催化学报
催化學報
최화학보
CHINESE JOURNAL OF CATALYSIS
2010年
4期
435-440
,共6页
何松波%赖玉龙%毕文君%杨旭%荣欣%孙承林
何鬆波%賴玉龍%畢文君%楊旭%榮訢%孫承林
하송파%뢰옥룡%필문군%양욱%영흔%손승림
铂%锡%碱金属钾%长链烷烃%脱氢%酸性%积炭
鉑%錫%堿金屬鉀%長鏈烷烴%脫氫%痠性%積炭
박%석%감금속갑%장련완경%탈경%산성%적탄
platinum%tin%alkali metal%long-chain paraffin%dehydrogenation%acidity%coking
以络合真空浸渍法制备了Pt-Sn-K/γ-Al_2O_3,催化剂.采用吡啶吸附红外光谱、CO脉冲吸附、程序升温还原、热重及程序升温氧化等手段对催化剂进行了表征,研究了K助剂对Pt-Sn-K/γ-Al_2O_3催化剂结构及其催化C_(16)正烷烃临氢脱氢反应性能的影响.结果表明,K的引入减弱了SnO_x和Al_2O_3间的相互作用,促进了Pt对SnO_x的还原,并导致催化剂的脱氢反应活性降低.K的加入还减少了强酸中心数目,一方面减少了催化剂酸性位上的副反应,提高了产物选择性;另一方面提高了催化剂的抗积炭能力,催化剂稳定性有所改善.但过量的K助剂减弱了催化剂的金属位-酸性位的协同作用,使得催化剂活性和稳定性均有所降低.
以絡閤真空浸漬法製備瞭Pt-Sn-K/γ-Al_2O_3,催化劑.採用吡啶吸附紅外光譜、CO脈遲吸附、程序升溫還原、熱重及程序升溫氧化等手段對催化劑進行瞭錶徵,研究瞭K助劑對Pt-Sn-K/γ-Al_2O_3催化劑結構及其催化C_(16)正烷烴臨氫脫氫反應性能的影響.結果錶明,K的引入減弱瞭SnO_x和Al_2O_3間的相互作用,促進瞭Pt對SnO_x的還原,併導緻催化劑的脫氫反應活性降低.K的加入還減少瞭彊痠中心數目,一方麵減少瞭催化劑痠性位上的副反應,提高瞭產物選擇性;另一方麵提高瞭催化劑的抗積炭能力,催化劑穩定性有所改善.但過量的K助劑減弱瞭催化劑的金屬位-痠性位的協同作用,使得催化劑活性和穩定性均有所降低.
이락합진공침지법제비료Pt-Sn-K/γ-Al_2O_3,최화제.채용필정흡부홍외광보、CO맥충흡부、정서승온환원、열중급정서승온양화등수단대최화제진행료표정,연구료K조제대Pt-Sn-K/γ-Al_2O_3최화제결구급기최화C_(16)정완경림경탈경반응성능적영향.결과표명,K적인입감약료SnO_x화Al_2O_3간적상호작용,촉진료Pt대SnO_x적환원,병도치최화제적탈경반응활성강저.K적가입환감소료강산중심수목,일방면감소료최화제산성위상적부반응,제고료산물선택성;령일방면제고료최화제적항적탄능력,최화제은정성유소개선.단과량적K조제감약료최화제적금속위-산성위적협동작용,사득최화제활성화은정성균유소강저.
A Pt-Sn-K/γ-Al_2O_3 catalyst was prepared by complex impregnation under vacuum. The effect of the K promoter on the catalytic properties of the Pt-Sn-K/γ-Al_2O_3 catalyst for the dehydrogenation of long-chain paraffins to mono-olefins was investigated using n-hexadecane dehydrogenation as a test reaction. The catalyst was characterized by infrared spectroscopy of pyridine adsorption, CO pulse chemisorption, temperature-programmed reduction with H_2, thermogravimetric analysis, and temperature-programmed oxidation with O_2. The results show that the addition of K decreases the interaction of SnO_x and Al_2O_3, promotes the reduction of SnO_x species, and suppresses the catalyst activity for dehydrogenation. The K promoter also neutralizes the acidity and decreases the amount of strong acidic centers of the catalyst. Thus, the side reactions on the catalyst are inhibited, and the selectivity for monoolefins is increased. The stability of the catalyst is slightly enhanced with the addition of K because of the increased resistance to coke formation on the catalyst. However, the synergistic effect of active sites and acidic sites is weakened by the excess addition of the K promoter, which results in a great decrease in the activity and a low stability of the catalyst.