以噻吩/石油醚模拟油为原料、Ag/γ-Al2O3为催化剂、氧气为氧化剂,研究了催化氧化深度脱硫技术,对催化剂进行了X射线衍射(XRD)和低温氮吸附表征,并考察了催化剂用量、反应温度、反应时间和萃取条件对脱硫效果的影响。在噻吩/石油醚模拟油20 mL、Ag/γ-Al2O3催化剂0.12 g、氧化温度70℃的反应条件下,氧化50 min后,将得到的产物采用甲醇为萃取剂,在20℃、剂油体积比1∶1的条件下萃取30 min,脱硫率达到98.1%。反应动力学研究结果表明,噻吩氧化过程可用一级反应动力学方程式来表示,其表达式为:k=0.049 45 exp[-10 683.4/(RT)]。
The deep catalytic oxidation desulfurization of model oil(thiophene/petroleum ether) was studied using Ag/γ-Al 2 O 3 as catalyst and gaseous oxygen as oxidant.The catalyst was characterized by X-ray diffraction(XRD) and low temperature N 2-adsorption techniques.The effects of catalyst amount,reaction temperature and time,as well as extraction conditions on the oxidation desulfurization were investigated.Test results showed that using 20 mL of model oil,0.12 g of catalyst,reacting at 70 ℃ for 50 min,the obtained material was extracted by methanol at 20 ℃ for 30 min with a solvent/oil volume ratio of 1,the rate of desulphurization reached 98.1%.The kinetic study indicates that catalytic oxidation of thiophene is a pseudo first-order reaction,which could be expressed as k = 0.049 45 × exp[-10 683.4/(RT) ].