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convection heat transfer相关的网络例句

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与 convection heat transfer 相关的网络例句 [注:此内容来源于网络,仅供参考]

Because the limitation of the conventional method,A lot of work were done for the calculation of average overall heat transfer coefficient of building external wall and heat transfer coefficient of building block filling wall needs mass calculation.

由于常规算法的局限性,在实际项目中换算外墙平均传热系数与外墙主墙体传热系数需要计算的工作量较大。

The experiment was conducted to investigate the heat transfer of supercritical carbon dioxide in tubes. The effects of mass flux, pressure and inlet temperature on heat transfer characteristics and pressure drop were analyzed.

摘要对超临界CO2在套管内的换热特性进行了实验研究,探讨了超临界CO2换热过程中,质量流率、压力和入口温度的变化对换热性能特性和压降的影响。

The experiment was conducted to investigate the heat transfer of supercritical carbon dioxide in tubes. The effects of mass fluxpressure and inlet temperature on heat transfer characteristics and pressure drop were analyzed.

摘要对超临界CO2在套管内的换热特性进行了实验研究,探讨了超临界CO2换热过程中,质量流率、压力和入口温度的变化对换热性能特性和压降的影响。

Based on the analysis of physics course of heat transfer, the mathematical model of single-phase flow in the rectangular narrow channel is proposed. And the boundary conditions are given to get the unique numerical result. The finite volume method is used to found the discrete scheme of equations. According to the flow of SIMPLER arithmetic, the computing program is developed and the correctness of program is validated.Then the program is used to solve the problem of flow and heat transfer in rectangular narrow channel.The stable two dimension velocity and temperature fields in rectangular narrow channel and plate fuel are obtained.

在明确窄缝流道及燃料板换热物理过程的基础上,建立了描述矩形窄缝内单相流动与换热问题的数学模型,并给出了合理的边值条件;然后利用有限容积法对方程进行离散,根据SIMPLER算法的流程编制了模型求解程序;在验证程序正确性的基础上,对矩形窄缝流动与换热问题进行了求解,得到了矩形窄缝流道和板状燃料元件内部温度场、速度场的二维分布。

3The heat transfer in the charging and discharging process are unsteady, and the heat transfer capability of the system will change against time, and the charging rate and discharging rate decreases gradually with time, as should be noticed in the design.

蓄冷和放冷过程都是非稳态传热过程,整个过程中系统的传热能力是不断变化的,蓄冷率和释冷率都是逐渐降低的,在蓄冷设计时应该注意到这点。

The synthetic gas and ash composition heat transfer and flow in vertical pipe of coal gasifier are simulated and analyzed by the theory and program presented. The temperature、velocity and concentration variations of synthetic gas and ash composition are accomplished. The influences of coal gasifier working condition and vertical pipe parameters on the gas and ash cooling process are discussed. The law of solid-gas two phase turbulent flow and heat transfer is further revealed.

本文还应用上述理论和程序,在国内首次对气化炉激冷室下降管内合成气和灰份的流动和传热过程进行了数值计算和分析,得到下降管内合成气和灰份的温度、速度和浓度等参数的变化,还讨论了气化炉运行参数和下降管结构参数如气化温度、下降管尺寸、灰份性质等参数变化对合成气降温过程的影响,进一步揭示了下降管内气固两相的流动和传热规律。

The deficiency in traditional method for calculating heat transfer quantity in the wall of wood drying kiln was pointed out,and the heat transfer quantity in the wall of wood drying kiln was calculated by the shape factor method.

指出了木材干燥窑壳体传热量的传统计算方法中的不足,并利用形状因子法来分析计算木材干燥窑壳体的传热量。

The results show that the precooling time of the probe is shortened significantly with the help of the vapor liquid separator, and decreases with the driven pressure. With the helical coiled wire and the helical mesh, significant thermal Oscillation corresponding the density-wave is observed in the precooling time. The average heat transfer coefficient enhances 1.5 times with the mentioned heat transfer enhancement techniques, and the temperature of the 2.5 min cryoprobe surface can reach -160℃ in 17℃ brine within 10 min.

结果表明:使用了快速预冷汽液分离器后,探针预冷时间大大缩短,并随驱动压力增大而减小;加入螺旋丝和螺旋丝网后,在预冷阶段出现明显的热力振荡,并伴有密度波振荡,平均换热系数为原来的1.5倍,在17℃生理盐水中10min时2.5min探针表面温度最低可达-160℃,大大提高了探针的冷却性能。

The flow-field around a hemisphere and a flat-nosed cylinder in the shock tube is simulated numerically by using non-equilibrium Navier-Stokes equations with an air chemical model of 5 species 17 reactions, and the catalytic rate constant of surface materials such as Pt, SIC:, Ni and a flight vehicle materials is determined by using the heat transfer rate of testing in the shock tube and the distribution of heat transfer rate along with the catalytic rate constants.

用5组分17个化学反应Durm-Kang空气化学模型和轴对称热化学非平衡Navier-Stokes方程,对激波管中球头和平头圆柱模型绕流流场进行了数值模拟,给出了驻点热流随催化速率常数变化的分布,并根据激波管实验测量的热流值确定了表面材料Pt、SiO2、Ni和某种飞船材料的催化速率常数,建立了数值分析高焓流动边界层催化特性的软件。

The highest heat transfer coefficient for air flowing in the nine 3-D IFT with staggered arrangement fins is No9 tube. In the turbulent region, the heat transfer coefficient of No9 tube is a factor of 10.36 compared with smooth tube, and its thermodynamic performance coefficient is as high as 6.49; The average Nusselt number in the most superior 3-D IFT with staggered arrangement can be increased by about 1.04 times in the laminar flow, and 6.38 times in the transitional flow as compared with that in the smooth tube. The friction factor between fluid and tube wall can be 0.96 times in laminar flow, and 12.68 times in transitional flow as compared with that inside the smooth tube.

在进行实验的九根肋叉排三维内肋管中,换热最强的No9管与光管相比,在紊流区的换热强化比平均可达10.36倍,阻力增大比约为4.06倍,其热力性能系数高达6.49;在过渡流区的换热强化比平均可达6.38倍,同时阻力增大比约12.68倍;在层流区的换热强化比为1.04倍,而阻力增大比仅约0.96倍。

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