Die steigende Anzahl an Verfahren, in denen eine Filtration und eine Aufreinigung des gebildeten Filterkuchens durch Waschung notwendig ist, und die Steigerung deren Effizienz und Wirtschaftlichkeit verlangen nach einer Optimierung der Prozesse. Die Erarbeitung eines grundlegenden Verständnisses der Verdrängungsprozesse zwischen polaren und unpolaren Flüssigkeiten in einem Haufwerk schafft Erkenntnisse, die bei der Auswahl der verwendeten Lösungsmittel/Feststoffkombinationen während des Syntheseweges hilfreich sind. Durch die Verwendung von Silanen als Beschichtung kann die Oberflächeneigenschaft der Partikel variiert werden, während granulometrische Eigenschaften konstant bleiben. So dienen die Partikelsysteme als Basis der Untersuchungen zum Einfluss der Benetzungseigenschaften auf die Waschung unter Ausschluss anderer prozessbestimmender Variablen. Bei der Waschung der Partikelsysteme muss die Bedeutung der sich ausbildenden Phasengrenze herausgestellt werden. Sind Wasch- und Porenflüssigkeit nicht mischbar, bestimmt die auftretende Flüssig/Flüssig-Phasengrenze die Phänomenologie und die Effizienz des Prozesses. Das Auftreten einer Phasengrenze zwischen beiden Flüssigkeiten erlaubt die Aufnahme einer Flüssig/Flüssig-Kapillardruckkurve, die als Grenzkurve die zu erwartenden technischen Waschergebnisse darstellt. So kann eine Aussage darüber getroffen werden, welche Austauschverhältnisse und Restgehalte an Verunreinigung im Kuchen bei der Auswaschung mit nichtmischbaren Flüssigkeiten maximal zu erwarten ist.:ABBILDUNGSVERZEICHNIS SYMBOLVERZEICHNIS 1 EINLEITUNG 2 GRUNDLAGEN 2.1 FILTRATION 2.1.1 Kuchenbildung 2.1.2 Entfeuchtung 2.2 FILTERKUCHENWASCHUNG 2.3 SYSTEMEIGENSCHAFTEN 2.3.1 Feststoffe 2.3.2 Flüssigkeiten 2.3.3 Suspension 2.3.4 Haufwerk- und Kuchenstruktur 2.4 GRENZFLÄCHEN UND BENETZUNG DISPERSER SYSTEME 2.4.1 Oberflächenenergie 2.4.2 Benetzung 2.4.3 Kapillarität 2.5 BENETZUNG UND KAPILLARITÄT IN BEZUG ZUR FILTRATION 2.5.1 Die Kapillardruckkurve 2.5.2 Zusammenspiel von Benetzung und Filtration 2.5.3 Die Umnetzungskurve 2.6 SILANE – AUFBAU UND FUNKTION 3 MATERIALIEN UND METHODEN 3.1 STOFFSYSTEME 3.1.1 Partikelsystem 3.1.2 Flüssigkeiten 3.1.3 Silane 3.2 SILANISIERUNG ZUR VARIATION ZUR BENETZUNG 3.3 FESTSTOFFCHARAKTERISIERUNG 3.3.1 Laserbeugung 3.3.2 Statische Bildanalyse 3.3.3 Rasterelektronenmikroskopie 3.3.4 Energiedispersive Röntgenspektroskopie 3.3.5 Stickstoffadsorption 3.3.6 Thermogravimetrische Analyse 3.3.7 Ellipsometrie 3.3.8 Goniometrie 3.4 PROZESSRELEVANTE FLUID- UND SUSPENSIONSCHARAKTERISIERUNG 3.4.1 Tensiometrie 3.4.2 Grenzflächenrheometrie 3.4.3 Sedimentations- und Kompressionsmessung 3.5 VERSUCHSDURCHFÜHRUNG 3.5.1 Filtration 3.5.2 Waschung 3.5.3 Bestimmung Filtrat- und Retentatkonzentration 3.5.4 Kapillardruckkurve 3.5.5 Umnetzungskurve 4 OBERFLÄCHENKONFIGURATION DER PARTIKELSYSTEME MITTELS SILANEN 