Integrated biodiesel production: a comparison of different homogeneous catalysts systems

The most common catalysts for biodiesel production are homogeneous basic catalysts. In the present paper, a comparison is made of different basic catalysts (sodium methoxide, potassium methoxide, sodium hydroxide and potassium hydroxide) for methanolysis of sunflower oil. All the reactions were carried out under the same experimental conditions in a batch stirred reactor and the subsequent separation and purification stages in a decanter. The analytical methods included gas chromatography and the determination of fat and oil conventional parameters. The biodiesel purity was near 100 wt.% for all catalysts. However, near 100 wt.% biodiesel yields were only obtained with the methoxide catalysts. According to the material balance of the process, yield losses were due to triglyceride saponification and methyl ester dissolution in glycerol. Obtained biodiesel met the measured specifications, except for the iodine value, according to the German and EU draft standards. Although all the transesterification reactions were quite rapid and the biodiesel layers achieved nearly 100% methyl ester concentrations, the reactions using sodium hydroxide turned out the fastest.     

Microwave assisted alkali-catalyzed transesterification of Pongamia pinnata seed oil for biodiesel production

In this study, microwave assisted transesterification of Pongamia pinnata seed oil was carried out for the production of biodiesel. The experiments were carried out using methanol and two alkali catalysts i.e., sodium hydroxide (NaOH) and potassium hydroxide (KOH). The experiments were carried out at 6:1 alcohol/oil molar ratio and 60 °C reaction temperature. The effect of catalyst concentration and reaction time on the yield and quality of biodiesel was studied. The result of the study suggested that 0.5% sodium hydroxide and 1.0% potassium hydroxide catalyst concentration were optimum for biodiesel production from P. pinnata oil under microwave heating. There was a significant reduction in reaction time for microwave induced transesterification as compared to conventional heating.     

Selective separation of homogeneous catalysts using silicalite membranes

The recovery of a homogeneous catalysts can be performed effectively by means of a zeolite membrane, which in many cases has a crystalline structure with pores smaller than transition metal catalysts but larger than the products. This concept has been successfully applied to the Diels-Alder reaction between acroleine and cyclopentadiene, catalyzed by a cationic dinuclear Pd(II) complex. A reaction mixture containing 5-norbornene-2-carboxyaldehyde and the catalyst employed for its synthesis [Pd(μ-Cl)(Ph₂P-(CH₂)₄-PPh₂)](CF₃SO₃)₂ shows close to 100% recovery of the metallic compound.     

Performance Evaluation of Carbon-based Heterogeneous Acid Catalyst Derived From <Emphasis Type="Italic">Hura crepitans</Emphasis> Seed Pod for Esterification of High FFA Vegetable Oil

Efficient and recyclable heterogeneous catalysts from low-cost material is a research target in biodiesel industry to reduce production cost and minimize waste generation. The performance of carbon-based heterogeneous acid catalysts prepared from Hura crepitans seed pod via partial carbonization and sulfonation was evaluated in this study. Different catalysts, 0HuSO₃H, 30HuSO₃H, 60HuSO₃H, 90HuSO₃H, and 120HuSO₃H, obtained by varying preparation conditions were characterized using emission scanning electron microscope, Fourier transform infrared spectroscopy, X-ray powder diffraction, and thermogravimetric and titrimetric analyses. The activity of the catalysts towards esterification of high free fatty acid-containing H. crepitans seed oil was assessed. Effects of process parameters, temperature, catalyst load, methanol/oil ratio, reaction time, and their various optimum levels on the esterification reaction, were investigated using Taguchi L9 orthogonal array method of optimization. The results showed that the H. crepitans seed pod-derived solid acid catalysts exhibited superior catalytic properties primarily due to high acid density (2.0 mmol/g). The resident time of carbonization before sulfonation showed a strong influence on the acid site density, pore sizes, hydrophobicity, and acid site retention capacity. The optimum process conditions as predicted by the optimization model gave 94.81% ester conversion. The catalyst was effective up to four cycles with only 1.44% decrease in activity.     

