This thesis deals with converting a mixture of H2 and CO, also referred to as syngas or producer gas, to higher or mixed alcohols and other fuels through a process called Fischer Tropsch Synthesis (FTS). It is a beneficial pathway that minimizes the dependence on oil and similar fossil fuels which contribute to rapid climate change by releasing harmful greenhouse gases. The syngas used in FTS, is generally obtained through gasification of biomass to make the entire process renewable and to make the resulting fuel carbon neutral. The products are pure due to prior cleaning of syngas mixture to remove oxides of nitrogen, sulphur and other particulate matter, before the process, thereby drastically reducing the net exhaust gas emissions. The major objective of this project is to design a novel catalyst system and subject it to a series of experimentation for testing its selectivity towards alcohols. This is because the present catalytic systems are either very expensive to assemble or confer to a low yield. Two cobalt (Co) based catalysts, one without a promoter and the other which is promoted by zirconium (Zr), are prepared. The activity and selectivity of Co catalysts are finally compared with the existing Swedish Biofuels AB’s Iron (Fe) based catalyst promoted by copper (Cu) and chromium (Cr) along with characterization of the optimum reaction parameters like temperature, pressure, GHSV and syngas ratio for FTS. Aqueous incipient impregnation approach was adopted wherein the Co active metal and Zr promoter (only in second catalyst) are introduced step-wise on a ϒ-alumina support to synthesize the catalyst after which it is heat treated through drying, calcination and reduction to obtain the active Co metal catalyst. A high temperature FTS, was employed for the yield of alcohols and other gasoline derivatives according to literature. Finally, the liquid and gaseous products are analyzed through GC or GC/MS analysis techniques. The unpromoted Co catalyst’s activity is regarded as a failure due to satisfactory results. There were a few problems associated with the catalyst alone like poor mechanical stability that could be attributed to the use of an incorrect binder. Other problems included methanation due to haphazard temperature variations and inefficient catalyst reduction. For the promoted Co catalyst, the yield of alcohols and hydrocarbons was significantly higher than the unpromoted Co catalyst. A temperature of 300 °C, a GHSV of 360 h-1 , a pressure of 10 bar and a H2:CO ratio of 1.3:1 were the optimal background conditions for FTS. Higher temperature caused methanation and reduced the chain growth probability factor, α, that resulted in the formation of lower hydrocarbons only. Any increase in gas ratio and GHSV, also increased the rate of methane formation and caused diffusion limitations. For a one-stage setup with the reversal of exhaust gases, the conversion rates of CO and H2 were quite promising. This success can be attributed to a higher calcination temperature that increased the degree of reduction of Co due to formation of promoter oxides thereby enabling CO hydrogenation and H2 insertion. It helped to reduce CO2 formation as well. Even for the Fe catalyst, a low temperature, a low GHSV and low syngas ratio were preferred. But unlike its Co counterpart, a higher pressure favored an increase in yield of alcohols and other long chain hydrocarbons. Fe’s ability to support WGS reaction disturbed the molar ratio of CO and also released more CO2 that could affect the rate of syngas conversion. But, on the whole, Fe catalyst was efficient than Co catalyst for alcohol synthesis. The overall yield of alcohols was just 5% of the liquid products. Nearly 86% of the alcohol fraction comprised of C1, C2 and C3 alcohols alone and very few C4, C5 and C6 alcohols were obtained. / Denna avhandling behandlar omvandling av en blandning av H2 och CO, även kallad syngas eller producentgas, till högre eller blandade alkoholer och andra bränslen genom en process som kallas Fischer Tropsch Synthesis (FTS). Det är en bra väg som minimerar beroendet av olja och liknande fossila bränslen som bidrar till snabba klimatförändringar genom att släppa ut skadliga växthusgaser. Syngasen som används i FTS erhålls generellt genom förgasning av biomassa för att göra hela processen förnybar och för att göra det resulterande bränslet kolneutralt. Produkterna är rena på grund av föregående rengöring av syngasblandningen för att avlägsna kväveoxider, svavel och annat partikelformigt material före processen och därigenom drastiskt minska utsläppen av avgaserna. Huvudsyftet med detta projekt är att utforma ett nytt katalysatorsystem och utsätta det för en serie experiment för att testa dess selektivitet gentemot alkoholer. Detta beror på att de nuvarande katalytiska systemen antingen är mycket dyra att montera eller ge ett lågt utbyte. Två koboltbaserade (Co) -baserade katalysatorer, en utan en promotor och den andra som befordras av zirkonium (Zr), framställs. Aktiviteten och selektiviteten hos Co-katalysatorer