. Were investigated two configurations in the unit FAD ( configurations A and B) where the length (Lcz) and height (Hcz) of contact zone were varied, allowing the variation of Tzc and keeping the values of Gcz controlled (with the introduction or not of different modules in the metal grille in CZ) and vice versa, without changes in other process variables FAD, such as rate of surface application (TAS) in the separation zone, flocculation time, among others. For the configuration A were studied three different heights in the CZ and in configuration B, four different heights in the CZ, which resulted, for each value of Gcz (relative to the chosen value of Lcz) the variation of Tzc. For each configuration of CZ were also tested three values of recirculation flow of air saturated in order to obtain three different values of concentration in air (A/V) in the flotation process. For all parameters analyzed (turbidity, color, absorbance), the highest efficiencies were obtained in assays performed using the grille #25 mm, both in configuration A (TAScz = 136 m/h and L = 6,1 s-1) and configuration B (TAScz = 87 m/h and G = 3,2 s-1). The results indicate that the pair of values (Tcz, Gcz) is more suitable for project of the CZ of units FAD than the pair (Tcz, TAScz) usually adopted by the designers, and values in the range investigated in UPFAD showed performed better for Tcz of 41 s and Gcz of 6,1 s-1.