Enantioselective cyanoformylation of aldehydes catalyzed with solid base mediated chiral V(V) salen complexes

Polymeric and monomeric V(V) chiral salen complexes‐catalyzed enantioselective ethyl cyanoformylation of aldehydes using ethyl cyanoformate as a source of cyanide was accomplished in the presence of several basic cocatalysts viz., NaOH, KOH, basic Al₂O₃ and hydrotalcite. Excellent yield (>95%) of chiral ethyl cyanohydrincarbonate with high enantioselectivity up to 94% was achieved in 24–36 h when hydrotalcite was used as an additive. The polymeric catalyst 1 is more reactive than the monomeric catalyst 2 to produce chiral ethyl cyanohydrincarbonate in high optical purity. The chiral polymeric catalyst 1 and cocatalysts hydrotalcite and basic alumina used in this study were recoverable and recyclable several times with retention of its performance. Chirality, 2010. © 2009 Wiley‐Liss, Inc.     

One-step hydrogenation-esterification of furfural and acetic acid over bifunctional Pd catalysts for bio-oil upgrading

This contribution focuses on one-step hydrogenation-esterification (OHE) of furfural and acetic acid, which are difficult to treat and typically present in crude bio-oil, as a model reaction for bio-oil upgrading. A bifunctional catalyst is needed for OHE reaction. Among tested bifunctional catalysts, the 5%Pd/Al₂(SiO₃)₃ shows the best catalytic performance. Compared to the physical mixture of 5%Pd/C + Al₂(SiO₃)₃, there is a synergistic effect between metal sites and acid sites over 5%Pd/Al₂(SiO₃)₃ for the OHE reaction. A moderate reaction condition would be required to obtain high yields of alcohol and ester along with lower byproduct yields. In this work, the optimum selectivity to desired products (alcohol and ester) of 66.4% is obtained, where the conversion of furfural is 56.9%. Other components, typically present in bio-oils, have little effects on the OHE of FAL and HAc. This OHE method is a promising route for efficient upgrading of bio-oil.     

The mechanistic aspects of iron(III) porphyrin catalyzed oxidation reactions in mixed solvents

In the iron(III) porphyrin catalyzed oxidation reactions, the formation of various reactive intermediates have been observed to depend upon the nature of the catalyst, the oxidant and the solvent used for the study. The various iron(III) porphyrin catalysts such as F₂₀TPPFeCl, F₁₆TPPFeCl, F₁₂TPPFeCl and F₈TPPFeCl have been used in the present study to understand the effect of solvent system in the activation of the catalysts. As the terminal oxidant t-BuOOH has been used. It has been observed that acetonitrile contaminated with water activates all the catalysts. It has been noted that ∼9% of water in acetonitrile is the best solvent system for the activation of all the catalysts. The results obtained have been applied to successfully oxidize cyclohexene and cyclohexane by these oxidizing systems. It has also been observed that CH₃OH mixed with CH₂Cl₂ play a very important role in the activation of catalyst in hydroperoxide oxidizing system. The 33 ± 3% ratio of CH₃OH in CH₂Cl₂ acts as the most suitable solvent system to convert organopalladium compound 1a-c to 2a-c.     

A facile transesterification route to ferrocenyl esters

In the presence of tetrabutylammonium hydroxide as catalyst and at room temperature, ethyl ferrocenecarboxylate, ethyl ferrocenylacetate, ethyl 3-ferrocenylpropanoate, 1,1′-ferrocenyl-bis(ethyl propanoate), ethyl 3-ferrocenylpropenoate and 1,1′-ferrocenyl-bis(ethyl propenoate) undergoes facile transesterification reaction with aliphatic, benzyl and allyl alcohols to furnish the corresponding ferrocenyl esters in good to excellent yields. Ring closing metathesis of the ester Fc-1,1′-(CHCH-CO₂CH₂CHCH₂)₂ yields the corresponding closed loop ferrocenyl ester.     