jämförs slutligen med de befintliga Swedish Biofuels AB: s Iron (Fe) -baserade katalysator som främjas av koppar (Cu) och krom (Cr) tillsammans med karaktärisering av de optimala reaktionsparametrarna som temperatur, tryck, GHSV och syngasförhållande för FTS. Vattenhaltig begynnande impregneringsmetod användes där den Co-aktiva metallen och Zr-promotorn (endast i den andra katalysatorn) införs stegvis på ett ϒ-aluminiumoxidstöd för att syntetisera katalysatorn, varefter den värmebehandlas genom torkning, kalcering och reduktion för att erhålla aktiv Co-metallkatalysator. En hög temperatur FTS användes för utbytet av alkoholer och andra bensinderivat enligt litteratur. Slutligen analyseras de flytande och gasformiga produkterna genom GC- eller GC / MS-analystekniker. Den outpromoterade Co-katalysatorns aktivitet betraktas som ett misslyckande på grund av tillfredsställande resultat. Det fanns några problem associerade med katalysatorn ensam som dålig mekanisk stabilitet som kunde tillskrivas användningen av ett felaktigt bindemedel. Andra problem inkluderade metanering på grund av variationer i slumpmässiga temperaturer och ineffektiv katalysatorreduktion. För den befordrade Co-katalysatorn var utbytet av alkoholer och kolväten betydligt högre än den opromoterade Co-katalysatorn. En optimal temperatur på 300 ° C, en GHSV på 360 h-1, ett tryck av 10 bar och ett H2: CO-förhållande på 1,3: 1 var de optimala bakgrundsbetingelserna för FTS. Högre temperatur orsakade metanering och reducerade sannolikhetsfaktorn för kedjan tillväxt, a, vilket resulterade i bildandet av endast lägre kolväten. Varje ökning av gasförhållandet och GHSV, ökade också metanbildningshastigheten och orsakade diffusionsbegränsningar. För en inställning i ett steg med reversering av avgaser var omvandlingsgraden för CO och H2 ganska lovande. Denna framgång kan tillskrivas en högre kalcineringstemperatur som ökade graden av reduktion av Co på grund av bildning av promotoroxider och därigenom möjliggör CO-hydrering och H2-införing. Det hjälpte också till att minska koldioxidbildningen. Även för Fe-katalysatorn föredrog man en låg temperatur, ett lågt GHSV och lågt syngasförhållande. Men till skillnad från Co-motsvarigheten gynnade ett högre tryck en ökning av utbytet av alkoholer och andra långkedjiga kolväten. Fe: s förmåga att stödja WGS-reaktion störde det molära förhållandet CO och frigav också mer CO2 som kan påverka hastigheten på syngasomvandlingen. Men i stort sett var Fe-katalysator mer effektiv än Cokatalysator för alkoholsyntes. Det totala utbytet av alkoholer var bara 5% av de flytande produkterna. Nästan 86% av alkoholfraktionen bestod av C1-, C2- och C3-alkoholer enbart och mycket få C4-, C5- och C6-alkoholer erhölls.

Membrane processes have received growing attention due to their low energy consumption and ease of operation. Thin-film composite reverse osmosis membranes based on polyamides are the most widely applied commercial membranes, because of their high flux and selectivity. However, their application for gas separation processes is still limited. This is the due to the presence of defects in the membrane when in the dry state. Traditionally, thin-film composite membranes are made by interfacial polymerization between a polar (aqueous) phase and a non-polar (organic) phase. The most commonly applied thin-film composite membranes are made by dissolving m-phenylene diamine in the aqueous phase and trimesoyl chloride in the organic phase. This work investigated the possibility of fabricating thin-film composite membranes when an aliphatic alcohol (methanol, ethanol or isopropanol) is used as the polar phase. This is further extended to examining the ability of a PDMS coating to plug the defects in such layers. The effects of temperature and support type on the membrane performance were also studied. Solubility tests were conducted to determine the solubility limit of commercial and in-house fabricated amine monomers in water, methanol, ethanol and isopropanol. Water-insoluble monomers were found to be soluble in ethanol and methanol. Gas permeation tests were conducted on membranes made using water, methanol, ethanol and isopropanol as the polar phase. The results showed that the membranes produced by aliphatic alcohols had higher selectivities. The highest H2/CO2 selectivity of ~ 26 was observed in the ethanol-based membranes when they were coated with PDMS and tested at 80 C. It was confirmed that PDMS is able to plug the defects in the membrane. Membranes made on the polysulfone support were found to have higher permeance and comparable selectivity relative to the membranes made on the polyacrylonitrile supports. It was also found that a change in the polar phase solvent is able to alter the morphology of the membranes. SEM micrographs showed clear differences in the surface structure of each membrane. The average thickness values obtained from ellipsometry measurements showed a correlation with the interface miscibility. The thickest membrane corresponded to the most miscible interface (IPA/Isopar).

