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1)  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。
2)  n heptane hydroisomerization
庚烷临氢异构化
3)  hydroisomerization process
临氢异构化过程
4)  hydroisomerization
临氢异构
1.
The Improvement of Pt/SAPO-11 Hydroisomerization Catalysts;
Pt/SAPO-11临氢异构催化剂的改进
2.
It was shown that reaction temperature has the greatest impact on the hydroisomerization of n-tetr.
获得了正十四烷临氢异构的最佳条件为300℃~330℃,0。
3.
The present problems for Ca utilization are separation of single component and removal of residual butadiene in C_4 streams,n-Butene hydroisomerization technology takes advantages of reaction reversibility,low temperature,selective hydrogenation of butadiene and easily to combine with catalytic distillation,which is the spot of recent interest.
分析了不同来源的碳四的组成及国内外碳四资源的利用情况,指出单组分分离、去除丁二烯是碳四综合利用的难点;介绍了正丁烯临氢异构技术具有反应可逆、反应温度低、可同时进行选择加氢除丁二烯及易与精馏技术配套的优势;综述了国内外与催化精馏技术相结合的临氢异构技术在裂解碳四和炼厂碳四利用中的应用进展,包括最大化生产1-丁烯、生产1-丁烯/2-丁烯、生产高纯度异丁烯及利用碳四烯烃的组合工艺等。
5)  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。
6)  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。
补充资料:临氢异构化
分子式:
CAS号:

性质:对戊烷、己烷或两者混合馏分在催化剂(一种特殊处理的含铂剂)和氢压(1.4~3.5MPa)下进行异构化以提高辛烷值的过程。原料要先经脱硫,脱硫后的碳五、碳六馏分与循环氢混合,并被加热进入预处理反应器,使芳烃和烯烃饱和,且有少量正构烷烃异构化为异构烷烃。由于转化率不高,冷却后再进入后反应器在压力较高温度更低进行异构化。高压分离器出来的液体,经稳定塔得到汽油调合组分。此法单程只能提高辛烷值10~15个单位。

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