A review on biodiesel production using catalyzed transesterification

Biodiesel fuel production by transesterification of oils.

Biodiesel processing and production

Industrial applications of microbial lipases

The world is confronted with the twin crises of fossil fuel depletion and environmental degradation. The indiscriminate extraction and consumption of fossil fuels have led to a reduction in petroleum reserves. Petroleum based fuels are obtained from limited reserves. These finite reserves are highly concentrated in certain region of the world. Therefore, those countries not having these resources are facing a foreign exchange crisis, mainly due to the import of crude petroleum oil. Hence it is necessary to look for alternative fuels, which can be produced from materials available within the country. Although vegetative oils can be fuel for diesel engines, but their high viscosities, low volatilities and poor cold flow properties have led to the investigation of its various derivatives. Among the different possible sources, fatty acid methyl esters, known as Biodiesel fuel derived from triglycerides (vegetable oil and animal fates) by transesterification with methanol, present the promising alternative substitute to diesel fuels and have received the most attention now a day. The main advantages of using Biodiesel are its renewability, better quality exhaust gas emission, its biodegradability and the organic carbon present in it is photosynthetic in origin. It does not contribute to a rise in the level of carbon dioxide in the atmosphere and consequently to the green house effect. This paper reviews the source of production and characterization of vegetable oils and their methyl ester as the substitute of the petroleum fuel and future possibilities of Biodiesel production.

Biodiesel production through the use of different sources and characterization of oils and their esters as the substitute of diesel: A review

Biodiesel derived from vegetable oils has drawn considerable attention with increasing environmental consciousness. We attempted continuous methanolysis of vegetable oil by an enzymatic process. Immobilized Candida antarctica lipase was found to be the most effective for the methanolysis among lipases tested. The enzyme was inactivated by shaking in a mixture containing more than 1.5 molar equivalents of methanol against the oil. To fully convert the oil to its corresponding methyl esters, at least 3 molar equivalents of methanol are needed. Thus, the reaction was conducted by adding methanol stepwise to avoid lipase inactivation. The first step of the reaction was conducted at 30°C for 10 h in a mixture of oil/methanol (1:1, mol/mol) and 4% immobilized lipase with shaking at 130 oscillations/min. After more than 95% methanol was consumed in ester formation, a second molar equivalent of methanol was added and the reaction continued for 14 h. The third molar equivalent of methanol was finally added and the reaction continued for 24 h (total reaction time, 48 h). This three-step process converted 98.4% of the oil to its corresponding methyl esters. To investigate the stability of the lipase, the three-step methanolysis process was repeated by transferring the immobilized lipase to a fresh substrate mixture. As a result, more than 95% of the ester conversion was maintained even after 50 cycles of the reaction (100 d).

Conversion of vegetable oil to biodiesel using immobilized Candida antarctica lipase

Candida antarctica lipase is inactivated in a mixture of vegetable oil and more than 1∶2 molar equivalent of methanol against the total fatty acids. We have revealed that the inactivation was eliminated by three successive additions of 1∶3 molar equivalent of methanol and have developed a three-step methanolysis by which over 95% of the oil triacylglycerols (TAG) were converted to their corresponding methyl esters (ME). In this study, the lipase was not inactivated even though 2∶3 molar equivalent of methanol was present in a mixture of acylglycerols (AG) and 33% ME (AG/ME33). This finding led to a two-step methanolysis of the oil TAG: The first-step was conducted at 30°C for 12 h with shaking in a mixture of the oil, 1∶3 molar equivalent of methanol, and 4% immobilized lipase; the second-step reaction was done for 24 h after adding 2∶3 molar equivalent of methanol (36 h in total). The two-step methanolysis achieved more than 95% of conversion. When two-step reaction was repeated by transferring the immobilized lipase to a fresh substrate mixture, the enzyme could be used 70 cycles (105 d) without any decrease in the conversion. From the viewpoint of the industrial production of biodiesel fuel production, the two-step reaction was conducted using a reactor with impeller. However, the enzyme carrier was easily destroyed, and the lipase could be used only several times. Thus, we attempted flow reaction using a column packed with immobilized Candida lipase. Because the lipase packed in the column was drastically inactivated by feeding a mixture of AG/ME33 and 2∶3 molar equivalent of methanol, three-step flow reaction was performed using three columns packed with 3.0 g immobilized lipase. A mixture of vegetable oil and 1∶3 molar equivalent of methanol was fed into the first column at a constant flow rate of 6.0 mL/h. The eluate and 1∶3 molar equivalent of methanol were mixed and then fed into the second column at the same flow rate. The final step reaction was done by feeding a mixture of eluate from the second column and 1∶3 molar equivalent of methanol at the same flow rate. The ME content in the final-step eluate reached 93%, and the lipase could be used for 100 d without any decrease in the conversion.

Continuous production of biodiesel fuel from vegetable oil using immobilized Candida antarctica lipase

Biodiesel Fuel Production from Plant Oil Catalyzed by Rhizopus oryzae Lipase in a Water-Containing System without an Organic Solvent

Pretreatment of immobilized Candida antarctica lipase for biodiesel fuel production from plant oil

A thermostable lipase from Pseudomonas cepacia has been purified to homogeneity as judged by SDS-PAGE and isoelectric focusing. The purification included treatment of the culture supernatant with acrinol, hydrophobic interaction chromatography, and gel filtration. The enzyme was a monomeric protein with M(r) of 36,500 and pI of 5.1. The optimal pH at 50 degrees C and optimal temperature at pH 6.5 were 5.5-6.5 and 55-60 degrees C, respectively, when olive oil was used as the substrate. Simple triglycerides of short and middle chain fatty acids (C < or = 12) were the preferred substrates over those of long chain fatty acids. The enzyme cleaved all the ester bonds of triolein, with some preference for the 1,3-ester bonds. The enzyme retained all its activity even after incubation at 75 degrees C (pH 6.5) for 30 min. Further, the activity was not impaired during 21 h storage at pH 6.5 in 40% water-miscible solvents including methanol, ethanol, acetone, acetonitrile, dimethylformamide, dimethylsulfoxide, and dioxane. The addition of dimethylsulfoxide or acetone to the assay mixture in the range of 0-35% stimulated the enzyme, whereas benzene or n-hexane had an inhibitory effect. These properties together with the N-terminal amino acid sequence confirmed that the enzyme differs from the known Pseudomonas sp. lipases.

https://www.jstage.jst.go.jp/article/biochemistry1922/112/5/112_5_598/_pdf

Yuji Shimada

Papers

Conversion of vegetable oil to biodiesel using immobilized Candida antarctica lipase

Continuous production of biodiesel fuel from vegetable oil using immobilized Candida antarctica lipase

Biodiesel Fuel Production from Plant Oil Catalyzed by Rhizopus oryzae Lipase in a Water-Containing System without an Organic Solvent

Pretreatment of immobilized Candida antarctica lipase for biodiesel fuel production from plant oil

Purification and characterization of a novel thermostable lipase from Pseudomonas cepacia.