Ethyl alcohol (ethanol) as secondary fluids is very popular as heat transfer fluid for indirect refrigeration system with ground source heat pump systems (GSHP) in several countries such as Sweden, Norway, Switzerland, Finland and other European countries. There have been several researches about the future ofthe refrigeration sector, refrigerants and refrigeration systems. Moreover, strict regulations such as F-gasregulation and Kigali Amendment forcing a phase down of many current widely used high global warming potential (GWP) refrigerants, i.e. R134a or R410A. Therefore, secondary refrigeration systems and their working fluids are expected to play a key role in order to minimize the refrigerant charge in the systems, reduce the indirect refrigerant leakages as well as increase the safety during operation. The aim of this thesis is to investigate the effect different additives to increase the flame point together with ethanol-based secondary fluids and validate their thermophysical properties by comparing them with reference values for pure ethanol water solutions. The study aims to design a new commercial ethyl alcohol-based product for GSHP system that could replace existing ones in the Swedish market and could workwith natural or flammable low GWP refrigerants. Different high flash point additives were tested such as 1-propyl alcohol, n-butyl alcohol, glycerol andpropylene carbonate. Thermophysical properties were investigated and a GSHP model in Excel was created in order to assess the energy performance of the resulted blends. After screening different blends and assessing the energy performance, glycerol as additive in low concentration seems to be the future for the ethyl alcohol-based secondary fluids because of its high flashpoint (160ºC) that will reduce the flammability risk associated to ethyl alcohol blends, the low viscosity (by 12% lower compared to pure ethyl alcohol blends) that help reduce pumping power by 4.5% compared topure ethyl alcohol blends. Moreover, ethyl alcohol and glycerol blend showed the lost in heat transfer coefficient by 4% lower compared to pure ethyl alcohol blends due to lower thermal conductivity compared to pure ethyl alcohol blends. Finally, it is a rather cheap and natural product which has no problem related to corrosion since ethyl alcohol and glycerol are less corrosive than water. Although, flash point test was not conducted so there is no data regarding the flash point, it is expected the flash point is increased due to the high flash point of glycerol compared to ethyl alcohol or other possible additives. Therefore, it is expected that the flammability risk associated to ethyl alcohol-based secondary fluids is reduced. / Etylalkohol (etanol) som köldbärare är mycket populärt som värmeöverföringsvätska för indirekt kylsystemmed bergvärmepumpsystem (BVP) i Sverige, Norge, Schweiz, Finland och andra europeiska länder. Fleraundersökningar har gjorts om kylsektorns framtid, köldmedier och kylsystem. Dessutom strängaförordningar som F-gas förordning och Kigali- förordning tvingar en utfasning av många nuvarande allmäntanvända köldmedier med den höga globala uppvärmningspotentialen (GWP), dvs. R134a eller R410A. Därför förväntas det att kylsystem och deras köldbärare spela en nyckelroll för att minimera köldmediumsmängd i systemen, minska de indirekta köldmedieläckage och öka säkerheten under drift. Syftet med detta examensarbete är att undersöka effekten av olika tillsatser för att öka flammanpunkten tillsammans med etanolbaserade köldbärare och validera deras termofysikaliska egenskaper genom att jämföra dem med referensvärden för rena etanolvattenlösningar. Studien syftar till att utforma en nykommersiell etylalkoholbaserad produkt för BVP-system som skulle kunna ersätta befintliga produkter på den svenska marknaden och kan arbeta med naturliga eller brandfarliga köldmedier med låg GWP. Olika tillsatser med hög flampunkt testades såsom 1-propylalkohol, n-butylalkohol, glycerol och propylenkarbonat. Termofysikaliska egenskaper undersöktes och en BVP-modell i Excel skapades för att bedöma energiprestanda för olika blandningarna. De erhållna resultaten för olika blandningar visar att glycerol i en låg koncentration som tillsats kan vara framtidens additiv för de etylalkoholbaserade köldbärare på grund av dess höga flampunkt (160 ºC) som förmodligen kan minska brandrisken för etylalkoholblandningar. Dessutom hade glycerol och etanolblandningar den lägsta viskositeten (c.a.12% lägre jämfört med ren etylalkoholblandningar) som bidrar tillen minskning av pumpeffekten med c.a. 4,5% jämfört med rena etylalkoholblandningar. Däremot visade etylalkohol och glycerol blandningen c.a. 4% lägre värmeöverövergångstal jämfört med de rena etylalkoholblandningar på grund av lägre värmeledningsförmåga jämfört med ren etylalkoholblandningar. Slutligen är glycerol en ganska billig och naturlig produkt som inte har några korrosionsproblem eftersom etylalkohol och glycerol är mindre frätande än vatten. Även om flampunkttest inte genomfördes i projektet, förväntas det att flampunkten ökas lite på grund av den höga flampunkten av glycerol jämfört med etylalkohol och andra tillsatser. Därför förväntas det att brännbarhetsrisken förknippad med etylalkoholbaserade köldbärare reduceras.

