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模拟计算结果
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  simulation result
    A numerical simulation is conducted based on the equation of conservation of momentum (N-S) and standard k- ε turbulent field, the relational numerical values between flow rate and rotation speed and pressure drawdown are calculated in combination with examples, the simulation result is consistent with measured values.
    为了给实验提供充分的理论依据,基于动量守恒(NS)方程和标准κε紊流模型,采用计算流体动力学(CFD)软件,对换热管内液轮机的三维紊流场进行了数值模拟,并结合实例计算出换热管内流速与液轮机转速和压降的关系数值,数值模拟计算结果与实验测定值基本相符。
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    The modeling ol multi-layer flat sheet AGMD module was performed. The simulation result shows that AGMD module is less sensitive to various operating conditions compared with DCMD, and its flux is also much less than DCMD.
    在此基础上,建立了多层AGMD平面膜组件的数学模型,数值模拟计算结果表明,AGMD组件对各种影响因素的反应远不如DCMD组件灵敏,通量水平与DCMD相比也有较为明显的差距。
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    The macrokinetic model of the cyclopentene oxidation was established and examined, and the model- based simulation result considerably complied with the experimental data, which showed that the macrokinetic model could be used in the research on the optimal operational condition.
    建立环戊烯氧化制戊二醛过程反应宏观动力学模型,并进行模型检验。 结果表明,根据模型进行的模拟计算结果与实验结果符合较好,说明采用所确定的反应动力学模型及模型参数,进行环戊烯氧化反应过程的模拟计算和优化研究是可行的。
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  “模拟计算结果”译为未确定词的双语例句
    STEADY-STATE AND DYNAMIC BEHAVIOR OF FIXED-BED CATALYTIC REACTOR FOR FISCHER-TROPSCH SYNTHESIS Ⅱ.STEADY-STATE AND DYNAMIC SIMULATION RESULTS
    固定床F-T合成反应器的稳态和动态行为特性 Ⅱ.稳态和动态模拟计算结果(英文)
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    The separation process of acetone and methanol using water as solvent is wellsimulated and the results prove the accuracy and commonality of the model.
    同时采用此模型对常规间歇萃取精馏分离丙酮-甲醇(水为溶剂)的过程进行了模拟计算,结果表明此模型的准确性和通用性是令人满意的。
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    The expressions calculating the concentration distribution of aluminium species in the coagulation process of Al base water clarifying agents are deduced based on the dissociation equilibrium equations, and the final calculating results are presented at the initial Al 3+ concentration of 10 -3 mol/L, 10 -4 mol/L and 10 -5 mol/L respectively.
    根据电离平衡方程,推导出了一个计算混凝过程中含铝络合物浓度分布的计算表达式,并给出了初始铝含量分别为10-3mol/L、10-4mol/L及10-5mol/L时的模拟计算结果
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    The simulation showed that the xylose solution was concentrated from 4% to 20% through the 4-stage series connection configuration.
    模拟计算结果表明采用纳滤方法浓缩水解法工业木糖粗品溶液 ,通过四级串联方式可将质量分数为 4 %的木糖溶液浓缩至 2 0 % .
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    Diglyol was selected as solvent of extraction separtion for DEM and Ethanol aqueous. Activity coefficients were calculated by UNQUAC equation. The separation results of extraction were simulated by phase separation coefficients (β) and materical balance equation.
    以二甘醇为DEM与乙醇水溶液萃取分离的溶剂,以UNIQUAC方程为活度系数计算的模型,采用相分配系数(β)和物料守恒方程模拟逆流萃取分离结果,建立了模拟计算程序框图,并进行逆流萃取试验,模拟计算结果和实验结果吻合,为进一步逆流萃取中试提供可行性依据。
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  simulation result
The finite element model is correct and simulation result is fine by adopting unequal interval plotting patterns.
      
Simulation result and LAN-environment experiment result both indicate that PWD is an effective method to detect and block P2P worms.
      
