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1)  n heptane hydroisomerization
庚烷临氢异构化
2)  hydroisomerization of n-heptane
正庚烷临氢异构化
1.
Their catalytic activities were evaluated in the hydroisomerization of n-heptane with an atmospheric fixed-bed reactor.
用超稳Y沸石(USY)负载SO42-/ZrO2固体超强酸,并以此为载体制备含Pt双金属催化剂,用XRD和H2-TPR表征了催化剂的物化性质,并在常压固定床反应器上考察催化剂的正庚烷临氢异构化反应性能。
2.
Their catalytic behaviors were measured in the hydroisomerization of n-heptane in an atmospheric fixed-bed microreactor.
采用XRD和IR对催化剂进行了表征,并采用常压固定床反应器,考察了催化剂的正庚烷临氢异构化反应性能,与USY同时负载SiW和Pt的催化剂进行比较。
3)  n-heptane hydroisomerization
正庚烷临氢异构化
1.
The Pt/WGZ catalyst gave a constant n-heptane hydroisomerization activity for over 80 h with a high n-C7 conversion(76%) and C7 isomer selectivity(94%).
考察了Ga2O3掺杂的Pt/WO3/ZrO2(Pt/WGZ)催化剂在200oC时正庚烷临氢异构化反应性能。
4)  n-heptane isomerization
正庚烷异构化
5)  hydroisomerization
临氢异构化
1.
Therefore, the Pt catalyst supported on the SAPO-11 synthesized in the biphase medium exhibited much higher catalytic activity for the hydroisomerization of n-dodecane than that supported on the SAPO-11 synthesized in an aqueous medium.
水-丁醇两相介质有利于在SAPO-11中引入更多的Si,从而产生较多的酸性位,以所得SAPO-11为载体的Pt催化剂在正十二烷临氢异构化反应中表现出较高的催化活性。
2.
Based on the reported reaction networks, a novel six components hydroisomerization reaction network with a new lumped species including C8-naphthenes and C8-paraffins was proposed and a kinetic model for commercial unit was also developed.
针对某实际工业异构化装置,在已开发的八碳芳烃临氢异构化反应网络的基础上,将系统中的八碳环烷烃和八碳链烷烃作为一个集总组分,提出新的六组分异构化反应网络,由此建立了适用于工业生产的八碳芳烃临氢异构化反应动力学模型。
3.
The action of the paraffin hydroisomerization technology were summarized in the paper,the paper introduced the characteristic of the three kind catalyst and five kind processing flow used by the technology as well as the patent technology of the UOP company,analyzed how to select the technic.
对烷烃临氢异构化工艺的作用进行了综述,对该工艺所使用的3种催化剂的特点和5种加工流程及UOP公司的专利技术进行了介绍,并对如何选用该工艺技术进行了分析。
6)  hydroisomerization process
临氢异构化过程
补充资料:临化示弟子
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全唐诗:卷852-7
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