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The objective of this study was to determine the potential for biodegradation in subsurface soils and groundwater from sites in Williamsport, PA, Wayland, NY, and Dumfries, VA. These subsurface systems were characterized both physically, chemically and biologically. Bacterial populations were substantial in all systems and ranged from 10³ to 10⁸ colony forming units per gram. Soil sampling was done in a quality-controlled aseptic manner using conventional drilling end sampling equipment. A matrix of test-tube microcosms was used to determine biodegradation rates of methanol and t-butyl alcohol at concentrations ranging from 1 to 1000 mg/L. Methanol degraded readily at all sites ranging from 0.8 mg/L/day to 20.4 mg/L/day and rates were generally greater in the saturated zone. TBA biodegraded at all sites, but was refractory in nature. Biodegradation rates for TBA in anaerobic subsurface systems were found to increase directly with initial concentration from 10⁻⁴ mg/L/day for 1 mg/L to 10⁻¹ mg/L/day for 80 mg/L. TBA biodegradation in the aerobic system was essentially constant over all concentrations. Biokinetic coefficients were determined for methanol and TBA at each site based on plots of utilization rates versus substrate concentration and reciprocal plots of these values. The K values found suggest that aerobic subsurface systems can utilize alcohols at a greater rate than anoxic subsurface systems and can be used for comparative purposes. The K_s of anoxic subsurface systems were found to be large due to the low temperature (10°C) found in aquifers. The results indicate that methanol contamination in groundwater has much less associated risk to drinking water supplies due to the ease of biodegradation. However, TBA poses a much greater risk due to the very slow removal rates at low concentrations, which could result in a residual level for over a decade in some cases. / Ph. D.

The purpose of this thesis is to determine the effect of hexadecanol on the populations of Pseudomonas and Alcaligenes species in reservoirs and determine their ability to utilize this compound as a carbon source.

New GC-MS method combined with SPE preconcentration step has been developed and optimized for the determination of selected fluorotelomer alcohols in aqueous samples by advanced statistical method in this thesis. 1H,1H,2H,2H-perfluoro-1-octanol (6:2 FTOH) and 1H,1H,2H,2H-perfluoro-1-decanol (8:2 FTOH) have been selected as the analytes. The influence of several factors, such as the sample volume, the carrier gas pressure, the sampling time and the injector temperature on the system response have been studied during the optimization. Utilizing the statistical software Minitab 16 and series of experiments, the optimal values of relevant factors and a suitable type of ionization were found for both analytes. Limits of detection of GC-MS method are 0.24 ng/mL for 6:2 FTOH and 0.42 ng/mL for 8:2 FTOH. Several factors, such as the type and the volume of conditioning agent, the speed of conditioning, the speed of sample flow, the method of column drying, the type and the volume of eluent have been tested for SPE. The optima of these factors were determined using Minitab 16 software. The extraction efficiency dependence on the concentration and volume of the stock solution was used to set the limitation of SPE for the determination of fluorotelomer alcohols. The maximum volume of sample equals to 400 mL...

