No description available.

No description available.

Performance data for three rainbow trout (Oncorhynchus mykiss) strains (Erwin, Shasta, and Duncan River Kamloops) were collected to guide fish culture operations at White Sulphur Springs National Fish Hatchery (NFH). The performance of the strains was evaluated in terms of survival, growth, disease resistance, reproductive performance (number of ripe and culled females, spawning time, number of egg takes, number of eggs per female, egg size, and percent eye up), feed conversion, and feed costs, and was compared with data from Ennis NFH, MT, and two Arizona Game and Fish Department hatcheries. Prespawning survival rates were higher for Erwin (90%) and Shasta (95%) strains than for the Kamloops strain (<75%). The Shasta strain exhibited the lowest feed conversion ratio (mean=1.89) and feed costs ($0.15 per stockable individual and $0.92 per spawning individual) than Erwin (1.96, $0.16, $1.56) and Kamloops (1.66, $0.18, N/A) strains. The Shasta strain exhibited larger egg size (mean=15,967/1) than the Erwin strain (mean=21,900/1). Reproductive performance for the Kamloops strain was not evaluated, as the strain was not sexually mature at the close of the study. Vulnerability of Erwin strain rainbow trout to cold water disease, Cytophaga psychrophila, bacterial kidney disease, Renibacterium salmoninarum, and four other bacteria was observed, while Shasta and Kamloops strains were less vulnerable to disease. Based on findings of this study and on programmatic considerations, the Shasta strain will be the only one to remain in full production at White Sulphur Springs NFH. / Master of Science

Thesis (MScEng)--Stellenbosch University, 2011. / ENGLISH ABSTRACT: In a first stage atmospheric leach at the Lonmin Marikana base metals refinery, nickel-copper-iron-sulphur Peirce Smith converter matte is leached in recycled electrolyte from the electrowinning section. The electrolyte contains sulphuric acid, copper and nickel sulphates, and a small amount of iron sulphate. The converter matte contains mostly nickel, copper and sulphur (typically 48 %, 28 % and 23 %, respectively), but also minor amounts (<5 %) iron and cobalt. The matte also contains platinum group elements (PGEs) and other precious metals totalling 0.2 – 0.7 % (platinum, palladium, iridium, rhodium, ruthenium, osmium and some gold). The predominant mineral phases are heazlewoodite, chalcocite and a nickel-copper alloy phase, as well as some entrained slag and spinel minerals. The purpose of the first stage leach is to extract nickel, while simultaneously precipitating copper and PGEs contained in the recycled electrolyte. Nickel, cobalt and iron are leached by acid and oxygen. Copper is precipitated by a redox reaction in which copper ions oxidise nickel from the matte. The purpose of this study was to determine the effects of key variables on the performance of the first stage leach (specifically on the removal of PGEs and copper from solution and the overall extraction of nickel) and to improve fundamental understanding of these effects. Batch leaching tests were carried out to investigate the effects of the following factors: availability of oxygen, initial acid concentration, initial copper concentration, iron endpoint (iron content of the matte), solids/liquid ratio and stirring rate. Liquid samples were analysed with Atomic Absorption Spectroscopy (AA) to determine leaching kinetics. Characterisation of solid samples from leach tests by quantitative X-Ray diffraction (XRD) and scanning electron microscopy with an energy dispersive system (SEM-EDS) helped to improve understanding of the leaching mechanism. The oxidative leaching mechanism