4.1 VARIATION DER OBERFLÄCHENENERGIE 4.2 AUSBILDUNG DER SILANSCHICHT 4.3 KONSISTENZ DER DISPERSEN FESTSTOFFEIGENSCHAFTEN 5 BENETZUNGSEFFEKTE BEI DER WASCHUNG VON FILTERKUCHEN 5.1 STRUKTURBILDUNG BEI DER FILTRATION 5.1.1 Sedimentationseigenschaften 5.1.2 Filterkuchenbildung 5.2 KUCHENWASCHUNG 5.2.1 Kuchenwaschung mit mischbaren Systemen 5.2.2 Kuchenwaschung mit nichtmischbaren Systemen 5.2.3 Viskositätsdifferenz 5.2.4 Nachweis der aufgestellten Theorien 6 DARSTELLUNG DES WASCHUNGSGLEICHGEWICHTES ÜBER EINE UMNETZUNGSKURVE 6.1 MESSTECHNISCHE ERFASSUNG 6.1.1 Technische Methode 6.1.2 Druckmethode 6.2 HAUPTEINFLUSSPARAMETER AUF DIE UMNETZUNGSKURVE 6.2.1 Variation der Benetzung 6.2.2 Variation der Partikelform 6.2.3 Variation der Partikelgröße 6.3 VERGLEICH: UMNETZUNGS- UND KAPILLARDRUCKKURVEN 7 SCHLUSSWORT LITERATURVERZEICHNIS ANHANG

Gegenstand dieser Arbeit ist die Entwicklung und Untersuchung eines Aufbereitungsprozesses zur Gewinnung von Bitumen aus kanadischem Athabasca Ölsand, der im Tagebau gewonnen wurde. Es wird ein mechanisch-thermisches Verfahren zur Fest-Flüssig-Trennung eingesetzt. Dabei handelt es sich um vier Schritte: (1) Suspendierung des Ölsandes mit den organischen Lösungsmitteln, Toluol und n-Heptan, (2) Filterkuchenbildung, (3) Waschung des Filterkuchens mit Wechsel der Waschflüssigkeiten (gradierte Waschung) und (4) Dampfbeaufschlagung. Der Prozess stellt eine Alternative zur herkömmlichen Heißwasser-extraktion des Ölsandes dar. Die Nachteile der Heißwasserextraktion sind ökologische Probleme, ein hoher Energie- und Frischwasserbedarf. Die Ziele des Alternativprozesses sind die Minimierung des Wasser- und Energiebedarfs, Vermeidung schädlicher Abfallstoffe sowie die Maximierung der Bitumenausbeute. Als Produkte sollen feststofffreies Bitumen und rückstandsfreier, deponierbarer Feststoff gewonnen werden.

Gegenstand dieser Arbeit ist die Entwicklung und Untersuchung eines Aufbereitungsprozesses zur Gewinnung von Bitumen aus kanadischem Athabasca Ölsand, der im Tagebau gewonnen wurde. Es wird ein mechanisch-thermisches Verfahren zur Fest-Flüssig-Trennung eingesetzt. Dabei handelt es sich um vier Schritte: (1) Suspendierung des Ölsandes mit den organischen Lösungsmitteln, Toluol und n-Heptan, (2) Filterkuchenbildung, (3) Waschung des Filterkuchens mit Wechsel der Waschflüssigkeiten (gradierte Waschung) und (4) Dampfbeaufschlagung. Der Prozess stellt eine Alternative zur herkömmlichen Heißwasser-extraktion des Ölsandes dar. Die Nachteile der Heißwasserextraktion sind ökologische Probleme, ein hoher Energie- und Frischwasserbedarf. Die Ziele des Alternativprozesses sind die Minimierung des Wasser- und Energiebedarfs, Vermeidung schädlicher Abfallstoffe sowie die Maximierung der Bitumenausbeute. Als Produkte sollen feststofffreies Bitumen und rückstandsfreier, deponierbarer Feststoff gewonnen werden.

