The global oil refining industry with its present product distribution essentially shifted towards fuels such as gasoline and diesel will most likely hold the fort for considerable time. However, conditions are changing and refinery survival will very much depend on long-term planning, process and product flexibility and being at the frontiers of refining technology, a technology where catalysts play leading roles. Today oil refiners are faced with the challenge of producing fuels that meet increasingly tight environmental specifications, in particular with respect to maximum sulphur content. At the same time, the average quality of crude oil is becoming poorer with higher amounts of aromatics, heteroatoms (sulphur and nitrogen) and heavy metals. In order to stay competitive, it is of decisive importance for refiners to upgrade dense petroleum fractions of low quality to highly value-added products. A practicable route, for example, is upgrading the catalytic cracking by-product Light Cycle Oil (LCO) into a high-quality diesel-blending component in a two-step catalytic process. In the first step the LCO is hydrotreated over a Pt Pd based acidic catalyst bringing about heteroatom and aromatic reduction and isomerization of C6 to C5 naphthenic structures. In the second step these naphthenic structures are selectively opened over an Ir-based catalyst to improve the cetane value. The present thesis is mainly devoted to the second catalytic step of LCO upgrading and was partly conducted within the framework of the European Union project RESCATS. From the patent literature it is evident that iridium-based catalysts could be good candidates for ring-opening purposes. A literature survey covering ring opening of naphthenic structures made in the beginning of the project (in 2001), showed the need for extending investigations to heavier hydrocarbons, more representative of the diesel fraction than model compounds such as alkylated mono C5 and C6 naphthenic rings frequently employed in previous academic studies. Ring-opening catalysts, mainly Pt-Ir based, were synthesised at KTH by two different techniques: the microemulsion and the incipient wetness techniques. Paper I is a review of the microemulsion technique and its applications in heterogeneous catalysis. Characterization of catalysts was performed employing a multitude of techniques including quantitative TPR, TEM-EDX, XPS, CO FT-IR, NH3-DRIFTS and XRF etc. Catalytic screening at 325 oC and atmospheric pressure with hydrogen and pure indan as model substance was conducted to investigate ring-opening activity in terms of conversion and selectivity to desired cetane-boosting products. This development process is the topic of Papers II-IV. The possible industrial implementation of the best catalyst candidate is demonstrated in Paper V. When designing a catalytic system aimed at refining petroleum, it is crucial to monitor the evolution of the sulphur distribution throughout the different stages of the process so that catalyst properties and reaction parameters may be optimised. The final section of this thesis and Paper VI are devoted to high-resolution sulphur-distribution analysis by means of a sulphur chemiluminescence detector (SCD) following gas chromatographic separation. / QC 20101014

Made available in DSpace on 2016-06-02T19:55:36Z (GMT). No. of bitstreams: 1 5188.pdf: 6910424 bytes, checksum: 50b02c26311d2e058a7ac27b5419e05d (MD5) Previous issue date: 2011-06-08 / Environmental laws and stricter quality specifications have driven the development of technologies for improving the cetane number in diesel fuel. In addition to the saturation of (poly)aromatic compounds, responsible for limited gains, ring opening of at least one ring of (poly)cycloalkane, without loss of yield by cracking, is a promising strategy to maximize this property. Numerous studies have demonstrated the significant performance of Pt, Rh and Ir supported on zeolites for naphthenic ring opening in the hydroconversion of model compounds (naphthalene, tetralin and decalin). This study aimed to systematically assess the role of acid and hydrogenating functions for hydroconversion of decalin. It was also evaluated the effect of activation conditions (calcination and reduction), type of zeolite (Faujasite, FAU, or Beta, BEA), the content and type of metal (Pt, Ir or Rh). The influence of Pt-Ir and Pt-Rh bimetallic systems, as well as the inhibition by H2S, were studied in terms of the performance of these catalysts. For the catalytic precursors prepared, better activity and selectivity to ringopening products were obtained from calcination at 573 K and reduction at 713 K. This performance was consistent with a more homogeneous distribution of metallic particles on the support, and thus greater