新型自然循环自动清洗式蒸发器及设计原理

以高效蒸发器为目标，旨在以自然循环替代高能耗的强制循环泵、以自动清洗取代加热面盐垢的周期性停车清洗．主要研究沸腾室内的不平衡汽化过程机理，提出动力温度的新概念，采用显热与汽化热转换平衡的研究方法，得到自然循环推动力的工程设计计算式，并且由此引出推动力强化的基本原则，进而获得中试的成功．还提出加热室必须采用能够低流速下自转清洗又高效传热强化的螺旋齿带，才能保障循环总阻力低于推动力．     

Bilayer rGO-Based Photothermal Evaporator for Efficient Solar-Driven Water Purification[]**

Interfacial evaporation has emerged as a promising approach to produce freshwater. However, an urgent concern is that, due to the illegal discharge of industrial wastewater, most water bodies are polluted by trace volatile organic compounds (VOCs), which are easily volatilized and enriched in the collected water during the interfacial evaporation process. Herein, a bilayer photothermal evaporator was reasonably designed for contaminated water purification. The bottom hydrophilic rGO-sodium alginate (SA) sheets purposefully disintegrate water transport channels, thus quickly removing VOCs through physical adsorption. The rGO-SA-TiO₂ upper layer sufficiently absorbs incident light and therefore persistently generates reactive oxidizing species to degrade upward VOCs. Notably, the oriented microchannels inside the evaporator allow sustained light reflections to improve the utilization of solar energy. The evaporation rate can reach 1.63 kg m⁻² h⁻¹ with a considerably high VOC removal efficiency of up to 96 %. Such an integrated bilayer evaporator provides an effective strategy to obtain clean water via solar distillation.     

连续螺旋折流板蒸发器壳侧流动换热数值模拟研究

本文对相同几何尺寸的连续螺旋折流板蒸发器与传统弓形折流板蒸发器进行对比性的数值模拟研究,结果表明:在相同壳侧体积流量和折流板数条件下,连续螺旋折流板蒸发器的传热因子和摩擦因子约是弓形折流板的1/3和1/4;当以换热因子和摩擦因子比值评价蒸发器综合性能时,连续螺旋折流板蒸发器比弓形折流板蒸发器提高57%;当最小流通截面流...     

Characterization of sugar juice heat exchanger tube deposit

Fouling of heat exchanger surfaces during sugar manufacture reduces productivity and increases energy demand. This study characterizes a deposit (including its internal structure) formed in a sugar factory's evaporator unit using a variety of X‐ray diffraction and scanning electron microscopy techniques (including X‐ray powder diffraction, X‐ray fluorescence, elemental mapping with energy dispersive spectroscopy and backscattered electron imaging). Calcium sulfate dihydrate, calcium oxalate mono‐ and dihydrate, hydroxyapatite, amorphous silica and organic matter are present in the deposit. The composition of the deposit (which contains three layers) varies along the height of the tube. There are noticeable differences in the composition and porosity among the layers in the deposit. A porous structure consisting of a mixture of amorphous silica, calcium oxalate dihydrate and organic matter is attached to the surface of the deposit in contact with sugar juice, while a denser morphology of amorphous silica and hydroxyapatite is attached to the tube wall. Elemental mapping identifies an association between Si, Al, Mg, Fe and O, suggesting the presence of a silicate compound as a minor component in the deposit. An attempt is made to rationalize the formation of the observed phases. Copyright © 2010 John Wiley & Sons, Ltd.     

中高温工质在蒸发器中的换热模拟分析

本文采用分布参数的方法,建立了水源热泵中普遍采用的壳管式蒸发器稳态数学模型.通过中高温水源热泵试验台的实验数据同模拟计算结果的对比,验证了数学模型的准确性。应用此数学模型对中高温工质HTR01、HTR02及R134a在蒸发器典型制热运行工况,进行了模拟计算。得出了三种工质制冷剂侧换热系数沿管长的变化关系并对三种工质的换热性能进行了对比分析,为采用中高温工质的水源热泵换热器设计提供了参考依据.     

