Clean preparation of methyl esters in one-step oxidative esterification of primary alcohols catalyzed by supported gold nanoparticles

Methyl esters were prepared by the clean, one-step catalytic esterification of primary alcohols using molecular oxygen as a green oxidant and a newly developed SiO(2)-supported gold nanoparticle catalyst. The catalyst was highly active and selective in a broad range of pressure and temperature. At 3 atm O(2) and 130 degrees C benzyl alcohol was converted to methyl benzoate with 100% conversion and 100% selectivity in 4 h of reaction. This catalytic process is much ""greener"" than the conventional reaction routes because it avoids the use of stoichiometric environmentally unfriendly oxidants, usually required for alcohol oxidation, and the use of strong acids or excess of reactants or constant removal of products required to shift the equilibrium to the desired esterification product.

A modified pore-filling isotherm for liquid-phase adsorption in activated carbon

This article modifies the usual form of the Dubinin-Radushkevich pore-filling model for application to liquid-phase adsorption data, where large molecules are often involved. In such cases it is necessary to include the repulsive part of the energy in the micropores, which is accomplished here by relating the pore potential to the fluid-solid interaction potential. The model also considers the nonideality of the bulk liquid phase through the UNIFAC activity coefficient model, as well as structural heterogeneity of the carbon. For the latter the generalized adsorption integral is used while incorporating the pore-size distribution obtained by density functional theory analysis of argon adsorption data. The model is applied here to the interpretation of aqueous phase adsorption isotherms of three different esters on three commercial activated carbons. Excellent agreement between the model and experimental data is observed, and the fitted Lennard-Jones size parameter for the adsorbate-adsorbate interactions compares well with that estimated from known critical properties, supporting the modified approach. On the other hand, the model without consideration of bulk nonideality, or when using classical models of the characteristic energy, gives much poorer bts of the data and unrealistic parameter values.

The use of liquid phase adsorption isotherms for characterization of activated carbons

The characterization of three commercial activated carbons was carried out using the adsorption of various compounds in the aqueous phase. For this purpose the generalized adsorption isotherm was employed, and a modification of the Dubinin-Radushkevich pore filling model, incorporating repulsive contributions to the pore potential as well as bulk liquid phase nonideality, was used as the local isotherm. Eight different flavor compounds were used as adsorbates, and the isotherms were jointly fitted to yield a common pore size distribution for each carbon. The bulk liquid phase nonideality was incorporated through the UNIFAC activity coefficient model, and the repulsive contribution to the pore potential was incorporated through the Steele 10-4-3 potential model. The mean micropore network coordination number for each carbon was also determined from the fitted saturation capacity based on percolation theory. Good agreement between the model and the experimental data was observed. In addition, excellent agreement between the bimodal gamma pore size distribution and density functional theory-cum-regularization-based pore size distribution obtained by argon adsorption was also observed, supporting the validity of the model. The results show that liquid phase adsorption, using adsorptive molecules of different sizes, can be an effective means of characterizing the pore size distribution as well as connectivity. Alternately, if the carbon pore size distribution is independently known, the method can be used to measure critical molecular sizes. (C) 2001 Elsevier Science.

Development of a multistrain bacterial bioreporter platform for the monitoring of hydrocarbon contaminants in marine environments.

Petroleum hydrocarbons are common contaminants in marine and freshwater aquatic habitats, often occurring as a result of oil spillage. Rapid and reliable on-site tools for measuring the bioavailable hydrocarbon fractions, i.e., those that are most likely to cause toxic effects or are available for biodegradation, would assist in assessing potential ecological damage and following the progress of cleanup operations. Here we examined the suitability of a set of different rapid bioassays (2-3 h) using bacteria expressing the LuxAB luciferase to measure the presence of short-chain linear alkanes, monoaromatic and polyaromatic compounds, biphenyls, and DNA-damaging agents in seawater after a laboratory-scale oil spill. Five independent spills of 20 mL of NSO-1 crude oil with 2 L of seawater (North Sea or Mediterranean Sea) were carried out in 5 L glass flasks for periods of up to 10 days. Bioassays readily detected ephemeral concentrations of short-chain alkanes and BTEX (i.e., benzene, toluene, ethylbenzene, and xylenes) in the seawater within minutes to hours after the spill, increasing to a maximum of up to 80 muM within 6-24 h, after which they decreased to low or undetectable levels. The strong decrease in short-chain alkanes and BTEX may have been due to their volatilization or biodegradation, which was supported by changes in the microbial community composition. Two- and three-ring PAHs appeared in the seawater phase after 24 h with a concentration up to 1 muM naphthalene equivalents and remained above 0.5 muM for the duration of the experiment. DNA-damage-sensitive bioreporters did not produce any signal with the oil-spilled aqueous-phase samples, whereas bioassays for (hydroxy)biphenyls showed occasional responses. Chemical analysis for alkanes and PAHs in contaminated seawater samples supported the bioassay data, but did not show the typical ephemeral peaks observed with the bioassays. We conclude that bacterium-based bioassays can be a suitable alternative for rapid on-site quantitative measurement of hydrocarbons in seawater.