Made available in DSpace on 2016-06-02T18:57:46Z (GMT). No. of bitstreams: 1 5305.pdf: 946081 bytes, checksum: 81e4f5bc1df570d2fc2c0af3a06d0f34 (MD5) Previous issue date: 2012-09-21 / Financiadora de Estudos e Projetos / The agro-industrial residues have great potential for providing silicon (Si) and other nutrients for crops. The objective of this work to assess the supply of silicon for organic waste agribusiness, and to evaluate the influence of this nutrient in the accumulation of nitrogen (N), phosphorus (P), potassium (K), calcium (Ca), magnesium (Mg ) and sulfur (S) in maize. We analyzed the accumulation of silicon in the leaves and stems of the plant and the effect of these sources in stem diameter, the height and mass of dry corn plant, as well as the accumulation of N, P, K, Ca, Mg and S in corn leaves provided by agro-industrial residues and by levels of silicon used. The experiment was conducted in a greenhouse in a completely randomized design (4x3) + 1. We evaluated three sources organic agribusiness (bagasse ash from sugar cane filter cake rotary sugarcane and rice hulls), and for the supply of silicon also evaluated the mineral source (calcium silicate PA); three strengths of SiO2 (175 kg ha-1, 350 kg ha-1 and 700 kg ha-1) and additional treatment (control), which received no SiO2. The sources and doses of SiO2 did not affect the mass of dried corn plants. However, the addition of SiO2 dose provided an increase in the diameter of stem of the maize plant. The rice hulls was more efficient among all treatments in Si supply to the corn crop. The supply of Si favors the absorption and consequent accumulation of potassium and phosphorus from the corn plant. There was no relationship between the supply of Si and Mg and S uptake by corn plant. Finally, there was no relationship between the accumulation of Si and the reduction of leaf N in corn plants. / Os resíduos agroindustriais possuem elevado potencial para fornecimento de silício (Si) e outros nutrientes para as culturas agrícolas. Objetivou-se, com esse trabalho, avaliar o fornecimento de silício por resíduos orgânicos agroindustriais, e avaliar a influência desse nutriente no acúmulo de nitrogênio (N), fósforo (P), potássio (K), cálcio (Ca), magnésio (Mg) e enxofre(S) na planta de milho. Foi analisado o acúmulo de silício nas folhas e nos colmos da planta e o efeito dessas fontes no diâmetro do colmo, na altura e na massa da planta de milho seca, assim como o acúmulo de N, P, K, Ca, Mg e S nas folhas de milho proporcionado pelos resíduos agroindustriais e pelas doses de silício utilizadas. O experimento foi instalado em casa de vegetação no delineamento experimental inteiramente casualizado (4x3) + 1. Foram avaliadas três fontes orgânicas agroindustriais (cinza de bagaço de cana-de-açúcar, torta de filtro rotativo de cana-de-açúcar e casca-de-arroz carbonizada), e para o fornecimento de silício também avaliou-se a fonte mineral (silicato de cálcio P.A.); três dosagens de SiO2(175 Kg ha-1, 350 Kg ha-1 e 700 Kg ha1) e o tratamento adicional (testemunha), o qual não recebeu SiO2. As fontes e doses de SiO2 não influenciaram a massa das plantas secas de milho. Entretanto, o acréscimo das doses de SiO2 proporcionou o aumento no diâmetro de colmo da planta de milho. A casca-de-arroz carbonizada mostrou-se mais eficiente entre todos os tratamentos no fornecimento de Si para a cultura do milho. O fornecimento de Si favoreceu a absorção e consequente acúmulo de P e K pela planta de milho. Não se observou relação entre o fornecimento de Si e a absorção de Mg e S pela planta de milho. Por fim, não houve relação entre o acúmulo de Si e a redução do N foliar nas plantas de milho.

