应用化工
應用化工
응용화공
APPLIED CHEMICAL INDUSTRY
2014年
12期
2177-2181,2185
,共6页
Ti-USY%光催化%FCC汽油%氧化脱硫
Ti-USY%光催化%FCC汽油%氧化脫硫
Ti-USY%광최화%FCC기유%양화탈류
Ti-USY%photocatalytic%FCC gasoline%oxidation desulfuration
以钛酸四正丁酯为钛源,浸渍法制备了Ti-USY分子筛光催化剂,对光催化氧化汽油脱硫工艺条件(催化剂的加入量、氧化剂H2 O2的用量、反应温度、萃取剂)、催化剂再生性和二次重复使用的稳定性进行考察。结果表明, TiO2高度分散在USY分子筛表面上,催化剂样品均为典型的Ⅳ型吸附等温线,孔分布较窄。在催化剂的加入量为2 g/L,反应温度为40℃,水作为萃取剂,水油体积比为1:1,1.5 h光照反应条件下,FCC汽油的脱硫率可达到62.4%。Ti-USY催化剂经7次高温再生后,脱硫率下降较小,仍在58%以上。2次重复使用脱硫率为42.66%。证明Ti-USY分子筛光催化剂良好的催化性能、再生性及稳定性。动力学分析表明,Ti-USY分子筛对汽油硫化物的光催化氧化动力学遵循标准一级反应,表观活化能为9.046 kJ/mol。
以鈦痠四正丁酯為鈦源,浸漬法製備瞭Ti-USY分子篩光催化劑,對光催化氧化汽油脫硫工藝條件(催化劑的加入量、氧化劑H2 O2的用量、反應溫度、萃取劑)、催化劑再生性和二次重複使用的穩定性進行攷察。結果錶明, TiO2高度分散在USY分子篩錶麵上,催化劑樣品均為典型的Ⅳ型吸附等溫線,孔分佈較窄。在催化劑的加入量為2 g/L,反應溫度為40℃,水作為萃取劑,水油體積比為1:1,1.5 h光照反應條件下,FCC汽油的脫硫率可達到62.4%。Ti-USY催化劑經7次高溫再生後,脫硫率下降較小,仍在58%以上。2次重複使用脫硫率為42.66%。證明Ti-USY分子篩光催化劑良好的催化性能、再生性及穩定性。動力學分析錶明,Ti-USY分子篩對汽油硫化物的光催化氧化動力學遵循標準一級反應,錶觀活化能為9.046 kJ/mol。
이태산사정정지위태원,침지법제비료Ti-USY분자사광최화제,대광최화양화기유탈류공예조건(최화제적가입량、양화제H2 O2적용량、반응온도、췌취제)、최화제재생성화이차중복사용적은정성진행고찰。결과표명, TiO2고도분산재USY분자사표면상,최화제양품균위전형적Ⅳ형흡부등온선,공분포교착。재최화제적가입량위2 g/L,반응온도위40℃,수작위췌취제,수유체적비위1:1,1.5 h광조반응조건하,FCC기유적탈류솔가체도62.4%。Ti-USY최화제경7차고온재생후,탈류솔하강교소,잉재58%이상。2차중복사용탈류솔위42.66%。증명Ti-USY분자사광최화제량호적최화성능、재생성급은정성。동역학분석표명,Ti-USY분자사대기유류화물적광최화양화동역학준순표준일급반응,표관활화능위9.046 kJ/mol。
Ti-USY zeolite photocatalys were successfully synthesized by impregnation method using the ti-tanium-butoxide( TB)as titanium source. Study the photocatalytic oxidation desulfurization performance by using FCC gasoline as the raw material under UV light irradiation. The effects of the amount of cata-lyst,the amount of oxidant H2 O2 ,the reaction temperature,the extraction solvent,the regeneration and the secondary reuse stability of catalyst were investigated. Results showed that TiO2 dispers well on the surface USY. Samples are typical Ⅳ type adsorption isotherm and narrow pore size distribution. Under suitable conditions:the amount of catalyst was added at 2 g/L,the reaction temperature was 40℃,water as extrac-ting agent is selected,the volume ratio of water to oil is 1:1,illumination time is 1. 5 h. FCC gasoline des-ulfurization rate can reach 62 . 4%. After the Ti-USY catalyst were high-temperature regenerated by 7 times or was repeated using by 2 times,the desulfurization rate decreased less,still more than 58%and 42. 66%. Ti-USY zeolite catalytic has good performance in photocatalyst,reproducibility and stability. Ki-netic analysis showed that reaction kinetics of Ti-USY zeolite photocatalytic oxidation gasoline desulfura-tion is first-order,apparent activation energy is 9. 046 kJ/mol.