化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2014年
12期
3393-3398
,共6页
离子液体%Schiff碱%Co络合物%氧化%脱硫
離子液體%Schiff堿%Co絡閤物%氧化%脫硫
리자액체%Schiff감%Co락합물%양화%탈류
ionic liquids%Schiff-base%Cobalt complex%oxidation%desulfurization
将离子液体FeCl3/BmimCl与Schiff碱Co络合物CoL组成催化体系,以氧气为氧化剂,噻吩的正辛烷溶液为模拟油,考察该脱硫体系脱除模拟油中噻吩硫的性能。结果表明,最佳脱硫条件为:模拟油25mL;IL-FeCl3/BmimCl摩尔比为1,8mL;O250mL/min;反应温度62℃;CoL0.13g;时间6h,最终脱硫率可达96%(质量分数),脱硫后油品中噻吩含量最终可降到50μg/g 以下。噻吩的氧化产物为 SO42-离子。离子液体再生4次后脱硫性能开始下降。该脱硫体系对实际柴油中的噻吩硫催化氧化脱硫效果可达100%,该脱硫体系具有实际应用意义。
將離子液體FeCl3/BmimCl與Schiff堿Co絡閤物CoL組成催化體繫,以氧氣為氧化劑,噻吩的正辛烷溶液為模擬油,攷察該脫硫體繫脫除模擬油中噻吩硫的性能。結果錶明,最佳脫硫條件為:模擬油25mL;IL-FeCl3/BmimCl摩爾比為1,8mL;O250mL/min;反應溫度62℃;CoL0.13g;時間6h,最終脫硫率可達96%(質量分數),脫硫後油品中噻吩含量最終可降到50μg/g 以下。噻吩的氧化產物為 SO42-離子。離子液體再生4次後脫硫性能開始下降。該脫硫體繫對實際柴油中的噻吩硫催化氧化脫硫效果可達100%,該脫硫體繫具有實際應用意義。
장리자액체FeCl3/BmimCl여Schiff감Co락합물CoL조성최화체계,이양기위양화제,새분적정신완용액위모의유,고찰해탈류체계탈제모의유중새분류적성능。결과표명,최가탈류조건위:모의유25mL;IL-FeCl3/BmimCl마이비위1,8mL;O250mL/min;반응온도62℃;CoL0.13g;시간6h,최종탈류솔가체96%(질량분수),탈류후유품중새분함량최종가강도50μg/g 이하。새분적양화산물위 SO42-리자。리자액체재생4차후탈류성능개시하강。해탈류체계대실제시유중적새분류최화양화탈류효과가체100%,해탈류체계구유실제응용의의。
The oxidative desulfurization performance on model oil with thiophene was investigated with ionic liquid FeCl3/BmimCl and Schiff-base cobalt complex CoL and oxygen as the desulfurization system. Thiophene removal rate could reach 96%under the optimum condition,in which model oil dosage was 25mL,mole ratio of FeCl3/BmimCl was 1∶1 and its dosage was 8 mL,oxygen flow rate was 50 mL/min,reaction temperature was 62℃,CoL dosage was 0.13g,reaction time was 6h. The final thiophene content in the desulfurized model oil could be less than 50μg/g,and the oxidation product of thiophene was SO42?. The ionic liquid FeCl3/BmimCl could be recycled 4 times without significant decrease in desulfurization capability. The oxidative desulfurization rate of diesel oil could reach 100%with the above desulfurization system,which had good application prospect.