Orientadores: Maria Angela de Almeida Meireles, Carlos Eduardo Vaz Rossell / Dissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia de Alimentos / Made available in DSpace on 2018-08-06T15:36:00Z (GMT). No. of bitstreams: 1 Shintaku_Alberto_M.pdf: 7098448 bytes, checksum: b538eba167ccbd49382fabb569cc75ee (MD5) Previous issue date: 2006 / Resumo: Neste trabalho estimou-se o custo de obtenção de extratos de cera, por extração supercrítica, a partir do resíduo da industria de açúcar e álcool, a torta de filtro. Foram realizados ensaios para determinação das isotermas de rendimento global, as curvas globais de extração (cinéticas de extração) e a identificação da composição química dos extratos obtidos. Na determinação da isoterma de rendimento global foram estudadas as pressões no intervalo de 100 a 350 bar com variações de 50 bar para as temperaturas de 30 e 50 ºC inicialmente para a matéria prima A. A quantidade utilizada de matéria prima (matéria prima A) foi de 2,5 gramas e uma vazão de CO2 de 0,249 ± 0,002 kg/h. Todos os ensaios foram realizados em duplicata e o tempo de extração de 60 min.. Para obtenção das curvas globais de extração foram utilizadas matérias primas distintas provenientes de 3 regiões do estado de São Paulo (matérias primas A, B e C). A temperatura de 50 ºC foi escolhida inicialmente para a matéria prima A, com as pressões de 200 bar e 350 bar respectivamente. Em seguida foi utilizado o binômio: temperatura e pressão, de 60 ºC e 200 bar para a matéria prima A, B e C sendo a temperatura escolhida pela característica do extrato de alta viscosidade (sólido à temperatura ambiente). A quantidade de matéria prima utilizada em cada ensaio foi de 25 gramas, uma vazão de 0,249 ± 0,003 kg/h de CO2, que fornece uma relação de 15 kg de CO2/kg de matéria prima. O tempo de extração utilizado para cada ensaio foi de 360 minutos. A partir do rendimento de extração, do tempo de extração do período CER (Constant Extraction Rate) e das características físicas da matéria prima (densidade, porosidade, etc.), foi estimada a capacidade dos extratores tomando-se o cuidado de dimensionar um extrator compatível com a capacidade de extratores comerciais existentes. Esta estimativa de capacidade permitiu a obtenção do custo do produto, a partir de uma análise econômica. A análise de sensibilidade do custo de produção para variações no custo de investimento, custo de insumos, custo de energia, custo de mão de obra e rendimento de extração, mostrou que o mesmo é influenciado principalmente pela variação no custo de investimento e pela variação do rendimento de extração. O custo de produção do extrato de cera foi estimado em US$ 13.626,93/tonelada / Abstract: The purpose of this work was to determine the manufacturing cost for the wax extract obtained from residues of the sugar cane and ethanol industry (filter cake), using SFE (Supercritical Fluid Extraction). Experiments were accomplished to determine the global yield isotherms, the overall extraction curves (kinetic of extraction) and to identification chemical composition of the extracts. The global yield isotherms were determined at the pressures of 100, 150, 200, 250, 300 and 350 bar and temperatures of 50 ºC and 30 ºC The amount of raw material (raw material A) used in each trial was 2.5 grams and a CO2 flowrate of 0.249 ± 0.002 kg/h. The experiments were duplicated. In order to determine the overall extraction curves (OEC), distinct raw materials were used from three different regions of São Paulo State (raw materials A, B and C). The