dispersion of the metallic phase. The reaction steps of ring contraction, ring opening and cracking were consecutive for the hydroconversion of decalin. It is noteworthy that the catalytic systems studied, under the operating conditions employed, yielded up to 45 mol% ring opening products and less than 15 mol% cracking products, at decalin conversions as high as 90 %. The Pt/BEA catalyst presented the best performance, thiotolerance (lower production of cracking products) and thioresistence (selectivity recovery after removal of H2S), followed by the Pt-It/BEA and Ir/BEA catalysts. This study allowed to highlight some peculiarities of the hydroconversion of decalin on noble metal/zeolite catalysts. Although decalin is a saturated molecule, his naphthenic character and probably the presence of a tertiary carbon in its structure, facilitates activation of the molecule directly on the strong acid sites of zeolite, even at relatively moderate temperatures. Thus, it is not necessary to form an olefin on a metal site and undergo subsequent protonation, as in a classical bifunctional mechanism, such as in hydroisomerization and hydrocracking of n-paraffins. However, the hydrogenation component of the catalyst influences the selectivity of the reaction, controlling the process of desorption/adsorption of any intermediate olefins formed. Greater hydrogenation activity implies lower availability of adsorbed carbocations that can be converted to cracking products. This proposition is consistent with the results obtained by varying the type and content of metal, support acidity and poisoning of the hydrogenation sites in the catalysts. / Legislações ambientais e especificações de qualidade mais restritivas têm impulsionado o desenvolvimento de tecnologias visando melhoria de cetano em óleo diesel. Adicionalmente à saturação de (poli)aromáticos, responsável por ganhos limitados, à abertura de pelo menos um anel do (poli)cicloalcano, sem perda de rendimento por craqueamento, consiste em estratégia potencial para maximização desta propriedade. Inúmeros trabalhos vêm demonstrando desempenho significante de catalisadores de Pt, Rh e Ir suportados em zeólitas para abertura de anel naftênico na hidroconversão de compostos-modelo (naftaleno, tetralina e decalina). O presente trabalho teve por objetivo avaliar sistematicamente o papel das funções ácidas e hidrogenantes para a hidroconversão de decalina. Foram abordados os efeitos das condições de ativação (calcinação e redução), do tipo de zeólita (Beta, BEA, ou Faujasita, FAU), do teor e do tipo de metal (Pt, Ir ou Rh). Também foi analisado o efeito de sistemas bimetálicos Pt-Ir e Pt-Rh, bem como a influência da inibição por H2S, no desempenho destes catalisadores. Para os precursores catalíticos preparados, melhores atividade e seletividade aos produtos de abertura de ciclo foram obtidas a partir da calcinação a 573 K e redução em 713 K. Este desempenho foi compatível com uma distribuição mais homogênea de partículas metálicas no suporte e, portanto, maior dispersão da fase metálica. As etapas reacionais de contração, abertura de ciclo e craqueamento são consecutivas para a hidroconversão de decalina. Destacam-se para os sistemas catalíticos estudados e condições operacionais empregadas, rendimentos de produtos de abertura de ciclo de até 45 %mol e craqueamento inferior a 15 %mol, obtidos para conversões de decalina tão elevadas quanto 90 %. O catalisador Pt/BEA apresentou melhores desempenho, tiotolerância (menor seletividade a craqueados na presença de H2S) e recuperação da seletividade após remoção do H2S, seguido pelo bimetálico de Pt-Ir/BEA e monometálico de Ir/BEA. O presente estudo permitiu colocar em evidência algumas peculiaridades da hidroconversão da decalina sobre catalisadores metal nobre/zeólita. Apesar de se tratar de uma molécula saturada, seu caráter naftênico e, provavelmente, a presença de um carbono terciário na sua estrutura, facilita a ativação da molécula diretamente sobre os sítios ácidos fortes da zeólita, mesmo em temperatura relativamente moderadas. Dessa forma, não necessita a formação de uma olefina num sítio metálico para posterior protonação, como num mecanismo bifuncional clássico de hidroisomerização e hidrocraqueamento de n-parafinas. A componente de hidrogenação do catalisador influencia, no entanto, a seletividade da reação, controlando o processo de dessorção/adsorção e hidrogenação das olefinas intermediárias formadas. Quanto maior a atividade hidrogenante, menor a disponibilidade de carbocátions adsorvidos que podem ser convertidos a produtos de craqueamento. Esta proposição é consistente com os resultados obtidos ao se variar o tipo e o teor de metal, a acidez do suporte e pelo envenenamento dos sítios de hidrogenação dos catalisadores.