Measurement of biologically available naphthalene in gas and aqueous phases by use of a Pseudomonas putida biosensor.

Genetically constructed microbial biosensors for measuring organic pollutants are mostly applied in aqueous samples. Unfortunately, the detection limit of most biosensors is insufficient to detect pollutants at low but environmentally relevant concentrations. However, organic pollutants with low levels of water solubility often have significant gas-water partitioning coefficients, which in principle makes it possible to measure such compounds in the gas rather than the aqueous phase. Here we describe the first use of a microbial biosensor for measuring organic pollutants directly in the gas phase. For this purpose, we reconstructed a bioluminescent Pseudomonas putida naphthalene biosensor strain to carry the NAH7 plasmid and a chromosomally inserted gene fusion between the sal promoter and the luxAB genes. Specific calibration studies were performed with suspended and filter-immobilized biosensor cells, in aqueous solution and in the gas phase. Gas phase measurements with filter-immobilized biosensor cells in closed flasks, with a naphthalene-contaminated aqueous phase, showed that the biosensor cells can measure naphthalene effectively. The biosensor cells on the filter responded with increasing light output proportional to the naphthalene concentration added to the water phase, even though only a small proportion of the naphthalene was present in the gas phase. In fact, the biosensor cells could concentrate a larger proportion of naphthalene through the gas phase than in the aqueous suspension, probably due to faster transport of naphthalene to the cells in the gas phase. This led to a 10-fold lower detectable aqueous naphthalene concentration (50 nM instead of 0.5 micro M). Thus, the use of bacterial biosensors for measuring organic pollutants in the gas phase is a valid method for increasing the sensitivity of these valuable biological devices.

Recovery of carboxylic acids from aqueous streams by extraction and back extraction

Separation of carboxylic acids from aqueous streams is an important part of their manufacturing process. The aqueous solutions are usually dilute containing less than 10 % acids. Separation by distillation is difficult as the boiling points of acids are only marginally higher than that of water. Because of this distillation is not only difficult but also expensive due to the evaporation of large amounts of water. Carboxylic acids have traditionally been precipitated as calcium salts. The yields of these processes are usually relatively low and the chemical costs high. Especially the decomposition of calcium salts with sulfuric acid produces large amounts of calcium sulfate sludge. Solvent extraction has been studied as an alternative method for recovery of carboxylic acids. Solvent extraction is based on mixing of two immiscible liquids and the transfer of the wanted components form one liquid to another due to equilibrium difference. In the case of carboxylic acids, the acids are transferred from aqueous phase to organic solvent due to physical and chemical interactions. The acids and the extractant form complexes which are soluble in the organic phase. The extraction efficiency is affected by many factors, for instance initial acid concentration, type and concentration of the extractant, pH, temperature and extraction time. In this paper, the effects of initial acid concentration, type of extractant and temperature on extraction efficiency were studied. As carboxylic acids are usually the products of the processes, they are wanted to be recovered. Hence the acids have to be removed from the organic phase after the extraction. The removal of acids from the organic phase also regenerates the extractant which can be then recycled in the process. The regeneration of the extractant was studied by back-extracting i.e. stripping the acids form the organic solution into diluent sodium hydroxide solution. In the solvent regeneration, the regenerability of different extractants and the effect of initial acid concentration and temperature were studied.