Thesis advisor: Amir H. Hoveyda / Chapter 1. Mechanistic Insights and Factors Influencing Polytopal Rearrangements in Stereogenic-at-Ru Carbenes. Herein, the mechanistic elucidation of the stereochemical inversion in stereogenic-at-Ru carbene complexes through olefin metathesis (OM) and non-olefin metathesis (non-OM) based polytopal rearrangements is provided. Our investigations involve the isolation and characterization of previously hypothesized higher-energy (e.g., endo-anti) and lower-energy (e.g., exo-anti) diastereomers, and their interconversion under thermal and/or acid-catalyzed conditions is demonstrated. Furthermore, our computational efforts highlighting the importance of the anionic ligands, due to their critical role in trans influence, dipolar interactions, and e-e repulsions, in polytopal rearrangements are reported. Finally, the positive influence of H-bonding in OM and non-OM processes is also rationalized. (a) Khan, R. K. M.; Zhugralin, A. R.; Torker, S.; O'Brien, R. V.; Lombardi, P. J. and Hoveyda, A. H. "Synthesis, Isolation, Characterization, and Reactivity of High-Energy Stereogenic-at-Ru Carbenes: Stereochemical Inversion Through Olefin Metathesis and Other Pathways," J. Am. Chem. Soc. 2012, 134, 12438-12441. (b) Torker, S.; Khan, R. K. M. and Hoveyda, A. H. "The Influence of Anionic Ligands on Stereoisomerism of Ru Carbenes and Their Importance to Efficiency and Selectivity of Catalytic Olefin Metathesis Reactions," J. Am. Chem. Soc. 2014, 136, 3439-3455. Chapter 2. Highly Z- and Enantioselective Ring-Opening/Cross-Metathesis of Enol Ethers Through Curtin-Hammett Kinetics. The first instances of Z- and enantioselective Ru-catalyzed olefin metathesis are presented. Ring-opening/cross-metathesis (ROCM) reactions of oxabicyclic alkenes and enol ethers and a phenyl vinyl sulfide are promoted by 0.5-5.0 mol % of enantiomerically pure stereogenic-at-Ru complexes with an aryloxy chelate tethered to the N-heterocyclic carbene. Products are formed efficiently and with exceptional enantioselectivity (up to >98:2 enantiomer ratio). Surprisingly, the enantioselective ROCM reactions proceed with high Z selectivity (up to >98% Z). Moreover, reactions proceed with the opposite sense of enantioselectivity versus aryl olefins, which afford E- isomers exclusively. DFT calculations and deuterium-scrambling experiments, indicating fast interconversion between endo- and exo-Fischer carbene diastereomers, support a Curtin-Hammett situation. On this basis, models accounting for the stereoselectivity levels and trends are provided. Furthermore, the correlation of Fischer carbene character to the observed chemoselectivity in ROCM with enol ethers is also disclosed. Finally, a general proposal for the substrate-controlled Z selectivity in OM is also discussed. (a) Khan, R. K. M.; O'Brien, R. V.; Torker, S.; Li, B. and Hoveyda, A. H. "Z- and Enantioselective Ring-Opening Cross-Metathesis with Enol Ethers Catalyzed by Stereogenic-at-Ru Carbenes: Reactivity, Selectivity, and Curtin-Hammett Kinetics," J. Am. Chem. Soc. 2012, 134, 12774-12779. (b) Torker, S.; Koh, M. J.; Khan, R. K. M. and Hoveyda, A. H. "Origin of Z selectivity in Olefin Metathesis Reactions of Certain Terminal Alkenes Catalyzed by Typically E-Selective Ru Carbenes," manuscript submitted. Chapter 3. A New Class of Highly Efficient Ru Catalysts for Z-Selective Olefin Metathesis. Herein, we outline a general design for Z-selective OM, which led to the development of a new class of stereogenic-at-Ru carbene complexes (Ru4-9). Furthermore, we demonstrate that the newly developed dithiolate complexes Ru4b and Ru5 efficiently promote high activity and selectivity in ROMP reactions of norbornene and cyclooctene. Notably, the catechothiolate Ru4b catalyzes Z-selective ROCM with a broad scope of alkenes involving various functional groups (e.g., alcohols, enol ethers, vinyl sulfides, amides, heterocycles, and conjugated 1,3-dienes). More importantly, we disclose that the catecholate complex Ru4a is kinetically non-selective in OM and readily decomposes in the presence of mildly acidic moieties (e.g., alcohols and CDCl3). Subsequently, Ru9 is