OEC for the raw material A was initially determined at 50 ºC, with 200 bar and 350 bar of pressure respectively. In spite of 50 ºC be chosen initially, the experiments were accomplished in the SFE (Supercritical Fluid Extraction) equipment at 60 ºC and 200 bar for the raw material A, B and C being the temperature chosen due to characteristics of extract high viscosity (solid state at the ambient or room temperature). A 25 grams raw material sample was used in each trial with an outflow of 0,249 ± 0,003 kg/h of CO2 (a relation of 15 kg of CO2/kg of raw material). The extractors capacity was estimated from the extraction yield, the extraction time of Constant Extraction Rate period (CER) and the physical characteristics of the raw material (density, porosity, etc.). Extractors sizing considered the compatibility with existent extractors commercial capacity. This capacity estimation allowed the attainment of the product cost, from an economic analysis where investment cost, equipment cost, cost of operating labor, cost of operating supplies, etc. have been determined, composing the total extraction cost. The cost sensitivity was analyzed for variations in the investment cost, cost of operating supplies, energy cost, cost of operating labor and extraction income, showing that the production cost is influenced mainly by the variation in the investment cost and by the variation of the extraction yield. The determined wax extract obtaining cost, with SFE technology, was US$ 13,626.93/ton except for taxes / Mestrado / Mestre em Engenharia de Alimentos

Die Durchströmungswäsche von Filterkuchen aus innenporösen Partikeln wird anhand von makro- und mesoporösen Kieselgelen untersucht. Die Filterkuchenbildung der KCl-haltigen Suspensionen erfolgt in einer Drucknutsche nach VDI-2762-2. Die Filterkuchen werden über einen perforierten Stempel mit entionisiertem Wasser durchströmt und der Wascherfolg über die Bilanzierung der K+-Ionen ermittelt. Die Porosität der Kieselgel-Filterkuchen beträgt 80 %, wobei sich 50 % der gesamten Mutterlauge in den Innenporen befindet. Dennoch zeigen sich mit 1 % Restbeladung ähnliche Waschergebnisse wie für unporöse Feststoffe (Quarz und Glas). Die Innenporen werden gereinigt, der in der Literatur postulierte ausgeprägte Diffusionsbereich in der Waschkurve wird nicht sichtbar. Berechnungen nach CARMAN-KOZENY, FICK und mittels dimensionsloser Kennzahlen verdeutlichen, dass Perfusion und Diffusion die Wäsche poröser Systeme beeinflussen. Die vorgestellten Modelle eignen sich auch für die Anwendung in der Praxis. / The displacement washing of filter cakes consisting of porous particles is investigated using macro- and mesoporous silica gels. The filter cakes of KCl-containing suspensions are formed in a pressure filter device according to VDI-2762-2. The filter cakes are flown through with deionized water via a perforated piston and the washing success is determined by balancing the K+ ions. The porosity of the silica gel filter cakes is 80 % and 50 % of the mother liquor is trapped in the inner pores. Nevertheless, with 1 % residual loading, washing results are similar to those for non-porous solids (quartz, glass). The inner pores are cleaned, the distinct diffusion region in the washing curve postulated in the literature is not visible. Calculations according to CARMAN-KOZENY, FICK and by means of dimensionless quantities illustrate that both perfusion and diffusion influence the washing of porous systems. The presented models are also suitable for practical applications.

