Optimization of Dividing Wall Column with Heat Transfer Process Across the Wall for Feed Properties Variation

This paper investigates the thermal-coupled effect across the wall and the optimal heat transfer region of the wall for enhancing the energy saving effect of dividing wall column (DWC), and also studies the effects of feed thermal condition (q) and middle component composition of feed (cB) on the heat transfer process, the optimal heat transfer region, and the maximum heat transfer quantity across the wall. The simulation results show that the maximum heat transfer quantity across the wall and the potential for energy saving increase with the increase of q, while with the limitation of temperature difference across the wall, the beneficial heat transfer effect between certain range of stages, which are involved in the optimal heat transfer region, cannot be realized completely for a specific value of q. Besides, compared with q, a changing cB does not change the degree of realizing the beneficial heat transfer effect, but can bring about the variation of liquid split ratio (RL) and vapor split ratio (Rv). Thus, for achieving a maximum energy-saving effect of DWC, different q and cB need to find its own corresponding suitable heat transfer process across the wall.

Heat transfer performance for DCLL blanket with no-wetting insulator walls

Magnetohydrodynamic (MHD) effect and heat transfer are two key issues for design of dual coolant lead lithium (DCLL) blanket. Flow channel insert (FCI) has been applied to decouple the liquid metal from the walls to efficiently decline MHD pressure drops and reduce heat losses from the liquid metal for increasing bulk exit temperatures of the blanket. However, there are still big pressure drops and a higher velocity jet located at the gap flow. Moreover, the FCI made from silicon carbide (SiC) constitutes a complex blanket structures which potentially causes special flow phenomena. In the present work, the characteristics of fluid flow and heat transfer in the DCLL blanket channel are investigated for the first wall (FW) sprayed a layer of no-wetting nano coating (NWNC) on its inner surface. The results show that the pressure drop with NWNC wall is oneorder magnitude lower than that with FCI in the general DCLL blanket. The Nusselt number on the NWNC wall is about half of that on the general wall. On this basis, a heat transfer criterion equation of DCLL channel is achieved for the NWNC wall without FCI. The results are compared with that criterion equation of general wall conditions, which indicates the criterion equation can well predict the convection heat transfer of DCLL channel.

MHD non-Newtonian micropolar fluid flow and heat transfer in channel with stretching walls

A study is presented for magnetohydrodynamics （MHD） flow and heat transfer characteristics of a viscous incompressible electrically conducting micropolar fluid in a channel with stretching walls. The micropolar model introduced by Eringen is used to describe the working fluid. The transformed self similar ordinary differential equations together with the associated boundary conditions are solved numerically by an algorithm based on quasi-linearization and multilevel discretization. The effects of some physical parameters on the flow and heat transfer are discussed and presented through tables and graphs. The present investigations may be beneficial in the flow and thermal control of polymeric processing.

Heat transfer analysis of Williamson fluid over exponentially stretching surface

This study explores the effects of heat transfer on the Williamson fluid over a porous exponentially stretching surface. The boundary layer equations of the Williamson fluid model for two dimensional flow with heat transfer are presented. Two cases of heat transfer are considered, i.e., the prescribed exponential order surface temperature （PEST） case and the prescribed exponential order heat flux （PEHF） case. The highly nonlinear partial differential equations are simplified with suitable similar and non-similar variables, and finally are solved analytically with the help of the optimal homotopy analysis method （OHAM）. The optimal convergence control parameters are obtained, and the physical fea- tures of the flow parameters are analyzed through graphs and tables. The skin friction and wall temperature gradient are calculated.

Mathematical Modelling of Mass Transfer and Free Convection Current Effects on Unsteady Viscous Flow with Ramped Wall Temperature

An exact analysis of the flow of an incompressible viscous fluid past an infinite vertical plate is conducted taking into account the presence of foreign mass or constant mass flux and ramped wall temperature. The dimensionless governing coupled linear partial differential equations are solved using the Laplace transform technique. Two different solutions for the fluid velocity are obtained–one valid for the fluids of Schmidt numbers different from unity, and the other for which the Schmidt number is unity. The effects of Prandtl number (Pr), Schmidt number (Sc), time (t) and mass to thermal buoyancy ratio parameter (N) for both aiding and opposing buoyancy effects on the velocity and skin-friction are studied. Also, the heat and mass transfer effects on the flow near a ramped temperature plate have been compared with the flow near a plate with constant temperature.