entails an initial period in which the alloy phase is leached by acid and oxygen, while copper reacts with the nickel-copper-alloy and heazlewoodite phases (which react galvanically with each other) to form a chalcocite precipitate. In a second reaction period, heazlewoodite was transformed to millerite by acid leaching and the particle structure became more porous. The rate of copper precipitation and nickel extraction were faster during the second reaction period than the first reaction period. Some copper leaching occurred once the leachable nickel (60 – 70 %) had been dissolved, provided that the solution was strongly acidic (pH < 2). The non-oxidative leaching mechanism entails a galvanic interaction, between the nickel-copper-alloy and heazlewoodite phases, in which nickel is leached from both phases and copper is precipitated as chalcocite. Leaching by acid was negligible in most non-oxidative tests. An initial fast period of copper precipitation was followed by a second slower period. The decrease in reaction rate can probably be linked to the decreasing availability of the nickel-copper-alloy phase. During non-oxidative leaching, the particle structure remained mostly intact. Copper precipitation kinetics under non-oxidative conditions was found to be slower than under oxidative conditions. The faster copper precipitation kinetics under oxidative conditions is most likely caused by an increase in porosity and reaction area as nickel is leached from the matte by acid and oxygen. The initial acid concentration, solids/liquid ratio and Fe-endpoint were the most important factors determining reaction kinetics under oxidative conditions. Low initial acid concentrations (37 g/L) and a high solids/liquid ratio improved the extent of copper precipitation. Nickel extraction was enhanced by low solids/liquid ratios and high initial acid concentrations (74 g/L). Nickel extraction was significantly less (56 % less in one instance) when leaching high iron mattes (5.7 % Fe) rather than low iron mattes (< 1 % Fe). Copper precipitation was initially faster when leaching a high iron matte, but slower nickel leaching from high iron mattes led to an excess of available acid, which resulted in copper being leached. The results suggest that high iron mattes will lead to poor copper and PGE precipitation in the first stage leach and also to lower nickel extractions. Consequently, Peirce Smith converting at the plant must be carefully controlled to avoid high iron mattes. Under non-oxidative conditions, the solids/liquid ratio and Fe-endpoint were the most important factors. The rate of copper precipitation was faster when a high iron matte was leached, so that a higher percentage copper was precipitated and more nickel was extracted from the matte. / AFRIKAANSE OPSOMMING: As ‘n eerste stap in die Lonmin Marikana basis-metale veredelingsaanleg word nikkel-koper-yster-swawel Peirce-Smith-converter-mat geloog in elektroliet wat hersirkuleer word vanaf die aanleg se koper-elektroplaterings-afdeling. Die loging word by atmosferiese druk uitgevoer. Die elektroliet bevat swawelsuur, koper- en nikkel-sulfate en ‘n klein hoeveelheid ystersulfaat. Die mat bevat hoofsaaklik nikkel, koper en swawel (tipies 48 %, 28 % en 23 %), maar ook klein hoeveelhede (< 5 %) yster en kobalt. Verder maak Platinum Groep Elemente (PGE’s) en ander waardevolle metale (platinum, palladium, iridium, rhodium, ruthenium, osmium en goud) 0.2 % tot 0.7 % van die massa van die mat uit. In terme van minerale bestaan die materiaal hoofsaaklik uit heazlewoodite, chalcocite en ‘n nikkel-koper allooi fase, asook slak en spinel minerale, wat tydens Peirce-Smith-converting weens meesleuring in die mat