The simulation result shows that the aggregation of conduction grains can greatly affect the degree of catalyst utilization.
      
It is demonstrated that the simulation result correctly reproduces the AMS data, and differences in spectra averaged over longitudes on various magnetic latitudes are small (including the low-energy range) for different models of the magnetosphere.
      
According to the numerical simulation result, the center-configuration coefficients for these nine configurations have been calculated and compared to validate this technique.
      
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In this paper,the possibility of applying CSTRinseries to the slurry phase Fischer-Tropsh synthesis is examined using a mathematical model.The com- putation results were supported by the observed data of Rheinpreussen-Koppers demostration plant.Also,it has been shown that,through examing the effect of some parameters on reactor performance and by comparing the computation results of different flow models,the performance of BCSR for slurry phase Fis- cher-Tropsch synthesis may be to some extent modelled by a...

In this paper,the possibility of applying CSTRinseries to the slurry phase Fischer-Tropsh synthesis is examined using a mathematical model.The com- putation results were supported by the observed data of Rheinpreussen-Koppers demostration plant.Also,it has been shown that,through examing the effect of some parameters on reactor performance and by comparing the computation results of different flow models,the performance of BCSR for slurry phase Fis- cher-Tropsch synthesis may be to some extent modelled by a simple CSTR inseries model provided that the number of CSTR is reasonally selected.

本文应用数学模拟方法,探讨了多级串联 CSTR 在浆态相 FT 合成工艺中使用的可性能。模拟计算的结果得到了 Rheinpreussen—Koppers 示范厂的实验数据的支持。此外,通过若干参数对反应器性能影响的考察,以及不同流动模型计算结果的比较表明,采用简单易算的多级串联CSTR 模型,只要合理选择反应器级数,可以不同程度地模拟鼓泡塔浆液反应器的性能。

The kinetics of green magnetite pellets in drying process was investigated by means of thermogravimetry, using nitrogen gas flow at different velocities in a temperature range from 100 to 300 @. Experimental results showed that the whole drying process goes through with its function in four steps,i.e., accele ration,constant,deceleration I and Ⅱ .Moisture in green pellets are mostly removed during the first three steps.A unified kinetic model of drying process is developed for the first three steps, based on...

The kinetics of green magnetite pellets in drying process was investigated by means of thermogravimetry, using nitrogen gas flow at different velocities in a temperature range from 100 to 300 @. Experimental results showed that the whole drying process goes through with its function in four steps,i.e., accele ration,constant,deceleration I and Ⅱ .Moisture in green pellets are mostly removed during the first three steps.A unified kinetic model of drying process is developed for the first three steps, based on a theoretical analysis in which both the heat transfer and mass transfer processes go on simultaneously. Parameters and expressions of the model are derived and given from experimental data.Calculation results by the model are found quite in agreement with those measured thus testifying its applicability.

采用热重分析实验技术,在氮气流下,100—300℃温度区间,不同的气流速度范围研究了磁铁矿生球团干燥过程动力学。实验表明,干燥过程可分为增速、恒速、减速(一)和减速(二)4个阶段。生球中绝大部分水分是在前3个阶段中脱除的,在热量和质量传递过程同时进行的理论分析基础上,对前3个阶段建立了统一的干燥过程动力学模型。由实验数据求得了模型中参数或表达式。应用此模型对球团干燥过程进行模拟计算的结果与实验测定结果相当符合,证明了本动力学模型的适用性。

This paper provides a method of modeling and simulation of spiral—wound membrane equipment for gas separation process.An analyticalaffects of process parameters (such as α,θ,Pr) with membraneseparation process was undertaken by using computer calculation datafor oxygen enrichment of air equipment show good agreement withexperiment.

本文通过对卷式气体膜分离装置的模型化及计算机模拟计算,得到了α、θ、Pr 等参数对气体膜分离过程的影响关系,并将对富氧的膜分离过程的模拟计算结果与实际富氧装置的实验数据进行了比较,结果令人满意。

 
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