CHAPTER I INTRODUCTION 1. Introduction 1.1. Antioxidant Billions of dollars are spent each year on antioxidant supplements (nearly $2 billion, in fact, just on beta carotene and vitamins C and E), believing they will dramatically lower the risk of cancer, heart disease, and memory loss. Most experts, however, are convinced that taking antioxidants is not a shortcut to good health or the answer to staying young [1]. Oxidation is a chemical reaction that transfers electrons or hydrogen from a substance to an oxidizing agent. Oxidation reactions can produce free radicals. In turn, these radicals can start chain reactions. When the chain reaction occurs in a system, it can cause damage to the system. Antioxidants terminate these chain reactions by removing free radical intermediates, and inhibit other oxidation reactions. They do this by being oxidized themselves, so antioxidants are often reducing agents such as thiols, ascorbic acid, or polyphenols. Free radicals are believed to play a role in preventing the development of such chronic diseases as cancer, heart disease, stroke, Alzheimer's disease, rheumatoid arthritis, and cataracts. Generation of free radicals not only affects the biological system, it also affects the lipids [2]. Electron transfer is one of the fundamental processes in chemistry. The passage of an electron or a pair of electrons from a donor (reducing species) to an acceptor (oxidizing species) results in a change in properties of both partners in the reaction [3]. A typical schematic of oxidation reaction is given in Figure 1.1. Oxidation was once defined as the incorporation of oxygen into a substance, but now can be more precisely defined as the conversion of a chemical substance into another having fewer electrons. The propensity of chemical compounds to undergo reduction or oxidation has been studied for nearly 300 years, probably beginning with the Becher-Stahl theory of combustion, popularly known as the "phlogiston theory," formulated in the early 18th century [2, 4]. 1 Figure.. 1.1 : Schematic diagram of redox reaction Oxidative stress occurs when the production of free radicals is beyond the protective capability of the antioxidant defenses. Free radicals are chemically active atoms or molecular fragments that have a charge due to an excess or deficient number of electrons. Examples of free radicals are the superoxide anion, hydroxyl radical, transition metals such as iron and copper, nitric acid, and ozone [2, 5]. Damage by free radicals is impossible to avoid.. Free radicals arise from sources both inside (endogenous) and outside (exogenous) our bodies. Oxidants that develop from processes within our bodies form as a result of normal aerobic respiration, respiration metabolism, and inflammation. Exogenous free radicals form from environmental factors such as pollution, sunlight, strenuous exercise, X-rays, X smoking and alcohol (Figure 1.2) [6]. Figure Figure.1.2 : Reasons for free radical formation 2 1.2. The Antioxidant’s Function Antioxidants block the process of oxidation by neutralizing free radicals. In doing so, the antioxidants themselves become oxidized. That is why there is a constant need for antioxidant replenishment. How they work can be classified in one of the following two ways: • Chain-breaking - When a free radical releases or accepts an electron, a second radical is formed. This molecule then turns around and does the same thing to a third molecule, further continuing the generation of unstable products. • Preventive - Antioxidant enzymes like superoxide dismutase, catalase and glutathione peroxidase prevent oxidation by reducing the rate of chain initiation. That is, by scavenging initiating radicals, such antioxidants can thwart an oxidation chain from ever setting in motion [2, 4]. Some phytochemicals that are currently under study for their antioxidant activities are listed in table 1.1. Phytochemical Source Allyl sulfides Onions, garlic, leeks, chives Carotenoids (e.g., lycopene, lutein, zeaxanthin) Tomatoes, carrots, watermelon, kale, spinach Curcumin Turmeric Flavonoids (e.g., anthocyanins, resveratrol, quercitin, catechins) Grapes, blueberries, strawberries, cherries, apples, grapefruit, cranberries, raspberries, blackberries Glutathione Green leafy vegetables Indoles Broccoli, cauliflower, cabbage, Brussels sprouts, bok choy Isoflavones (e.g., genistein, daidzeins) Legumes (peas, soybeans) Isothiocyanates (e.g., sulforaphane) Broccoli, cauliflower, cabbage, Brussels sprouts, bok choy Phytochemical Lignans Source Seeds (flax seeds, sunflower seeds) 3 Monoterpenes Citrus fruit peels, cherries, nuts Phenols, polyphenols, phenolic compounds (e.g., ellagic acid, ferulic acid, tannins) Grapes, blueberries, strawberries, cherries, grapefruit, cranberries, raspberries, blackberries, tea Saponins Beans, legumes Table 1.1: Sources of antioxidants from plants 1.3. CLASSIFICATION OF ANTIOXIDANTS Antioxidants may be broadly grouped according to their mechanism of action: primary or chain breaking antioxidants, and secondary or preventive antioxidants. According to this classification, some antioxidants exhibit more than one mechanism of activity, therefore, referred to as multiple-function antioxidants. Another commonly used classification categorizes antioxidants into primary, oxygen scavenging, and secondary, enzymatic and chelating/sequestering antioxidants. However, synergistic antioxidants are not included in this classification. During the past two decades, several naturally occurring compounds have been added into the list of antioxidants that are effective against oxidation of unsaturated fats and oils and most of them fall into the multifunctional category. Classification of antioxidants according to the mode of activity as primary and secondary is preferred in this discussion. 1.3.1. Primary Antioxidants Primary antioxidants are also referred to as type 1 or chain-breaking antioxidants. Because of the chemical nature of these molecules, they can act as free radical acceptors/scavengers and delay or inhibit the initiation step or interrupt the propagation step of autoxidation. Figure 1.3 illustrates possible events that primary antioxidants may interfere with along the lipid autoxidation pathway. Primary antioxidants cannot inhibit photosensitized oxidation or scavenge singlet oxygen. ROO* + AH ROOH +A* R* + AH RH +A* ROO* + A* RO**OA RO* + AH ROH + A* 4 RO* + A* RO*A A* + A* AA Figure. 1.3: Mechanism of primary antioxidant activity The first kinetic study of antioxidant activity was conducted by Boland and tenHave [7]. The primary antioxidants (AH) react with lipid and peroxy radicals (ROO*) and convert them to more stable, nonradical products as shown in Figure. 