共查询到20条相似文献,搜索用时 203 毫秒
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采用热-流耦合方法对火焰筒壁温三维数值模拟 总被引:1,自引:0,他引:1
考虑了流场变化对换热的影响,使用热-流耦合方法,对某型燃烧室整个流场、温度场进行完全的数值模拟。该方法对流场和固壁内换热进行耦合计算,得出了三维燃烧室壁温分布。计算中,对完全发展的湍流燃气采用了标准“k-ε”湍流模型,运用DO模型计算了燃气的热辐射,燃烧模型使用涡-耗散模型来计算化学反应速度,固壁材料使用了变比热和变导热系数。数值模拟结果表明流场与固壁相互作用得更充分,能更精确地反映流场和温度场的整个形态,可以模拟出较为合理的流场和温度场分布以及相应的流动换热特性。 相似文献
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生物质热压成型温度场数值模拟 总被引:5,自引:0,他引:5
根据生物质热压成型的工作原理及加热方式,在合理假设的基础上建立了生物质热分析有限元模型。以木屑作为压缩成型的对象,借助大型有限元软件ANSYS对其温度场进行计算,得到了木屑内部温度场的分布情况。借助APDL语言对其计算过程进行参数化设计,分别计算了在两种不同情况下的温度场,并讨论了在不同温度场下木屑的变化。 相似文献
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一、管道热伸长补偿概述为了防止供热管道因受热伸长而发生变形和减少(或消除)因受热伸长而产生的应力,采取了分段设置固定支座并在两个固定支座之间设置管道补偿器(也称伸缩器)的技术措施。补偿方式很多,除利用管道走向及坡度的改变而形成的L形、Z形管段对热伸长作自然补偿外,专门采用的补偿器有方形、套筒式、波形、球形补偿器四种。方形补偿器是过去应用最广泛的补偿器。其优点是:可以在施工现场弯制、制造方便。运行中无泄漏,不需要维护。可应用 相似文献
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缸套瞬态温度场的有限元分析 总被引:2,自引:0,他引:2
本文提供了计算二维温度场的通用方法,即瞬态温度场的非线性有限元解法.首先,以实测的温度确定缸壁与燃气的接触边界条件,计算出稳定温度场.以稳定温度场做初始条件,考虑活塞运动情况,利用所确定的放热系数确定缸套与燃气的接触边界条件计算了铸铁缸套的瞬态温度场,给出了缸套表面层的温度波动情况. 相似文献
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整体球墨铸铁活塞是一种新型活塞。为了设计合理及缩短试制时间,我们用有限单元法对活塞的温度场、热流量分配及应力场进行了计算。本文介绍的计算方法是三角形剖分和二次插值,其精度较三角形线性插值为高,热边界条件可以输入第一类边界条件或第三类边界条件,也可以输入第一类及第三类的混合边界条件。可以节省计算时间,也减少了数据的准备及处理的工作量。本文还介绍了计算活塞时热边界条件的处理;及活塞振荡冷却腔冷却条件、活塞内腔冷却条件、冷却油温度、活塞材料导热系数和活塞顶部厚度等因素变化时,活塞温度场或应力场变化规律的探索。为设计、生产和运转提供了一定的资料。在12V400型柴油机的研究工作中,我们设计了一种整体球墨铸铁活塞。为了尽可能达到等强度、结构尺寸合理和重量轻等要求,采用高精度元有限单元法对活塞顶部的温度场及应力场进行了计算。计算中变换了各种热边界条件和一些结构参数,使计算结果比较符合实际情况;同时摸索热边界条件变化时对活塞温度场的影响,以便为优化设计探求规律及减少今后的试验工作量。由于对燃气侧的热边界条件所做的工作比较少,因此本文侧重点是活塞冷却侧热边界条件变化时对温度场影响的研究。 相似文献
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D系列柴油机缸套轴对称稳定温度场的有限元分析 总被引:3,自引:1,他引:3
邱国平 《柴油机设计与制造》1995,(2):2-9
本文对D系列柴油机的上部带凸缘的中部支承式缸套进行轴对称稳定温度场的有限元分析。在有限元分析中,采用Woschni经验公式计算气缸内燃气与壁面间的瞬时综合换热系数,并编制程序计算缸套内壁任一点的当地平均换热系数,用Hausen换热公式计算缸套外壁面与冷却水之间的换热系数,并根据缸套几个特征的壁面实测温度对换热系数进行适当的调整,以此来确定缸套温度场有限元计算的边界条件。计算结果表明,上部凸缘中支式缸套温度场分布不同于传统的上部支承式缸套。 相似文献
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王梅 《柴油机设计与制造》2021,27(4):17-21
为获得某天然气发动机比较精确的缸盖温度场,采用边界单向映射的方法将获得的冷却水侧和燃气侧的热边界映射至缸盖固体网格上,根据经验通过赋予机油侧和外围边界处的热边界,建立缸盖计算的有限元模型.对模型进行传热计算,获得该天然气发动机缸盖的最终温度场结果,将计算结果同发动机试验结果对比,最大误差为9.3%,满足工程要求.通过水套CFD分析和缸内流动燃烧分析能较准确地得到缸盖温度场分布,为后续缸盖强度及热疲劳分析提供有效热载荷. 相似文献
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新型发动机排气温差发电器结构探索 总被引:3,自引:2,他引:1
根据汽车发动机排气可利用能量的形式,提出了一种新型的置于排气通道内的热电转换系统,使热电偶与热气流直接进行对流/辐射换热,将强化热流密度和转换电流密度、提高系统的温差。在使用现有热电材料的条件下,提高温差发电器的功率密度。 相似文献
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Measurements are reported of heat transfer to supercritical carbon dioxide (SCD) flow in a natural convection circulation system that consists of a closed-loop circular pipe. Systematic data of heat transfer coefficients are given for various pressures and pipe diameters. Heat transfer coefficients of SCD flow are confirmed to be very much higher than those of usually encountered fluid flow and are shown to be expressed by a nondimensional correlation equation