试验结果表明，该环氧树脂体系的固化动力学符合自催化固化反应模型。
From the experimental data, it was found that the autocatalytic cure kinetic modeling correctly represented the cure kinetics of this system.
在流体力学方程组中，加入催化剂再生反应动力学方程，构成了再生过程流化反应模型。
The model was established by incorporating the dynamic equation of catalyst regeneration with the hydrodynamic equations.
提出了含两个水分子的双核铜配合物催化PNPP水解的动力学数学模型。
A kinetic mathematical model of PNPP cleavage catalyzed by dinuclear copper (II) complex was proposed.
本文介绍了应用序贯实验设计方法对“B109”型催化剂中温变换反应动力学竞争模型进行模型筛选及参数估计的过程。
In this paper a sequential experimental program used for model discrimination and parameter estimation of kinetic models for the high temperature-shift reaction over "B109" catalyst is presented.
利用计算流体动力学(CFD)软件，建立了催化转化器流场的二维模型，对催化转化器的稳态流动进行了数值模拟。
A two-dimension model for the flow field in catalytic converter was established, and the steady state flow was simulated with the computational fluid dynamics (CFD) code.
本文介绍了当前多相光催化反应体系中反应动力学模型以及反应器数模研究领域内的主要方法及成果。
This article introduces the main existing methods and achievements in the field of the math models of reaction kinetics and reactor of the heterogeneous photocatalysis reaction system.
基于物料衡算、热量衡算和反应动力学建立的催化裂化过程动态模型是具有非线性、分布参数的模型形式。
Based on the material balance, energy balance and reaction kinetics, a dynamic model, having the form of a nonlinear distributed parameter has been presented for catalytic cracking process.
采用等温积分反应器，测试了KD306型耐硫甲烷化催化剂的本征动力学，建立了幂函数动力学模型。
The intrinsic kinetics of KD306 type sulfur tolerant methanation catalyst was studied in an isothermal integrated reactor and the reaction model of power functions type was established.
从四个方面分析了近年来催化剂分形研究的方向和进展分形维数与催化剂评定和筛选，催化剂分形孔结构，分形与反应动力学，模型建立。
The development of fractal catalysts study in recent years was analyzed from four aspects: selection and assessment of catalysts, fractal pore structure, reaction dynamics and mathematics model.
研究了硫氢化钠和2 -溴丙烷在催化剂作用下合成异丙硫醇的反应动力学，建立了动力学模型。
Kinetics for synthesizing isopropyl mercaptan from NaHS and 2-bromopropane in the presence of catalyst was studied; the reaction and the kinetic model of the whole process were investigated.
以动力学模型为基础，借助ASPEN软件用平衡级模型进行了催化精馏过程的模拟与预测。
ASPEN software was chosen to simulate and predict the temperature, concentration and other profiles of the catalytic distillation column by equilibrium stage mode.
催化剂可以明显促进固化反应，但不改变反应的动力学模型。
The catalyst can facilitate the curing without change the kinetic model.
建立了催化反应的动力学数学模型，获得了催化反应相关的热力学和动力学参数。
The catalytic mechanism was proposed and the kinetic mathematical model of the catalytic reaction for obtaining the thermodynamic and kinetic pa.
采用计算流体动力学（CFD）模型预测某600MW电厂选择性催化还原法烟气脱硝系统不同设计情况下的流场状态。
The computation fluid dynamics(CFD) is used to predict the flow filed inside the selective catalytic reduction(SCR)system of a 600MW power plant.
利用反应动力学方法，探讨了含有多种中间复合物的酶催化反应动力学模型。
Taking advantage of kinetic method, we discussed the kinetic model Of multiple substrat enzymatic reaction.
本文针对催化裂化工业装置的提升管反应器以三集总催化裂化反应动力学模型为基础，利用工业装置的现场数据对模型中的参数进行了拟合。
Based on three lumping kinetic model of catalytic cracking, the parameters in the model are estimated with actual operation data of a commercial catalytic cracking riser.
该结果可为催化重整单事件反应动力学模型的建立提供理论基础。
The results provide the foundation for establishing the single-event micro-kinetic model of catalytic reforming.
依据催化裂化催化剂水热失活过程伴随着超稳化过程，确定了催化剂自抑制水热失活动力学模型方程。
The kinetic model of hydrothermal deactivation and the model of unit balance activity for FCC catalyst were established.
建立了重油催化裂解七集总动力学模型，给出了模型的反应网络和数学表达式。
A 7-lump kinetic model was proposed for heavy oil catalytic pyrolysis. The reaction network and mathematics expressions were also given.
将动力学方程和催化剂捆包的效率因子归入到催化精馏塔的数学模型当中。
The kinetic equation and effective factor of the structured catalytic bag were incorporated into the mathematical model of a catalytic distillation column.
应用动力学模型，结合工业生产数据，讨论了高浓度CO气体组成中一段催化剂的装填精度问题。
Using the dynamic module and connecting with the industrial production data, the filling accuracy problem was discussed on the first stage catalyst used in high concentration co gas composition.
以阳离子交换树脂为催化剂，对醋酸甲酯催化水解本征动力学进行研究，并建立了消除催化剂包内扩散的本征动力学模型。
The eigen-kinetics of hydrolysis of methyl acetate in cation-exchange resins was studied. The eigen-kinetics model in removing diffusion of catalyst-capsule was found.
以四氟化铀与水蒸汽反应为例，说明建立气——固非催化反应动力学模型及其参数估计方法。
With the reaction between uranium tetrafluoride and steam as an example, the method for the development of the gas -solid non-cata…
该方法应用于催化裂化十集总动力学模型轻循环油反应网络动力学参数估计，降低了搜索算法对初值和实验误差的要求，保证了收敛稳定性。
The new method not only lowered the requirements to initial values, but also insured the convergence stability in using it to predict the parameters of the rate consta…
该方法应用于催化裂化十集总动力学模型轻循环油反应网络动力学参数估计，降低了搜索算法对初值和实验误差的要求，保证了收敛稳定性。
The new method not only lowered the requirements to initial values, but also insured the convergence stability in using it to predict the parameters of the rate consta…
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