Specialty Fats from Beef Tallow and Canola Oil: Establishment of Reaction Conditions, Characterization of Products, and Evaluation of Crystal Stability

The effect of reaction time (0–90 min), catalyst concentration (0.2–0.5% CH₃ONa powder), and temperature (60–90 °C) of chemical interesterification (CIE) was studied to determine the optimal conditions for maximal change of solid fat content (SFC) in minimal time in a beef tallow (BT)/canola oil (CaO) blend (80:20, w/w, herein after referred to as BT/CaO blend 80:20). The optimal conditions were obtained as: CH₃ONa 0.4%, 60 °C, 30 min. BT/CaO blends (60:40, 65:35, 70:30, 75:25, 80:20, and 85:15) were each interesterified on a laboratory scale under afore-determined optimal conditions, and the corresponding 12 samples, before and after CIE, were characterized in terms of the SFC profile and compatibility. SFC profiling showed an increase in SFC (<5%) between 5 and 21.1 °C and a slight drop (<3%) in SFC between 40 and 45 °C for the interesterified blends. Compatibility analysis showed the presence of monotectic systems in original blends, proven through isothermal solid diagrams and isosolid diagrams. The incompatibility among the fats and oils was eliminated after reaction and the solution behavior shifted to a continuous solid solution. The interesterified 85:15, 80:20/75:25, 70:30, 65:35, and 60:40 BT/CaO blends displayed characteristics suited to application, respectively, for bakery shortenings, frying fats, all-purpose bakery shortenings, and bakery and roll-in margarines. The model shortenings produced from interesterified blends had more stable crystal morphology, crystal sizes, and double-chain (2L) stacking β′ polymorphs than blended shortenings under temperature fluctuation storage. Sensory analysis also showed that the former had less graininess and better spreadability than the latter during storage.     

Studies on Guizotia abyssinica L. oil: Biodiesel synthesis and process optimization

Guizotia abyssinica seeds, a common bird feedstock, have been explored for the potential of biodiesel synthesis. The oil was extracted from the seeds by solvent extraction and composition of G. abyssinica oil was examined. The reaction parameters for biodiesel synthesis have been optimized. Temperature, oil: methanol ratio, catalyst type and catalyst concentration were found to have significant role on ester conversion. According to this study, the maximum yield of ester (98.7%) can be obtained with optimized sodium methoxide catalyst dosage (0.6%) at an operational temperature of 65 °C. Methyl ester of G. abyssinica oil was also studied for its oxidation stability and low temperature properties. Further, the synthesized product was blended in diesel at 5–20% ratios and evaluated for physico-chemical properties.     

Selective hydrogenolysis of raw glycerol to 1,2-propanediol over Cu–ZnO catalysts in fixed-bed reactor

The catalytic properties of Cu–ZnO catalysts for glycerol hydrogenolysis to 1,2-propanediol (1,2-PDO) were tested in a fixed-bed reactor at 250 °C and 2.0 MPa H₂. The relation between composition, surface properties, and catalytic performance of glycerol hydrogenation of Cu–ZnO catalysts was studied using nitrogen adsorption (BET methods), XRD, H₂ temperature-programmed reduction, and N₂O chemisorptions. It was found that there was a close link between the surface CuO amount of Cu–ZnO catalyst and the reactivity for glycerol hydrogenation. The Cu–ZnO catalyst (Cu/Zn = 1.86) which had the highest surface Cu amount showed the best catalytic activity for glycerol hydrogenolysis. Furthermore, Cu–ZnO catalyst presented good stability and remarkable catalytic activity for glycerol hydrogenolysis to 1,2-PDO using raw glycerol derived from the fat saponification as feedstock.     

Atomically Dispersed Mo Supported on Metallic Co9S8 Nanoflakes as an Advanced Noble‐Metal‐Free Bifunctional Water Splitting Catalyst Working in Universal pH Conditions