Viscoelastic Effects on Unsteady Two-Dimensional and Mass Transfer of a Viscoelastic Fluid in a Porous Channel with Radiative Heat Transfer

An analysis of oscillatory flow of a viscoelastic fluid and mass transfer along a porous oscillating channel with radiative heat transfer in presence of first-order chemical reaction is considered. The problem is concerned with the flow through a channel in which the viscoelastic fluid is injected on one boundary of the channel with a constant velocity, while it is sucked off at the other boundary with the same velocity. The two boundaries are considered to be in close contact with the two plates placed parallel to each other. The effect of temperature oscillations at the plate (upper wall) where the suction takes place is taken into consideration. The plates are supposed to be oscillating with a given velocity in their own planes. Analytical expressions for velocity profile, the temperature, concentration profile, wall shear stress on the upper wall are obtained. The profiles of the velocity and skin friction have been presented graphically for different values of the viscoelastic parameters with the combination of the other flow parameters encountered in the problem under investigation. It is observed that velocity decrease with the increasing values of the viscoelastic parameter in comparison with Newtonian fluid. Also, the wall shear stress increase with the increasing values of the viscoelastic parameter.

干式装配式墙体非均匀性传热规律

干式连接的装配式建筑因连接缝的存在会造成接缝与墙体间的传热不均,对墙体传热及建筑能耗产生重要影响。分析了干式装配外墙的非均匀传热特征,提出外墙内表面的累计温差比T′来评价墙体的传热非均匀性,确定了干式装配墙体传热的非均匀判定准则。提出用热桥影响区域等效传热系数K′_(T)来评价接缝非均匀传热影响区域,分析了非均匀性传热对建筑采暖能耗的影响。结果表明,装配式墙体在接缝两侧的温度波动较大,且墙体构造越复杂波动越显著。干式装配墙体接缝的非均匀影响区域明显大于传统砖混建筑。T′越大墙体传热越不均,建筑采暖能耗越大。接缝宽每增加5 mm导致的墙体传热不均使得建筑能耗变化约为3%~4%,含空气层的预制墙体变化尤为大,约为3.2%~6.7%。

MATHEMATICAL MODELING OF NEAR-WALL FLOWS OF TWO- PHASE MIXTURE WITH EVAPORATING DROPLETS

In the framework of the two-continuum approach, using the matched asymptotic expansion method, the equations of a laminar boundary layer in mist flows with evaporating droplets were derived and solved. The similarity criteria controlling the mist flows were determined. For the flow along a curvilinear surface, the forms of the boundary layer equations differ from the regimes of presence and absence of the droplet inertia deposition. The numerical results were presented for the vapor-droplet boundary layer in the neighborhood of a stagnation point of a hot blunt body. It is demonstrated that, due to evaporation, a droplet-free region develops near the wall inside the boundary layer. On the upper edge of this region, the droplet radius tends to zero and the droplet number density becomes much higher than that in the free stream. The combined effect of the droplet evaporation and accumulation results in a significant enhancement of the heat transfer on the surface even for small mass concentration of the droplets in the free stream.

果香香韵单体在壁式加热卷烟中转移行为分析研究

为量化表征果香单体香原料在壁式加热卷烟中的调香可用性,基于气相色谱质谱联用技术和嗅觉感官阈值测定,分别研究了果香单体香料在壁式加热卷烟中的转移分布、加香贡献度及逐口释放行为。通过研究发现:1)果香单体香原料的加香贡献度D值差距甚大,其中D值最大的γ-辛内酯(12485.0)是苯甲醇(0.1)的10万倍;2)果香单体香料的主流烟气转移率不高,约7%~37%,但高沸点香料损失主要原因是冷凝截留而低沸点香料损失主要原因是抽吸过程中空气散失;3)果香单体香料的逐口释放量随抽吸口序增加有两种趋势,一种呈逐口递减趋势,另一种呈先增后递减趋势。其中庚酸乙酯,辛酸乙酯,癸酸乙酯,乙酰丙酸乙酯和苯乙酸乙酯属递减,肉桂酸乙酯,γ-庚内酯,γ-辛内酯,γ-癸内酯等属先增后减。

