Egyptian Jatropha oil extraction for biodiesel production

Biodiesel is the most desirable biofuel economically andtechnically and it can be made from any vegetable oil. InEGYPT jatropha oil seems to be the best source for biodiesel production because jatropha tree is easily growing and easily propagated.Also jatropha tree thrives in marginal and desert areas that are unable to support crops and it can be irrigated with primary treated municipal wastewater.The main purpose of this investigation is to compare andoptimize the oil yield extracted from jatropha seeds on both bench and pilot scale.Different solvents under different extraction conditions were studied to determine optimum solvent type, solid: liquid ratio and extraction time which gave maximum oil yield.Oil extracted specifications, losses in seeds dehulling &washing, losses in solvent used and extracted meal analysis& uses were also concluded

Biodiesel production from Jatropha seeds using heterogeneous integrated extraction reaction process

Integrated extraction and transesterification process forbiodiesel production from Jatropha Curcas (JCL) seeds using hexane and methanol via base catalyzed transesterificationis reported in this paper.The effects of reaction time, catalyst dose, liquid to solidratio, type of solvent and grain size of JCL seeds onbiodiesel production were investigated. It was found thathexane played the role of both co – solvent and co – extractantwhich enhanced the efficiency of oil extraction and facilitated mass transfer. The highest biodiesel yield (90.8%) was obtained at hexane to seed ratio of 5:1 (vol /wt), methanol to seed ratio 1:1 (vol /wt), activated Ca O of 1% by wt of seeds, stirring speed 700 rpm, temperature of 70°C at reaction time 6 hours

Studying the ultrasonic assisted transesterification of castor oil by using factorial design for optimization of biodiesel production

This work presents the biodiesel production from castor oil with methanol in presence of potassium hydroxide as catalyst at room temperature using ultrasonic bath. A factorial design of experiments and a central composite design have been used to evaluate the influence of operating conditions on biodiesel synthesis from inedible castor oil. The response chosen was viscosity while the variables studied were catalyst concentration and the methanol/vegetable oil molar ratio at room temperature in an ultrasonic bath. The methanol/vegetable oil molar ratio is the most important factor, having a negative influence on viscosity.The catalyst concentration has a small negative influence on viscosity and this is attributed to the presence of ultra-sonification. A second order model was obtained to predict the produced biodiesel viscosity. Within the experimental range studied the model matched the results from the experiments

Effect of Extractive Solvents on Bio – Oil Production From Microalgae via Hydrothermal Liquefaction

Bio–oil from spirulina sp. is complicated mixture with valued chemicals. The hydrothermal liquefaction (HTL) converts directly the spirulina microalgae into liquid oil at reaction temperature 300°C with heating rate 10°C /min,100 bars pressure and 30 min. reaction time eight different organic solvents with different polarities were applied to extract the bio – oil from these chemicals. The order of bio–oil extraction yield of the eight solvents from high to low were as follow tetrahydrofuran (THF) ˃ dichloromethane (DCM) ˃ acetone (ACE) ˃ chloroform (CHL) ˃ methanol (MeOH)˃ ethyl-acetate (EAC) ˃ hexane (HEX) ˃toluene (TOL).The results obtained from single stage extraction process showed that maximum percentage oil yield was (26.55%). with rather high heating value (HHV ≈ 30 MJ/kg). The combination of THF, EAC and n-hexane was selected to extract and separate the bio – oil into three fraction heavy oil (48.9%) mid weight oil (37.8%) and light oil (62.2%). These three oils were characterized using gas chromatography mass spectrum (GC – mass). Keywords:- Bio–oil , extractives, hydrothermal , liquefaction, micro- algae.