1.3. These antioxidants are capable of donating a hydrogen atom to lipid radicals and produce lipid derivatives and antioxidant radicals (A*) that are more stable and less readily available to participate in propagation reactions. Primary antioxidants have higher affinities for peroxy radicals than lipids and react predominantly with peroxy radicals. Many reasons have been listed for their high affinity. Propagation is a slow step in lipid oxidation process; thus, peroxy radicals are found in comparatively larger quantities than other radicals. In addition, peroxy radicals have lower energies than alkoxy radicals; therefore, they react more readily with the low energy hydrogen of primary antioxidants than with unsaturated fatty acids. As the free radical scavengers are found in low concentration, they do not compete effectively with initiating radicals (e.g., hydroxyl radicals) [8, 9]. Therefore, primary antioxidants inhibit lipid oxidation more effectively by competing with other compounds for peroxy radicals, and are able to scavenge peroxy- and alkoxy-free radicals formed during propagation and other reactions in autoxidation. The antioxidant radical produced because of donation of a hydrogen atom exhibits very low reactivity toward the unsaturated lipids or oxygen; therefore, the rate of propagation is very slow. The antioxidant radicals are relatively stable and do not initiate a chain or free radical propagating autoxidation reaction unless present in very large quantities. These free radical interceptors react with peroxy radicals (ROO*) to stop chain propagation thereby inhibiting the formation of peroxides. Also, the reaction with alkoxy radicals (RO*) decreases the decomposition of hydroperoxides to harmful degradation products. Most of the primary antioxidants that act as chain breakers or free radical interceptors are mono- or polyhydroxy phenols with various ring substitutions. The antioxidant effectiveness is influenced by the chemical properties of the compound including hydrogen bond energies, resonance delocalization, and susceptibility to autoxidation. The ability of the primary antioxidant molecule to donate a hydrogen atom to the free radical is the initial requirement. The ability of the free radical interceptor (scavenger) to donate a hydrogen atom to a free radical can be predicted from standard one-electron potentials. Each 5 oxidizing species is capable of accepting an electron (or H atom) from any reduced species. species That means when the standard one-electron one electron reduction potential is concerned, the free radical scavengers that have reduction potential below peroxy radicals radicals are capable of donating an H atom to peroxy radical and form a peroxide. The resulting antioxidant radical should be of low energy, ensuring the lesser possibility of catalyzing the oxidation of other molecules. The formed antioxidant radical is stabilized stabilized by delocalization of the unpaired electron around the phenol ring to form a stable resonance hybrid (Figure ( 1.4)) and as a result attains attain low-energy levels [10]. Figure. 1.4: Stable resonance structure of phenoxy radical of phenolic antioxidant Antioxidant tioxidant radicals are capable of participating in termination reactions with peroxy, alkoxy,, or antioxidant radicals removing reactive free radicals from the system. Dimers of antioxidant molecules are usually found in fats and oils containing phenolic antioxidants. an This is a good indication that antioxidant radicals readily undergo termination reactions and form dimers as proposed in Figure 1.3.. When considering all of these, the primary antioxidants or free radical scavengers can inactivate at least two free radicals, the first one during the interaction with peroxy radical and the second in the termination reaction with another peroxy radical. The compounds that exhibit primary antioxidant activity include polyhydroxy phenolics as well as the hindered phenolics. phenolics. There are several synthetic ring substituted phenolics as well as naturally occurring phenolic compounds that may perform via the primary antioxidant mechanism. mechanism A common feature of all of these antioxidants is that they are mono- or polyhydroxy phenols enols with various ring substitutes (Figure ( 1.5 1.5). 6 Figure. 1.5 : Chemical structure of synthetic phenolic antioxidants commonly used in fats and oils. Substitution with electron-donating electron donating group/s ortho and/or para to the hydroxyl group of phenol increases the antioxidant activity of the compound by an inductive effect (e.g., 2,6-di2,6 tert-butyl-4-methylphenol methylphenol or BHA). Thus, the presence of a second hydroxyl group in the 22 (ortho) or the 4-position position (para) of a phenol increases the antioxidant activity (e.g., TBHQ). In the dihydroxybenzene derivatives, the semiquinoid radical produced initially can be further oxidized to a quinone by reacting with another lipid radical as shown in Figure 1.6. This semiquinoid radical may disproportionate into a quinone and a hydroquinone hydroquinone molecule, and the process of this conversion contributes to antioxidant activity as peroxy peroxy radical scavenging potential [11, 12]. Table 1.22 summarizes most commonly used primary antioxidants in fats and oils and lipid containing foods. Substitution Substitution with butyl or ethyl group/s para to the hydroxy groups also enhances the antioxidant activity. Substitution of branched alkyl groups at ortho positions enhance the ability of the molecule to form a stable resonance structure that reduces the antioxidant nt radical’s participation in propagation reactions [13,, 14]. 7 Figure. 1.6 : Mechanism of antioxidant activity in dihydroxy benzene derivative To be most effective, primary antioxidants should be added during the induction or initiation stage of the autoxidation reaction cascade. Antioxidants can then scavenge the formed free radicals, as the cyclical propagation steps have not occurred at this stage. Addition of primary antioxidants to a lipid that already contains substantial amounts of lipid peroxides may result in loss of antioxidant activity [15]. Table 1.2 provides examples of some of these compounds that exhibit secondary antioxidant activity. Natural Synthetic Carotenoids Butylated hydroxyanisole (BHA) Flavonoids Butylated hydroxytoluene (BHT) Phenolic acids Ethoxyquin Tocopherols and Tocotrienols Propyl gallate (PG), Tertiary butylhydroquinone (TBHQ) Table 1.2 : Commonly used primary antioxidants. 1.3.2. Secondary Antioxidants Secondary antioxidants are also classified as preventive or class II antioxidants. They offer their antioxidant activity through various mechanisms to slow the rate of oxidation reactions. Unlike primary antioxidants, secondary antioxidants do not convert free radicals into stable molecules. They act as chelators for pro-oxidant or catalyst metal ions, provide H+ to primary antioxidants, decompose hydroperoxide to non-radical species, deactivate singlet 8 oxygen, absorb ultraviolet radiation, or act as oxygen scavengers. They often enhance the antioxidant activity of primary antioxidants. Table 1.3 provides examples of some of these compounds that exhibit secondary antioxidant activity. Activity Compounds in use Metal chelation Citric, Malic, Succinic and Tartaric acids, Ethylenediaminetetraacetic acid, phosphates. Oxygen scavenging and reducing agents Ascorbic acid, Ascorbyl palmitate, Erythorbic acid, Sodium erythorbate, Sulfites Singlet oxygen quenching Carotenoids (Lycopene and Lutein) Table 1.3: Compounds that exhibit secondary antioxidant activity 1.3.2.1. Sequestering/Chelating Agents Sequestering/chelating agents or metal deactivators are heavy metals with two or more valence states with a suitable oxidation-reduction potential between them (e.g., Co, Cu, Fe, Mn, etc.), shorten the induction period and increase the maximum rate of oxidation of lipids. Trace amounts of these metal ions are present in lipid-containing