预制内外复合保温模壳拼装墙体热工性能研究

为探究预制内外复合保温模壳拼装墙体结构中的卡板连接件对墙体热工性能的影响,通过热工理论计算、试验研究、ANSYS有限元热分析模拟软件3种方法,对比分析了无连接件、不同数量连接件以及双面抹灰不同条件下墙体的传热系数。结果表明:在无连接件条件下,实际墙体热工试验测试值与热工理论计算值的误差较小;连接件数量越多,热桥效应越明显,墙体的热工性能越差;采用有限元模拟软件对墙体进行热工设计结果较精确,可作为设计依据;研究结果可为模壳拼装墙体在超低能耗建筑的应用及能耗分析提供借鉴。

夏热冬冷地区办公建筑节能改造设计研究

本文主要探究了夏热冬冷地区某办公建筑的节能改造设计方案。调查发现,该办公建筑一天之中8-18时能耗较高;一年之中夏季能耗最高,冬季次之;空调能耗在总能耗中的占比最大。基于实用性和经济性原则,选择建筑围护结构进行了节能设计,外墙方面使用EPS保温板,屋顶设计成种植屋面,外窗改造成真空玻璃窗和双层玻璃幕墙。结果表明,相比于原建筑,使用节能设计方案后外墙、屋顶和外窗的传热系数均有大幅度的降低,使得建筑保温隔热性能明显提升,达到了节能降耗的效果。

油滴与高温固体壁面碰撞的流动与传热及飞溅特性

考虑油滴(油膜)/固体壁面接触角动态变化和油液热力学特征参数受温度影响,基于流体体积法建立了油滴与高温固体壁面碰撞的三维流动与传热数值计算模型,通过试验验证了数值计算模型的正确性。基于数值计算模型,分析了油滴碰撞高温固体壁面后的流动与传热及飞溅特性,以试验和数值计算结果为基础,建立了描述油膜铺展/飞溅临界判据。结果表明:油滴碰撞高温固体壁面后的状态与碰撞条件有关,破碎、飞溅有利于油膜的铺展流动;二次油滴是油膜边缘破碎产生的油带断裂而成,大直径二次油滴分裂为小直径油滴;随油膜铺展进程,壁面平均热流密度增大,而油膜的径向热流密度则逐渐减小;增大碰撞速度、油滴直径和润滑油温度,有利于油膜的破碎与飞溅,二次油滴数量和下飞溅角均随之增大。

寒冷地区光伏墙体综合传热特性的数值模拟研究

近年来BIPV项目逐渐增多,对光伏墙体的研究多以光伏组件电热性能为重点,少有结合节能墙体热工性能对不同构造光伏墙体的综合传热特性优化开展的研究。以天津地区为应用场景,分别建立符合天津市居住建筑四步节能设计技术指标的基础墙体、普通光伏墙体和嵌入保温隔热一体化板的新型光伏墙体的传热模型,采用ANSYS FLUENT软件对其温度分布、表面热流密度进行数值模拟,对模拟结果进一步分析获得不同类型墙体的传热系数和光伏组件的电性能。结果表明:较基础墙体,夏季普通光伏墙体内表面得热量可增加46.88%,冬季普通光伏墙体内表面失热量可减少5.47%;新型光伏墙体中的保温隔热层厚度宜不小于20 mm,此时,夏季新型光伏墙体内表面得热量最大可增加18.16%,冬季新型光伏墙体内表面失热量最小可减少20.07%。基于计算结果,寒冷地区的建筑外墙应用光伏组件时,散热构造措施可简化。

能源连续墙对室内侧壁面热湿耦合传递行为的影响

目前国内外针对能源连续墙的研究主要集热交换性能,鲜有研究关注其对邻近地下建筑热湿环境的影响。本文通过建立热湿耦合传递三维数值模型,研究了能源连续墙对相邻地下室墙体壁面热湿状态和与室内环境热湿交互通量的影响。研究结果表明,能源连续墙的运行明显改变了室内侧壁面的热湿流方向和热湿流密度大小;与纯传热结果相比,虽然传湿过程对壁面温度的影响小于0.2℃,但是这部分差异会造成显热热流密度预测偏差超过10%;不计潜热热流会造成对地下室内热负荷的低估超过2.4%;绝缘层的隔热防潮作用能够阻碍流向室内的热量和湿汽。