Made available in DSpace on 2015-05-14T13:21:46Z (GMT). No. of bitstreams: 1 arquivototal.pdf: 1804420 bytes, checksum: 7f1229339fc39b87970bae7fb09a5054 (MD5) Previous issue date: 2009-11-30 / Coordenação de Aperfeiçoamento de Pessoal de Nível Superior - CAPES / The major purposes for the production and use of biodiesels are environmental, social and economic benefits. However the production of 90 cubic meters of biodiesel generates about 10 cubic meters of glycerin, so partial or total replacement of diesel by biodiesel can because of glycerin generate a lot of problems. A great surplus (without market), could force the devaluation of its price, and glycerin factories losing competitiveness might be forced to close down. However the world is in a race to develop new processes and add new technologies for the rational use of bio-fuel co-products like glycerin. This study obtained "New Materials" by using glycerin with applicability to biology, diesel fuels, and bio-fuels with cetane improvers. We obtained five organic nitrates characterized as 2-nitrate-1,3-diethoxypropane (NDM); 2-nitrate-1,3- dimethoxypropane (NDE); 2-nitrate-1,3-dipropoxypropano (NDP); 2-nitrate-1.3-dibutoxypropano (NDB) and (+/-)-2,2-dimethyl-1,3- dioxolan-4-metilnitrato (nitrate solketal - NSKT). pharmacological evaluation showed that the nitrates of diesters have hypotensive activity on the cardiovascular system revealing NDB as the compound that showed greater potency and effectiveness against the vasorelaxant effect in the superior mesenteric artery isolated from rats in the order of 115.58 ± 5.59. The nitrate solketal ((+/-)-2,2-dimethyl-1,3-dioxolan-4-metilnitrato) (NSKT) was tested as a cetane improver for biodiesel so as to obtain a new low cetane bio-fuel. The addition of NSKT 7% to ethanol, formed a low cetane fuel capable of operating diesel engines. / O grande propósito para a produção e o uso do biodiesel são os benefícios ambientais, sociais e econômicos. Entretanto na produção de 90 m3 de biodiesel são gerados cerca de 10 m3 de glicerina, assim com a substituição parcial ou total do diesel pelo biodiesel a glicerina gerada no processo pode ser um grande problema econômico e ambiental. Uma grande produção de glicerina provoca a desvalorização do produto e conseqüentemente fábricas que produzem ou a usam como insumo podem perder competitividade até não ser mais viável o seu funcionamento. Todavia o mundo busca o desenvolvimento de novos processos e agregar novas tecnologias visando o aproveitamento racional da glicerina. Neste trabalho foram obtidos Novos Materiais pelo aproveitamento da glicerina do biodiesel com aplicabilidades biológicas na síntese de moléculas bioativas e em combustíveis ou biocombustíveis com os melhoradores de Cetano. Assim foram obtidos cinco nitratos orgânicos: 2-nitrato-1,3- dimetoxipropano (NDM); 2-nitrato-1,3-dietoxipropano (NDE); 2-nitrato- 1,3-dipropoxipropano (NDP) e o 2-nitrato-1,3-dibutoxipropano (NDB). A avaliação farmacológica mostrou que os nitratos dos diéteres possuem atividade hipotensora sobre o sistema cardiovascular sendo NDB o composto que apresentou maior potencia e eficácia frente ao efeito vasorelaxante na arteria mesentérica superior isolada de rato na ordem de 115,58 ± 5,59. O Nitrato de solketal ((+/-)-2,2-Dimetil-1,3-dioxolano-4- metilnitrato) (NSKT) foi testado como melhorador de cetano tanto para o biodiesel como para a obtenção de um novo biocombustível de baixo cetano. A adição de NSKT no teor de 7% ao etanol formou um combustível de baixo cetano capaz de funcionar um motor do ciclo diesel.

