PRODUCTION OF BIODIESEL USING PRODUCTION OF BIODIESEL USING HETEROGENEOUS CATALYST HETEROGENEOUS CATALYST PHASE II – viva voice PHASE II – viva voice NAME:K. RAMACHANDRAN NAME:K. RAMACHANDRAN ROLL NO:2009409013 ROLL NO:2009409013 M.TECH-PRPC M.TECH-PRPC GUIDE GUIDE Dr.S.RENGANATHAN Dr.S.RENGANATHAN Assistant professor Assistant professor
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PRODUCTION OF BIODIESEL USING PRODUCTION OF BIODIESEL USING HETEROGENEOUS CATALYSTHETEROGENEOUS CATALYST
GUIDEGUIDEDr.S.RENGANATHANDr.S.RENGANATHANAssistant professorAssistant professor
ABSTRACTABSTRACT
Ba(HSO4)3 and Zn(HSO4)2 heterogeneous acid catalyst was prepared by the sulfonation of anhydrous BaCl2 and ZnCl2.
This catalyst was employed to catalyze transesterification reaction to synthesis methyl ester when a mixed waste vegetable oil was used as feedstock.
The catalyst were characterized by SEM, EDAX and titration method.
The conversion was achieved as 88 wt% and 81.5 wt% with 60 min reaction time at methanol reflux temperature, 10:1 molar ratio of methanol to oil and 1 wt% & 1.25 wt% of catalyst respectively.
The fuel properties of methyl ester were analyzed. The fuel properties were found to be observed within the limits of ASTM D6751.
INTRODUCTIONINTRODUCTION
Biodiesel - Alternative fuel, - reducing the level of pollutants
& carcinogen agents.Catalyst
Homogeneous Heterogeneous
Base catalyst – MgO, Ba(OH)2, Zeolites etc…
Acid catalyst
Source selection
OBJECTIVEOBJECTIVE
The proposed project work is designed to:Prepare catalystCharacterize the catalystBiodiesel production
To characterize the used mixed waste vegetable oil. Process optimization
SEM - Structure and Pore size EDAX - Elements of the catalyst Titration method - H+ content
METHODMETHOD
Catalytic reaction procedure In this work, the mixed waste vegetable oils used as feedstock. The molar ratio of methanol to mixed oil required was calculated by treating 3 mol of FFA as 1 mol of triglyceride. The reaction was carried out in a 250 ml standard flask equipped with reflux condenser and a magnetic stirrer. The mixed oil and a known amount of catalyst were charged into the reactor. When the required temperature was reached, methanol was added into the reactor. The reaction was started by stirring (at 250 rpm). Then the transesterification were stopped when reaction was completed.
METHODMETHOD
Oil characterization
Fatty acid content by gas chromatography analysis. Product analysis
FAME yield determined by using the H NMR technique.FAME yields can be calculated by using the following equation:
YBD = 2 * A1 / {3 * A2}*100Where, methoxylic (A1)
methylenic groups (A2)
The fuel properties such as viscosity, density, cetane number, flash point and cold filter plugging point of the methyl ester were analyzed.
RESULTS & DISCUSSIONDISCUSSION
Catalyst Characterization
SEM AnalysisBaCl2 and ZnCl2 - Loose irregular network structure.
Pores became larger - Treated with conc.H2SO4
Pore size - ↑the accessibility of H2SO4 into the Ba & Zn powder bulk, which would give a higher concentration of covalently bonded Ba or Zn with an –SO3H group.
RESULTS & DISCUSSIONDISCUSSIONREACTION STUDIES Effect of types of alcohol:
RESULTS & DISCUSSIONDISCUSSIONREACTION STUDIES Effect of catalyst loading:
RESULTS & DISCUSSIONDISCUSSIONREACTION STUDIES Effect of temperature:
RESULTS & DISCUSSIONDISCUSSIONREACTION STUDIES Effect of oil to methanol molar ratio:
RESULTS & DISCUSSIONDISCUSSIONREACTION STUDIES Effect of reaction time:
RESULTS & DISCUSSIONDISCUSSIONREACTION STUDIES Effect of stirring speed:
RESULTS & DISCUSSIONDISCUSSIONREACTION STUDIES Deactivation of catalyst:
RESULTS & DISCUSSIONDISCUSSIONProduct analysis and specification:
NMR Result of :
Ba(HSO4)2 & Zn(HSO4)2 by considering the peak at 3.6 (due to -CH3 ester proton) and 2.3 (due to α methylene proton). The percentage conversion is equal to (2*A3.6 / 3*A2.3)*100.
RESULTS & DISCUSSIONDISCUSSIONProduct analysis and specification:
Biodiesel Specifications:
Properties Obtained Biodiesel Diesel ASTM D 6751 EN 14214
Water content (wt %) 0.01 0.01 0.01 0.02 0.05 max 0.05 max
Ash content (wt %) 0.01 0.01 0.01 0.01 0.02 0.02
RESULTS & DISCUSSIONDISCUSSION
Comparison of Biodiesel Production:
Conversion
Al(HSO4)3
≈ & < Ba(HSO4)2. Zn(HSO4)2
Ba(HSO4)2 and Zn(HSO4)2 was effective acid catalyst for the production of biodiesel from mixed waste vegetable oil.
The high activity of the catalyst was described to the high acid site density and the bonded hydrophilic functional groups (-SO3H) that allowed more methanol to contact the carbonyl group of triglyceride.
The maximum conversion was achieved as 88% and 81.5%with 60 min reaction time at MeOH reflux Temp, 10:1 molar ratio of methanol to oil and 1wt% & 1.25 wt% of catalyst respectively.
The properties of obtained biodiesel are close to commercial diesel fuel. The properties of biodiesel were found to meet the biodiesel standard of ASTM D6751 and EN41214.
Conclusion
1. Kasirajan Ramachandran, Pandian Sivakumar, Tamilarasan Suganya, Sahadevan Renganathan., Production of biodiesel from mixed waste vegetable oil using an Aluminium hydrogen sulphate as a heterogeneous acid catalyst, Bioresource Technology (2011), doi: 10.1016/j.biortech.2011.04.100