rapporteer. Die doel van die eerste stadium loog is om nikkel op te los, terwyl koper en PGE’s wat in die elektroliet voorkom presipiteer moet word. Nikkel, kobalt en koper word geloog in reaksies met suurstof en swawelsuur. Koper word presipiteer deur middel van ‘n redoks reaksie waarin koper-ione nikkel in die mat oksideer. Die doel van hierdie studie was om die effekte van sleutelveranderlikes op die proses te bepaal (spesifiek hoe nikkel-loging en koper presipitasie affekteer word) en om fundamentele begrip van die veranderlikes en hul effekte te verkry. Lot loogtoetse is uitgevoer op ‘n laboratorium-skaal en die effekte van die volgende faktore is ondersoek: beskibaarheid van suurstof, begin suurkonsentrasie, yster eindpunt (die ysterinhoud van die mat), vastestof/vloeistof verhouding en die roertempo. Vloeistof monsters geneem tydens loogtoetse is geanaliseer met behulp van Atoom Absorpsie Spektroskopie (AA) om kinetika te bepaal. Vastestof monsters is ook geneem tydens loogtoetse en kwantitatiewe X-straal diffraksie (XRD), asook skanderings-elektron-mikroskopie met ‘n energie dispersie sisteem (SEM-EDS) is gebruik om die materiaal te karakteriseer en die logingsmeganisme te verduidelik. Die oksidatiewe logingsmeganisme behels ‘n aanvanklike periode waartydens die allooi fase geloog word deur suur en suurstof, terwyl koper presipiteer om chalcocite te vorm as gevolg van ‘n reaksie waarin galvanise interaksie tussen die nikkel-koperallooi en heazlewoodite fases ‘n belangrike rol speel. In ‘n tweede reaksie periode is heazlewoodite geloog deur suur om millerite te vorm. Tydens hierdie tweede fase het die partikel struktuur meer porieus geword. Die tempo van koper presipitasie en nikkel loging was vinniger tydens die tweede reaksie periode as tydens die eerste. Koper is geloog indien die oplossing baie suur was (pH < 2) en die loogbare nikkel (60 – 70 %) reeds opgelos het. Die nie-oksidatiewe logingsmeganisme behels galvaniese interaksie tussen die nikkel-koper-allooi en heazlewoodite fases, wat lei tot koper presipitasie as chalcocite. Loging deur swawelsuur was onbeduidend. ‘n Aanvanklike vinnige periode van koper presipitasie tydens nie-oksidatiewe toetse is gevolg deur ‘n tweede stadiger periode. Die afname in reaksietempo kan waarskynlik verklaar word deur die afnemende beskikbaarheid van die nikkel-koper-allooi fase. Tydens nieoksidatiewe loging het die partikel struktuur redelik onveranderd gebly. Koper presipitasie kinetika in nie-oksidatiewe toetse was stadiger as in oksidatiewe toetse. Die belangrikste faktore wat kinetika in oksidatiewe toetse beïnvloed het was die suurkonsentrasie, vastestof/vloeistof verhouding en die yster-eindpunt. Lae beginsuurkonsentrasies (37 g/L) en ‘n hoë vastestof/vloeistof verhouding het gelei daartoe dat meer koper uit die elektroliet herwin is. Nikkel ekstraksie was hoër indien die vastestof/vloeistof verhouding laag was en die begin suurkonsentrasie hoog (74 g/L). Nikkel ekstraksie was beduidend laer (56 % laer in een geval) wanneer hoë-yster mat (5.7 % Fe) geloog is, eerder as lae yster mat (< 1 % Fe). Wanneer ‘n hoë yster mat geloog is, was koper presipitasie aanvanklik vinniger, maar weens stadige nikkel-ekstraksie-tempos was ‘n oormaat van suur beskikbaar sodat koper uiteindelik geloog is. PGE presipitasie is ook nadelig beïnvloed wanneer koper geloog is en veral tydens toetse met hoë yster mat. Die mees belangrike faktore wat nie-oksidatiewe loging beïnvloed het was die vastestof/vloeistof verhouding en die yster-eindpunt. Die tempo van koper presipitasie was vinniger in toetse met ‘n hoë yster mat, sodat ‘n hoër persentasie koper presipiteer het en meer nikkel opgelos het wanneer ‘n hoë yster mat geloog is.