Modification of thermal and oxidative properties of biodiesel produced from vegetable oils

Trans esterification of three vegetable oils, sunflower oil, linseed oil and mixed oils as; sunflower-soyabean and olein were carried out using methanol, and potasium hydroxide as catalyst. The methyl esters of the corresponding oils were separated from the crude glycerol and characterized by physical-chemical methods to evaluate their thermal properties. This methods are determination of densities, cloud points, pour points, flash points, kinematic viscosities, hydrogen/carbon ratios, sulfur contents, ash contents and triglycerides. The physico-chemical characteristic of biodiesel treated with ozone showed improvement of pour point and flash point indicating higher degree of safety for fuel. Methyl esters mixed with their corresponding ozonated oil were subjected to comparison and evaluation for their thermal properties by the thermo gravimetric analysis differential thermal analysis from which the calculated heat of enthalpy and comparison with the heat of conventional diesel. The results showed that the oxygen content of biodiesel samples treated with ozone increased weight % and resulted in more extensive chemical reaction, promoted combustion characteristics and less carbon residue was produced. Gas chromatography appeared more suitable to address the problem of determining/verifying biodiesel methyl ester and showed that methyl ester content was impurity free. Ultra violet-detection was used for rapid quantization of triglycerols. From the analyses performed biodiesel treated with ozone modified the thermal and oxidative stability shown by the high combustion efficiency indicated by the high heat of enthalpy and reducing the emission of particulate matter

Protection of biodiesel and oil from degradation by natural antioxidants of Egyptian Jatropha

Residue of methanolic extract of Egyptian Jatropha curcas contains bioactive substances such as phenolic compounds, which succeeded to be used as natural antioxidants for the protection of oils and their corresponding biodiesel against oxidative deterioration. In the present work, the residue of Jatropha roots were extracted with methanol and resulting residues, were investigated regarding their content of total phenolic compounds by folin-Cioalteau assay. Further, the antioxidant activities of the extracts were characterized by the 2,2-diphenyl-1-picrylhydrazyl radical method and proved remarkable results. Oxidation stability of Jatropha oil, used fried oil and olive oil and their corresponding biodiesel obtained by conventional transesterification were tested using thermal oxidation. Natural antioxidants such as (á-trocopherol), synthetic antioxidants as butylated hydroxytoluene and natural Jatropha root extract were used in the present study in comparison to investigate their addition effect on the oxidative stability of oils and their corresponding biodiesel. In the rapied thermal treatment test, results showed that addition of butylated hydroxytoluene 0.25 % was able to stabilize Jatropha oil 6 h, but poorly stabiliz biodiesel. Addition of 0.25 % á-trocopherol to Jatropha oil showed less oxidation stability after 2 h thermal treatment. Crude root extract addition at 0.25% to Jatropha oil showed good stability up to 4 h thermal treatment while addition of root extract at 0.25 % to biodiesel showed better stability up to 6 h thermal treatment. Besides addition of 220 ppm crude root extract to biodiesel was enough sufficient to occure oxidative stabilization. Also Jatropha root residue addition at 400 ppm was effective antioxidant for fresh Jatropha oil

Degradation of 2, 4, 6-trinitotoluene in aqueous solution by ozonation and multi-stage ozonation biological treatment

The objective of this study was to explore the extent of 2,4,6-trinitrotoluene synthetic solution and red water mineralization by comparing conventional direct ozonation and multi-stage ozonation-biological treatment process. The alkaline hydrolysis was used for remediation 2, 4, 6-trinitrotoluene and red water at pH = 10.9. Nevertheless, the hydroxyl radicals would be generated by ozone decomposition with ozone dose of 0.177 g/L. The samples were subjected to chemical oxygen demand and total organic carbon analysis to monitor pollutants removal. The rate of 2, 4, 6-trinitrotoluene and red water pollutants degradation were quantified using high performance liquid chromatography. 2, 4, 6-trinitrotoluene synthetic solution resulted 55.5 % chemical oxygen demand removal by 3 h direct ozonation. Following direct ozonation the biological treatment twenty four hours chemical oxygen demand reached 98.9 % and 98.7 % removal using humic acid and river water 1 % ( v/v) inoculation singly and respectively. Conventional direct ozonation showed non significant change in total organic carbon degradation. While on using multi-stage ozone-biological treatment process where humic acid and/or river water were used as inoculums singly and respectively, total organic carbon fulfilled 73 % and 98.3 % removal. The process was one hour direct ozonation and followed by three days multistage ozone-biological treatment. In multi-stage ozone-biological treatment process, ozonation was effective to decompose total organic carbon and to produce biodegradable dissolved organic carbon easily removed by ozone oxidation up to 98.3 % in 2,4,6-trinitrotoluene synthetic solution. Pollutants removal achieved 99 % in authentic red water effluent using river inoculation 1 % (v/v) in 5 days. Nuclear Magnetic Resonance and Fourier Transformation Infra Red methods were performed to confirm types of pollutants content in red water