Catalytic upgrading of biomass extractives to fine chemicals over supported ionic liquid catalysts (SILCAs)

Behovet av förnyelsebar energi ökar ständigt eftersom det finns en strävan att minska beroendet av fossila bränslen. Dessutom är tillgångar av fossila bränslen begränsade. Miljövänliga processer för bioraffinaderier erbjuder en stor möjlighet för produktion av energi, bränslen och kemikalier. Den finska och svenska skogsindustrin har en lång tradition i utnyttjandet av skogsbiomassor. Bioraffinaderier som integreras med pappers- och cellulosaindustrin kan frambringa både ekonomiska och ekologiska fördelar i framställning av traditionella och biobaserade produkter. I doktorsarbetet studerades omvandling av extraktivämnen till finkemikalier som kan användas t.ex. av läkemedelsindustrin. Extraktivämnen fås ur biomassa. I forskningsarbetet framställdes biobaserade finkemikalier med hjälp av katalysatorer som baserar sig på joniska vätskor. Biomassan består av cellulosa, hemicellulosa, lignin och extraktivämnen, vilka huvudsakligen är terpener, vaxer och fettsyror. Extraktivämen är vedens komponenter, som kan separeras ur vedmaterialet med hjälp av neutrala lösningsmedel. Joniska vätskekatalysatorer som var immobiliserade på fasta bärare utnyttjades för isomerisering av α,β-pinenoxider samt hydrogenering citral. Inverkan av joniska vätskor på katalysatorns aktivitet och reaktionernas produktfördelning undersöktes under varierande reaktionsbetingelser. Kinetiska modeller för pinenoxidens isomeriseringsreaktioner beskrev väl experimentellt upptäckta skillnader mellan olika katalysatorer. --------------------------------------------------- Uusiutuvan energian tarve on kasvussa, koska riippuvuutta fossiilisista polttoaineista pyritään vähentämään. Tämän lisäksi fossiilisten polttoaineiden varannot ovat rajalliset. Ympäristöystävälliset biojalostusprosessit ovat näin ollen suuri mahdollisuus energian, polttoaineiden ja kemikaalien tuotannossa. Suomen ja Ruotsin metsäteollisuudella on pitkät perinteet metsäbiomassojen hyödyntämisessä. Paperi- ja selluteollisuuden yhteyteen integroiduilla biojalostamoilla voidaan luoda taloudellisia ja ympäristöllisiä etuja sekä perinteisten että biopohjaisten tuotteiden valmistuksessa. Väitöstyössä on tutkittu biomassan uuteaineiden kemiallista muuntamista hienokemikaaleiksi, joita voidaan käyttää esimerkiksi lääkeaineteollisuudessa. Biopohjaisia hienokemikaaleja on valmistettu biomassan uuteaineista ionisiin nesteisiin perustuvilla katalyyteillä. Biomassa koostuu selluloosasta, hemiselluloosasta, ligniinistä sekä uuteaineista, jotka ovat pääosin terpeenejä, vahoja tai rasvahappoja. Uuteaineet ovat puun komponentteja, jotka voidaan erottaa puusta neutraalien liuottimien avulla. Kiinteän kantajan päälle immobilisoituja ionisia nestekatalyyttejä (Supported Ionic Liquid Catalyst) hyödynnettiin α,β-pineenioksidien isomerisointireaktioissa sekä sitraalin vedytysreaktioissa. Ionisten nesteiden vaikutusta katalyyttien aktiivisuuteen sekä reaktioiden tuotejakaumaan tutkittiin erilaisissa reaktio-olosuhteissa. Pineenioksidien isomerisointireaktioiden kineettiset mallit kuvasivat hyvin kokeellisesti todettuja katalyyttien eroavaisuuksia.

Modifications to the Suzuki reaction and mechanistic insights on the NBS mediated cleavage of benzylidene acetals /

