轻烃异构化一般以C_(5)和C_(6)烃为原料,C_(7)及C_(7)以上烃类在异构化过程中由于存在较为剧烈的裂化反应,致使异构化油收率较低。作为一种新型低温轻烃异构化催化剂,离子液体对大分子烃类原料的适应性不佳。因此,在大分子烃类异构化过...轻烃异构化一般以C_(5)和C_(6)烃为原料,C_(7)及C_(7)以上烃类在异构化过程中由于存在较为剧烈的裂化反应,致使异构化油收率较低。作为一种新型低温轻烃异构化催化剂,离子液体对大分子烃类原料的适应性不佳。因此,在大分子烃类异构化过程中,抑制副反应、提高异构化油收率一直是研究的难点和重点。基于离子液体催化烷烃异构化反应机理,通过异丁烷循环抑制副反应、促进异构化反应的进行,进而降低异构化产物中C_(4)烷烃的含量,提高异构化油的收率。系统考察了异丁烷引入量、反应温度、反应时间、搅拌速率以及酸烃比等工艺条件对氯铝酸离子液体催化正庚烷异构化反应的影响规律。结果表明,体系中大量异丁烷的循环提高了氢转移速率,抑制了裂化、歧化等副反应,使副产物C 4组分的含量大幅降低。在异丁烷引入量为正庚烷体积的30%、反应温度为50℃、反应时间为1 h、搅拌速率为1500 r min和酸烃比(离子液体与正庚烷体积比)为1的条件下,正庚烷转化率达到91.0%,异构烷烃选择性和液体收率分别达到87.2%和93.5%;与未引入异丁烷体系相比,正庚烷转化率相近时,引入异丁烷体系的异构烷烃选择性和液体收率分别提高了16.0百分点和14.8百分点。展开更多
为了理解甲醇/柴油双燃料机的自燃特性并为燃烧计算所需骨架机理提供理论依据,以正庚烷作为柴油替代物,应用快速压缩机对宽广实验条件下甲醇/正庚烷混合燃料的自燃特性进行了研究。实验条件覆盖了甲醇/柴油双燃料机的典型工况。实验研...为了理解甲醇/柴油双燃料机的自燃特性并为燃烧计算所需骨架机理提供理论依据,以正庚烷作为柴油替代物,应用快速压缩机对宽广实验条件下甲醇/正庚烷混合燃料的自燃特性进行了研究。实验条件覆盖了甲醇/柴油双燃料机的典型工况。实验研究结果显示,随着压力升高、甲醇比例减少或当量比增大,混合燃料滞燃期变短。根据实验数据验证了爱尔兰国立大学(National University of Ireland,NUI)的正庚烷详细机理对甲醇/正庚烷的适用性,并利用该机理在CHEMKIN PRO软件中进行了化学动力学分析。结果表明,甲醇与正庚烷竞争羟基(hydroxyl,OH)从而抑制系统氧化过程。敏感性分析结果显示,超氧化氢(HO_(2))反应生成过氧化氢(H_(2)O_(2))是燃烧过程中最敏感的反应,抑制系统氧化过程的进行。本研究可为获得适用于甲醇/柴油双燃料机燃烧计算的骨架机理提供理论依据。展开更多
The Pt-supported USY zeolite catalysts doped with Cr, Al or Zn were prepared by impregnation, and characterized by XRD, low temperature nitrogen physisorption, H2-chemisorption and IR spectroscopy of the pyridine adso...The Pt-supported USY zeolite catalysts doped with Cr, Al or Zn were prepared by impregnation, and characterized by XRD, low temperature nitrogen physisorption, H2-chemisorption and IR spectroscopy of the pyridine adsorption. Catalytic activities were evaluated via the hydroisomerization of n-heptane with an atmospheric fixed-bed reactor. The Pt dispersion and acidity of the Pt-supported USY catalyst were influenced by the addition of the promoters. The Pt-supported catalysts promoted by Cr, Al or Zn, especially by Cr, were catalytically much more stable and exhibited much higher catalytic activity and selectivity for isomerization of n-heptane than the catalysts without the dopant. Both the conversion and selectivity are discussed in relation with the physicochemical properties of catalysts.展开更多
The Pt-bearing SO42-/ZrO2 superacid catalysts supported on ultra stable Y (USY) zeolite were prepared by impregnation and characterized by X-ray diffracti on, nitrogen adsorption and Hammett indicators. Their catalyti...The Pt-bearing SO42-/ZrO2 superacid catalysts supported on ultra stable Y (USY) zeolite were prepared by impregnation and characterized by X-ray diffracti on, nitrogen adsorption and Hammett indicators. Their catalytic activities were evaluated in the hydroisomerization of n-heptane with an atmospheric fixed-bed r eactor. The catalysts possessed a high surface area, superacidity and well maint ained pore structure of USY support. The supported catalysts with a suitable SO4 2-/ZrO2 loading exhibited a higher catalytic activity and selectivity than the u nsupported SO42-/ZrO2 catalyst or the Pt supported on USY catalyst without super acid. At the reaction temperature of 220 ℃, over the catalyst with a Pt loading of 0.8wt% and ZrO2 loading of 10wt%, the conversion of n-heptane could be as hi gh as 35.2% with a selectivity of 87.9% for isomerization products.展开更多