Reliable information about the micro-processes during filtration and dewatering of filter cakes allows more accurate statements about process development and design in any industrial application with solid-liquid separation units. Distributed particle properties such as shape, size, and material influence the formation of the porous network structure, which can show considerable local fluctuations in vertical and horizontal alignment in the cake forming apparatus. The present work relates to a wide range of particle sizes and particle shapes and presents their effects on integral, but preferably local, structural parameters of cake filtration. Current models for the relationship between particle properties and resulting porous structure remain inaccurate. Therefore, the central question focus on the model-based correlation between obtained tomographic 3D information and characteristic cake and process parameters. In combination with X-ray computed tomography and microscopy (ZEISS Xradia 510), data acquisition of the structural build-up of filter cakes is possible on a small scale (filter area 0.2 cm²) and a conventional laboratory scale (filter area 20 cm², VDI 2762 pressure nutsch). Thereby, the work focuses on structural parameters at the local level before, during, and after cake dewatering, such as porosity, coordination number, three-phase contact angle, characteristics of pores and isolated liquid regions, the liquid load of individual particles, tortuosity, and capillary length, and the corresponding spatial distributions. Seven different particle systems in the range of 20 and 500 µm, suspended in aqueous solutions with additives for contrast enhancement, served as raw materials for the filter cake formation. Image data processing from 16-bit greyscale images with a resolution of 2 to 4 µm/voxel edge length includes various operations with a two-stage segmentation to identify air, solid particles, and liquid phase, resulting in a machine learning-based automated approach. Subsequent modeling and correlation of measured parameters rely on experimentally verified quantities from mercury porosimetry, laser diffraction, dynamic image analysis, static and dynamic droplet contour analysis, as well as filtration and capillary pressure tests according to VDI guidelines. The tomography measurements provide microscopic information about the porous system, quantified using characteristic key parameters and distribution functions. By studying the cake structure concerning the local distribution of particle size and shape and the resulting porosity, segregation effects can be avoided by increasing the feed concentration of particles, whereby swarm inhibition of particles in the initial suspension strongly hinders or completely suppresses layer formation in the cake according to distributed particle properties (Publication A). In the subsequent dewatering of the filter cake to the irreducible saturation, the measurement of the local coordination number as well as the remaining liquid volumes at the particle contacts allows the determination of a discrete liquid load distribution by correlation with the respective particle volume (Publication B). The determination of the capillary length - shortest capillary for single-phase pore flow and capillary of least resistance for multiphase pore flow - provides modeling approaches for the cake formation from publication A as well as the dewatering process from publication B (Publication C). The parameter sets obtained also help to transfer and extend existing, theoretical models of multiphase pore flow to the application example of filter cake dewatering (Publication D). At the microscopic level, the measurement of the three-phase contact angle at isolated liquid volumes within the porous matrix provides a deeper understanding of the macroscopic models from publications C and D (Publication E).:List of Figures List of Tables Notation 1 Introduction 2 Multiphase Processes in Porous Media 2.1 Cake Filtration and Single Phase Porous Media Flow 2.2 Cake Dewatering 2.2.1 Particle Surface Wettability 2.2.2 Capillarity in Porous Media 2.2.3 Static Capillary Pressure 2.2.4 Dynamic Capillary Pressure 3 Acquisition of 3D Information of Porous Media 3.1 Absorption and Scattering of X-rays 3.2 X-ray Microscopy 3.2.1 Image Acquisition 3.2.2 Image Reconstruction 3.2.3 Image Quality and Artifacts 3.3 Image Post-Processing 3.3.1 Image Enhancement 3.3.2 Segmentation and Thresholding 3.3.3 Processing Binary Images 3.4 Image Measurement 4 Materials and Methods 4.1 The Solid Phase 4.2 The Liquid Phase 4.3 Suspension Stability 4.4 Experimental Design and Down-Scale for Tomography Measurements 4.5 Experimental Characterization of Filtration and Dewatering Properties 4.5.1 Cake Filtration 4.5.2 Cake Dewatering (Capillary Pressure Measurements) 5 Conclusion and Outlook Literature Publications A to E Appendix