Dans un contexte de recherche de nouveaux modes de combustion propres, la combustionhomogène à allumage par compression HCCI s’inscrit comme une stratégie prometteuse.Cependant, cette combustion est limitée par un niveau élevé de bruit. La recherche descarburants permettant de relaxer cette contrainte constitue l’objectif global de cette étude.Particulièrement, on s’intéresse ici à l’influence de l’Indice de Cétane, de la volatilité et de lacomposition chimique des carburants sur les Délais d’Auto-Inflammation et sur les vitesses decombustion globales évaluées par les taux maximaux d’accroissement de la pression et dudégagement d’énergie apparente. L’étude se base dans un premier temps sur l’analyse d’essaissur banc moteur dans lesquels on a testé plusieurs carburants de synthèse à l’état pur et enmélange avec un Gazole conventionnel. Dans un deuxième temps des essais ont été préparés etréalisés sur Machine à Compression Rapide avec deux configurations en injection directe et enmélange homogène. Les essais Moteur ont permis d’orienter les paramètres expérimentauxciblés sur ce dispositif. D’autre part, pour étudier les régimes de combustion, des mesures dechamps de température locale ont été réalisées en mélange inerte (N2, CO2, Ar) par FluorescenceInduite par Laser avec un traceur Toluène. L’étude montre les limites des paramètres habituelspour caractériser l’adéquation carburant combustion HCCI et propose un nouveau critère basésur la dépendance des délais d’auto-inflammation à la température et à la richesse. / Advanced combustion strategies such as Homogeneous Charge Compression Ignition (HCCI)usually enable cleaner combustion with less NOx and Particulate Matter emissions comparedto conventional Diesel combustion. However, these strategies are difficult to implement due todifficulties related to combustion timing and burn rate control. Lately various studies have beenfocusing on extending advanced combustion functioning with new technologies and withsearching fuels properties to enable such combustion modes. This study is focused on theimpact of fuel Cetane Number, volatility and chemical composition on Ignition Delay, HeatRelease Rate and Pressure Rise Rate. The study is based on three complementary experiments.First, several synthetic fuel was tested on a research engine and analysis was focused on theHeat Release Rate. Secondly, experiments on a Rapid Compression Machine were performedto study the auto-ignition phenomena at homogeneous conditions with surrogate fuels (blendsof n-Heptane and Methyl-Cyclohexane). Analysis of the combustion regimes was supported bya study of the temperature field based on a Toluene Laser Induced Fluorescence experiment ininert (N2, CO2, Ar) mixture. Finally, the RCM was adapted to allow direct injection of fuel tostudy the auto-ignition at less homogeneous conditions. Results showed the limits of theconventional fuels properties to describe an adequate fuel formulation for the HCCI combustionmode. A new criterion based on the dependency of ignition delays to temperature and air fuelratio variations is proposed.

