TY - JOUR
T1 - Selective synthesis of middle isoparaffins via a two-stage Fischer-Tropsch reaction
T2 - Activity investigation for a hybrid catalyst
AU - Zhao, Tian Sheng
AU - Chang, Jie
AU - Yoneyama, Yoshiharu
AU - Tsubaki, Noritatsu
PY - 2005/2/16
Y1 - 2005/2/16
N2 - The activity of hybrid catalysts for the direct isoparaffin synthesis, especially C4-C6 with a very high octane number, from Fischer-Tropsch synthesis (FTS) in a two-stage reactor was investigated. The hybrid of Co/SiO2 and H-ZSM-5 was used as the first-stage reaction catalyst, and different types of H zeolites alone or their hybrid with Pd/SiO2 were used as the second-stage reaction catalysts. The obtained results demonstrated that the carbon number of products could terminate at 6 and isoparaffin hydrocarbons could be synthesized in very high selectivity from synthesis gas compared with that in a single-stage reaction using a physically mixed Co/SiO2 and H-ZSM-5 catalyst. The first-stage Co/SiO2 + H-ZSM-5 catalyst made the products mainly distribute in the C1-C11 range and considerably increase in the corresponding isoparaffins because of successive cracking, as well as isomerization, of the primary FTS products on H-ZSM-5. The selectivities of isoparaffins with much lower carbon number were further raised through the hydrocracking and isomerization of the first-stage reaction products on the second-stage H-zeolite catalysts in the presence of hydrogen. In addition, the effect of the reaction temperature suggested that an appropriate temperature combination of the first- and second-stage reactions was necessary. Using Co/SiO2 + H-ZSM-5 and H-Beta + Pd/SiO2 as the first- and second-stage catalysts, respectively, with a suitable temperature selection for the first- and second-stage reactor, a selectivity of 64.4% for C 4-C6 isoparaffins was achieved. With the hybrid of H-ZSM-5 in the first-stage catalyst, heavier hydrocarbon deposition was removed near Co/SiO2 and the catalyst life was stabilized; with the hybrid of Pd/SiO2 in the second-stage catalyst, the acid sites of H zeolites were maintained and strengthened by means of supposed hydrogen spillover. As a result of the overall effect, the lifetime of the catalysts was effectively extended.
AB - The activity of hybrid catalysts for the direct isoparaffin synthesis, especially C4-C6 with a very high octane number, from Fischer-Tropsch synthesis (FTS) in a two-stage reactor was investigated. The hybrid of Co/SiO2 and H-ZSM-5 was used as the first-stage reaction catalyst, and different types of H zeolites alone or their hybrid with Pd/SiO2 were used as the second-stage reaction catalysts. The obtained results demonstrated that the carbon number of products could terminate at 6 and isoparaffin hydrocarbons could be synthesized in very high selectivity from synthesis gas compared with that in a single-stage reaction using a physically mixed Co/SiO2 and H-ZSM-5 catalyst. The first-stage Co/SiO2 + H-ZSM-5 catalyst made the products mainly distribute in the C1-C11 range and considerably increase in the corresponding isoparaffins because of successive cracking, as well as isomerization, of the primary FTS products on H-ZSM-5. The selectivities of isoparaffins with much lower carbon number were further raised through the hydrocracking and isomerization of the first-stage reaction products on the second-stage H-zeolite catalysts in the presence of hydrogen. In addition, the effect of the reaction temperature suggested that an appropriate temperature combination of the first- and second-stage reactions was necessary. Using Co/SiO2 + H-ZSM-5 and H-Beta + Pd/SiO2 as the first- and second-stage catalysts, respectively, with a suitable temperature selection for the first- and second-stage reactor, a selectivity of 64.4% for C 4-C6 isoparaffins was achieved. With the hybrid of H-ZSM-5 in the first-stage catalyst, heavier hydrocarbon deposition was removed near Co/SiO2 and the catalyst life was stabilized; with the hybrid of Pd/SiO2 in the second-stage catalyst, the acid sites of H zeolites were maintained and strengthened by means of supposed hydrogen spillover. As a result of the overall effect, the lifetime of the catalysts was effectively extended.
UR - http://www.scopus.com/inward/record.url?scp=13544259557&partnerID=8YFLogxK
U2 - 10.1021/ie040097o
DO - 10.1021/ie040097o
M3 - 学術論文
AN - SCOPUS:13544259557
SN - 0888-5885
VL - 44
SP - 769
EP - 775
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 4
ER -