developed to efficiently promote highly Z-selective CM of a diol cross-partner with a wide range of alkene substrates. Most remarkably, the aforementioned protocol is employed in two natural product syntheses and the OM-based Z-selective cracking of oleic acid, which is unprecedented with existing Ru-carbenes and Mo/W-alkylidenes. (a) Khan, R. K. M.; Torker, S. and Hoveyda, A. H. "Readily Accessible and Easily Modifiable Ru-Based Catalysts for Efficient and Z-Selective Ring-Opening Metathesis Polymerization and Ring-Opening Cross-Metathesis," J. Am. Chem. Soc. 2013, 135, 10258-10261. (b) Koh, M. J.; Khan, R. K. M.; Torker, S. and Hoveyda, A. H. "Broadly Applicable Z- and Diastereoselective Ring-Opening/Cross-Metathesis Catalyzed By a Dithiolate Ru Complex," Angew. Chem., Int. Ed. 2014, 53, 1968-1972. (c) Khan, R. K. M. ; Torker, S. and Hoveyda, A. H. "Reactivity and Selectivity Differences Between Catecholate and Catechothiolate Ru Complexes. Implications Regarding Design of Stereoselective Olefin Metathesis Catalysts," J. Am. Chem. Soc. 2014, 136, 14337-14340. (d) Koh, M. J.; Khan, R. K. M.; Torker, S.; Yu, M.; Mikus, M. S. and Hoveyda, A. H. "Synthesis of High-Value Alcohols, Aldehydes and Acids by Catalytic Z-Selective Cross-Metathesis" manuscript submitted. / Thesis (PhD) — Boston College, 2014. / Submitted to: Boston College. Graduate School of Arts and Sciences. / Discipline: Chemistry.

Este trabalho tem como objetivo estudar as fontes de matéria orgânica em sedimentos ao longo do Sistema Estuarino-Lagunar de Cananéia-Iguape, por meio de diferentes indicadores geoquímicos. Foram coletados 12 testemunhos. Os 10 centímetros superficiais foram fatiados de 2 em 2 centímetros, totalizando 60 amostras. Análises granulométricas, de razão C/N, 13C/12C e a datação de alguns dos testemunhos, foram feitos pelo grupo de Oceanografia Geológica do IOUSP. Os marcadores orgânicos moleculares utilizados foram os hidrocarbonetos alifáticos, álcoois graxos e esteróides, analisados por GCFID. O total de hidrocarbonetos alifáticos variou entre 0,571 a 9,932 g g-1. Os álcoois totais variaram de 0,318 a 35,291 g g-1. Os esteróides totais variaram de 0,241 a 11,054 g g-1. Para interpretação dos dados foram utilizadas as razões entre n-alcanos ímpares e pares leves (C21) e pesados (C22), somatório de álcoois graxos leves e pesados, relação entre a soma de coprostanol e epicoprostanol sobre o total de esteróides e relação entre epicoprostanol e coprostanol. Os resultados das razões indicam uma origem terrestre dos compostos orgânicos analisados com uma clara predominância da contribuição da vegetação de manguezal da região. Entretanto, existe uma discreta introdução de hidrocarbonetos de petróleo e esgoto domésticos nãotratados em alguns pontos isolados do Sistema Estuarino-Lagunar de Cananéia-Iguape. / This work has the objective in evaluate the sources of organic matter in sediments of the Cananéia-Iguape Estuarine-Lagunar System, using several geochemical markers. For the study area, 12 sample points were chosen, where the corers were obtained. For each point, the superficial 10 centimeters, sliced in each 2 centimeters, totalizing 60 samples. Granulometric analysis, C/N and 13C/12C ratios and dating of some cores, were realized by the Geological Oceanography group of IOUSP. The molecular organic markers used were the aliphatic hydrocarbons, fatty alcohols and steroids, analyzed by GC-FID. The total hydrocarbons varied from 0.571 to 9.932 g g-1. The total fatty alcohols ranged from 0.318 to 35.291 g g-1. The total steroids varied from 0.241 to 11.054 g g-1. For interpretation of data, some relations were used such as odd/even hydrocarbons C21 and C22, total short and long chain fatty alcohols, the coprostanol + epicoprostanol divided by total sterols and epicoprostanol/coprostanol. The results of the ratios showed a terrestrial origin of the organic matter with a clear predominance of the contribution of the mangrove higher plants of the region. However, there is a discrete introduction of petroleum hydrocarbons and untreated domestic sewage in isolated points of the Estuarine-Lagunar System of Cananéia-Iguape.