The global oil refining industry with its present shift inproduct distribution towards fuels such as gasoline and dieselwill most likely hold the fort for many years to come. However,times will change and survival will very much depend onprocessing flexibility and being at the frontiers of refiningtechnology, a technology where catalysts play leading roles.Today oil refiners are faced with the challenge to producefuels that meet increasingly tight environmentalspecifications, in particular with respect to maximum sulphurcontent. At the same time, the quality of crude oil is becomingworse with higher amounts of polyaromatics, heteroatoms(sulphur and nitrogen) and heavy metals. In order to staycompetitive, it is desirable to upgrade dense streams withinthe refinery to value-added products. For example, upgradingthe fluid catalytic cracking (FCC) by-product light cycle oil(LCO) into a high quality diesel blending component is a veryattractive route and might involve a two-step catalyticprocess. In the first step the LCO is hydrotreated andheteroatoms are removed and polyaromatics are saturated, in thesecond step naphthenic rings are selectively opened to improvethe cetane number of the final product. The present research is devoted to the second catalytic stepof LCO upgrading and was carried out within the framework of aEuropean Union project entitled RESCATS. From the patent literature it is evident that iridium-basedcatalysts seem to be good candidates for ring-opening purposes.A literature survey covering ring opening of naphthenicmolecules shows the need for extending investigations toheavier model substances, more representative of the dieselfraction than model compounds such as alkylated mono C5 and C6-naphthenic rings frequently employed in academic studies. Ring-opening catalysts, mainly Pt-Ir based, were synthesisedat KTH by two different methods: the microemulsion and theincipient wetness methods. Characterization of the catalystswas performed using a number of techniques including TPR,TEM-EDX, AFM and XPS etc. Catalytic screening at atmosphericpressure using pure indan as model substance was utilized todetect ring-opening activity and the magnitude of selectivityto desired cetane-boosting products. The development of suchring-opening catalysts is the topic of Paper I. When designing a catalytic system aimed at refiningpetroleum, it is crucial to monitor the evolution of thesulphur distribution throughout the different stages of theprocess so that catalyst properties and reaction parameters canbe optimised. The final section of this thesis and Paper II arethus devoted to high-resolution sulphur distribution analysisby means of a sulphur chemiluminescence detector (SCD). Keywords:ring opening, naphthenes, cetane numberimprovement, indan, light cycle oil (LCO), Pt-Ir catalyst,catalyst characterization, aromatic sulphur compounds, GC-SCD,distribution, analysis.

Diesel fuel is composed of a complex mixture of hundreds of hydrocarbons that vary globally depending on crude oil sources, refining processes, legislative requirements and other factors. In order to simplify the study of this fuel, researchers create surrogate fuels with a much simpler composition, in an attempt to mimic and control the physical and chemical properties of Diesel fuel. The first surrogates were single-component fuels such as n-heptane and n-dodecane. Recent advancements have provided researchers the ability to develop multi-component surrogate fuels and apply them to both analytical and experimental studies. The systematic application of precisely controlled surrogate fuels promises to further enhance our understanding of Diesel combustion, efficiency, emissions and particulates and provide tools for investigating new and alternative engine combustion systems. This thesis employed analytical and experimental methods to develop, validate and study a library of multi-component surrogate Diesel fuels. The first step was to design a surrogate fuel to precisely match the physical and chemical properties of a full-range petroleum Diesel fuel with 50 cetane number and a typical threshold soot index value of 31. The next step was to create a Surrogate Fuel Library with 18 fuels that independently varied two key fuel properties: cetane number and threshold soot index. Within the fuel library cetane number ranged from 35 to 60 at three threshold soot index levels of 17, 31 and 