Pt/SAPO-11催化剂上正十四烷临氢异构化 Ⅰ.反应条件对催化性能及稳定性的影响

Hydroisomerization of n-tetradecane over Pt/SAPO-11 catalyst Ⅰ.Effect of reaction parameters on catalyst performance and stability

以正十四烷为原料,在连续流动的固定床反应装置上,通过改变温度、压力、空速以及氢烃摩尔比等参数,考察了0.6%Pt/SAPO-11催化剂的异构化性能。结果表明,反应压力与氢烃摩尔比较低时,该催化剂仍具有良好的异构化选择性和催化稳定性。正十四烷反应的转化率高达95%时,异构化选择性仍保持在90%左右。正十四烷的转化率随温度的升高,压力、进料空速和氢烃摩尔比的降低而增大;异构化选择性呈现复杂的变化规律,反应压力和温度过高、进料空速和氢烃摩尔比太小都不利于异构体的生成。各反应参数不是单独起作用,它们之间存在相互作用;即一个参数变化时,需要其他参数的调整来获得最大的异构体收率。获得了正十四烷临氢异构的最佳条件为300℃~330℃,0.5MPa^2.0MPa,WHSV<10 h-1,H2/CH摩尔比1.1~8.7。

Hydroisomerization of n -tetradecane over a Pt/SAPO-11 catalyst with 0.6% metal loading was carded out in a fixed-bed down-flow reactor system. Reaction parameters such as temperature, pressure and WHSV, as well as the H2/CH molar ratio were varied in order to investigate the catalytic behavior, and thus to obtain the optimum reaction conditions. The catalytic performance was influenced by those reaction variables. It was shown that reaction temperature has the greatest impact on the hydroisomerization of n -tetradecane. The conversion of n -tetradecane increases up to 95% with increasing reaction temperature up to 340 ℃, while the isomerization selectivity lowers to about 87%. Increasing reaction pressure up to 3.0 MPa has a negative effect on hydroconversion of n -tetradecane, but has little impact on the isomerization selectivity. With increasing WHSV, the n -tetradecane conversion decreases accordingly, but the isomerization selectivity increases a few units. The influence of H2/CH ratio on the catalytic performance presented a more complicated picture, and its effect was found to be relevant with other reaction parameters. At low reaction temperatures with conversion level less than 92%, nearly the same trends, sharp change of conversion and small change of selectivity, were observed as that of changing WHSV. However, at higher reaction temperatures with conversion level of above 95 %, the HJCH rise favors the isomerization selectivity, while the conversion decreases a little. Catalytic stability was found to be largely influenced by both reaction pressure and the H2/CH ratio. Fast deactivation was observed at atmospheric pressure, and stable catalytic performance was realized under high pressures above 0.5 MPa. It should be point out that a critical minimal H2/CH ratio should be used in order to maintain the stable catalytic performance under higher pressures. It was also found that the ratio should be increased when the hydroisomerization was carried out at higher reaction temperatures. These results were in good agreement with our previous findings for the hydroisomerization of n-heptane over 0.4% Pt/SAPO-11 catalyst. The conclusion could be drawn from the obtained data that the reaction parameters interact with each other, which indicates that variation of one parameter needs the adjusting of others in order to gain a maximum isomerization yield. Moreover, the optimum reaction parameters are obtained for an optimal performance of hydroisomerization n -tetradecane ： temperature 300 ℃ - 330 ℃, pressure 0.5 MPa -2.0 MPa, WHSV 〈 10 h^-1 and H2/CH 1.1 - 8.7. Under these conditions, excellent selectivity and stability of the catalyst were observed at low pressure and H2/CH ratio. High selectivity to i -C 14 above 90% could be maintained even with conversion up to 95%.