One of the most challenging tasks for a synthetic organic chemist today, is the development of chemo, regio, and stereoselective methodologies toward the total synthesis of macromolecules. r . The objective of my thesis was to develop methodologies towards this end. The first part of my project was to develop highly functionalized chirons from D-glucose, a cheap, chiral starting material, to be utilized in this capacity. The second part of the project dealt with modifying the carbon-carbon bond forming Suzuki reaction, which is utilized quite often as a means of combining molecular sub units in total synthesis applications. As previously stated the first area of the project was to develop high value chirons from D-glucose, but the mechanism of their formation was also investigated. The free radical initiated oxidative fragmentation of benzylidene acetals was investigated through the use of several test-case substrates in order to unravel the possible mechanistic pathways. This was performed by reacting the different acetals with N-bromosuccinimide and benzoyl peroxide in chlorobenzene at 70^C in all cases. Of the three mechanistic pathways discussed in the literature, it was determined, from the various reaction products obtained, that the fragmentation of the initial benzylic radical does not occur spontaneously but rather, oxidation proceeds to give the benzyl bromide, which then fragments via a polar pathway. It was also discovered that the regioselectivity of the fragmentation step could be altered through incorporation of an allylic system into the benzylidene acetal. This allows for the acquisition of a new set of densely functionalized. chiral, valuable synthetic intermediates in only a few steps and in high yields from a-Dglucose. The second part of the project was the utilization of the phosphonium salt room temperature ionic liquid tetradecyltrihexylphosphonium chloride (THPC) as an efficient reusable medium for the palladium catalyzed Suzuki cross-coupling reaction of aryl halides, including aryl chlorides, under mild conditions. The cross-coupling reactions were found to proceed in THPC containing small amounts of water and toluene using potassium phosphate and 1% Pd2(dba)3. Variously substituted iodobenzenes, including electron rich derivatives, reacted efficiently in THPC with a variety of arylboronic acids and afforded complete conversion within 1 hour at 50 ^C. The corresponding aryl bromides also reacted under these conditions with the addition of a catalytic amount of triphenylphosphine that allowed for complete conversion and high isolated yields. The reactions involving aryl chlorides were considerably slower, although the addition of triphenylphosphine and heating at 70 ^C allowed high conversion of electron deficient derivatives. Addition of water and hexane to the reaction products results in a triphasic system in which the top hexane phase contained the biaryl products, the palladium catalyst remained fully dissolved in the central THPC layer, while the inorganic salts were extracted into the lower aqueous phase. The catalyst was then recycled by removing the top and bottom layers and adding the reagents to the ionic liquid which was heated again at 50 ^C; resulting in complete turnover of iodobenzene. Repetition of this procedure gave the biphenyl product in 82-97% yield (repeated five times) for both the initial and recycled reaction sequences.

Développement de papier bioactif par couchage à grande échelle d’enzymes immobilisées par microencapsulation

L’objectif principal de cette recherche est de contribuer au développement de biocapteurs commerciaux utilisant des surfaces de papier comme matrices d’immobilisation, capables de produire un signal colorimétrique perceptible dans les limites sensorielles humaines. Ce type de biocapteur, appelé papier bioactif, pourrait servir par exemple à la détection de substances toxiques ou d’organismes pathogènes. Pour atteindre l’objectif énoncé, ce travail propose l’utilisation de systèmes enzymatiques microencapsulés couchés sur papier. Les enzymes sont des catalyseurs biologiques dotés d’une haute sélectivité, et capables d'accélérer la vitesse de certaines réactions chimiques spécifiques jusqu’à des millions des fois. Les enzymes sont toutefois des substances très sensibles qui perdent facilement leur fonctionnalité, raison pour laquelle il faut les protéger des conditions qui peuvent les endommager. La microencapsulation est une technique qui permet de protéger les enzymes sans les isoler totalement de leur environnement. Elle consiste à emprisonner les enzymes dans une sphère poreuse de taille micrométrique, faite de polymère, qui empêche l’enzyme de s’echapper, mais qui permet la diffusion de substrats à l'intérieur. La microencapsulation utilisée est réalisée à partir d’une émulsion contenant un polymère dissous dans une phase aqueuse avec l’enzyme désirée. Un agent réticulant est ensuite ajouté pour provoquer la formation d'un réseau polymérique à la paroi des gouttelettes d'eau dans l'émulsion. Le polymère ainsi réticulé se solidifie en enfermant l’enzyme à l'intérieur de la capsule. Par la suite, les capsules enzymatiques sont utilisées pour donner au papier les propriétés de biocapteur. Afin d'immobiliser les capsules et l'enzyme sur le papier, une méthode courante dans l’industrie du papier connu sous le nom de couchage à lame est utilisée. Pour ce faire, les microcapsules sont mélangées avec une sauce de couchage qui sera appliquée sur des feuilles de papier. Les paramètres de viscosité i de la sauce et ceux du couchage ont été optimisés afin d'obtenir un couchage uniforme répondant aux normes de l'industrie. Les papiers bioactifs obtenus seront d'abord étudiés pour évaluer si les enzymes sont toujours actives après les traitements appliqués; en effet, tel que mentionné ci-dessus, les enzymes sont des substances très sensibles. Une enzyme très étudiée et qui permet une évaluation facile de son activité, connue sous le nom de laccase, a été utilisée. L'activité enzymatique de la laccase a été évaluée à l’aide des techniques analytiques existantes ou en proposant de nouvelles techniques d’analyse développées dans le laboratoire du groupe Rochefort. Les résultats obtenus démontrent la possibilité d’inclure des systèmes enzymatiques microencapsulés sur papier par couchage à lame, et ce, en utilisant des paramètres à grande échelle, c’est à dire des surfaces de papier de 0.75 x 3 m2 modifiées à des vitesses qui vont jusqu’à 800 m/min. Les biocapteurs ont retenu leur activité malgré un séchage par évaporation de l’eau à l’aide d’une lampe IR de 36 kW. La microencapsulation s’avère une technique efficace pour accroître la stabilité d’entreposage du biocapteur et sa résistance à l’exposition au NaN3, qui est un inhibiteur connu de ce biocapteur. Ce projet de recherche fait partie d'un effort national visant à développer et à mettre sur le marché des papiers bioactifs; il est soutenu par Sentinel, un réseau de recherche du CRSNG.