foods coming from naturally present compounds or included during processing operations. The effectiveness of copper as a catalyst for hydroperoxide decomposition has been reported [15, 16]. Transition metals such as iron exhibit low solubility at pH values near neutrality [17]. That means in foods, transition metals may exist chelated to other compounds. Many compounds form complexes with these metals and change their catalytic activity. Chelation can increase the pro-oxidant activity of transition metals by making them more non-polar, and some can increase oxidative reactions by increasing metal solubility or altering redox potential [18]. According to Graf and Eaton, chelators may exert antioxidant activity by prevention of metal redox cycling, occupation of all metal coordination sites, and formation of insoluble metal complexes and steric hindrance of interactions between metals and lipids or oxidation intermediates (e.g., peroxides) [19]. Chelation of these metal ions or use of metal deactivators reduces the pro-oxidant activity by raising the energy of activation for initiation reactions. The most effective form of chelating agents are secondary antioxidants, which form s-bonds with metal ions because they reduce the redox potential and stabilize the oxidized form of the metal ion. Chelating agents such as heterocyclic bases that form p-complexes raise the redox potential and may accelerate metal-catalyzed hydroperoxide decomposition and act as pro-oxidants. 9 Multiple carboxylic acid compounds such as citric acid, ethylene diamine tetraacetic acid (EDTA), and phosphoric acid derivatives (polyphosphates and phytic acid) are commonly used in extending the shelf life of lipid-containing foods because of their metal chelating properties. Typically these chelators are water soluble, but citric acid exhibits solubility in lipids, which allows it to inactivate metals in the lipid phase [33]. Chelator’s activity depends on pH and the presence of other chelatable ions (e.g., Ca). Most food grade chelators are unaffected by food-processing operations and storage; however, polyphosphates may decrease their antioxidant activity because of possible hydrolysis by endogeneous phosphatases in foods, especially in raw meat [20]. 1.3.2.2. Oxygen Scavengers and Reducing Agents As oxygen is essential and is one of the reactants in the autoxidation process, scavenging of oxygen molecular species is one way of providing antioxidant activity. Ascorbic acid acts as a reducing agent and as an oxygen scavenger. Singlet oxygen is the excited state oxygen, and its inactivation is an effective way of preventing initiation of lipid oxidation. Carotenoids are capable of inactivating photoactivated sensitizers by physically absorbing their energy to form the excited state of the carotenoid. Later, the excited state carotenoid returns to ground state by transferring energy to the surrounding solvent. Other compounds found in food, including amino acids, peptides, proteins, phenolics, urates, and ascorbates also can quench singlet oxygen [20]. Compounds such as superoxide anion and peroxides do not directly interact with lipids to initiate oxidation; they interact with metals or oxygen to form reactive species. Superoxide anion is produced by the addition of an electron to the molecular oxygen. It participates in oxidative reactions because it can maintain transition metals in their active reduced state, can promote the release of metals that are bound to proteins, and can form the conjugated acid, perhydroxyl radical depending on pH, which is a catalyst of lipid oxidation. The enzyme superoxide dismutase that is found in tissues catalyzes the conversion of superoxide anion to hydrogen peroxide. Catalase is capable of catalyzing the conversion of hydrogen peroxides to water and oxygen [21]. Glucose oxidase coupled with catalase is well used commercially to remove oxygen from foods, especially fruit juices, mayonnaise, and salad dressings [19]. Glutathione peroxidase that is found in many biological tissues also helps to control both lipid and hydrogen peroxides [22]. These enzymatic reactions help to 10 reduce various types of radicals that could be formed in lipid-containing biological systems. 1.4. Synthetic Antioxidants Synthetic antioxidants are manmade and are used to stabilize fats, oils, and lipid containing foods and are mostly phenolic-based. Many compounds are active as antioxidants, but only a few are incorporated into food because of strict safety regulations. These phenolic derivatives usually contain more than one hydroxyl or methoxy group. Ethoxyquin is the only heterocyclic, N-containing compound that is allowed for use in animal feeds. Synthetic phenolic antioxidants are p-substituted, whereas the natural phenolic compounds are mostly o-substituted. The p-substituted phenolic antioxidants are preferred because of their lower toxicity. The m-substituted compounds are inactive. Synthetic phenolic antioxidants are always substituted with alkyl groups to improve their solubility in fats and oils and to reduce their toxicity [23, 24]. The primary mechanism of activity of these antioxidants is similar to those of primary antioxidants. An antioxidant molecule reacts with a peroxy radical produced by the oxidizing lipid, thus forming a hydroperoxide molecule and an antioxidant free radical. A similar path of reaction may occur with the alkoxy free radicals formed during the decomposition of hydroperoxides. The antioxidant free radical so formed may be deactivated by a lipid peroxy or an alkoxy radical or with another antioxidant radical. Dimers and even trimers of antioxidant molecules are formed because of the reaction of antioxidant radicals, and these may have a modest antioxidant activity of their own. With the help of synergists such as ascorbic acid, some of these original antioxidant molecules may be regenerated. Quinones are formed from phenolic antioxidants by reaction with peroxy radicals. When antioxidants are present in excess, the reaction of antioxidant free radicals with oxygen may become important; even their reaction with polyunsaturated fatty acids has some impact on the course of oxidation [24]. 1.4.1. Butylated Hydroxyanisole (BHA) BHA exists as a mixture of two isomers, 3-tertiary-butyl-4-hydroxyanisole (90%) and 2-tertiary-butyl-4-hydroxyanisole (10%). The 3-isomer shows a higher antioxidant activity than the 2-isomer. BHA is commercially available as white, waxy flakes and is lipid soluble. BHA exhibits good antioxidant activity in animal fats as compared to vegetable oils. It has good carry-through properties but is volatile at frying temperatures. When BHA is included 11 into packaging materials it easily migrates to the containing food and delays lipid oxidation [25, 26]. 1.4.2. Butylated Hydroxytoluene (BHT) BHT is also a monohydroxyphenol and is widely used in foods. This fat-soluble antioxidant is available as a white crystalline compound. BHA is less stable than BHT at high temperatures and has lower carry-through properties. BHA and BHT act synergistically, and several commercial antioxidant formulations contain both of these antioxidants. BHT is effectively used in oxidation retardation of animal fats. It is postulated that BHA interacts with peroxy radicals to produce a BHA phenoxy radical. This BHA phenoxy radical may abstract a hydrogen atom from the hydroxyl group of BHT. BHA is regenerated by the H radical provided by BHT. The BHT radicals so formed can react with a peroxy radical and act as a chain terminator [27]. 