proposed in this work. Numerical model calculations are also presented for the velocity and temperature distributions in SCD flow to elucidate the exceedingly high value of heat transfer coefficient. The heat transfer enhancement of SCD is concluded to result from the high-speed flow near the pipe wall. This strong flow is shown to have velocity and temperature gradients steep enough to cause the enhancement of the rate of heat transfer in the vicinity of the pipe wall. 相似文献
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A heat pipe heat exchanger (HPHE) was used to investigate the heat transfer performance of steam-air mixture condensation, analogous to the dew condensation of flue gas, when the steam volume fraction ranged from 0 to 20%, and the inlet temperature of steam-air mixture varied from 70 to 120°C. Self-assembled monolayers (SAMs) treatment with n-octadecyl mercaptan was adopted to modify the condensation surface of the heat pipe. The comparisons were conducted to examine the influence of SAMs on condensation heat transfer of steam-air mixture vapor. The results indicate that the convection condensation heat transfer coefficient increases with the increase of steam volume fraction and Re number of the steam-air mixture. As the inlet temperature increases, the heat transfer coefficient decreases accordingly. The heat transfer performance can be improved by the SAMs surface, with a heat transfer enhancement ratio up to 1.6 at a condition of 20% of the steam volume fraction and 1500 Re number. 相似文献
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《International Journal of Hydrogen Energy》2023,48(79):30858-30867
Hydrogen is an energy carrier which can be utilized in many sectors like stationary and transportation energy with nearly zero emission. Hydrogen energy is more efficient when compared to other energy sources. Hydrogen can be a replacement for fossil fuels in future as it emits only water when it is burned. In this work a mathematical model of transfer of hydrogen between two tanks has been developed using MATLAB simulink software version 21. Flow of hydrogen inside the pipe is controlled by orifice and diameter of this orifice and pipe diameter itself has some impact on outcome parameters such as inlet temperature of pipe, outlet temperature of pipe, heat transfer from one tank to other tank and hydrogen gas flow rate. The influence of orifice diameter as well as initial pressures on outcome parameters of hydrogen gas transfer model has analyzed in this work. From the simulation results it is inferred that when one initial pressure kept constant and other initial pressure keep on varying, no change in inlet temperature, decrease in outlet temperature, increase in heat transfer and increase in gas flow rate were observed when orifice diameter increase in size from 2 cm then 4 cm and then 6 cm. The research work has significant guidance for safety and efficient way of transporting hydrogen through pipeline from one tank to other tank. 相似文献