New magnetic nano-absorbent for the determination of n-octanol/water partition coefficients

A novel and generic miniaturization methodology for the determination of partition coefficient values of organic compounds in noctanol/water by using magnetic nanoparticles is, for the first time, described. We have successfully designed, synthesised and characterised new colloidal stable porous silica-encapsulated magnetic nanoparticles of controlled dimensions. These nanoparticles absorbing a tiny amount of n-octanol in their porous silica over-layer are homogeneously dispersed into a bulk aqueous phase (pH 7.40) containing an organic compound prior to magnetic separation. The small size of the particles and the efficient mixing allow a rapid establishment of the partition equilibrium of the organic compound between the solid supported n-octanol nano-droplets and the bulk aqueous phase. UV-vis spectrophotometry is then applied as a quantitative method to determine the concentration of the organic compound in the aqueous phase both before and after partitioning (after magnetic separation). log D values of organic compounds of pharmaceutical interest (0.65-3.50), determined by this novel methodology, were found to be in excellent agreement with the values measured by the shake-flask method in two independent laboratories, which are also consistent with the literature data. It was also found that this new technique gives a number of advantages such as providing an accurate measurement of log D value, a much shorter experimental time and a smaller sample size required. With this approach, the formation of a problematic emulsion, commonly encountered in shake-flask experiments, is eliminated. It is envisaged that this method could be applicable to the high throughput log D screening of drug candidates. (c) 2005 Elsevier B.V. All rights reserved.

Preparation of nanomagnetic absorbent for partition coefficient measurement

In this paper, we report a new method based on supercritical carbon dioxide (scCO(2)) to fill and distribute the porous magnetic nanoparticles with n-octanol in a homogeneous manner. The high solubility of n-octanol in scCO(2) and high diffusivity and permeability of the fluid allow efficient delivery of n-octanol into the porous magnetic nanoparticles. Thus, the n-octanol-loaded magnetic nanoparticles can be readily dispersed into aqueous buffer (pH 7.40) to form a homogenous suspension consisting of nano-sized n-octanol droplets. We refer this suspension as the n-octanol stock solution. The n-octanol stock solution is then mixed with bulk aqueous phase (pH 7.40) containing an organic compound prior to magnetic separation. The small-size of the particles and the efficient mixing enable a rapid establishment of the partition equilibrium of the organic compound between the solid supported n-octanol nano-droplets and the bulk aqueous phase. UV-vis spectrophotometry is then applied to determine the concentration of the organic compound in the aqueous phase both before and after partitioning (after magnetic separation). As a result, log D values of organic compounds of pharmaceutical interest determined by this modified method are found to be in excellent agreement with the literature data. (c) 2006 Elsevier B.V. All rights reserved.

