Biodiesel Production from Free Fatty Acid using ZrO 2/Bagasse Fly Ash Catalyst
被引:4
|
作者:
Rahma, Fadilla Noor
论文数: 0引用数: 0
h-index: 0
机构:
Univ Islam Indonesia, Chem Engn Dept, Jalan Kaliurang Km 14, Yogyakarta 55584, IndonesiaUniv Islam Indonesia, Chem Engn Dept, Jalan Kaliurang Km 14, Yogyakarta 55584, Indonesia
Rahma, Fadilla Noor
[1
]
Hidayat, Arif
论文数: 0引用数: 0
h-index: 0
机构:
Univ Islam Indonesia, Chem Engn Dept, Jalan Kaliurang Km 14, Yogyakarta 55584, IndonesiaUniv Islam Indonesia, Chem Engn Dept, Jalan Kaliurang Km 14, Yogyakarta 55584, Indonesia
Hidayat, Arif
[1
]
机构:
[1] Univ Islam Indonesia, Chem Engn Dept, Jalan Kaliurang Km 14, Yogyakarta 55584, Indonesia
This study utilizes ZrO2/Bagasse Fly Ash as a solid catalyst to convert Free Fatty Acid (FFA) from Palm Fatty Acid Distillate (PFAD) into biodiesel. The ZrO2/Bagasse fly ash catalyst was characterized by several physicochemical techniques, i.e., N-2 adsorption-desorption, X-ray diffraction (XRD), and X-ray fluorescent (XRF). The catalyst was then applied for FFA esterification under different conditions. The highest FFA esterification conversion was 90.6%, which was reached at the optimal reaction condition as follows: methanol/PFAD mass ratio of 10:1; catalyst amount of 10 wt%; and reaction temperature of 60 degrees C. It was also found that the catalyst could be reused up to four times by an activation process. This study presented the Eley-Rideal kinetic model to describe the reaction mechanism. The model demonstrated an excellent fit to the experimental result with an R-2 value of 0.99, showing that Eley-Rideal is a valid model to describe the reaction and that the surface reaction step acts as the rate-determining step. Additionally, the reaction kinetics and adsorption equilibrium parameters were determined using non-linear regression. The correlation between the parameters with temperature was evaluated using Arrhenius and van't Hoff equations.
机构:
Petr Gas Univ Ploiesti, Fac Petr Refining & Petrochem, Ploiesti 100680, RomaniaPetr Gas Univ Ploiesti, Fac Petr Refining & Petrochem, Ploiesti 100680, Romania
Oprescu, Elena E.
Velea, Sanda
论文数: 0引用数: 0
h-index: 0
机构:
Natl Res & Dev Inst Chem & Petrochem ICECHIM, Bucharest 06002, RomaniaPetr Gas Univ Ploiesti, Fac Petr Refining & Petrochem, Ploiesti 100680, Romania
Velea, Sanda
Doncea, Sanda
论文数: 0引用数: 0
h-index: 0
机构:
Natl Res & Dev Inst Chem & Petrochem ICECHIM, Bucharest 06002, RomaniaPetr Gas Univ Ploiesti, Fac Petr Refining & Petrochem, Ploiesti 100680, Romania
Doncea, Sanda
Radu, Adrian
论文数: 0引用数: 0
h-index: 0
机构:
Natl Res & Dev Inst Chem & Petrochem ICECHIM, Bucharest 06002, RomaniaPetr Gas Univ Ploiesti, Fac Petr Refining & Petrochem, Ploiesti 100680, Romania
Radu, Adrian
Stepan, Emil
论文数: 0引用数: 0
h-index: 0
机构:
Natl Res & Dev Inst Chem & Petrochem ICECHIM, Bucharest 06002, RomaniaPetr Gas Univ Ploiesti, Fac Petr Refining & Petrochem, Ploiesti 100680, Romania
Stepan, Emil
Bolocan, Ion
论文数: 0引用数: 0
h-index: 0
机构:
Petr Gas Univ Ploiesti, Fac Petr Refining & Petrochem, Ploiesti 100680, RomaniaPetr Gas Univ Ploiesti, Fac Petr Refining & Petrochem, Ploiesti 100680, Romania
Bolocan, Ion
[J].
ICHEAP12: 12TH INTERNATIONAL CONFERENCE ON CHEMICAL & PROCESS ENGINEERING,
2015,
43
: 595
-
600
机构:
Univ Putra Malaysia, Fac Sci, Catalysis Sci & Technol Res Ctr, Serdang 43400, Selangor, Malaysia
Univ Putra Malaysia, Fac Sci, Dept Chem, Serdang 43400, Selangor, Malaysia
Univ Teknol MARA, Fac Sci Appl, Sch Chem, Shah Alam 40450, Selangor, MalaysiaUniv Putra Malaysia, Fac Sci, Catalysis Sci & Technol Res Ctr, Serdang 43400, Selangor, Malaysia
Lokman, Ibrahim M.
Rashid, Umer
论文数: 0引用数: 0
h-index: 0
机构:
Univ Putra Malaysia, Inst Adv Technol, Serdang 43400, Selangor, MalaysiaUniv Putra Malaysia, Fac Sci, Catalysis Sci & Technol Res Ctr, Serdang 43400, Selangor, Malaysia