48 (low, mid-range and high). Extensive ASTM fuel property tests showed that good agreement with important physical and chemical properties of petroleum Diesel fuel such as density, viscosity, heating value and distillation curve. An experimental investigation was conducted to evaluate the combustion, emissions, soot and exhaust particles from the petroleum Diesel fuel and the matching surrogate fuel. A fully-instrumented single-cylinder Diesel engine was operated with combustion strategies including Premixed Charge Compression Ignition (PCCI), Low-Temperature Combustion (LTC) and Conventional Diesel Combustion (CDC). For combustion, the ignition delay, low-temperature (first stage) and high temperature (second stage) heat-release matched very well. Gaseous emissions, soot and exhaust particles maintained good agreement as exhaust gas recirculation and combustion phasing were varied. This thesis demonstrated that fully representative Diesel surrogate fuels could be tailored with the proper blending of the following hydrocarbon components: n-hexadecane, 2,2,4,4,6,8,8-heptamethylnonane, decahydronaphthalene and 1-methylnaphthalene. It was also established that the volumetric blending fractions of these four components could be varied to independently control the fuel cetane number and threshold soot index while retaining the combustion, physical and chemical properties of full-range petroleum Diesel fuel. The Surrogate Fuel Library provided by this thesis supplies Diesel engine researchers and designers the ability to analytically and experimentally vary fuel cetane number and threshold soot index. This new capability to independently vary two key fuel properties provides a means to further enhance the understanding of Diesel combustion and design future combustion systems that improve efficiency and emissions. / El combustible diésel está compuesto por cientos de hidrocarburos cuya presencia y proporción varía dependiendo del origen del crudo, del proceso de refinado, de los requerimientos legislativos, y de muchos otros factores. Para evitar las dificultades que produce esta variabilidad y complejidad en su composición, en los estudios sistemáticos, los investigadores suelen trabajar con combustibles de sustitución, mucho más sencillos, pero que reproducen las propiedades químicas y físicas del gasóleo. Los primeros combustibles de sustitución estuvieron formados por un solo componente, como el n-heptano y el n-dodecano. Recientemente se han desarrollado combustibles de sustitución multi-componentes, que se aplican tanto a estudios experimentales como de modelado. La aplicación sistemática de combustibles de sustitución controlados con precisión es una vía prometedora para mejorar la comprensión de la combustión Diesel, su eficiencia, y sus emisiones y proporciona herramientas para la investigación de sistemas de combustión nuevos y alternativos. En esta tesis se han empleado métodos experimentales y de cálculo para desarrollar, estudiar y validar una librería de combustibles de sustitución multi-componentes. El primer combustible de sustitución se diseñó para reproducir con precisión las propiedades físicas y químicas de un gasóleo con número de cetano 50 y un índice de hollín umbral (TSI) de 31.El siguiente paso fue crear una biblioteca de combustibles de sustitución con 18 combustibles que pueden modificar independientemente dos propiedades clave del combustible: índice de cetano y TSI. En la biblioteca de combustibles el número de cetano osciló entre 35 y 60 con tres niveles de TSI iguales a 17, 31 y 48 (bajo, medio y alto rango). Los ensayos según la normativa ASTM demostraron una buena coincidencia con las propiedades del gasóleo como densidad, viscosidad, poder calorífico y curvas de destilación. Para comprobar la validez de la librería, se realizó un estudio experimental comparativo sobre el proceso de combustión, las emisiones gaseosas, hollín y partículas de un gasóleo y de su combustible de sustitución ajustado. El estudio se realizó con un motor monocilíndrico Diesel completamente instrumentado y operando con estrategias de combustión en premezcla parcial (PPCI) y de baja temperatura (LTC), además de la combustión Diesel convencional (CDC). Los parámetros de la combustión como el retraso al encendido y la liberación de calor tanto de baja como de alta temperatura se aproximaron muy bien. Las emisiones de gases, hollín y partículas también