共查询到20条相似文献,搜索用时 250 毫秒
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为研究加强筋结构对离子膜内场分布特性的影响,采用多孔介质渗流模型、稀物质传递及二次电流分布模型,对电场条件下含加强筋的离子膜内物质迁移过程进行了数值模拟,得到了物质在膜内的对流速度、浓度及电流密度分布,考察了加强筋形状、间距及成网方式对场分布特性的影响。利用拍照法和图像处理技术对电解后膜表面离子浓度进行了测量,实验结果与模拟结果吻合良好。结果表明,在加强筋所围成的空隙中心处对流速度最大;越靠近加强筋,速度越低,浓度和电流密度越大;采用正交型加强筋,膜内具有较高的对流速度和电流密度;加强筋间距越大,电流密度越低,分布越均匀;采用椭圆形长轴迎流的加强筋时,膜内具有最高的电流密度,但其电流密度分布最不均匀。 相似文献
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为研究加强筋结构对离子膜内场分布特性的影响,采用多孔介质渗流模型、稀物质传递及二次电流分布模型,对电场条件下含加强筋的离子膜内物质迁移过程进行了数值模拟,得到了物质在膜内的对流速度、浓度及电流密度分布,考察了加强筋形状、间距及成网方式对场分布特性的影响。利用拍照法和图像处理技术对电解后膜表面离子浓度进行了测量,实验结果与模拟结果吻合良好。结果表明,在加强筋所围成的空隙中心处对流速度最大;越靠近加强筋,速度越低,浓度和电流密度越大;采用正交型加强筋,膜内具有较高的对流速度和电流密度;加强筋间距越大,电流密度越低,分布越均匀;采用椭圆形长轴迎流的加强筋时,膜内具有最高的电流密度,但其电流密度分布最不均匀。 相似文献
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采用贴体曲线坐标、SIMPLEC算法和完全压力修正,在非正交性非常大的结构型同位网格上求解了圆排波瓣喷管引射器内流场的不可压Navier-Stokes方程,湍流采用标准k-ε涡黏模型.计算得到了引射器中热混合效率沿混合管轴向的变化规律和流向涡的演变规律.混合管中的流向涡阵列大大强化了主次流的掺混.但该型引射器的总体热混合效率不高,实验的3种主流温度下最大热混合效率为0.874.将混合管出口截面速度分布和温度分布的数值模拟结果与实验值比较,两者比较一致;模拟结果与混合管沿轴向的静压系数分布规律实验值也基本相同. 相似文献
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以静电场中水分子的极化和受力特性为基础,对热干烟气中极板表面液膜内水分子输运过程进行分析。考察了电场特征、液膜物性对静态高压电场中液膜蒸发特性的影响并提出了蒸发模型;同时研究了多场(温度、速度和静电)耦合作用下液膜蒸发过程中的主导作用机制。结果表明:离子风为静态高压电场中液膜蒸发的主要动力,蒸发速率是自然蒸发的6.7倍(25 kV)。液膜蒸发为等速过程,蒸发速率与电场强度呈正相关关系;液膜加入溶质,蒸发过程受抑制,蒸发模型变为等速和降速两个过程,最终液膜表面析出溶质;流场耦合静电场作用下,液膜蒸发速率随电压升高先缓慢上升(U20 kV)后快速上升(U20 kV),流速和电压分别是这两阶段的主要影响因素;温度场耦合静电场作用下,蒸发速率大于单场叠加数值。研究结果为热干烟气中极板表面稳定成膜、系统水耗及空间电场中温湿度分布等问题的研究提供理论支撑。 相似文献
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以静电场中水分子的极化和受力特性为基础,对热干烟气中极板表面液膜内水分子输运过程进行分析。考察了电场特征、液膜物性对静态高压电场中液膜蒸发特性的影响并提出了蒸发模型;同时研究了多场(温度、速度和静电)耦合作用下液膜蒸发过程中的主导作用机制。结果表明:离子风为静态高压电场中液膜蒸发的主要动力,蒸发速率是自然蒸发的6.7倍(25 kV)。液膜蒸发为等速过程,蒸发速率与电场强度呈正相关关系;液膜加入溶质,蒸发过程受抑制,蒸发模型变为等速和降速两个过程,最终液膜表面析出溶质;流场耦合静电场作用下,液膜蒸发速率随电压升高先缓慢上升(U<20 kV)后快速上升(U>20 kV),流速和电压分别是这两阶段的主要影响因素;温度场耦合静电场作用下,蒸发速率大于单场叠加数值。研究结果为热干烟气中极板表面稳定成膜、系统水耗及空间电场中温湿度分布等问题的研究提供理论支撑。 相似文献
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T型翅片板喷淋式降膜蒸发器传热性能研究 总被引:6,自引:0,他引:6
采用喷淋降膜蒸发形式,将蒸发器的传热面用机械线切割方法加工成T型翅片板。对这种蒸发器进行了传热性能的研究,并与池式光板进行传热性能对比,实验结果表明,T型翅片板降液膜蒸发能在低温差下维持沸腾且有较高的给热系数。同时对沸腾传热的强化机理也进行了研究,并探讨了T型翅片板喷淋降液膜蒸发器具有优良传热性能时主要原因。 相似文献
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Lixin Cheng 《Chemical Engineering Communications》2013,200(7):975-993