Heightened concerns for cleaner air and increasingly more stringent regulations on sulphur content in transportation fuels will make desulphurization more and more important. The sulphur problem is becoming more serious in general, particularly for diesel fuels as the regulated sulphur content is getting an order of magnitude lower, while the sulphur contents of crude oils are becoming higher. This thesis aimed to develop a desulphurisation process (based on oxidation followed by extraction) with high efficiency, selectivity and minimum energy consumption leading to minimum environmental impact via laboratory batch experiments, mathematical modelling and optimisation. Deep desulphurization of model sulphur compounds (di-n-butyl sulphide, dimethyl sulfoxide and dibenzothiophene) and heavy gas oils (HGO) derived from Libyan crude oil were conducted. A series of batch experiments were carried out using a small reactor operating at various temperatures (40-100 °C) with hydrogen peroxide (H2O2) as oxidant and formic acid (HCOOH) as catalyst. Kinetic models for the oxidation process are then developed based on 'total sulphur approach'. Extraction of unoxidised and oxidised gas oils was also investigated using methanol, dimethylformamide (DMF) and N-methyl pyrolidone (NMP) as solvents. For each solvent, the 'measures' such as: the partition coefficient (KP), effectiveness factor (Kf) and extractor factor (Ef) are used to select the best/effective solvent and to find the effective heavy gas oil/solvent ratios. A CSTR model is then developed for the process for evaluating viability of the large scale operation. It is noted that while the energy consumption and recovery issues could be ignored for batch experiments these could not be ignored for large scale operation. Large amount of heating is necessary even to carry out the reaction at 30-40 °C, the recovery of which is very important for maximising the profitability of operation and also to minimise environmental impact by reducing net CO2 release. Here the heat integration of the oxidation process is considered to recover most of the external energy input. However, this leads to putting a number of heat exchangers in the oxidation process requiring capital investment. Optimisation problem is formulated using gPROMS modelling tool to optimise some of the design and operating parameters (such as reaction temperature, residence time and splitter ratio) of integrated process while minimising an objective function which is a coupled function of capital and operating costs involving design and operating parameters. Two cases are studied: where (i) HGO and catalyst are fed as one feed stream and (ii) HGO and catalyst are treated as two feed streams. A liquid-liquid extraction model is then developed for the extraction of sulphur compounds from the oxidised heavy gas oil. With the experimentally determined KP multi stage liquid-liquid extraction process is modelled using gPROMS software and the process is simulated for three different solvents at different oil/solvent ratios to select the best solvent, and to obtain the best heavy gas oil to solvent ratio and number of extraction stages to reduce the sulphur content to less than 10 ppm. Finally, an integrated oxidation and extraction steps of ODS process is developed based on the batch experiments and modelling. The recovery of oxidant, catalyst and solvent are considered and preliminary economic analysis for the integrated ODS process is presented.

A thesis in fulfilment of the requirements for the Master of Technology: Radiography, Durban University of Technology, 2006. / The study will determine the sulphur dioxide (SO2) levels in the x-ray department and evaluate it’s effects on the health of the radiology workers. The aim of the study is to mainly create awareness of occupational hazards posed by processing chemistry to radiology workers. / M

During recent decades many lakes have become browner in the northern hemisphere and more specific in Sweden. This process is called brownification. Brownification of lakes makes it more difficult to clean water to drinking water and may have negative ecological effects on biota. Browning of lakes is generally thought to be caused by an increase of humic substances that consist of organic matter which colour the water brown or yellow. However, more recent studies show that dissolved iron can interact with humic substances in browning lakes. Since the concentrations of dissolved iron have increased during recent years and the mechanisms behind brownification and the contribution of iron to this process is not clearly understood it is important to investigate this subject. In this study 17 lakes in south of Sweden were sampled for iron concentration, dissolved organic carbon (DOC), absorbance (420nm) and pH. Further, data was added about atmospheric sulphur deposition and additional data from 17 lakes in the north part of Sweden. Iron had a stronger significant correlation towards absorbance than DOC had in the south of Sweden. A similar amount of dissolved iron seems to colour lakes differently based on their location in Sweden. This indicates that different mechanisms are involved in the interaction between iron and absorbance. However, pH had a stronger relationship with absorbance than either DOC or iron. Overall results suggested that iron do have a strong browning effect on Swedish fresh water lakes in the presence of DOC and that iron-increase driven processes may be due to a change of pH.