fueron similares al variar el nivel de EGR y la fase de la combustión. La tesis demuestra que se pueden encontrar combustibles de sustitución perfectamente representativos de un gasóleo corriente, en base a mezclas apropiadas de n-hexadecano, 2,2,4,4,6,8,8-heptamethylnonano, decahidronaftaleno y 1-metilnaftaleno. Asimismo, se concluye que variando la proporción de estos cuatro componentes se puede controlar independientemente el número de cetano y el índice de hollín umbral, a la vez que se mantienen las propiedades físico-químicas y de combustión del gasóleo. La librería de combustibles de sustitución definida en esta tesis es una herramienta a disposición de los investigadores para profundizar en el conocimiento de la combustión diésel y avanzar en el diseño de sistemas futuros de combustión con mejor rendimiento y menores emisiones. / El combustible Diesel està compost per centenars d'hidrocarburs, la presència i proporció dels quals varia depenent de l'origen del cru, del procés de refinat, dels requeriments legislatius, i de molts altres factors. Per a evitar les dificultats que produeix aquesta variabilitat i complexitat en la seua composició, en els estudis sistemàtics, els investigadors solen treballar amb combustibles de substitució, molt més senzills, però que reprodueixen les propietats químiques i físiques del gasoil. Els primers combustibles de substitució van estar formats per un sol component, com el n-heptà i el n-dodecà. Recentment s'han desenvolupat combustibles de substitució multi-components, que s'apliquen tant a estudis experimentals com de modelatge. L'aplicació sistemàtica de combustibles de substitució controlats amb precisió és una via prometedora per a millorar la comprensió de la combustió Dièsel, la seua eficiència, i les seues emissions i proporciona eines per a la recerca de sistemes de combustió nous i alternatius. En aquesta tesi s'han emprat mètodes experimentals i de càlcul per a desenvolupar, estudiar i validar una llibreria de combustibles de substitució multi-components. El primer combustible de substitució es va dissenyar per a reproduir amb precisió les propietats físiques i químiques d'un gasoil amb índex de cetà 50 i un índex de sutge límit (TSI) de 31. El següent pas va ser crear una biblioteca de combustibles de substitució amb 18 combustibles que poden modificar independentment dues propietats clau del combustible: índex de cetà i TSI. En la biblioteca de combustibles l'índex de cetá va oscil·lar entre 35 i 60 amb tres nivells de TSI iguals a 17, 31 i 48 (baix, mitjà i alt rang). Els assajos segons la normativa ASTM van demostrar una bona coincidència amb les propietats del gasoil com a densitat, viscositat, poder calorífic i corbes de destil·lació. Per a comprovar la validesa de la llibreria, es va realitzar un estudi experimental comparatiu sobre el procés de combustió, les emissions gasoses, sutge i partícules d'un gasoil i del seu combustible de substitució ajustat. L'estudi es va realitzar amb un motor monocilíndric Dièsel completament instrumentat i operant amb estratègies de combustió en premescla parcial (PPCI) i de baixa temperatura (LTC), a més de la combustió Dièsel convencional (CDC). Els paràmetres de la combustió com el retard a l'encès i l'alliberament de calor tant de baixa com d'alta temperatura es van aproximar molt bé. Les emissions de gasos, sutge i partícules també van ser similars en variar el nivell d'EGR i la fase de la combustió. La tesi demostra que es poden trobar combustibles de substitució perfectament representatius d'un gasoil corrent, sobre la base de mescles apropiades de n-hexadecà, 2,2,4,4,6,8,8-heptamethylnonà, decahidronaftalé i 1-metilnaftaleno. Així mateix, es conclou que variant la proporció d'aquests quatre components es pot controlar independentment l'índex de cetà i l'índex de sutge límit, alhora que es mantenen les propietats físic-químiques i de combustió del gasoil. La llibreria de combustibles de substitució definida en aquesta tesi és una eina a la disposició dels investigadors per a aprofundir en el coneixement de la combustió Diesel i avançar en el disseny de sistemes futurs de combustió amb millor rendiment i menors emissions. / Szymkowicz, P. (2017). ANALYTICAL AND EXPERIMENTAL INVESTIGATION OF MULTI-COMPONENT SURROGATE DIESEL FUELS [Tesis doctoral no publicada]. Universitat Politècnica de València. https://doi.org/10.4995/Thesis/10251/90406 / TESIS