粉体の微粒子化に伴い，固液分離操作の中でも高精度かつ多量処理が可能なろ過の重要性はますます高まっている．しかしながら，微粒子スラリーのろ過抵抗は非常に大きく，所望の処理能力を得られないことが多い．本論文では，ろ過操作設計におけるろ材抵抗，スラリー凝集・分散状態，ケークろ過抵抗の予測に関して数値シミュレーションを利用した検討を行うことで，微粒子スラリーのろ過抵抗の低減に有用な知見を得ることができた． / 著者名の「吉」は「土」の下に「口」の置き換え / 博士(工学) / Doctor of Philosophy in Engineering / 同志社大学 / Doshisha University

Em face ao bom desempenho da agricultura brasileira, cresce também a responsabilidade por uma produção sustentável. Particularmente, o sistema produtivo da cana-de-açúcar vem se adaptando a uma produção sem queima, e busca formas alternativas de manejo dos resíduos da produção que sejam sustentáveis tanto economicamente, quanto ambientalmente. Neste trabalho apresentamos resultados dos tratamentos de solo agriculturável com resíduos de i) cinzas de bagaço de cana aplicado em cobertura e ii) torta de filtro na entrelinha da cultura, em diferentes doses. Avaliamos o impacto desses tratamentos no conteúdo de carbono e na matéria orgânica do solo. Para determinar se os tratamentos podem ser considerados sequestradores de carbono e ambientalmente sustentáveis nos detemos na preservação seletiva como mecanismo de retenção da matéria orgânica do solo, a qual leva a acumulação de componentes orgânicos químicos mais recalcitrantes. Utilizamos as técnicas espectroscópicas de fluorescência de luz UV-Visível, espectroscopia de fluorescência matriz excitação-emissão para avaliar a fração de ácido húmico do solo e o aumento da recalcitrância química, a fluorescência induzida por laser (FIL) para observar a matéria orgânica como um todo e a espectroscopia de emissão ótica com plasma induzido por laser (LIBS) utilizada como uma nova ferramenta para avaliar o conteúdo de carbono do solo. No tratamento de solo com adição de cinza de bagaço de cana tivemos potencial de estoque de carbono na dose 40 t/ha. Quanto a torta de filtro, o carbono total do solo aumenta menos significativamente que na cinza, mas não houve potencial de estoque de carbono. Na fração ácido húmico não observamos modificação do grau de humificação do solo com os tratamentos, mesmo a torta sendo um produto rico em matéria orgânica, porém houve um aumento de grupos carbonílicos, que estão associados ao aumento das interações intermoleculares favorecendo por exemplo a complexação do ácido húmico com metais. Nossos resultados de fluorescência induzida por laser apontam que a cinza possivelmente ofereceu melhora nas condições de crescimento da cultura havendo aumento de grupos alifáticos na MOS. Concluímos portanto, que não houve impacto negativo para o estoque de carbono no solo e qualidade da matéria sob tratamento de adição de cinza de bagaço de cana e torta de filtro. / Given the good performance of Brazilian agriculture, grows the responsibility for sustainable production. Particularly, the sugarcane production system has been adapting to a production without burning, and seeks alternative forms of waste management in production that are both economically and environmentally sustainable. We present results of arable soil treatments with i) sugarcane bagasse ash applied in coverage soil and ii) filter cake applied between the lines of culture in different doses. We assess the impact of these treatments on the content and quality of soil organic matter and carbon sequestration capacity. To determine if treatments can be considered environmentally sustainable and carbon sequestration we embrace the selective preservation as a retention mechanism of soil organic matter, which leads to accumulation of chemical organic compounds recalcitrant. We use bidimensional fluorescence UV-Visible spectroscopy and fluorescence excitation-emission matrix to assess the fraction of soil humic acid, the laser-induced fluorescence spectroscopy (LIF) for observing the whole organic matter and laser breakdown induced spectroscopy (LIBS) used as a new tool to assess the soil carbon content. The soil treatment with sugarcane bagasse ash had increased carbon stock in dose 40 t / ha. In humic acid fraction did not observe any change in the degree of humification treatment with AML, but there was an increase of carbonyl groups, which are associated with increased intermolecular interactions and enhancing the complexation of metals with humic acid. Our results suggest a possible improvement in crop growth conditions with an increase of aliphatic groups in MOS. The filter cake is no carbon content recorded, also did not observe any impact on soil organic matter with the incorporation of filter cake although this is a product rich in organic matter. In this context, we conclude that there was no negative impact on the carbon stock and quality of soil organic matter under treatment addition of sugarcane bagasse ash and filter cake.