Development and evaluation of biodiesel fuel and by-products from jatropha oil

Biodiesel is an environmentally friend renewable diesel fuel alternative. Jatropha seeds can be a feedstock to produce a valuable amount of oil to be converted to biodiesel using transesterification reaction. Jatropha plant has been successfully grown in southern Egypt using primary treated municipal wastewater for its irrigation. A bench scale production of biodiesel from Jatropha oil (using methyl alcohol and sodium hydroxide as catalyst) was developed with methyl esters yield of 98 %. Biodiesel was produced on a pilot scale based on the bench scale experiment results with almost the same methyl esters yield of 98 %. The produced biodiesel was evaluated as a fuel and compared with petroleum diesel according to its physical and chemical parameters such as viscosity, flash point, pour point, cloud point, carbon residue, acid value and calorific value. The experimental techniques and product evaluation results show that such properties of the produced biodiesel are near to that of petroleum diesel. A mass balance representing the transesterification process is presented in this study. Glycerol of 85 % purity was produced and evaluated as a valuable byproduct of the process. Free fatty acids and sodium phosphate salts which have industrial interesting are also produced and evaluated

Production optimization and quality assessment of biodiesel from waste vegetable oil

Biodiesel production is worthy of continued study and optimization of production procedures because of its environmentally beneficial attributes and its renewable nature. In Egypt, millions L. of oil used for frying foods are discarded each year into sewage systems. Thus, it adds to the cost of treating effluent or pollutes waterways. This study is intended to consider aspects related to the feasibility of the production of biodiesel from waste/recycled oils in an attempt to help reduce the cost of biodiesel and reduce waste and pollution coming from waste oils. The variables affecting the yield and characteristics of the biodiesel produced from used frying oil were studied, the achieved results were analyzed and a set of recommendations was proposed. From the obtained results, the best yield percentage was obtained using a methanol/oil molar ratio of 6:1, potassium hydroxide as catalyst (1%) and 65°C temperature for one hour. The yield percentage obtained from waste vegetable oil was comparable to that obtained from neat vegetable oil which reached 96.15% under optimum conditions. From the results it was clear that the produced biodiesel fuel, whether from neat vegetable oil or waste vegetable oil, was within the recommended standards of biodiesel fuel

Catalytic hydrocracking of jatropha oil over natural clay for bio-jet fuel production

Abstract Currently, the conversion of biomass to produce high-valued biofuels such as biodiesel and bio-jet fuel has attached booming interests, when used for partial replacement of petroleum fuels in different ratios is a promising solution due to the problem of depleting petroleum reserves and environmental purposes. Non-edible Jatropha oil can be transformed to biofuel when subjected to were hydrocracking at hydrogen pressure using an activated natural clay as a catalyst in a high pressure batch reactor. The type of product and its quality and quantity depend on the process conditions such as reaction time, temperature, and catalyst type, form, and amount. The present work aims to study the hydrocracking process of Jatropha oil at different operating conditions. The catalyst is characterized using SEM, FTIR, XRF, and XRD. The effect of process conditions variation have been studied and discussed. The results showed the highest yield of 40% bio-jet fuel was achieved at a temperature of 350 °C, H2 pressure of 4 bar, and reaction time of 18 min. the bio-jet fuel products were tested and their specifications were conformed to ASTM D1655 specifications, viz the freezing point (−56 °C), the flash point (53 °C), and existent gum content (5.9 mg/100 ml)