Water splitting requires development of cost‐effective multifunctional materials that can catalyze both the hydrogen evolution reaction (HER) and the oxygen evolution reaction (OER) efficiently. Currently, the OER relies on the noble‐metal catalysts; since with other catalysts, its operation environment is greatly limited in alkaline conditions. Herein, an advanced water oxidation catalyst based on metallic Co₉S₈ decorated with single‐atomic Mo (0.99 wt%) is synthesized (Mo‐Co₉S₈@C). It exhibits pronounced water oxidization activity in acid, alkali, and neutral media by showing positive onset potentials of 200, 90, and 290 mV, respectively, which manifests the best Co₉S₈‐based single‐atom Mo catalyst till now. Moreover, it also demonstrates excellent HER performance over a wide pH range. Consequently, the catalyst even outperforms noble metal Pt/IrO₂‐based catalysts for overall water splitting (only requiring 1.68 V in acid, and 1.56 V in alkaline). Impressively, it works under a current density of 10 mA cm^?2 with no obvious decay during a 24 h (0.5 m H₂SO₄) and 72 h (1.0 m KOH) durability experiment. Density functional theory (DFT) simulations reveal that the synergistic effects of atomically dispersed Mo with Co‐containing substrates can efficiently alter the binding energies of adsorbed intermediate species and decrease the overpotentials of the water splitting.     

Application of dimeric orthopalladated complex in Suzuki-Miyaura cross coupling reaction under microwave irradiation and conventional heating

The Suzuki-Miyaura reaction of various aryl halides using [Pd{C₆H₂(CH₂CH₂NH₂)-(OMe)₂,3,4} (μ-Br)]₂ have been investigated. This orthopalladated complex is an efficient, stable and non-sensitive to air and moisture catalyst for the hetrocoupling reaction in DMF as the reaction solvent at 130 °C. The combination of dimeric complex as homogenous catalyst and microwave irradiation can be very useful and efficient methods in organic synthesis, so the application of microwave irradiation have been investigated using homogenous dimeric complex [Pd{C₆H₂(CH₂CH₂NH₂)-(OMe)₂,3,4} (μ-Br)]₂. Application of dimeric complex as catalyst caused to produce the desired coupling products and the using of microwave irradiation improving the yields of the reactions and shortening the reaction times.     

Tin Oxide as a Protective Heterojunction with Silicon for Efficient Photoelectrochemical Water Oxidation in Strongly Acidic or Alkaline Electrolytes

Photoelectrodes without a p–n junction are often limited in efficiency by charge recombination at semiconductor surfaces and slow charge transfer to electrocatalysts. This study reports that tin oxide (SnO_x) layers applied to n‐Si wafers after forming a thin chemically oxidized SiO_x layer can passivate the Si surface while producing ≈620 mV photovoltage under 100 mW cm^?2 of simulated sunlight. The SnO_x layer makes ohmic contacts to Ni, Ir, or Pt films that act as precatalysts for the oxygen‐evolution reaction (OER) in 1.0 m KOH(aq) or 1.0 m H₂SO₄(aq). Ideal regenerative solar‐to‐O₂(g) efficiencies of 4.1% and 3.7%, respectively, are obtained in 1.0 m KOH(aq) with Ni or in 1.0 m H₂SO₄(aq) with Pt/IrO_x layers as OER catalysts. Stable photocurrents for >100 h are obtained for electrodes with patterned catalyst layers in both 1.0 m KOH(aq) and 1.0 m H₂SO₄(aq).     

Biodiesel production from rubber seed oil using poly (sodium acrylate) supporting NaOH as a water-resistant catalyst

Poly (sodium acrylate) supporting NaOH (NaOH/NaPAA) was prepared by in situ polymerization of aqueous solution of acrylic acid with an over-neutralization by adding excess of NaOH. NaOH/NaPAA presented a promising selectivity for water absorbency and good water retention with negligible swelling capacity in the organic solvents of methanol, glycerol, rubber seed oil methyl esters, and rubber seed oil. NaOH/NaPAA catalysts showed a basic strength of 15.0 < H_ < 18.4 and their basicity increased with the increase of the NaOH loading amount. NaOH/NaPAA catalysts exhibited almost the same catalytic activity in the transesterification of rubber seed oil with methanol under the optimized reaction conditions compared to conventional homogeneous NaOH catalyst. Furthermore, the functional absorbent/catalyst system presented a good water resistance in the transesterification which retained high catalytic activity when a water concentration in the reaction system was less than 2 wt.%.     