Em face ao bom desempenho da agricultura brasileira, cresce também a responsabilidade por uma produção sustentável. Particularmente, o sistema produtivo da cana-de-açúcar vem se adaptando a uma produção sem queima, e busca formas alternativas de manejo dos resíduos da produção que sejam sustentáveis tanto economicamente, quanto ambientalmente. Neste trabalho apresentamos resultados dos tratamentos de solo agriculturável com resíduos de i) cinzas de bagaço de cana aplicado em cobertura e ii) torta de filtro na entrelinha da cultura, em diferentes doses. Avaliamos o impacto desses tratamentos no conteúdo de carbono e na matéria orgânica do solo. Para determinar se os tratamentos podem ser considerados sequestradores de carbono e ambientalmente sustentáveis nos detemos na preservação seletiva como mecanismo de retenção da matéria orgânica do solo, a qual leva a acumulação de componentes orgânicos químicos mais recalcitrantes. Utilizamos as técnicas espectroscópicas de fluorescência de luz UV-Visível, espectroscopia de fluorescência matriz excitação-emissão para avaliar a fração de ácido húmico do solo e o aumento da recalcitrância química, a fluorescência induzida por laser (FIL) para observar a matéria orgânica como um todo e a espectroscopia de emissão ótica com plasma induzido por laser (LIBS) utilizada como uma nova ferramenta para avaliar o conteúdo de carbono do solo. No tratamento de solo com adição de cinza de bagaço de cana tivemos potencial de estoque de carbono na dose 40 t/ha. Quanto a torta de filtro, o carbono total do solo aumenta menos significativamente que na cinza, mas não houve potencial de estoque de carbono. Na fração ácido húmico não observamos modificação do grau de humificação do solo com os tratamentos, mesmo a torta sendo um produto rico em matéria orgânica, porém houve um aumento de grupos carbonílicos, que estão associados ao aumento das interações intermoleculares favorecendo por exemplo a complexação do ácido húmico com metais. Nossos resultados de fluorescência induzida por laser apontam que a cinza possivelmente ofereceu melhora nas condições de crescimento da cultura havendo aumento de grupos alifáticos na MOS. Concluímos portanto, que não houve impacto negativo para o estoque de carbono no solo e qualidade da matéria sob tratamento de adição de cinza de bagaço de cana e torta de filtro. / Given the good performance of Brazilian agriculture, grows the responsibility for sustainable production. Particularly, the sugarcane production system has been adapting to a production without burning, and seeks alternative forms of waste management in production that are both economically and environmentally sustainable. We present results of arable soil treatments with i) sugarcane bagasse ash applied in coverage soil and ii) filter cake applied between the lines of culture in different doses. We assess the impact of these treatments on the content and quality of soil organic matter and carbon sequestration capacity. To determine if treatments can be considered environmentally sustainable and carbon sequestration we embrace the selective preservation as a retention mechanism of soil organic matter, which leads to accumulation of chemical organic compounds recalcitrant. We use bidimensional fluorescence UV-Visible spectroscopy and fluorescence excitation-emission matrix to assess the fraction of soil humic acid, the laser-induced fluorescence spectroscopy (LIF) for observing the whole organic matter and laser breakdown induced spectroscopy (LIBS) used as a new tool to assess the soil carbon content. The soil treatment with sugarcane bagasse ash had increased carbon stock in dose 40 t / ha. In humic acid fraction did not observe any change in the degree of humification treatment with AML, but there was an increase of carbonyl groups, which are associated with increased intermolecular interactions and enhancing the complexation of metals with humic acid. Our results suggest a possible improvement in crop growth conditions with an increase of aliphatic groups in MOS. The filter cake is no carbon content recorded, also did not observe any impact on soil organic matter with the incorporation of filter cake although this is a product rich in organic matter. In this context, we conclude that there was no negative impact on the carbon stock and quality of soil organic matter under treatment addition of sugarcane bagasse ash and filter cake.