1.4.3. Tertiary-Butylhydroquinone (TBHQ) TBHQ is a diphenolic antioxidant and is widely used in a variety of fats and oils. TBHQ has excellent carry-through properties and is a very effective antioxidant for use in frying oils. It is available as a beige color powder that is used alone or in combination with BHA or BHT. TBHQ can be used in a variety of lipid-containing foods and fats and oils. Chelating agents such as monoacyglycerols and citrates enhance the activity of TBHQ, mainly in vegetable oils and shortenings. TBHQ reacts with peroxy radicals to form a semiquinone resonance hybrid. The semiquinone radical intermediate may undergo different reactions to form more stable products; they can react with one another to form dimers, dismutate, and regenerate as semiquinones; and they can react with another peroxy radical [28]. 2. Biodiesel Relentless efforts in pursuing human comfort and luxury have led to the deterioration of our environment paving the way for global warming. Automobiles that consume fossil fuels lead to production of tones of toxic gases like carbon monoxide, carbon dioxide, oxides of nitrogen, oxide of sulphur, hydro-carbons etc., that not only cause pollution but also reasons for critical changes in climate. Depletion of fossil fuels and a steady increase in their price necessitate the search of alternative renewable sources of fuels that will meet the increasing energy demand. One possible alternative to fossil fuel is the use of oils of plant 12 origin like vegetable oils and tree borne oil seeds. These alternative diesel fuels can be termed as biodiesel. Such fuel is biodegradable, free of sulphur and aromatic compounds, non-toxic, renewable and has low emission profiles as compared to petroleum diesel. The fuel must be technically feasible, economically competitive, environmentally acceptable and readily available. Chemically, the oils/fats consist of triglyceride molecules of three long chain fatty acids that are ester bonded to a single glycerol molecule. These fatty acids differ by the length of carbon chains, the number, orientation and position of double bonds in these chains. Thus biodiesel refers to lower alkyl esters of long chain fatty acids, which are synthesized either by transesterification with lower alcohols or by esterification of fatty acids [26]. 2.1. GLOBAL STATUS OF BIODIESEL With the crude fossil fuel prices near all-time high, biodiesel has emerged as one of the fastest growing industries worldwide. Several countries, especially United States and members of European Union are actively supporting the production of biodiesel from the agriculture sector. It is interesting to note that 75% of the total biodiesel production comes from European countries. This is mainly due to substantial support from the European government such as consumption incentives (fuel tax reduction) and production incentive (tax incentives and loan guarantees) which is expected to catalyze the growth of biodiesel market in the next ten years. The United States has spent around US$ 5.5 billion to 7.3 billion a year to accelerate biofuel production during the last few years. As a result, around 450 million gallons of biodiesel was produced in the United States in the year 2007 compared to only 25 million gallons in 2004 [25]. This 1700% rise was indeed a shocking increase in the entire history of biodiesel production. However, by the year 2020, it is predicted that biodiesel production from Brazil, China, India and some South East Asian countries such as Malaysia and Indonesia could contribute to as much as 20% of the total global production. The driving forces for development of biodiesel in these countries are economic, energy and environmental security, improving trade balances and expansion of agriculture sector. In addition, Brazil, China and India each have set targets to replace 5 to 20% of total diesel with biodiesel by the year 2010 with emphasis on second generation non-edible feedstock. Figure 1.7 illustrates the world biodiesel production and capacity till 2008 [29]. 13 Figure. 1.7: Biodiesel production and capacity till 2008 14 2.2. COMPARISION OF PETRODIESEL Vs BIODIESEL Diesel exhaust consists of hundreds of gas-phase, semi-volatile, and particle-phase organic compounds that are produced through the combustion of fossil fuel [30]. Increasing energy demand, climate change and carbon dioxide (CO2) emission from fossil fuels make it a high priority to search for low-carbon energy resources. Biodiesels represent a key target for the future energy market that can play an important role in maintaining energy security. It is primarily considered as a potentially cheap, low-carbon energy source. Most life-cycle studies of biodiesel have found that bio-ethanol made from corn or sugarcane generally reduces greenhouse gases, replacing gasoline (petrol). Biodiesel have been increasingly explored as a possible alternative source to gasoline with respect mainly to transport. To summarise, interest in biodiesel is increasing for a number of reasons: 1. Reduced reliance on fossil fuels 2. Reduction in greenhouse gas emission 3. National independent security of fuel supply 4. Employment and economic benefits through the development of a new fuel production. 2.3. TRANSESTERIFICATION Vegetable oils cannot be used directly due to high viscosity, polyunsaturated characters and low volatility [31]. To solve these limitations, vegetable oil or animal fats are reacted with simple alcohol to produce fatty acid methyl esters (FAME). Transesterification is an important method of converting vegetable oils to biodiesel. Transesterification (also called alcoholysis) is the reaction of a fat or oil with an alcohol to form esters and glycerol. A catalyst is usually used to improve the reaction rate and yield. Excess alcohol is used to shift the equilibrium toward the product because of reversible nature of reaction. For this purpose primary and secondary monohybrid aliphatic alcohols having 1-8 carbon atoms are used [32]. 15 2.3.1. CHEMISTRY OF TRANSESTERIFICATION Transesterification also called alcoholysis which is the displacement of alcohol from an ester by another alcohol in a process similar to hydrolysis except that an alcohol is used instead of water. This has been widely used to reduce the viscosity of the triglycerides [33]. Figure 1.8 represents a typical transesterification reaction Figure. 1.8: Basic transesterification reaction 2.3.2. TYPES OF TRANSESTERIFICATION 2.3.2.1. Alkali Catalyzed Transesterification The reaction mechanism for alkali catalyzed transesterification was formulated in three steps [34]. The first step is an attack on the carbonyl carbon atom of the triglyceride molecule by the anion of the alcohol (methoxide ion) to form a tetrahedral intermediate that reacts with an alcohol to regenerate the anion of alcohol. The base-catalyzed process is relatively fast but is affected by water content and free fatty acids of oils or fats. Free fatty acids can react with base catalysts to form soaps and water. Soap not only lowers the yield of alkyl esters but also increases the difficulty in the separation of biodiesel and glycerol, and washing with water because of the formation of emulsions [34]. 