This article presents the modeling of heat transfer of upward annular flow in a smooth tube and a spirally internally ribbed tube. First, analytical models of two-phase flow dynamics and heat transfer of annular flow in flow boiling were derived from the liquid film momentum and energy equations for smooth tubes. Combined with empirical correlations for liquid droplet entrainment and deposition rates in annular flow, modeling of heat transfer of upward annular flow in the smooth tube was conducted. The predicted heat transfer coefficients of annular flow agree with the experimental results very well for the smooth tube. Based on the heat transfer model for smooth tubes, a simplified annular flow heat transfer model for the spirally internally ribbed tube was proposed by modifying the interfacial friction factor. The predicted heat transfer coefficients by the modified heat transfer model for the spirally internally ribbed tube agree with the experimental results to some extent. It is suggested that the heat transfer model for the spirally ribbed tube be further improved by modifying the correlations for liquid droplet entrainment and deposition rates in annular flow, which should describe the feature of annular flow in the spirally internally ribbed tube. Extensive experimental data are needed for this purpose. 相似文献
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《Chemical Engineering Communications》2007,194(7):975-993
This article presents the modeling of heat transfer of upward annular flow in a smooth tube and a spirally internally ribbed tube. First, analytical models of two-phase flow dynamics and heat transfer of annular flow in flow boiling were derived from the liquid film momentum and energy equations for smooth tubes. Combined with empirical correlations for liquid droplet entrainment and deposition rates in annular flow, modeling of heat transfer of upward annular flow in the smooth tube was conducted. The predicted heat transfer coefficients of annular flow agree with the experimental results very well for the smooth tube. Based on the heat transfer model for smooth tubes, a simplified annular flow heat transfer model for the spirally internally ribbed tube was proposed by modifying the interfacial friction factor. The predicted heat transfer coefficients by the modified heat transfer model for the spirally internally ribbed tube agree with the experimental results to some extent. It is suggested that the heat transfer model for the spirally ribbed tube be further improved by modifying the correlations for liquid droplet entrainment and deposition rates in annular flow, which should describe the feature of annular flow in the spirally internally ribbed tube. Extensive experimental data are needed for this purpose. 相似文献
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为研究内置螺旋弹簧换热管单管强化传热原理,采用Fluent软件对内置螺旋弹簧换热管内流体流动与传热特性进行数值模拟,考察了弹簧的应用对管内流场、压降和换热性能的影响,并分别取螺旋弹簧节距p分别为2 mm、4 mm、5 mm初步研究了弹簧的节距对强化传热效果的影响。模拟结果显示:弹簧管内流体呈螺旋流动状态,管壁附近流体切向速度和径向速度有一定程度的提高,从而加剧了管内流体的混合及边界层的扰动,充分换热,弹簧管进出口温度差较光管有所增加,最高增加了0.9 ℃;相同雷诺数条件下,内置螺旋弹簧换热管Nu数均高于光管,而压降和阻力系数相比光管有明显增加,随着弹簧节距减小换热增强而摩擦阻力系数增加。 相似文献
