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    Technoeconomic analysis of biofuel production from spent coffee grounds using supercritical ethyl acetate
    (2026-03-01)
    Supang, Wirasinee
    ;
    Ngamprasertsith, Somkiat
    ;
    ;
    Sawangkeaw, Ruengwit
    This study is a techno-economic analysis of biodiesel production from spent coffee grounds (SCGs) using ethyl acetate as an extracting solvent and a reactant through interesterification under supercritical conditions—a process called SCEA. Aspen Plus V12 was employed to simulate the SCEA process compared to the conventional biodiesel production process. Both processes operated at an original feed rate of 24,225 tonnes per year, but the production capacities of the conventional and SCEA processes were 1000 tonnes per year and 1800 tonnes per year, respectively. Because of the simplicity of SCEA, the fixed capital investment costs were lower than those of the conventional process. However, at the original feed rate, neither process was profitable within a project lifetime of 20 years. The production capacity of SCEA was increased to 4 times, 8 times, and 16 times its original size to identify the most effective scale for the production facility. The SCEA process commenced successfully with a production capacity of 7500 tonnes per year, but the payback period of 19.5 years was deemed unsatisfactory. The production capacities of 15,000 tonnes per year and 30,000 tonnes per year provided the payback periods of 7.67 years and 6.08 years, respectively. Nonetheless, the 15,000-ton plant requires 193,798 tonnes SCGs per year as feedstock, which is 12 times the annual coffee production in Thailand. Hence, this project is well-suited for large coffee producers when utilizing SCGs as a singular feedstock. Combining other feedstocks, such as microalgae, non-edible seeds, and waste fruit seeds, with SCGs presents an optional pathway for future research on biodiesel production.
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    Item type:Publication,
    Ethyl acetate as extracting solvent and reactant for producing biodiesel from spent coffee grounds: A catalyst- and glycerol-free process
    (2022-07-01)
    Supang, Wirasinee
    ;
    Ngamprasertsith, Somkiat
    ;
    ;
    Sawangkeaw, Ruengwit
    Oil was extracted from spent coffee grounds (SCGs) using ethyl acetate at atmospheric pressure; then, the ethyl acetate–SCG oil mixture was reacted under supercritical conditions, which involve a catalyst-free process. Moreover, ethyl acetate reacted with glycerol to form triacetin, which dissolves in biodiesel and acts as a fuel additive. Using this approach, the solvent removal step and glycerol byproducts are eliminated. The highest fatty acid ethyl ester contents of 91.80 wt% ± 1.62 wt% and 86.44 wt% ± 2.12 wt%. were obtained under optimal conditions in batch and continuous reactors, respectively. Based on gas chromatography–mass spectrometric analysis, no trace of glycerol was detected and triacetin was yielded at 4.22 wt%. This novel process simultaneously minimizes the number of chemicals used and the amount of waste generated because it employs only dried SCGs and ethyl acetate as the feedstock.
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    Item type:Publication,
    Lipase – Catalyzed modification of rice bran oil solid fat fraction
    (2018-01-01)
    Kosiyanant, Patchara
    ;
    Pande, Garima
    ;
    Tungjaroenchai, Wanna
    ;
    Akoh, Casimir C.
    This study used a rice bran oil solid fat fraction (RBOSF) to produce cocoa butter alternatives via interesterification reaction catalyzed by immobilized lipase (Lipozyme® RM IM) in hexane. Effects of reaction time (6, 12, and 18 h), temperature (55, 60, and 65°C), mole ratios of 3 substrates [RBOSF:palm olein:C18:0 donors (1:1:2, 1:2:3, and 1:2:6)] were determined. The substrate system was dissolved in 3 mL of hexane and 10% of lipase was added. Two sources of C18:0 donors, stearic acid (SAd) and ethyl stearate (ESd) were used. Pancreatic lipase – catalyzed sn-2 positional analysis was also performed on both substrates and structured lipids (interesterification products). Structured lipids (SL) were analyzed by gas – liquid chromatography (G40.35LC) for fatty acid composition. Major fatty acids of RBOSF were C18:1, oleic acid (OA, 41.15±0.01%), C18:2, linoleic acid (LA, 30.05±0.01%) and C16:0, palmitic acid (PA, 22.64±0.01%), respectively. A commercial raw cocoa butter (CB) contained C18:0, stearic acid (SA, 33.13±0.04%), OA (32.52±0.03%), and PA (28.90±0.01%), respectively. Fatty acids at sn-2 position of RBOSF were OA (46.52±0.63%) and LA (42.98±1.1%), while major fatty acid at sn-2 position of CB was OA (85.24±1.22%). The RBOSF had low SA (2.40±0.01%) compared to CB (33.13±0.04%). The content of OA (46.52±0.63%) at sn-2 position in RBOSF was half of that found in CB (85.24±1.22%). Optimal reaction was 1:2:6 mole ratio of the substrate (RBOSF:PO:SAd), at 65°C for 12 h. Fatty acid compositions of the SL were 31.72±0.99% SA, 30.91±0.53% LA, 23.18±0.32% OA, and 13.26±0.34% PA, respectively. Fatty acids at sn-2 position of the SL were 53.72±4.21% OA, 25.11±3.69% LA, 14.18±1.58% PA, and 6.99±0.02% SA, respectively. DSC curves showed the melting point of CB at 20.94°C, while those of the SL were 14.15 and 40.35°C, respectively. The melting completion temperature (T<inf>mc</inf>) of CB was 25.5°C while that of SL was 43.9°C, respectively.