TY  - JOUR
SN  - 10226680
PB  - Trans Tech Publications Ltd
EP  - 71
AV  - none
N1  - cited By 1; Conference of International Conference on Process Engineering and Advanced Materials, ICPEAM 2012 ; Conference Date: 12 June 2012 Through 14 June 2012; Conference Code:106208
SP  - 63
TI  - Bio-oil derived from palm kernel shell in fluidized bed reactor: Effect of particle size
Y1  - 2014///
UR  - https://www.scopus.com/inward/record.uri?eid=2-s2.0-84904060166&doi=10.4028%2fwww.scientific.net%2fAMR.917.63&partnerID=40&md5=3346df07b720ce9f493502760de31823
A1  - Norizan, A.
A1  - Uemura, Y.
A1  - Wissam, N.O.
A1  - Tsutsui, T.
JF  - Advanced Materials Research
VL  - 917
CY  - Kuala Lumpur
N2  - Bio-oil production from pyrolysis of 0.15-0.5 mm and 1-2 mm palm kernel shell (PKS) has been investigated in a fluidized bed reactor under the nitrogen gas flow rate of 25 L(NTP)/min, with reactor temperature of 450°C. The pyrolysis unit has six successive condensers. Thus, six fractions of bio-oil samples were acquired from the six condensers. The calorific value, water content, ashcontent, and element content of each bio-oil samples were determined. The bio-oil yield from palm kernel shell with the size of 0.15-0.5 mm and 1-2 mm were 20 and 26, respectively. The highest calorific value among the six bio-oil samples was 25.1 MJ/kg which was drawn from the forth condenser from pyrolysis of 0.15-0.5 mm of palm kernel shell. The incondensable gas was a mixture of hydrogen, methane, carbon dioxide and ethane. © (2014) Trans Tech Publications, Switzerland.
KW  - Acetic acid; Calorific value; Carbon dioxide; Chemical reactors; Fluid catalytic cracking; Fluidized bed furnaces; Methane; Phenols; Process engineering; Shells (structures)
KW  -  Bio oil; Bio-oil yield; Element contents; Fluidized bed reactors; Nitrogen gas flow; Palm kernel shells; Reactor temperatures
KW  -  Biofuels
ID  - scholars5162
ER  -