带扰流柱阵的双层壁间隙冲击传热特性

数值模拟研究了带扰流柱阵的双层壁结构间隙靶面、冲击面以及不同位置扰流柱面努塞尔数详细分布,分析了各个表面努塞尔数平均值随冲击雷诺数的变化规律以及不同位置扰流柱面换热特性差别。结果表明,靶面努赛尔数的第二峰值大于滞止点处的努赛尔数。冲击面展向平均努赛尔数最大值位于靠近冲击孔的第2排和第4排扰流柱处。在5排扰流柱中,与冲击孔处于同一排(第3排)的扰流柱面平均努塞尔数最大,表现为翻卷汇流传热特性;第2排和第4排扰流柱面平均努塞尔数次之,表现为翻卷绕流传热特性。远离冲击孔的第1排和第5排扰流柱面平均努塞尔数最小,表现为绕流传热特性。冲击雷诺数从1×104增加到6×104,第3排扰流柱面和第2、4排扰流柱面以及第1、5排扰流柱面努塞尔数增幅分别为306%、325%和360%。

柴油喷雾撞击高温壁面的瞬态传热特性

通过瞬态测温技术对定容燃烧室中柴油喷雾撞击高温壁面的瞬态传热特性进行了研究.结果表明:初始壁面温度从250℃升高到550℃,壁面上传热模式由膜态蒸发转化为核态沸腾,进而转化为过渡沸腾,这种转化使表面热流密度和换热系数先增大后减小,且分别在440℃和400℃达到最大值.增大喷射压力、减小撞壁距离和环境温度有助于提高表面热流密度和换热系数.初始表面温度的升高增加了喷射压力和撞壁距离对传热特性的影响,但降低了环境温度的作用.以毕渥数和傅里叶数表示的量纲为1表面热流密度曲线形态高度相似,且揭示了喷雾撞击高温壁面过程中的内部传热机制.此外,建立了一种准确性高、适用壁面温度范围广的预测最大表面热流密度的量纲为1模型.

湿工况下带翼翅片管传热传质特性的数值研究

采用壁面反应原理建立冷凝传热模型,模拟研究平直翅片管、矩形翼翅片管以及弓形翼翅片管的通道内湿空气流动及传热传质特性。结果表明:当湿空气入口温度为328 K,水蒸气质量分数为11.2%时,矩形翼翅片管和弓形翼翅片管的传热因子相比于平直翅片管分别提高了24.9%—35.7%、26.7%—36.4%,传质因子分别提高了24.1%—35.4%、25.9%—38.3%,但矩形翼翅片管和弓形翼翅片管通道内工质的流动阻力系数分别增加了19.4%—25.3%、16.8%—22.9%,说明了矩形翼和弓形翼均可提高翅片管的传热传质特性,但也造成了阻力损失的增加。通过对综合传热性能评价因子的分析,矩形翼翅片管和弓形翼翅片管的综合传热性能评价因子值均>1,其综合传热性能均优于平直翅片管,且弓形翼翅片管综合传热性能最优。

预制模块化高炉渣纤维保温外墙板传热分析

该研究旨在分析预制模块化高炉渣纤维保温外墙板的传热性能,评估其在建筑保温领域中的应用潜力。通过实验测试获取高炉渣纤维保温外墙板的物理性质和热导率,并进行传热分析。研究发现,预制模块化高炉渣纤维保温外墙板具有较低的热导率和良好的隔热性能。通过传热分析,观察到该外墙板可以有效地减少室内外温度差异,降低热能传递损失。此外,建筑内部的温度稳定性得到改善,达到良好的节能效果。基于传热分析的结果,预制模块化高炉渣纤维保温外墙板在建筑保温领域具备广阔的应用前景,有助于降低能源消耗,并提供舒适的室内环境。该研究为高炉渣纤维保温材料在建筑行业中的应用提供理论支持,为能源节约和减排作出贡献。