TY - JOUR
T1 - Industrial development of long chain paraffin (n-C10-C13) dehydrogenation catalysts and the deactivation characterization
AU - He, Songbo
AU - Wang, Bin
AU - Dai, Xihai
AU - Sun, Chenglin
AU - Bai, Ziwu
AU - Wang, Xiao
AU - Guo, Qi
PY - 2015
Y1 - 2015
N2 - Pt–Sn–K–Mg/Al2O3 catalysts for the dehydrogenation of long chain paraffins (n-C100–C130) were successfully developed and applied in the industry. The catalysts were tested on both the industrial side fixed bed reactor and the industrial PACOL dehydrogenation plant. The industrially deactivated Pt–Sn–K–Mg/Al2O3 catalysts were characterized by TG–DTA, elemental analysis, UV Raman spectroscopy, TPO, SEM, XRD, BET, MIP and CO-chemisorption. The industrial 72-day-run dada indicated that Pt–Sn–K–Mg/Al2O3 catalysts performed excellent dehydrogenation conversion of 11.6% and high mono-olefin selectivity of 94.1%. The daily output of alkylbenzene over Pt–Sn–K–Mg/Al2O3 catalysts was as high as 333.6 ton/day. The deactivated catalysts were deposited by the amorphous and graphitized coke, of which the weight percentage was 3.78% and the H/C mole ratio was 1.19. The coke covered parts of the Pt and support surface, while the pore and crystalline structure of the catalysts were not destroyed
AB - Pt–Sn–K–Mg/Al2O3 catalysts for the dehydrogenation of long chain paraffins (n-C100–C130) were successfully developed and applied in the industry. The catalysts were tested on both the industrial side fixed bed reactor and the industrial PACOL dehydrogenation plant. The industrially deactivated Pt–Sn–K–Mg/Al2O3 catalysts were characterized by TG–DTA, elemental analysis, UV Raman spectroscopy, TPO, SEM, XRD, BET, MIP and CO-chemisorption. The industrial 72-day-run dada indicated that Pt–Sn–K–Mg/Al2O3 catalysts performed excellent dehydrogenation conversion of 11.6% and high mono-olefin selectivity of 94.1%. The daily output of alkylbenzene over Pt–Sn–K–Mg/Al2O3 catalysts was as high as 333.6 ton/day. The deactivated catalysts were deposited by the amorphous and graphitized coke, of which the weight percentage was 3.78% and the H/C mole ratio was 1.19. The coke covered parts of the Pt and support surface, while the pore and crystalline structure of the catalysts were not destroyed
KW - n/a OA procedure
U2 - 10.1016/j.cej.2015.04.050
DO - 10.1016/j.cej.2015.04.050
M3 - Article
SN - 1385-8947
VL - 275
SP - 298
EP - 304
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
ER -