Direct acid-catalysed transmethylation of lactobacillic acid in lactic acid bacteria

Summary Cellular fatty acids inLactobacillus büchneri were transmethylated with H₂SO₄ catalyst in methanol at elevated temperature. By optimising the reaction time and the amounts of catalyst and methanol used at a fixed temperature it was possible to maximise the lactobacillic acid yield. The yield of lactobacillic acid with this method was better than with the traditional method using base-catalysed saponification followed by HCL-catalysed methylation.     

The preparation and electrochemistry of cysteine-ester oxovanadium(IV) complexes

An improved synthesis of VO(CysOCH₃)₂, (CysOCH₃  the anion of cysteine methyl ester), is reported, as is an analogous preparation of VO(CysOCH₂CH₃)₂, (CysOCH₂CH₃  the anion of cysteine ethyl ester). These are the first two examples of isolated vanadium-cysteine compounds. The oxidation of VO(CysOCH₃)₂ in DMSO is a reversible one electron change at 0.24 V versus SCE followed by a rapid chemical reaction which produces a stable vanadium(V) species. This species is reduced back to the vanadium(IV) complex at −1.30 V. The electrochemistry of VO(Cys-OCH₂CH₃)₂ is nearly identical to that of the methyl ester compound.     

Ultrathin High Surface Area Nickel Boride (NixB) Nanosheets as Highly Efficient Electrocatalyst for Oxygen Evolution

The overriding obstacle to mass production of hydrogen from water as the premium fuel for powering our planet is the frustratingly slow kinetics of the oxygen evolution reaction (OER). Additionally, inadequate understanding of the key barriers of the OER is a hindrance to insightful design of advanced OER catalysts. This study presents ultrathin amorphous high‐surface area nickel boride (Ni_x B) nanosheets as a low‐cost, very efficient and stable catalyst for the OER for electrochemical water splitting. The catalyst affords 10 mA cm^?2 at 0.38 V overpotential during OER in 1.0 m KOH, reducing to only 0.28 V at 20 mA cm^?2 when supported on nickel foam, which ranks it among the best reported nonprecious catalysts for oxygen evolution. Operando X‐ray absorption fine‐structure spectroscopy measurements reveal prevalence of NiOOH, as well as Ni‐B under OER conditions, owing to a Ni‐B core@nickel oxyhydroxide shell (Ni‐B@NiO_x H) structure, and increase in disorder of the NiO_x H layer, thus revealing important insight into the transient states of the catalyst during oxygen evolution.     

The effect of the acidity of rapeseed oil on its transesterification

The aim of this work is to study the transesterification of vegetable oil with a high acid number at unchanged reaction conditions. Rapeseed oil was used as the raw material and its acid number was changed by the addition of oleic acid (from 0.89 to 12.25 mg KOH/g). Methanol was used for transesterification (molar ratio of oil to methanol 1:6) and potassium hydroxide was used as a catalyst. After the reaction time, the residue of the catalyst was neutralised by gaseous carbon dioxide and the methanol excess was removed. After the separation of two phases, each of them was analyzed (in the ester phase: yield, content of methyl ester and acid number; in the glycerol phase: yield, density, viscosity, content of glycerol, soaps, methyl ester, potassium carbonate and hydrogen carbonate). The obtained data was compared with theoretical material balances and the effect on the saponification of oil was discussed. The results show that the yield of methyl ester (biodiesel) is significantly affected by a higher acid number, as well as enhanced soap formation. On the other hand, the conversion of the oil and acid number of the ester phase remain at constant values in studied borders.     

Biodiesel production by two-stage transesterification with ethanol

A two-stage process consisting of two reactions steps with glycerin separation and ethanol/catalyst addition in each of them was optimized for ethyl esters production. The optimal reaction temperature was 55 °C. At an ethanol/oil molar ratio of 4.25:1 (25%v/v alcohol with respect to oil), a 99% conversion value was obtained with low ethanol consumption. In contrast to methoxide catalysts, sodium and potassium hydroxide catalysts severely complicate the purification since no phase separation took place under most conditions. With a total sodium methoxide concentration of 1.06 g catalyst/100 g oil, and adding 50% of the catalyst in each reaction step, biodiesel with a total glycerin content of 0.172% was obtained. The optimal conditions found in this study make it possible to use the same industrial facility to produce either methyl or ethyl esters.