A remoção de compostos sulfurosos (sulfeto/sulfato) de águas residuárias tem grande importância para a saúde humana e para o ambiente. A biorremediação desses compostos, através da utilização de bactérias fototróficas anoxigênicas apresenta-se como alternativa viável ecológica e economicamente. Neste projeto de pesquisa realizaram-se ensaios em reatores em batelada expostos à iluminação fluorescente, com a finalidade de avaliar a utilização de sulfeto por cultura enriquecida de sulfubactérias fototróficas verdes, proveniente de sedimento de lagoa de estabilização. A avaliação da utilização de sulfeto e os resultados da cinética de crescimento da cultura visam a possibilidade de aplicação das bactérias fototróficas anoxigênicas no tratamento de águas residuárias. Na avaliação cinética de crescimento da cultura enriquecida de sulfubactérias fototróficas verdes foi verificado diminuição na velocidade de crescimento de 0,0346 h-1 para 0,0035 h-1 com o aumento da concentração inicial de sulfeto de 11,4 para 529,6 mg-S/L, respectivamente. O tempo de geração apresentou comportamento crescente com valores iguais a 19,98 h e 119,18 h, respectivamente. Os valores do coeficiente de conversão de sulfeto relativo ao crescimento de microrganismos (Yx/s), apresentaram diminuição progressiva com o aumento da concentração inicial de sulfeto, sendo esta queda mais acentuada no intervalo de concentrações de 40,5 a 147,2 mg-S/L. / The removal of sulphur compounds (sulfide/sulfate) from wastewaters is very important for human and for the environmental. The bioremediation of these compounds, applying anoxigenic phototrophic bacteria has been presented as a possible alternative. The aim of this work is to evaluate the utilization of sulfide by the enrichment of green sulphur bacteria proceeding from stabilization pond sediment, through the realization of batch reactors assays, which are exposed to fluorescent ilumination. The determination of the sulfide utilization and the results of the kinetic growth were done to clarify the possibility of the application of anoxigenic phototrophic bacteria in the wasterwater systems. In kinetic experiments it was observed that the specific rate of bacterial growth changed from 0.0346 h-1 to 0.0035 h-1. Then the initial sulfide concentration was increased form 11.4 mg-S/L to 529.6 mg-L. The doubling time showed an increase from 19.98 h to 119.18 h. The sulfide conversion to microorganism biomass (Yx/s) progressively decrease with the increase of sulfide concentration. Such a decrease was higher in between sulfide concentrations of 40.5 mg-S/L to 147.2 mg-S/L.

A baixa disponibilidade de nutrientes na exploração da pastagem é um dos principais fatores que interfere tanto na produtividade como na qualidade da forrageira. O presente trabalho objetivou avaliar os efeitos de combinações de doses de nitrogênio com doses de enxofre para a Brachiaria brizantha cv. Marandu, cultivada em solução nutritiva, utilizando sílica como substrato, em um experimento conduzido em casa-de-vegetação, em Piracicaba-SP, no período de setembro a dezembro de 2001. Utilizou-se um esquema fatorial 5 2 fracionado, com 13 combinações assim definidas, para nitrogênio e enxofre na solução nutritiva: 14 e 3,2; 14 e 32; 14 e 80; 126 e 12,8; 126 e 64; 210 e 3,2; 210 e 32; 210 e 80; 336 e 12,8; 336 e 64; 462 e 3,2; 462 e 32 e 462 e 80 mg L -1 , as quais foram distribuídas segundo delineamento estatístico de blocos ao acaso, com quatro repetições. Foram realizados dois cortes nas plantas, ocasiões em que se separou a parte aérea em folhas emergentes, lâminas de folhas recém-expandidas, lâminas de folhas maduras e colmos mais bainhas. Após o segundo corte as raízes foram separadas do substrato e tiveram o comprimento e a superfície avaliados. Os resultados demonstraram que a interação entre as doses de nitrogênio e enxofre foi significativa para o número total de perfilhos, o número total de folhas expandidas, o teor de clorofila, a área foliar, a produção de massa seca da parte aérea, a concentração de nitrogênio em folhas emergentes e nas raízes, a concentração de enxofre e a relação N:S em folhas emergentes, lâminas de folhas recém-expandidas e lâminas de folhas maduras em um ou ambos os cortes. Para a atividade da redutase do nitrato não foi observada significância quer para a interação entre as doses de nitrogênio e enxofre, quer