风速分布形状对空调中翅片管蒸发器性能的影响

通过建立空调蒸发器分布参数模型,并对模型进行了验证,进而研究了四种不同风速场对R22和R290翅片管蒸发器流动和换热性能的影响规律。研究表明:在上三角型、下三角型和三角型风速场分布下,蒸发器单位面积换热量、质量流量以及压降均较均匀风速场降低;上三角型较均匀型单位面积换热量下降达7%左右,下三角型和三角型较均匀型下降4%左右;在不同风速场下,各换热温差基本持平,总传热系数起主导作用;R290质量流量均较R22小40%左右,且压降均较R22小24%左右。在满足换热量的要求下,R290在协调压降与质量流量具有一定的优势,可以作为现有空调制冷剂R22的环保型替代工质。     

蒸发器出口状态热式测量的实验研究

根据热式感应原理,专门设计热式感应传感器,用于测量蒸汽压缩制冷循环中干式蒸发器出口的气液两相流动状态;热式感应传感器的测量数据与蒸发器出口流型、过热度等参数的综合比较分析表明:热式感应传感器可以辨识出蒸发器出口过热蒸汽、雾状流和二者交替三种流动状态.同时,实验数据表明蒸发器出口处于过热蒸汽、雾状流二者交替的过渡区时其换热效率最佳,因此热式感应传感器可以用于作为膨胀阀-干式蒸发器调节回路的反馈信号.应用热式感应传感器对蒸发器出口状态的随机性和周期性波动的测量证明:热式感应传感器动态性能良好,可以实时反映蒸发器出口状态变化.     

小型平板CPL蒸发器预热驱动过程研究

分析了小型平板CPL蒸发器毛细多孔芯上下表面温差对启动的影响,建立了蒸发器满液启动的数学模型.结果表明,对不同的金属外壁,多孔芯上下表面平均温差存在一个最大值,铜壁时,温差较小,侧壁效应明显;采用不锈钢壁及上壁铜、侧壁下壁不锈钢时,温差大,侧壁效应小;采用不锈钢外壁时蒸发器加热面的温度过高.上壁采用导热系数大、侧壁下壁为导热系数小的金属对小型平板CPL蒸发器的正常启动以及降低加热表面温度非常有利.     

On-line solvent evaporator for coupled LC systems

The mobile phase of a fraction eluted from a first LC column is removed by an on-line evaporator in order to reconcentrate the solute material or to exchange the eluent before performing a subsequent LC separation. Evaporation essentially occurs by concurrent evaporation, i.e. the solvent evaporates at a rate equal to the flow rate of the incoming eluent, and is driven by the overflow principle, i.e. vapors leave the tube as a result of the expansion resulting from evaporation. The liquid is introduced into a small tube (e.g., 4 cm × 1.3 mm i.d.) which is packed, e.g., with a coarse silica gel. The outlet of the evaporator is connected to vacuum in order to enable evaporation at reduced temperature and to increase retention of the volatile components. With normal phase eluents, evaporation rates may approach 1 ml/min; n-dodecane was the most volatile n-alkane fully retained by the evaporator.     

直接供液与重力供液制冷系统的对比研究

重力再循环供液是指蒸发器依靠制冷剂自身的重力送入蒸发器,在供液高度大于蒸发器对制冷剂的阻力情况下,部分制冷剂液体在蒸发器和气液分离器所形成的回路中再循环。由于再循环作用不需要外加动力,并强化管内制冷剂的沸腾换热,蒸发器的效率得以明显提高。文中介绍了重力再循环供液制冷系统和蒸发器的结构,提出采用J.Chawla关系式和Shah关联式相结合的方法预测再循环蒸发器制冷剂侧的换热系数。采用空气侧热平衡法,对直接膨胀供液和重力再循环供液制冷系统分别进行了多蒸发温度下的性能测试。表明重力再循环供液制冷系统比直接膨胀供液制冷系统的制冷量平均增加26%,COP平均增加18%,蒸发温度平均升高1.1℃,传热系数是直接供液的1.57倍。J.Chawla关系式和Shah关联式相结合预测再循环蒸发器制冷剂侧的换热系数,其曲线结构与实验值近似,平均误差不大于20.6%。文章还对各热工参数的变化原因进行了分析。