2016
DOI: 10.1016/j.jclepro.2015.06.112
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Cleaner production of methyl ester using waste cooking oil derived from palm olein using a hydrodynamic cavitation reactor

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Cited by 115 publications
(38 citation statements)
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“…The temperature of the reactor has been maintained at a desired level by heater temperature. The more detail information of newly designed four orifice plates had been reported in previous paper (Chuah et al, 2015b). The diameter, hole number, total flow area and total perimeter values of the orifice plates are plate 1 -4.58 mm, 1, 16.5 mm 2 and 14.39 mm, plate 2 -1.00 mm, 21, 16.5 mm 2 and 65.98 mm, plate 3 -2.00 mm, 9, 28.3 mm 2 and 56.56 mm and plate 4-3.00 mm, 5, 35.3 mm 2 and 47.13 mm.…”
Section: Hydrodynamic Cavitation Reactor Configuration and Experimentmentioning
confidence: 99%
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“…The temperature of the reactor has been maintained at a desired level by heater temperature. The more detail information of newly designed four orifice plates had been reported in previous paper (Chuah et al, 2015b). The diameter, hole number, total flow area and total perimeter values of the orifice plates are plate 1 -4.58 mm, 1, 16.5 mm 2 and 14.39 mm, plate 2 -1.00 mm, 21, 16.5 mm 2 and 65.98 mm, plate 3 -2.00 mm, 9, 28.3 mm 2 and 56.56 mm and plate 4-3.00 mm, 5, 35.3 mm 2 and 47.13 mm.…”
Section: Hydrodynamic Cavitation Reactor Configuration and Experimentmentioning
confidence: 99%
“…However, there is no detailed information in the literature regarding the hole spacing and distribution pattern of holes in the plates. So far it has not been many works published on the design of the plate geometry, which is a crucial factor for designing the large scale reactor and also enhance the performance of methyl ester conversion (Chuah et al, 2015b). This study exploits the results of the previous work (Chuah et al, 2015b), which investigated the transesterification reaction of waste cooking oil (2.04 mg KOH/g) in a pilot HC reactor.…”
Section: Introductionmentioning
confidence: 99%
“…The lower smoke density of 18.8 HSU was obtained, when the fuel B100K was tested at full load conditions. Since BK and its blends are oxygenated fuels, they endorse better combustion and the outcome is in the reduction of smoke density 19,20 .…”
Section: Smoke Densitymentioning
confidence: 99%
“…Thus, they need to be converted into biodiesel via a number of processes such as transesterification (Sharma et al, 2008). In the transesterification reaction, triglycerides react with an alcohol (methanol or ethanol) in the presence of a catalyst (Chuah et al, 2015b). The catalyst could be either acidic or basic depending on the free fatty acid content of the oil feedstock (Georgogianni et al, 2009).…”
Section: Introductionmentioning
confidence: 99%
“…Various non-edible oils have been used for biodiesel production through transesterification of triglycerides by using different methods, such as mechanical stirring, supercritical procedure (Ong et al, 2013), ultrasonic techniques (Ji et al, 2006), hydrodynamic cavitation (Chuah et al, 2015b), and microwave (Lee et al, 2010). However, only a few studies have reported on biodiesel production from Kapok seed oil (KSO).…”
Section: Introductionmentioning
confidence: 99%