2.3.2.2. Acid Catalyst Transesterification An alternative process is to use acid catalysts that some researchers have claimed are more tolerant of free fatty acids [35]. The protonation of carbonyl group of the ester leads to the formation of carbocation, which after a nucleophilic attack of the alcohol produces a tetrahedral intermediate. This intermediate eliminates glycerol to form a new ester. Generally, acid-catalyzed reactions are used to convert FFAs to esters, or soaps to esters as a pretreatment step for high FFA feedstocks [36]. Acid catalyst process requires excess alcohol, hence the transesterification reactor and alkali distillation column of acid-catalyzed process are larger than alkali catalyzed process for same biodiesel production 16 capacity. High conversion efficiencies with acid-catalyzed transesterification can be achieved by increasing the molar ratio of alcohol to oil, reaction temperature, concentration of acid catalyst and the reaction time [37]. Figure 1.10: Mechanism of alkali catalyst transesterification. Figure. 1.11: Mechanism of acid catalyst transesterification. 2.3.2.3. Lipase Catalysed Transesterification This transesterification process was similar to alkali transesterification, except that the ratio of catalyst and solvent stirring time was varied. Lipase was used as catalyst in this transesterification [38]. The process is explained as follows: Figure. 1.12: Steps in production of biodiesel using lipase. Lipases are known to have a property to act on long-chain fatty alcohols better than on short-chain ones. Thus, in general, the efficiency of the transesterification of triglycerides with methanol (methanolysis) is likely to be very low compared to that with ethanol in systems with or without a solvent. Various studies have been conducted with different catalyst, alcohol and methanol molar 17 ratios at different temperatures Linko et. al. have demonstrated the production of a variety of biodegradable esters and polyesters with lipase as the biocatalyst [39]. TYPE OF CATALYST ADVANTAGES • Very fast reaction rate - 4000 times faster than acid-catalyzed transesterification Homogeneous base catalyst • Reaction can occur at mild reaction condition and is less energy intensive • Catalysts such as NaOH and KOH are relatively cheap and widely available • Relatively faster reaction rate compared to acid-catalyzed transesterification • Reaction can occur at mild reaction conditions and is less energy intensive Heterogeneous base catalyst • Easy separation of catalyst from product • Catalyst reuse and regeneration highly possible DISADVANTAGES • Sensitive to FFA content in the oil • Soap formation occurs if the FFA content in the oil is more than 2 wt.% • Too much soap formation decreases biodiesel yield and hinders product purification especially generating huge amount of wastewater • Poisoning of the catalyst when exposed to ambient air • Sensitive to FFA content in the oil due to its basicity • Soap formation occurs if the FFA content in the oil is more than 2 wt.% • Too much soap formation decreases biodiesel yield and hinders product purification • Leaching of catalyst active sites may result in product contamination 18 • • TYPE OF T Heterogeneous acid catalyst • • • ADVANTAGES Insensitive to FFA and water content in the oil Preferred method if low-grade oil is used Esterification and transesterification occur simultaneously Easy separation of catalyst from product Catalyst reuse and regeneration highly possible • • • • DISADVANTAGES Complicated catalyst synthesis procedures lead to higher cost Normally, high reaction temperature, high alcohol to oil molar ratio and long reaction time are required Energy intensive Leaching of catalyst active sites may result in product contamination Table 1.4 : Advantages and disadvantages of various types of catalysts 2.3.2.4. Supercritical Transesterification The simple transesterification process is confronted with two problems, i.e. the process is relatively time consuming and it needs separation of the catalyst and saponified impurities from the biodiesel. The first problem is due to the phase separation of the vegetable oil/methanol mixture, which may be dealt with by vigorous stirring. These problems were not faced in the supercritical methanol method of transesterification. This is perhaps due to the fact that the tendency of two-phase formation of vegetable oil/methanol mixture was not encountered and a single phase was formed due to decrease in the dielectric constant of methanol in the supercritical state. As a result, the reaction was found to be complete in a very short time of about 2–4 min. Further, since no catalyst was used, the purification on biodiesel was much easier, trouble free and environment friendly [40]. 2.3.3. PROCESS VARIABLES The most important variables that influence the transesterification reaction are: 1. Reaction temperature 2. Ratio of alcohol to oil 3. Catalyst 4. Mixing intensity 5. Purity of reactants 2.3.3.1. Reaction Temperature 19 Previous reports have revealed that the rate of reaction is strongly influenced by the reaction temperature. However, the reaction is conducted close to the boiling point of methanol (60–70°C) at atmospheric pressure for a given time. Such mild reaction conditions require the removal of free fatty acids from the oil by refining or pre-esterification. Therefore, degummed and deacidified oil is used as feedstock [41]. Pre-treatment is not required if the reaction is carried out under high pressure (9000 kPa) and high temperature (240ºC), where simultaneous esterification and transesterification take place with maximum yield obtained at temperatures ranging from 60 to 80°C at a molar ratio of 6:1 [42]. 2.3.3.2. Ratio of Alcohol to Oil Another important variable is the molar ratio of alcohol to vegetable oil. As indicated earlier, the transesterification reaction requires 3 mol of alcohol per mole of triglyceride to give 3 mol of fatty esters and 1 mol of glycerol. In order to shift the reaction to the right, it is necessary to either use excess alcohol or remove one of the products from the reaction mixture. The second option is usually preferred for the reaction to proceed to completion. The reaction rate was found to be highest when 100% excess methanol was used. A molar ratio of 6:1 is normally used in industrial processes to obtain methyl ester yields higher than 98% (w/w) [41]. 2.3.3.3. Catalysts Alkali metal alkoxides are found to be more effective transesterification catalysts compared to acidic catalysts. Sodium alkoxides are the most efficient catalysts, although KOH and NaOH can also be used. Transmethylation occurs in the presence of both alkaline and acidic catalysts [43]. As they are less corrosive to industrial equipment, alkaline catalysts are preferred in industrial processes. A concentration in the range of 0.5–1% (w/w) has been found to yield 94–99% conversion to vegetable oil esters [44] and further increase in catalyst concentration does not affect the conversion but adds to extra cost, as the catalyst needs to be removed from the reaction mixture after completion of the reaction. 