对乙烯裂解装置中急冷油粘度增长的原因及反应机理进行了分析,并在此基础上开发出JNJ-3型急冷油减粘剂。
JNJ - 3 viscosity reductant for quench oil was developed on the basis of analyzing reasons for viscosity increase of quench oil in ethylene plant and its reaction mechanism.
根据三种材料作用机理的不同,研究探讨催化剂活性中心对热解气中焦油裂解率、催化裂解气体成分及反应速度(活化能)的影响。
The mechanism of the activated center of the catalysts on the tar removal efficiency, the gas component after tar cracking and the reaction speed or activation energy were studied.
该平台基于裂解反应动力学的严格机理模型和分子反应动力学模型,支持对多种热裂解原料的裂解过程模拟。
Based on the precise mechanistic model and molecular reaction kinetic model of cracking reaction kinetics, the platform can support the simulation of cracking process with various feeds.
同时探讨了可能的反应机理和反应溶剂对氧化裂解反应的影响。
The possible reation mechanism and the effects of different solvent on oxidation were investigated.
提出了乙烷与水蒸汽转化反应的新化学计量方程序,对已有的反应机理作了补充,指出甲烷同系物的水蒸汽转化与其加氢裂解反应的相似本质。
A new chemical equation for the reaction of ethane with steam is suggested. It is pointed out that the steam conversion is similar to hydrocracking of methane homologs.
实验表明,轻柴油裂解时,TLE结焦机理为传质、冷凝-表面缩聚反应机理。
It was clear from the experiment that the coking mechanism in TLE was mass transfer and condensation-surface poly-condensation reaction.
从离子碎裂反应机理的角度,分析了火焰中样品分子裂解和电离的可能机理,并总结出可能影响电离效率的相关因素。
The possible mechanism of split and ionization of sample molecules in flame is analyzed from the view point of fragmentation reaction.
并在分析纤维素一次反应、挥发份二次裂解以及各主要产物的生成和演变过程基础上,探讨得到完整统一的纤维素热裂解机理模型。
On the basis of the analysis of primary reaction, secondary reaction and main products formation, the mechanism model of cellulose pyrolysis was proposed.
该平台基于裂解反应动力学的严格机理模型和分子反应动力学模型,支持对多种热裂解原料的裂解过程模拟。
A six-lump kinetic model was derived on the basis of FCC reaction mechanism to represent the FCC naphtha olefin reformulation.
研究在冷等离子体条件下甲烷裂解并偶联产生C2烃的反应机理。
Methane conversion to C2 hydrocarbons by low temperature plasma was studied in different reactors.
研究在冷等离子体条件下甲烷裂解并偶联产生C2烃的反应机理。
Methane conversion to C2 hydrocarbons by low temperature plasma was studied in different reactors.
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