para as doses individuais de nitrogênio e enxofre. A máxima concentração de nitrogênio (31,6 g kg -1 ) nos componentes do capim foi observada nas folhas emergentes na dose de nitrogênio de 462 mg L -1 por ocasião do primeiro corte. Para o enxofre a máxima concentração (2,8 g kg -1 ) foi observada nos colmos+bainhas na dose de nitrogênio de 14 mg L -1 , à época do segundo corte. A relação N:S nas lâminas de folhas recém-expandidas variou de 2,8:1 a 37,2:1 sendo o mínimo observado com muito baixo suprimento de nitrogênio e o máximo dessa relação ocorrendo com fornecimento de alta dose de nitrogênio combinada com baixa disponibilidade de enxofre. É necessário suprir enxofre quando se incrementa a disponibilidade de nitrogênio para o capim-Marandu. / The low availability of nutrients in the exploration of the grassland is one of the main factors to interfere in grass productivity and quality. This experiment had the objectives of evaluating the effects of combinations of nitrogen and sulphur rates to Brachiaria brizantha cv. Marandu, grown in nutrient solution, using ground quartz as substrate. The experiment was carried out in a greenhouse located Piracicaba, São Paulo State from September to December of 2001. It was a incomplete factorial set in radomized blocks with four replications, and the 13 combinations of nitrogen and sulphur were: 14 and 3.2; 14 and 32; 14 and 80; 126 and 12.8; 126 and 64; 210 and 3.2; 210 and 32; 210 and 80; 336 and 12.8; 336 and 64; 462 and 3.2; 462 and 32; 462 and 80 mg L -1 . Forage grass was harvested twice and in each one plant tops were separated in emergent leaves, lamina of recently expanded leaves, lamina of mature leaves and culms plus sheaths. After the second harvest roots were taken from the substrate and had the lenght and surface determined. The results showed significant interaction between nitrogen and sulphur rates for the number of total tillers, number of total expanded leaves, chlorophyll concentration (SPAD), leaf area, plant tops dry weight, nitrogen concentration in emergent leaves and in the roots, and sulphur concentration and N:S ratio in emergent leaves, lamina of recently expanded leaves and in lamina of mature leaves in the Marandu grass at one or both harvests. Significant interaction between nitrogen and sulphur rates in the first harvest in the dry matter yield of the top parts. It was not significant either the interaction between nitrogen and sulphur rates or nitrogen and sulphur rate. Maximum nitrogen concentration (31.6 g kg -1) was found in emergent leaves at the nitrogen rate of 462 mg L -1, in the first harvest. Sulphur concentration was maximum in the culms plus sheaths (2.8 g kg -1) on nitrogen rate of 14 mg L -1 at the second harvest. The N:S ratio in the lamina of recently expanded leaves ranged from 2.8:1 to 37.2:1, with the minimum value observed with the very low nitrogen supply and the maximum with high nitrogen rate combined with low sulphur availability. There is a need of sulphur supply when nitrogen is made highly available to Marandu grass.

O nitrogênio tem sido indispensável na formação, manutenção e recuperação de pastagens e seu efeito tem mostrado ser dependente do suprimento de enxofre, pela relação desses nutrientes no metabolismo vegetal. Objetivou-se: a) estudar combinações de doses de nitrogênio e de enxofre em solo suportando capim-Braquiária (Brachiaria decumbens) em degradação; b) avaliar o efeito do nitrogênio e do enxofre na eficiência no uso de água pelo capim; c) caracterizar as formas de nitrogênio e de enxofre no solo, antes, durante e após as adubações desses nutrientes; d) determinar a influência das combinações desses nutrientes em características nutricionais e produtivas do capim em recuperação. Coletaram-se amostras com plantas + solo em cilindros de 15 cm de diâmetro e 20 cm de profundidade num Neossolo Quartzarênico de uma pastagem em degradação. Utilizaram-se cinco doses de nitrogênio (0; 100; 200; 300 e 400 mg dm-3) e cinco doses de enxofre (0; 10; 20; 30 e 40 mg dm-3), combinadas em estudo de superfície de resposta baseado em desenho experimental composto central modificado de um fatorial 52 fracionado. Realizaram-se três cortes nas plantas com intervalos regulares de 30 dias. O fornecimento simultâneo de nitrogênio e enxofre na adubação aumentou a área foliar e a produção de massa seca, o número de perfilhos