20 2.3.3.4. Mixing Intensity It has been observed that during the transesterification reaction, the reactants initially form a two-phase liquid system. The mixing effect has been found to play a significant role in the slow rate of the reaction. As phase separation ceases, mixing becomes insignificant. The effect of mixing on the kinetics of the transesterification process forms the basis for process scale-up and design. 2.3.3.5. Purity of Reactants Impurities in the oil affect the conversion level considerably. It is reported that about 65–84% conversion into esters using crude vegetable oils has been obtained as compared to 94– 97% yields refined oil under the same reaction conditions [41]. The free fatty acids in the crude oils have been found to interfere with the catalyst. This problem can be solved if the reaction is carried out under high temperature and pressure conditions. 2.3.4. METHODS TO ANALYZE BIODIESEL Various analytical methods have been developed for analyzing mixtures containing fatty acid esters and mono-, di-, and triglycerides obtained by transesterification. Analyses have been performed by thin layer chromatography/flame ionization detector (TLC/FID), gas chromatography (GC), high performance liquid chromatography (HPLC), gel permeation chromatography (GPC), proton nuclear magnetic resonance 1 ( H-NMR) and near infra-red spectroscopy (NIR). Most reports on the use of GC for biodiesel analysis employ flame-ionization detectors (FID), although the use of mass spectrometric detector (MSD) was employed in some cases to eliminate any ambiguities about the nature of the eluting materials since mass spectra unique to individual compounds would be obtained [43]. 2.3.5. Disadvantages of using Biodiesel One of the major drawbacks in maintaining the quality of biodiesel and its widespread commercialization is its oxidation stability. Unlike petroleum diesel fuel, the nature of biodiesel makes it more susceptible to oxidation or auto oxidation during long term storage. Storage conditions like exposure to water and exposure to oxygen, which are naturally present in the ambient air, influence the rate of oxidation. The biodiesel stability generally depends upon the fatty acid composition of the parent oil. Unsaturated fatty acids are significantly more reactive to oxidation than saturated compounds. With respect to long-chain 21 FAMEs, polyunsaturated fatty esters are approximately twice as reactive to oxidation as monounsaturated esters. This is attributed to the fact that these unsaturated fatty acid chains contain the most reactive sites, which are particularly susceptible to free-radical attack. While bis-allylic methylenes are much more susceptible to oxidation, biodiesel stability can also depend upon the presence of allylic methylenes in the hydrocarbon chain [45]. The bis-allylic configurations, where the central methylene group is activated by the two double bonds (i.e., -CH=CH-CH2-CH=CH-), react with oxygen via the auto oxidation mechanism, with the radical chain reaction steps of initiation, propagation, chain branching, and termination. During these reaction steps, several products can be formed, such as peroxides and hydro-peroxides, low molecular weight organic acids, aldehydes and keto compounds, alcohols, as well as high molecular-weight species (dimers, trimers, and cyclic acids) via polymerization mechanisms. The use of antioxidant additives can help slow the degradation process and improve fuel stability up to a point [46 - 50]. Fuel properties degrade during long-term storage as follows: (i) oxidation or autoxidation from contact with ambient air; (ii) thermal or thermal-oxidative decomposition from excess heat; (iii) hydrolysis from contact with water or moisture in tanks and fuel lines; or (iv) microbial contamination from migration of dust particles or water droplets containing bacteria or fungi into the fuel [51]. Monitoring the effects of auto oxidation on biodiesel fuel quality during long-term storage presents a significant concern for biodiesel producers, suppliers, and consumers [52]. Engine and injection pump producers insist on the parameter for oxidation stability which was finally fixed at a minimum limit of a 6-hour induction period at 110 °C [53]. The method adopted for determination of the oxidation stability is the so called Rancimat method which is commonly used in the vegetable oil sector. Especially high contents of unsaturated fatty acids, which are very sensitive to oxidative degradation, lead to very low values for the induction period. Thus, even the conditions of fuel storage directly affect the quality of the product. Several studies showed that the quality of biodiesel over a longer period of storage strongly depends on the tank material as well as on contact to air or light. Increase in viscosities and acid values and decreases in induction periods were observed during such storage [54, 55]. To improve the storage and oxidative stability of biodiesel, it has become a necessacity to find new additives. Intensive research is underway in this area to 22 investigate storage stability of biodiesel as highlighted by literature presented in chapters IV and V. The objective of this study was to investigate the oxidative stability and storage stability of Pongamia pinnata and Jatropha curcus oil methyl esters. The Rancimat procedure for oxidation stability and the ASTM procedure for storage stability have been used in this study. Using different antioxidants in different concentrations, the fuel properties such as acid value (AV), kinematic viscosity (KV) and peroxide value (PV) of Pongamia biodiesel (PBD) and Jatropha biodiesel (JBD) were determined at regular periods of time. Chapter IV discusses the effect of commercially available antioxidants such as BHT, BHA, GA, TBHQ and PY (Figure 1.5) on the stability of biodiesel. 3. Natural Antioxidants Use of plant parts (barks, leaves, seeds, etc.) and their extracts to preserve food from developing a rancid taste is a practice that has continued since prehistoric times. There is evidence that even for the industrial materials plant-based components were used as antidrying agents to prevent oxidation and polymerization of polyunsaturated fatty acid-rich plant oils [55, 56]. The high compatibility of biodiesel with petroleum diesel characterizes it as a good alternative capable of supplying most of the existing diesel fleet without great adaptations. It is also biodegradable and renewable, has a lubricant capacity in the pure form and is competitive with diesel in terms of fuel properties [52]. However, unlike fossil fuels that are relatively inert and maintain their essential characteristics with little alteration during storage, biodiesel degrades with time and can be altered due to the action of air, light, temperature and moisture. Contact with contaminants, both of inorganic and microbial nature, can also tend to introduce variations in product quality. Biodiesel is prone to undergo oxidative degradation when it is exposed to atmospheric air [49, 52]. In order to inhibit or delay oxidation in oils, fats and fatty foods, phenolic chemical compounds known as synthetic antioxidants and/or stabilizers are used [54]. Antioxidants occur naturally in vegetable oils and the most common are the tocopherols. However, some plant oil production processes include a distillation step to purify the triglycerides. The biodiesel obtained from these oils normally has little or no natural antioxidants so they become less stable and therefore antioxidants need to be applied to increase the biofuel stability and extend its properties for a longer period [56]. 