文摘轻烃异构化一般以C_(5)和C_(6)烃为原料,C_(7)及C_(7)以上烃类在异构化过程中由于存在较为剧烈的裂化反应,致使异构化油收率较低。作为一种新型低温轻烃异构化催化剂,离子液体对大分子烃类原料的适应性不佳。因此,在大分子烃类异构化过程中,抑制副反应、提高异构化油收率一直是研究的难点和重点。基于离子液体催化烷烃异构化反应机理,通过异丁烷循环抑制副反应、促进异构化反应的进行,进而降低异构化产物中C_(4)烷烃的含量,提高异构化油的收率。系统考察了异丁烷引入量、反应温度、反应时间、搅拌速率以及酸烃比等工艺条件对氯铝酸离子液体催化正庚烷异构化反应的影响规律。结果表明,体系中大量异丁烷的循环提高了氢转移速率,抑制了裂化、歧化等副反应,使副产物C 4组分的含量大幅降低。在异丁烷引入量为正庚烷体积的30%、反应温度为50℃、反应时间为1 h、搅拌速率为1500 r min和酸烃比(离子液体与正庚烷体积比)为1的条件下,正庚烷转化率达到91.0%,异构烷烃选择性和液体收率分别达到87.2%和93.5%;与未引入异丁烷体系相比,正庚烷转化率相近时,引入异丁烷体系的异构烷烃选择性和液体收率分别提高了16.0百分点和14.8百分点。
文摘为了理解甲醇/柴油双燃料机的自燃特性并为燃烧计算所需骨架机理提供理论依据,以正庚烷作为柴油替代物,应用快速压缩机对宽广实验条件下甲醇/正庚烷混合燃料的自燃特性进行了研究。实验条件覆盖了甲醇/柴油双燃料机的典型工况。实验研究结果显示,随着压力升高、甲醇比例减少或当量比增大,混合燃料滞燃期变短。根据实验数据验证了爱尔兰国立大学(National University of Ireland,NUI)的正庚烷详细机理对甲醇/正庚烷的适用性,并利用该机理在CHEMKIN PRO软件中进行了化学动力学分析。结果表明,甲醇与正庚烷竞争羟基(hydroxyl,OH)从而抑制系统氧化过程。敏感性分析结果显示,超氧化氢(HO_(2))反应生成过氧化氢(H_(2)O_(2))是燃烧过程中最敏感的反应,抑制系统氧化过程的进行。本研究可为获得适用于甲醇/柴油双燃料机燃烧计算的骨架机理提供理论依据。
文摘The Pt-supported USY zeolite catalysts doped with Cr, Al or Zn were prepared by impregnation, and characterized by XRD, low temperature nitrogen physisorption, H2-chemisorption and IR spectroscopy of the pyridine adsorption. Catalytic activities were evaluated via the hydroisomerization of n-heptane with an atmospheric fixed-bed reactor. The Pt dispersion and acidity of the Pt-supported USY catalyst were influenced by the addition of the promoters. The Pt-supported catalysts promoted by Cr, Al or Zn, especially by Cr, were catalytically much more stable and exhibited much higher catalytic activity and selectivity for isomerization of n-heptane than the catalysts without the dopant. Both the conversion and selectivity are discussed in relation with the physicochemical properties of catalysts.
文摘The Pt-bearing SO42-/ZrO2 superacid catalysts supported on ultra stable Y (USY) zeolite were prepared by impregnation and characterized by X-ray diffracti on, nitrogen adsorption and Hammett indicators. Their catalytic activities were evaluated in the hydroisomerization of n-heptane with an atmospheric fixed-bed r eactor. The catalysts possessed a high surface area, superacidity and well maint ained pore structure of USY support. The supported catalysts with a suitable SO4 2-/ZrO2 loading exhibited a higher catalytic activity and selectivity than the u nsupported SO42-/ZrO2 catalyst or the Pt supported on USY catalyst without super acid. At the reaction temperature of 220 ℃, over the catalyst with a Pt loading of 0.8wt% and ZrO2 loading of 10wt%, the conversion of n-heptane could be as hi gh as 35.2% with a selectivity of 87.9% for isomerization products.