e melhorou a eficiência no uso de água pelo capim. A adubação com nitrogênio teve efeito isolado para o número de perfilhos e produção de massa seca no segundo e no terceiro crescimentos. O número de folhas foi influenciado pelas doses de nitrogênio e de enxofre de forma isolada, no primeiro crescimento e pelas doses de nitrogênio no segundo e no terceiro crescimentos. As relações entre as doses de nitrogênio e as de enxofre para as máximas produções foram de maneira geral em torno de 10:1. A adubação nitrogenada resultou em aumento na produção de massa, o comprimento e a superfície das raízes. O valor SPAD dependeu da combinação de doses de nitrogênio e de enxofre apenas no primeiro crescimento e teve efeito do nitrogênio no segundo e no terceiro crescimentos. As concentrações de nitrogênio e de enxofre no capim atingiram máximos valores nas doses mais elevadas. A baixa relação N:S de 7:1 no capim na não aplicação de nitrogênio indicou maior demanda de nitrogênio do que de enxofre. A interação entre as doses de nitrogênio e de enxofre não foi significativa para as características químicas avaliadas no solo. O pH do solo diminuiu quando o nitrogênio foi aplicado. A matéria orgânica no solo não variou após três períodos de crescimento do capim. A adubação com nitrato de amônio aumentou os teores de nitrogênio total, nitrogênio nítrico e nitrogênio amoniacal no solo. O teor de nitrogênio na forma amoniacal foi superior ao da forma nítrica no solo. A adubação com sulfato de cálcio aumentou os teores de enxofre total e de enxofre sulfato no solo. A aplicação principalmente de nitrogênio, mas também de enxofre, influenciou o estádio nutricional do capim-Braquiária e conseqüentemente a sua recuperação. / Nitrogen is required for pastures establishment, maintenance and production recovery, and its effect has depended on sulphur supply, for the relationship between these nutrients in plant metabolism. The objectives were: a) to study the combinations between nitrogen and sulphur rates in soil with Signal grass (Brachiaria decumbens) under degradation; b) to evaluate the effect of nitrogen and sulphur on the water use efficiency by grass; c) to determine the nitrogen and sulphur in the soil, before, in the course of the combinations between these nutrients on productive and nutritional characteristics of the recovering grass. Samples of plants plus soil were collected in cylinders of 15 cm diameter and 20 cm depth from an Entisol with a degrading pasture. Five rates of nitrogen (0; 100; 200; 300 and 400 mg dm-3) were combined with five rates of sulphur (0; 10; 20; 30 and 40 mg dm-3) in a response surface methodology based on a central composite design modified from a fractional 52 factorial. Three harvests were done after each 30 days of plants growth. The supply of nitrogen and sulphur together increased Signal grass leaf area, dry matter yield, number of tillers and improved the water use efficiency by the grass. Nitrogen rates had effects on the number of tillers and dry matter yield at the second and third harvests of the grass. The number of leaves was changed by both nitrogen and sulphur rates at the first growth, and by nitrogen rates at the second and third growths. Maximum dry matter yields were attained when nitrogen and sulphur rates were at about 10:1 ratio. Nitrogen supply affected grass roots by increasing roots dry weight, length and surface. SPAD values changed with combined rates of nitrogen and sulphur at the first growth, and with nitrogen rates at the second and third growths. Nitrogen and sulphur concentrations were at maximum when maximum rates of these nutrients were applied. The low 7:1 N:S ratio in the grass with no nitrogen supply suggested higher demand for nitrogen than sulphur. The interaction between nitrogen and sulphur rates was not significant for the evaluated soil chemical parameters. Soil pH decreased when nitrogen was applied. Soil organic matter content did not change after the growth periods of the grass. Ammonium nitrate supply resulted in increases in total nitrogen, nitrate and ammonium in the soil. Ammonium concentration in the soil was higher than nitrate. Calcium sulphate application resulted in increases in total sulphur and sulphate-sulphur in the soil. The application of mainly nitrogen, but also of sulphur, affected the nutritional status of Signal grass, and its recovery.