23 Factors which influence the oxidative stability of biodiesel include fatty acid composition, natural antioxidant content, the level of total glycerin, and the conditions of fuel storage such as temperature, exposure to light and air, and tank material [58, 59, 60, 61]. Previous studies have found that antioxidants can be effective in increasing the stability of biodiesel [58, 60, 62, 63]. However, these effects have not been fully elucidated and results have been inconclusive or conflicting. Sendzikiene et al. found that butylated hydroxyanisole (BHA) and butyl-4-hydroxytoluene (BHT) have nearly the same effect on the oxidative stability of rapeseed oil, and tallow-based biodiesel, and the optimal level of synthetic antioxidants was determined to be 400 ppm [60]. Mittelbach et al. reported that pyrogallol (PY), propylgallate (PG), and t-butylhydroquinone (TBHQ) could significantly improve the stability of biodiesel obtained from rapeseed oil, used frying oil, and beef tallow, whereas BHT was not very effective [64]. Moreover, Domingos et al. found that BHT had the highest effectiveness for refined soybean oil-based biodiesel, while BHA displayed little effectiveness [59]. Natural antioxidants are constituents of many fruits and vegetables and they have attracted great deal of public and scientific attention because of their anticarcinogenic potential. Biodiesel is an environment friendly liquid fuel similar to petrodiesel in combustion properties. A new alternative to delay the biodiesel oxidative degradation process may be the use of natural antioxidants present in spices, bearing in mind that they do not damage the environment and are easily obtained [65]. According to some studies, rosemary (Rosmarinus officinalis L.) and sage (Salvia officinalis L.) are the spices with the greatest antioxidant potential [65, 66]. The antioxidant activity of carnosol and carnosic acid, found in rosemary, was validated in an emulsion containing methyl linoleate [67]. According to Nakatani and Inatani, the addition of natural antioxidants such as carnosol and carnosic acid, at a 0.01% concentration, in a linoleic acid emulsion, have activity levels similar to those of the synthetic antioxidants BHA (butyl hydroxy anisole) and BHT (butyl hydroxy toluene) added in the same concentration [68]. Five different phenolic compounds were isolated from oregano (Origanum vulgare L.); all presented antioxidant activity and one of them was identified as rosmarinic acid [69]. Furthermore, the study carried out by Bragagnolo and Mariuti reported several other phenolic compounds that were isolated from oregano, including luteolin, pcoumaric acid, carvacrol, thymol, p-cimen, and campherol [70]. These findings demonstrate a great possibility of using these spices as good antioxidants and possible substitutes for the synthetic antioxidants, especially in mixtures consisting of unsaturated carbon compounds as 24 substrate. Numerous strong antioxidant compounds have been identified in fruits, vegetables [71, 72] and in different beverages [73]. For example, high concentrations of antioxidants have been found in berries [74], apples [75], and citrus fruits [76]. 3.1. Application of Antioxidants 3.1.1. As food preservatives Antioxidants are used as food additives to help guard against food deterioration. Exposure to oxygen and sunlight are the two main factors in the oxidation of food, so food is preserved by keeping in the dark and sealing it in containers or even coating it with wax, as with cucumbers. However, as oxygen is also important for plant respiration, storing plant materials in anaerobic conditions produces unpleasant flavors and unappealing colors [77]. Consequently, packaging of fresh fruits and vegetables contains about 8% oxygen atmosphere. Antioxidants are an especially important class of preservatives as, unlike bacterial or fungal spoilage, oxidation reactions still occur relatively rapidly in frozen or refrigerated food. These preservatives include natural antioxidants such as ascorbic acid (AA, E300) and tocopherols (E306), as well as synthetic antioxidants such as propyl gallate (PG, E310), tertiary butylhydroquinone (TBHQ), butylated hydroxyanisole (BHA, E320) and butylated hydroxytoluene (BHT, E321) [78]. The most common molecules attacked by oxidation are unsaturated fats; oxidation causes them to turn rancid. Since oxidized lipids are often discolored and usually have unpleasant tastes such as metallic or sulfurous flavors, it is important to avoid oxidation in fat-rich foods. Thus, these foods are rarely preserved by drying; instead, they are preserved by smoking, salting or fermenting. Even less fatty foods such as fruits are sprayed with sulfurous antioxidants prior to air drying. Oxidation is often catalyzed by metals, which is why fats such as butter should never be wrapped in aluminium foil or kept in metal containers. Some fatty foods such as olive oil are partially protected from oxidation by their natural content of antioxidants, but remain sensitive to photooxidation [79]. Antioxidant preservatives are also added to fat-based cosmetics such as lipstick and moisturizers to prevent rancidity. 3.1.2. Industrial Application Antioxidants are frequently added to industrial products. A common use is as stabilizers in fuels and lubricants to prevent oxidation, and in gasoline to prevent the polymerization that leads to the formation of engine-fouling residues [78, 79]. 25 In 2007, the worldwide market for industrial antioxidants had a total volume of around 0.88 million tons. This created revenue of about 3.7 billion US-dollars. They are widely used to prevent the oxidative degradation of polymers such as rubbers, plastics and adhesives that causes a loss of strength and flexibility in these materials [80]. Polymers containing double bonds in their main chains, such as natural rubber and polybutadiene, are especially susceptible to oxidation and ozonolysis, which can be protected by anti-ozonants. Solid polymer products start to crack on exposed surfaces as the material degrades and the chains break. The mode of cracking varies between oxygen and ozone attack, the former causing a "crazy paving" effect, while ozone attack produces deeper cracks aligned at right angles to the tensile strain in the product. Oxidation and UV degradation are also frequently linked, mainly because UV radiation creates free radicals by bond breakage. The free radicals then react with oxygen to produce peroxy radicals which cause further damage, often in a chain reaction. Other polymers susceptible to oxidation include polypropylene and polyethylene. The former is more sensitive owing to the presence of secondary carbon atoms present in every repeat unit. Attack occurs at this point because the free radical formed is more stable than one formed on a primary carbon atom. 26 REFERENCES 1. McCann, H. G. Photochem. Photobiol. 1978, 29, 879-881. 2. Pukalskas, A. Isolation, identification and activity of natural antioxidants from sweet grass (Hierochloe odorata), costmary (Chrysanthemum balsamita) and horehound (Marrubium vulgare), cultivated in Lithuania. Thesis Wageningen University, 2008. 3. Smirnoff, N. New Phytol. 1993, 125, 27–58. 