Studies on Aromatic Hydrogenation Catalysts and Kinetics
博士 === 國立成功大學 === 化學工程研究所 === 83 === High aromatics content in diesel fuel lowers fuel quality and contributes significantly to the formation of undesired emissions in exhaust gases . Because of the health hazards associated with these emissions , the env...
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ndltd-TW-083NCKU00630792015-10-13T12:53:32Z http://ndltd.ncl.edu.tw/handle/95581844386595119599 Studies on Aromatic Hydrogenation Catalysts and Kinetics 芳香烴氫化觸媒及其反應動力學研究 Ben-Chang Kang 康文成 博士 國立成功大學 化學工程研究所 83 High aromatics content in diesel fuel lowers fuel quality and contributes significantly to the formation of undesired emissions in exhaust gases . Because of the health hazards associated with these emissions , the environmental regulations governing the composition and limitations of aromatics in diesel fuels are being tightened in the developed nations . In this work , biaromatic compound naphthalene dissolved in n- hexadecane was used as a model compound to simulate aromatics in diesel fuels . Platinum is the most active noble metal supported on γ-Al2O3 for aromatic hydrogentation at high pressure . The optimal content of Pt was about 0.6-1.0 wt% . The Pt/AAPx(alumina-aluminum phosphate) and Pt/ABx(aluminum borate) catalysts have better aromatic hydrogen-ation activity and thioresistance , but a lower cis-decalin selectivity than Pt/γ-Al2O3 due to the more acidity of AAPx and ABx supports than γ-Al2O3 . Large pore size of Pt/AAPcatalyst can be obtained with good hydrogenation activity and thioresistance . Adding phosphorus or boron to γ-Al2O3 support can improve the aromatic hydrogenation activity and thioresistance of Pt/γ-Al2 O3 catalyst . But the activity and thioresistance of Pt-Px/Al2 O3 is not so good as Pt/Bx-Al2O3 catalyst . Experimental results also in- dicate that more sulfur can be adsorbed on catalyst at lower temperature , higher sulfur concentration and low hydrogen pressure. The hydrogenation activity and selectivity were investigated by using a reaction network including isomerization of decalin and a power-law kinetic model . The rates of tetralin hydrogen- ation and cis-decalin isomerization could be described by pseudo- first-order kinetics in excess hydrogen . The apparent activation energy for hydrogenation of tetralin to cis-decalin and trans- decalin are 9.88 and 7.25 kcal/mole, respectively . Ting-Chia Huang 黃定加 1995 學位論文 ; thesis 179 zh-TW |
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博士 === 國立成功大學 === 化學工程研究所 === 83 === High aromatics content in diesel fuel lowers fuel quality and
contributes significantly to the formation of undesired
emissions in exhaust gases . Because of the health hazards
associated with these emissions , the environmental regulations
governing the composition and limitations of aromatics in
diesel fuels are being tightened in the developed nations . In
this work , biaromatic compound naphthalene dissolved in n-
hexadecane was used as a model compound to simulate aromatics
in diesel fuels . Platinum is the most active noble metal
supported on γ-Al2O3 for aromatic hydrogentation at high
pressure . The optimal content of Pt was about 0.6-1.0 wt% .
The Pt/AAPx(alumina-aluminum phosphate) and Pt/ABx(aluminum
borate) catalysts have better aromatic hydrogen-ation activity
and thioresistance , but a lower cis-decalin selectivity than
Pt/γ-Al2O3 due to the more acidity of AAPx and ABx supports
than γ-Al2O3 . Large pore size of Pt/AAPcatalyst can be
obtained with good hydrogenation activity and thioresistance .
Adding phosphorus or boron to γ-Al2O3 support can improve the
aromatic hydrogenation activity and thioresistance of Pt/γ-Al2
O3 catalyst . But the activity and thioresistance of Pt-Px/Al2
O3 is not so good as Pt/Bx-Al2O3 catalyst . Experimental
results also in- dicate that more sulfur can be adsorbed on
catalyst at lower temperature , higher sulfur concentration and
low hydrogen pressure. The hydrogenation activity and
selectivity were investigated by using a reaction network
including isomerization of decalin and a power-law kinetic
model . The rates of tetralin hydrogen- ation and cis-decalin
isomerization could be described by pseudo- first-order
kinetics in excess hydrogen . The apparent activation energy
for hydrogenation of tetralin to cis-decalin and trans- decalin
are 9.88 and 7.25 kcal/mole, respectively .
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author2 |
Ting-Chia Huang |
author_facet |
Ting-Chia Huang Ben-Chang Kang 康文成 |
author |
Ben-Chang Kang 康文成 |
spellingShingle |
Ben-Chang Kang 康文成 Studies on Aromatic Hydrogenation Catalysts and Kinetics |
author_sort |
Ben-Chang Kang |
title |
Studies on Aromatic Hydrogenation Catalysts and Kinetics |
title_short |
Studies on Aromatic Hydrogenation Catalysts and Kinetics |
title_full |
Studies on Aromatic Hydrogenation Catalysts and Kinetics |
title_fullStr |
Studies on Aromatic Hydrogenation Catalysts and Kinetics |
title_full_unstemmed |
Studies on Aromatic Hydrogenation Catalysts and Kinetics |
title_sort |
studies on aromatic hydrogenation catalysts and kinetics |
publishDate |
1995 |
url |
http://ndltd.ncl.edu.tw/handle/95581844386595119599 |
work_keys_str_mv |
AT benchangkang studiesonaromatichydrogenationcatalystsandkinetics AT kāngwénchéng studiesonaromatichydrogenationcatalystsandkinetics AT benchangkang fāngxiāngtīngqīnghuàchùméijíqífǎnyīngdònglìxuéyánjiū AT kāngwénchéng fāngxiāngtīngqīnghuàchùméijíqífǎnyīngdònglìxuéyánjiū |
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1716868121940197376 |