Biodiesel production from waste cooking oil utilizing Cu/Ca/AI203 catalyst / Muhamad Sharul Nizam Awang
Currently, biodiesel has been successfully yielded by transesterification of waste cooking oil (WCO) by using heterogeneous basic catalysts dissolved in methanol. The transesterification of waste cooking oil involves some challenges. For example, waste cooking oil usually contains a large amount...
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| Format: | Student Project |
| Language: | English |
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Faculty Of Applied Sciences
2017
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| Online Access: | http://ir.uitm.edu.my/id/eprint/25746/ http://ir.uitm.edu.my/id/eprint/25746/1/PPb_MUHAMAD%20SHARUL%20NIZAM%20AWANG%20AS%20C%2017_5.PDF |
| Summary: | Currently, biodiesel has been successfully yielded by transesterification of waste
cooking oil (WCO) by using heterogeneous basic catalysts dissolved in methanol.
The transesterification of waste cooking oil involves some challenges. For example,
waste cooking oil usually contains a large amount of free fatty acids (FFAs), which
could react with base catalyst to form soap, resulting in a decrease in percentage of
biodiesel yield. So, this study focused on the synthesis, optimization and
characterization of base heterogeneous catalyst, bimetallic CU/CalAh03 with
different parameters to test their effectiveness towards biodiesel production using
WCO. The physicochemical properties of the catalyst were determined by TGA,
FTIR, XRD and BET. The activity of the catalyst in transesterification reaction was
evaluated at reaction temperature of 65°C, 3 h reaction time and 12:1 M ratio of
methanol to oil. The investigation of the synthesized CU/CalAh03 catalyst showed
that the calcination temperature of 800, 900 and 1000°C, catalyst loading of 3, 4 and
5 wt.% as well as reaction time of 3, 4 and 5 hours have significant effects on the
catalytic performance. These critical parameters were investigated in order to
determine the optimum operating conditions for biodiesel production. The optimum
conditions were 900°C calcination temperature, 3 wt.% catalyst loading and 3
hours reaction time which gave 10.9% biodiesel yield. Due to very low biodiesel
yield, the study was continued with two steps reaction (esterificationtransesterification).
This two-step process could lower the content of FFAs in waste
cooking oil in the first step and also improve conversion of transesterification in the
second step. The acid value of treated waste cooking oil was successfully reduced
from 5.16 mg KOH/g to 3.63 mg KOH/g by using acidic catalysed esterification
reaction with sulfuric acid as catalyst, methanol to oil ratio of 12:1 and reaction time
of 1 hour at 65°C. The combination of these processes gave higher biodiesel yield
(36.16%) under the optimum conditions. The biodiesel synthesized was analysed
using FTIR and GCMS to confirm the present of FAME |
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