4. Unyayar, S.; Cekic, F. O. Tur. J. Biol. 2005, 29, 211–216. 5. Frankel, E. N. Prog. Lipid Res. 1980, 19, 1-22. 6. Gollnick, K. Mechanism and kinetics of chemical reactions of singlet oxygen with organic compounds. In: Singlet oxygen, ed. J. F. Rabek, John Wiley, New York, 1987; pp 111-134. 7. Bolland, J. L.; Ten Have P. Trans. Faraday Soc. 1947, 43, 201. 8. Pospisil, J.; Klemchuk, P. P. Oxidation Inhibition in Organic Materials. vols 1, 2. Boca Raton, F. L,; CRC Press, 1990. 9. Denisov, E. D.; Azatyan, V. V. Inhibition of Chain Reactions. London: Gordon and Breach. 2000. 10. Roginskii, V. A. Phenolic Antioxidants. Moscow: Nauka, 1988. 11. Das, L. M.; Bora, D. K.; Pradhan, S.; Naik, M. K.; Naik, S. N. Fuel 2009, 8, 2315–2318. 12. Karavalakis, G.; Hilari, D.; Givalou, L.; Karonis, D.; Stournas, S. Energy 2011, 36, 369-374. 13. Shahidi, F.; Wanasundara, P. K. J. P. D. Cri. Rev. Food Sci. Nut. 1992, 32, 67. 14. Nawar, W. W. in O. Fennema, ed., Food Chemistry, 3rd ed., Marcel Dekker, Inc. New York, 1996, 225. 15. Uri, N.; Sinclair, H. M. ed., Proceedings of International Conference in Biochemistry: Problems of Lipids. Academic Press, New York, 1958; pp 30. 16. Pokorny, J.; Chan, H. W. S. ed., Autooxidation of Unsaturated Lipids, Academic Press, London, 1987; pp 141. 17. Dunford, H. B. Free Rad. Biol. Med. 1987, 3, 405-421. 18. Mahoney, J. R.; Graf, E. J. Food Sci. 1986, 51, 1293. 19. Graf, E.; Eaton, J. W. Free Rad. Biol.Med. 1990, 8, 61. 20. Decker, E. A.; Akoh, C. C.; Min, D. B. Food Lipids: Chemistry, Nutrition and Biotechnology. 2nd ed., Marcel Dekker, Inc., New York, 2002, 517. 27 21. Claiborne, A.; Greenwald, C. R. A. CRC Hand Book of Methods of Oxygen Radical Research. Vol. I, CRC Press, Boca Raton, Florida, 1985, 283. 22. Gunzler, W. A.; Floh, L.; Greenwald, R. A. CRC Hand Book: Methods of Oxygen Radical Research, Vol 1. CRC Press, Boca Raton, Florida, 1985, 285. 23. Gordon, M. H.; Hudson, B. J. F. Food Antioxidants, Elsevier Applied Science, New York, 1990, 1. 24. Pokorn, J.; Pospısil, J.; Klemchuk, P. P. Oxidation Inhibition of Organic Materials, Vol. I, CRC Press, Boca Raton, Florida, 1989, 349. 25. Mittelbach, M.; Gangl, S. J. Am. Oil Chem. Soc. 2001, 78, 573–77. 26. Bondioli, P.; Gasparoli, A.; Lanzani, A.; Fedeli, E.; Veronese, S.; Sala, M. J. Am. Oil Chem. Soc. 1995, 72, 699–02. 27. Simkovsky, N. M.; Ecker, A. Erdöl Erdgas Kohle 1999, 115, 317–318. 28. Dunn, R. J. Am. Oil Chem. Soc. 2002, 79, 915–920. 29. Bond, T. C.; Streets, D. G.; Yarber, K. F.; Nelson, S. M.; Woo, J. H.; Klimont, Z. A. Geophysical Research 2004, 109, D14203. 30. Schauer, J.; Kleeman, M.; Cass, G. Characterization and Control of Organic Compounds., Emitted from Air Pollution Sources, California Air Resources Board: Sacramento, CA, 1998; pp 93-329. 31. Sheehan, J.; Camobreco, V.; Duffield, J.; Graboski, M.; Shapouri, H. National Renewable Energy Laboratory NREL/TP-580– 24772, 1998. 32. Sprules, F. J.; Price, D. US Patent 1950, 2, 366–494. 33. Enweremadu, C. C. Renew.Sus. Energy Rev. 2009, 13, 2205-2224. 34. Tomasevic, A. V.; Marinkovic, S. S. Fuel Process. Technol. 2003, 81, 1-6. 35. Freedman, B.; Pryde, E. H. Fatty esters from vegetable oils for use as a diesel fuel. Proceedings of International Conference on Plant & Vegetable oils as Fuels. ASAE St. Joseph, MI: 1982; 17–122. 36. Liu, K. J. Am. Oil Chem. Soc. 1999, 71(11), 1179–87. 37. Canakci, M.; Gerpen, J. V. Trans ASAE 1999, 42(5), 1203–10. 38. Shimada, Y.; Sugihara, A.; Minamigawa, Y.; Higasbiyama, K.; Akimoto, K.; Fujikawa, S.; Komemushi, S.; Tominaga, Y. J. Am. Oil Chem. Soc. 1998, 75, 1213–7. 39. Linko, Y. Y.; Liimsii, M.; Wu, X.; Uosukainen, W.; Sappiilii, J.; Linko, P. J. Biotechnol. 1998, 66, 41–50. 40. Eckey, E. W. J. Am. Oil Chem. Soc. 1956, 33, 575–79. 28 41. Pryde, E. H. J. Am. Oil Chem. Soc. 1984, 61, 1609–10. 42. Ziejewski, M.; Kaufman, K. R.; Schwab, A. W.; Pryde, E. H. J. Am. Oil Chem. Soc. 1984, 61, 1620–26. 43. Knothe, G. Trans ASAE 2001, 44(2), 193–200. 44. Feuge, R. O.; Gros, A. T. J. Am. Oil Chem. Soc. 1949, 26(3), 97. 45. Karavalakis, G.; Stournas, S. Energy Fuels 2010, 24, 3682–3686. 46. Schober, S.; Mittelbach, M. Eur. J. Lipid Sci. Technol. 2004, 106, 382–389. 47. Dunn, O. Fuel Process. Technol. 2005, 86, 1071–1085. 48. Ryu, K. Biores. Technol. 2010, 101, 578–582. 49. Tang, H.; Guzman, R. C. D.; Salley, S. O.; Simon, N. G. K. Y. Lipid Technol. 2008, 20, 249–252. 50. Bouaid, A.; Martinez, M.; Aracil, J. Biores. Technol. 2009, 100, 2234–39. 51. McCormick, R. L.; Westbrook, S. R. Energy Fuels 2010, 24, 690–98. 52. Bondioli, P.; Gasparoli, A.; Bella, L. D.; Tagliabue, S. Eur. J. Lipid Sci. Technol. 2002, 104, 777–84. 53. Mittelbach, M.; Gangl, S. J. Am. Oil Chem. Soc. 2001, 78, 573–77. 54. Bondioli, P.; Gasparoli, A.; Lanzani, A.; Fedeli, E.; Veronese, S.; Sala, M. J. Am. Oil Chem. Soc. 1995, 72, 699–02. 55. Simkovsky, N. M.; Ecker, A. Erdöl Erdgas Kohle 1999, 115, 317–318. 56. Shabnam Enayat, Sreeparna Banerjee, Food Chemistry 2009,116, 23–28. 57. Gezer, K.; Duru, M. E.; Kivrak, I.; Turkoglu, A.; Mercan, N.; Turkoglu, H. Afri. J, Biotechnol. 2006, 5(20), 1924–1928. 58. Domingos, A. K.; Saad E. B.; Vechiatto, W. W. D.; Wilhelm, H.; M.; Ramos, L. P. J. Brazil. Chem. Soc. 2007, 18, 416-23. 59. McCormick, R. L.; Alleman, T. L.; Ratcliff, M.; Moens, L.; Lawrence, R. Survey of the quality and stability of biodiesel and biodiesel blends in the United States in 2004. National Renewable Energy Laboratory, NREL/TP-540-38836. 2005. 60. Sendzikiene, E.; Makareviciene, V.; Janulis, P. Polish J. Environ. Stu. 2005, 14, 335-9. 61. Schober, S.; Mittellbach, M. Eur. J. Lipid Sci. Technol. 2004, 106, 382-89. 62. Liang, Y. C.; May, C. Y.; Foon, C. S.; Ngan, M. A.; Hock, C. C.; Basiron, Y. Fuel 2006, 85, 867-70. 63. Liang, C.; Schwarzer, K. J. Am. Oil Chem. Soc. 1998, 75, 1441-43. 64. Mittelbach, M.; Schober, S. J. Am. Oil Chem. Soc. 2003, 80, 817-23. 29 65. Pokorny, J. Eur. J. lipid Sci. Technol. 2007, 109, 629–642. 66. Amarowicz, R.; Pegg, B. R. J. Eur. J. lipid Sci. Technol. 2008, 110, 865 – 878. 67. Madsen, H. L.; Bertelsen, G. Trend. Food Sci. Technol. 1995, 6, 271–277. 68. Nakatani, N.; Inatarni, R. Agri.biol. chem. (Tokyo) 1984, 48, 2081–2085. 69. Kikuzaki, H.; Nakatani, N. Agri. Biol.Chem. (Tokyo) 1989, 53(2), 519-524. 70. Bragagnolo, H.; Mariuti, L. R. B. Brazil. J. Food Technol. 2007, 10, 96–103. 71. Robards, K.; Prenzler, P. D.; Tucker, G.; Swatsitang, P.; Glover, W. Food Chemistry 1999, 66, 401-436. 72. Velioglu, Y. S.; Mazza, G.; Gao, L.; Oomah, B. D. J. Agri.Food Chem. 1998, 46, 4113-4117. 73. Kulomaa, A.; Siren, H.; Riekkola, M. L. J. Chromat. A 1997, 781, 523-532. 74. Hakkinen, S. H.; Karenlampi, S. O.; Heinonen, I. M.; Mykkanen, H. M.; Torronen, A. R. J. Agri. Food Chem. 1999, 47, 2274-2279. 75. Bandoniene, D.; Murkovic, M. J. Agri. Food Chem. 2002, 50, 2482-2487. 76. Choi, H. S.; Song, H. S.; Ukeda, H.; Sawamura, M. J. Agri. Food Chem. 2000, 48, 4156-4161. 77. Verson, F. Cancer Lett. 1995, 93(1), 49–54. 78. Robards, K.; Kerr, A.; Patsalides, E. Analyst 1988, 113 (2), 213–24. 79. Del Carlo, M.; Sacchetti, G.; Di Mattia, C.; Compagnone, D.; Mastrocola, D.; Liberatore, L.; Cichelli, A. J. Agri. Food Chem. 2004, 52(13), 4072–9. 80. Charles, E. B.; George, S. H.; Chester, E. H.; Jyotirindra, N. A. J. Am. Chem. Soc. 1955, 77 (12), 3233–37. 30
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