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不同型面纵肋管束的综合能量特性研究 总被引:1,自引:0,他引:1
在研究得出梯形和矩形两种型面纵肋管束传热性能及流阻性能的基础上,依据换热过程的热力学能量原理,着重分析两肋片管束换热器的能量特性,探讨管束节距、肋高及厚度等结构参数和雷诺数及热流密度等工况参数对其能量利用的影响。研究结果表明:同为纵肋管束,但由于肋片截面形式不同,梯形和矩形纵肋管束综合能量利用程度差异较大;在相同的结构和工况条件下,梯形纵肋管束表现出良好的能量综合利用性能 相似文献
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帘式折流片换热器强化传热数值研究 总被引:1,自引:0,他引:1
为解决折流板换热器壳程流体阻力过大和折流杆换热器低Re下传热系数较小等管壳式换热器的不足,提出了壳程流体"斜向流"的新概念,研制了新型高效节能管壳式换热器?帘式折流片换热器,其壳程传热系数高于折流杆换热器20%~30%,而壳程压力损失大幅低于折流板换热器。以场协同原理分析了斜向流的强化传热机理,指出在帘式折流片换热器壳程中流体速度场与温度梯度场间的夹角小于折流杆换热器,是其强化传热的重要原因。对帘式折流片换热器中折流栅间距、折流片倾角、折流片宽度等重要几何参数对传热和压降的影响规律进行了数值模拟研究,并据此推导了壳程传热系数和流体阻力降准数关联式,为其工程设计和推广应用提供了参考依据。 相似文献
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螺旋内槽管内的层流流动与传热的数值模拟 总被引:3,自引:2,他引:3
应用数值方法对一种螺旋内槽管管内的流体层流流动和传热进行了数值分析。采用数学变量置换把控制方程由原坐标系中的三维动量、能量及连续性方程转化为二维螺旋坐标系下的数值计算模型,并利用现有的二维数值模拟软件进行模拟计算。计算考察了恒壁温、轴向恒热流螺旋内层流充分发展流体的流动与传热随雷诺数的变化,并研究了螺距的影响。 相似文献
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The characteristics of heat transfer were studied in both a gas‐solids concurrent downflow fluidized bed (downer) and a gas‐solids concurrent upflow fluidized bed (riser) with FCC particles. The radial and axial distribution profiles of the heat transfer coefficient between a suspended surface and the gas‐solids flow suspension were obtained using a miniature heat transfer probe, under different operating conditions. Comprising the results of the heat transfer in the downer and the riser shows that there exists some significant distinction between the heat transfer processes in the two reactors. The characteristics of heat transfer in both cases are closely related to their hydrodynamics and the distinct flow structures determinate the different heat transfer behaviors. The results also indicate that the operating conditions present some different effects in the two beds. 相似文献
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Chlorinated polyvinyl chloride (CPVC) is often used in injection molding for products that demand high heat resistance. However, proper control of its flow properties is difficult. To improve flow behavior some internal lubricants are usually used, but they reduce heat resistance of the products. Upper critical solution temperature (UCST) lubricants were found to enhance its flow properties, and also high heat resistance was retained. They act as internal lubricants during processing, improving flow and phase separation during cooling. Therefore they are present essentially as inert filler and thus have little effect on heat distortion temperature. 相似文献