TY - GEN
T1 - The effect of time dealumination and solvent concentration in synthesis of zeolite catalyst and catalytic test for DiEthyl Ether production process
AU - Widayat,
AU - Roesyadi, A.
AU - Rachimoellah, M.
PY - 2009
Y1 - 2009
N2 - Ethanol is an alternative energy, but its has three distinct disadvantages as a transportation fuel. Its availability is currently limited, and it has a lower volumetric heating value and a lower Reid vapour pressure (RVP) than gasoline. This paper focuses for this disadvantages and to solve this problem can do with converts ethanol to DiEthyl Ether product. This research produced DiEthyl Ether by ethanol dehydration process with zeolite as catalyst. The catalyst synthesis from natural material from District Gunung Kidul, Indonesia. The catalyst produced with dealumination, neutralization, drying and calcination processes. The zeolite catalyst was analysed of Si/Al, X-ray Diffraction and specific surface area. The catalyst product then used for ethanol dehydration to produce DiEthyl Ether. The results shown the biggest surface area is 184,52 m 2 /gram at catalyst production at 10 hours for time dealumination. The crystallite of catalyst product is similar like shown at diffractogram of XRD analysis. The ratio Si/Al biggest is 313.7 that obtaining at catalyst production with 7 hours for time dealumination. The catalytic test use fixed bed reactor with 1 inci diameter and ethanol fermentation borth as feed. The operation condition is 150°C at temperature and atmosphere pressure. The compounds product in liquid phase are diethyl ether, methanol and water.
AB - Ethanol is an alternative energy, but its has three distinct disadvantages as a transportation fuel. Its availability is currently limited, and it has a lower volumetric heating value and a lower Reid vapour pressure (RVP) than gasoline. This paper focuses for this disadvantages and to solve this problem can do with converts ethanol to DiEthyl Ether product. This research produced DiEthyl Ether by ethanol dehydration process with zeolite as catalyst. The catalyst synthesis from natural material from District Gunung Kidul, Indonesia. The catalyst produced with dealumination, neutralization, drying and calcination processes. The zeolite catalyst was analysed of Si/Al, X-ray Diffraction and specific surface area. The catalyst product then used for ethanol dehydration to produce DiEthyl Ether. The results shown the biggest surface area is 184,52 m 2 /gram at catalyst production at 10 hours for time dealumination. The crystallite of catalyst product is similar like shown at diffractogram of XRD analysis. The ratio Si/Al biggest is 313.7 that obtaining at catalyst production with 7 hours for time dealumination. The catalytic test use fixed bed reactor with 1 inci diameter and ethanol fermentation borth as feed. The operation condition is 150°C at temperature and atmosphere pressure. The compounds product in liquid phase are diethyl ether, methanol and water.
KW - Conversion of ethanol
KW - Spesific surface area
KW - Time dealumination
KW - XRD analysis
UR - http://www.scopus.com/inward/record.url?scp=70449595675&partnerID=8YFLogxK
U2 - 10.1061/41069(360)106
DO - 10.1061/41069(360)106
M3 - Conference contribution
AN - SCOPUS:70449595675
SN - 9780784410691
T3 - Pipelines 2009: Infrastructure's Hidden Assets - Proceedings of the Pipelines 2009 Conference
SP - 106
EP - 112
BT - Pipelines 2009
T2 - Pipelines 2009 Conference, Pipelines 2009: Infrastructure's Hidden Assets
Y2 - 15 August 2009 through 19 August 2009
ER -