Premium
Transesterification of Rapeseed Oil for Synthesizing Biodiesel by K/KOH/γ‐Al 2 O 3 as Heterogeneous Base Catalyst
Author(s) -
Ma Hongbin,
Li Shufen,
Wang Boyang,
Wang Ruihong,
Tian Songjiang
Publication year - 2008
Publication title -
journal of the american oil chemists' society
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.512
H-Index - 117
eISSN - 1558-9331
pISSN - 0003-021X
DOI - 10.1007/s11746-007-1188-4
Subject(s) - transesterification , catalysis , biodiesel , methanol , rapeseed , base (topology) , x ray photoelectron spectroscopy , biodiesel production , nuclear chemistry , yield (engineering) , materials science , heterogeneous catalysis , chemistry , chemical engineering , organic chemistry , composite material , mathematical analysis , food science , mathematics , engineering
The heterogeneous base catalyst, γ‐Al 2 O 3 loaded with KOH and K (K/KOH/γ‐Al 2 O 3 ) was first prepared and used in the transesterification of rapeseed oil with methanol to produce biodiesel. The prepared catalyst was characterized by X‐ray diffraction, scanning electron microscopy, Brunauer–Emmett–Teller method, infrared spectroscopy and X‐ray photoelectron spectroscopy. It was found that when γ‐Al 2 O 3 is loaded with KOH and K, the Al–O–K species is produced, resulting in an increase in the catalytic activity. The impacts of catalyst preparation conditions on the catalytic activities of K/KOH/γ‐Al 2 O 3 were investigated. The results demonstrate that the catalyst K/KOH/γ‐Al 2 O 3 has high catalytic activity when the added amounts of KOH and K are 20 and 7.5 wt% respectively. The transesterification of rapeseed oil to biodiesel with the prepared heterogeneous base catalyst was optimized. It was found that the yield of biodiesel can reach as high as 84.52% after 1 h reaction at 60°C, with a 9:1 molar ratio of methanol to oil, a catalyst amount of 4 wt%, and a stirring rate of 270 g .