对固定床中流体与换热管呈错流流动的传热进行了实验研究，并以二维传热模型进行模拟。
An experimental study was conducted on the cross-flow heat transfer in a fixed-bed, and simulated by a two-dimensional model.
将吸附带以某一虚拟速度运动，通过物料衡算可以建立固定床吸附操作模型方程。
Supposing adsorption belt moves at a suppositional rate, the adsorption model equation in fixed bed can be set up through material calculation.
利用“三传（动量、能量、质量传递）一反（反应工程）”的原理，建立了固定床加压气化过程的数学模型；
Utilizing principle of momentum transport, energy transport, quality transport and reaction engineering, the mathematical model for coal pressure gasification on fixed bed has been established.
提出了非绝热式固定床反应器基于改进混合模型的串级非线性推断控制策略。
A new cascade nonlinear inferential control strategy for a nonadiabatic fixed bed reactor based on improved hybrid model is proposed.
本文提出了轴向流固定床反应器的流动模型和基本方程。
In this paper, the flow model and basic equations in axial flow fixed-bed reactor are given.
建立了适用于模拟固定床水蒸气解吸的均相模型，并对实验结果进行模拟计算，结果表明，所建模型与实测结果能很好吻合。
A mathematical model has been developed to simulate the process of the desorption. The result shows that the simulated result can be in good agreement with the experimental one.
在小型固定床反应器上，以甲苯为模型化合物对生物质焦油在热解焦上的催化裂解反应进行了研究。
Experiments of tar cracking on char with toluene as a model compound were performed in an electrically heated tubular flow reactor.
反应是在固定床的条件下进行的，通过建立稳态反应模型，求出了异构化反应网络中的每一步动力学参数。
The reaction took place in the fixed bed reactor. By using steady state model, each step kinetic parameter in the reaction net was acquired.
本文推导了矩形波进料的固定床色谱的数学模型的解析解。
A analytical solution of mathematical model of fixed-bed chromatography is presented.
以国内应用最广的固定床气化炉为载体建立数学模型，对煤的高温气化过程进行了分析。
Fixed bed gasification is used as a carrier to build mathematical model, and then the process of high temperature coal gasification is analysed.
将此动力学模型预测固定床反应结果，计算值与实测值相对平均误差小于20%。
The model was used to predict the reaction results of fixed-bed reactor and the average deviations of the calculated values from experimental data were less than 20%.
以有机含氧化合物丁酸和丁醇为合成油品的模型化合物，在连续流动固定床反应器中考察了催化剂的加氢脱氧性能。
The performance of the catalysts for hydrodeoxygenation of model organic compounds, butyric acid and butanol, was investigated in a continuous fixed bed reactor.
固定床吸附模型模拟了吸附动态过程。
A fixed-bed adsorption model was proposed to simulate the adsorption dynamic processes.
建立了充填国产s101钒催化剂的、单段流向变换周期操作固定床反应器的非均相动态模型。
The heterogeneous transient model of a fixed - bed reactor packed with vanadium catalyst, S101, for catalytic oxidation of SO2 and operating in a flow direction switched periodically was developed.
用固定床连续流动微反装置，以苯加氢为模型反应考察了催化剂的加氢性能、热稳定性及抗硫毒性。
Hydrogenation activity, heat resistance, anti poisoning ability for benzene hydrogenation were determined in a microreactor GC system.
用固定床连续流动微反装置，以苯加氢为模型反应考察了催化剂的加氢性能、热稳定性及抗硫毒性。
Hydrogenation activity, heat resistance, anti poisoning ability for benzene hydrogenation were determined in a microreactor GC system.
应用推荐