Review Article

Recent Strategy of Biodiesel Production from Waste Cooking Oil and Process Influencing Parameters: A Review

Table 2

Recent research on waste cooking oil and operating parameters.

Oil types Type of alcohol Process methodParameters Catalyst type References
T°CC (catalyst percentage)M (alcohol to oil ratio and wt%)Speed (rpm)Time
A (acid catalyst)%B (base catalyst)%

Palm oilEthanolAcid-catalyzed transesterification90°C0.5, 1.0, 1.5, and 2.25 wt%25, 50, and 100%HCL, H2SO4 Al-Widyan and Al-Shyoukh (2002) [39]
Waste frying oilMethanolAlkali-catalyzed transesterification65°C5.3% of the KOH/MeOH solution5.3% of the KOH/MeOH solution90 minKOH Cvengroš and Cvengrošová (2004) [40]
Waste frying oilMethanolBase-catalyzed transesterification65°CBetween 0.2% and 1.0%3.6–5.41 hNaOH Felizardo et al. (2006) [41]
Waste cooking-oil collected from restaurantTwo-step catalyzed process95°C & 65°C0, 1, 2, 3, and 4 wt%1%3, 5, 7, 8, and 10 : 1, and 6 : 10.25 h, 0.5, 1, 2, 3 h, and 4 hFerric sulfate, KOH Wang et al. (2007) [42]
Sunflower oilMethanolBase-catalyzed transesterification25°C & 65°C0.5 and 1.0%3 : 1, 6 : 1, and 9 : 11–3 hKOH, NaOH Refaat et al. (2008) [43]
Canola oilEthanolBase-catalyzed transesterification60°C0.2, 0.4, 0.6, 0.8, 1.0, and 1.2%25 minNaOH Refaat et al. (2008) [44]
Sunflower oilBase-catalyzed transesterification40°C0.5–2.0%1 : 4.1 : 3, 3 : 1, 4 : 1, 6 : 1350 rpm3 hKOH, NaOH Hossain and Boyce (2009) [15]
Soybean oilMethanolethanol, butanol50°C–65°C0.5%1 : 4, 1 : 3, 1 : 2, 1 : 12 h and 6 hNaOH Hossain et al. (2010) [45]
Canola oilMethanolethanol, butanolBase-catalyzed transesterification0.5%1 : 4, 1 : 3, 1 : 2, 1 : 1250 rpm2 h and 6 hNaOH Hossain et al. (2010) [46]
Palm oilMethanolHeterogeneous transesterification90°C–150°C2–420 : 1, 30 : 1, 40 : 1120, 180, and 240 minZrO2 Wan Omar and Saidina Amin (2011) [47]
Palm oilMethanolEsterification50°C–65°C1–4%1 : 6, 1 : 1-0, 1 : 15700 rpm15–90 minIon-exchange resin catalysts Gan et al. (2012) [48]