Hydrophilic sulfonated bis-1,2,4-triazine ligands are highly effective reagents for separating actinides(iii) from lanthanides(iii) via selective formation of aqueous actinide complexes

We report the first examples of hydrophilic 6,6′-bis(1,2,4-triazin-3-yl)-2,2′-bipyridine (BTBP) and 2,9-bis(1,2,4-triazin-3-yl)-1,10-phenanthroline (BTPhen) ligands, and their applications as actinide(III) selective aqueous complexing agents. The combination of a hydrophobic diamide ligand in the organic phase and a hydrophilic tetrasulfonated bis-triazine ligand in the aqueous phase is able to separate Am(III) from Eu(III) by selective Am(III) complex formation across a range of nitric acid concentrations with very high selectivities, and without the use of buffers. In contrast, disulfonated bis-triazine ligands are unable to separate Am(III) from Eu(III) in this system. The greater ability of the tetrasulfonated ligands to retain Am(III) selectively in the aqueous phase than the corresponding disulfonated ligands appears to be due to the higher aqueous solubilities of the complexes of the tetrasulfonated ligands with Am(III). The selectivities for Am(III) complexation observed with hydrophilic tetrasulfonated bis-triazine ligands are in many cases far higher than those found with the polyaminocarboxylate ligands previously used as actinide-selective complexing agents, and are comparable to those found with the parent hydrophobic bis-triazine ligands. Thus we demonstrate a feasible alternative method to separate actinides from lanthanides than the widely studied approach of selective actinide extraction with hydrophobic bis-1,2,4-triazine ligands such as CyMe4-BTBP and CyMe4-BTPhen.

SAXS study of monodispersed silica nanospheres obtained by an amino acid route

Spherical silica nanoparticles were prepared using a basic amino acid catalysis route and the kinetics of the particles growth was investigated by small angle X-ray scattering (SAXS). L-arginine was used in the polar aqueous phase as the basic catalyst whereas the tetraethylorthosilicate (TEOS) was dissolved in the cyclohexane oil phase as the silicate monomer source. The SAXS measurements were taken in the aqueous phase at different reaction times. A high degree of monodispersity was clearly evidenced for the spherical nanoparticles as a result of the pronounced high-order oscillations observed in the SAXS curves. The SAXS data show that the particles number density remains unchanged since both the particle size as well as the volume fraction gradually increase. This process was discussed based on a reaction-controlled addition of monomer species at the surface of the growing particles. Consequently, the monodispersed spherical nanoparticles radius can as such be finely tuned from 7 to 12 nm by varying the reaction time. (C) 2010 Elsevier B.V. All rights reserved.

Estudo das propriedades de eletrocatalisadores de Pt-Ru nanoparticulados preparados via microemulsão para oxidação de metanol

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Craqueamento termocatalítico do óleo de fritura residual

Neste trabalho foi estudado o processo de craqueamento termocatalítico do óleo de fritura nas escalas de bancada e piloto, variando-se o percentual do catalisador carbonato de sódio de 5 e 10% m/m em relação a matéria prima utilizada e temperatura de 440 ºC. O objetivo foi obter misturas de hidrocarbonetos ricas na fração diesel. O óleo de fritura neutralizado e seco foi caracterizado em relação ao Índice de Acidez, Índice de saponificação, Viscosidade Cinemática, Densidade e Índice de Refração. Após o craqueamento, o produto líquido obtido foi purificado por decantação da fase aquosa e filtração simples em escala de bancada. Esse produto foi fracionado por destilação fracionada e os condensados foram coletados em um funil de decantação de acordo a faixa de destilação da gasolina (40ºC-175ºC), querosene (175ºC-235ºC), diesel leve (235°C-305ºC) e diesel pesado (305ºC-400 ºC). Foi realizada a caracterização tanto físico química quanto da composição dos produtos líquidos e suas respectivas frações. Também foi realizada a evolução do processo de craqueamento em escala piloto, acompanhando o comportamento das características físico químicas e de composição do produto formado no decorrer do processo de craqueamento. Os resultados mostraram que o catalisador carbonato de sódio forneceu produtos de baixa acidez e com boas características para uso como combustível. A variação do percentual de catalisador influencia significamente as propriedades físico químicas e composição tanto do produto quanto de suas frações. Verificou-se, ainda, que o craqueamento termocatalítico do óleo de fritura propicia a formação de hidrocarbonetos ricos na fração do diesel (19,16% diesel leve e 41,18% diesel pesado para o teste com 10% de Na₂CO₃ e de 13,53% leve e 52,73% diesel pesado para o teste com 5% de Na₂CO₃ ). Os intervalos de tempos finais do craqueamento geram um combustível com baixo teor de acidez e com propriedades físico químicas em conformidade a norma especificada para o diesel mineral.