共查询到19条相似文献,搜索用时 828 毫秒
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介绍一种基于空气加湿除湿技术的太阳能海水淡化装置,装置中除湿腔叠置在加湿腔的上部,以此缩小装置的占地面积并利用热湿空气自然上升的浮力,形成一种新结构。详细说明装置的结构和运行原理,并研究控制海水运行温度、流量、循环空气流率等参数对装置产水性能的影响。实验结果表明,装置产水量随进水流量和运行温度增加而增加,当温度为90℃时,进水流量为420 kg/h,装置的最大产水量达到10.38 kg/h,装置性能系数GOR最大为1.33。系统在类似条件下的理论产水率达到约15.6 kg/h,性能系数达到1.90。对生化小球和加湿帘2种填料及不同填料厚度的产水性能进行测试,结果表明填料的选择,要结合装置体积和传质效率来综合考虑。 相似文献
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提出一种多级鼓泡式加湿除湿型海水淡化装置。该装置主要由多曲面太阳能聚光系统、加湿层和除湿层以及相应的泵和管路组成。经聚光器加热后的高温空气在风机驱动下分别进入加湿层和除湿层,热风穿过各级筛板及筛孔,产生气泡,增大了空气与水的接触面积,强化了传热传质过程。在不同天气下对装置进行实验研究,结果表明:在晴朗天气下,装置的太阳能利用率最高可达0.41,淡化装置效率最大可达1.23,最大产水速率为3.66 kg/h,全天产水量为17.08 kg;在非晴朗天气下,装置产水量为12.43 kg。 相似文献
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为评估湿空气透平循环中湿燃气对透平叶片燃气侧换热特性的影响,以及湿空气对透平叶片冷却效果的影响,以C3X叶片为例,采用热流固耦合的数值计算方法,研究了湿燃气含湿量对透平叶片表面温度和传热系数的影响,对比分析了干空气与湿空气冷却效果的差异.同时在研究范围内给出了透平叶片燃气侧传热系数的无量纲关系式,为湿化燃气轮机透平叶片的优化和冷却结构设计提供参考.结果 表明:湿燃气含湿量对透平叶片燃气侧的流动性能基本无影响;当湿燃气含湿量从0 g/kg增加到150 g/kg,主流进口温度为1473 K时,透平叶片表面平均传热系数增加10%,且增加幅度随着主流进口温度的升高而增大,叶片表面最高温度平均提高10 K;与干空气相比,湿空气作为冷却工质时的叶片表面温度更低,冷却效率更高,且冷却效率随着湿空气合湿量的增加而提高. 相似文献
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以上海徐汇某别墅空调系统为例,利用TRNSYS软件对太阳能溶液除湿新风系统的运行情况进行数值模拟,以验证该系统夏季供冷工况下运行的稳定性和可靠性。主要模拟太阳能溶液除湿新风系统运行过程中新风经过各级除湿塔后含湿量的变化、除湿溶液经各级除湿塔后浓度的变化以及除湿溶液再生前后浓度的变化。结果表明:一、二级除湿塔的除湿效率较高,三、四级除湿塔的除湿效率相对较低;使用者可根据室外含湿量具体情况选择除湿塔运行级数,而四级除湿塔的联合运行能保证全夏季空调期内送风含湿量均低于设计送风含湿量11.22 g/kg;除湿溶液经四级除湿后的平均浓度保持在34%~35%之间,仍保留有一定的除湿能力;夏季空调期内溶液再生前后浓度差的平均值为6.48%,溶液再生效率高,能为除湿环节提供稳定的除湿浓溶液。太阳能溶液除湿新风系统运行稳定,能满足不同室内外气象参数条件下系统送风参数的要求。 相似文献
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对一种聚光直热式加湿除湿太阳能海水淡化装置进行实验测试,根据其产淡水速率和经济成本,对其长期运行的经济性进行分析。在室内稳定条件下,测试给出海水喷淋温度、加热功率等对产水速率的影响曲线。结果表明,采用双层加湿小球作为加湿层材料的系统产水效果最好,在喷淋温度为73℃时,其产水速率为1.12 kg/h。在实际天气下,也测试给出装置内部的工作温度和产水性能随时间的变化曲线。实验结果表明,在平均太阳直射辐照度为692 W/m~2时,最大产水速率达到0.52 kg/h,装置的平均性能系数达到0.84。 相似文献
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对逆流喷雾式饱和器内部空气的湿化过程进行实验研究,实验中不仅测量了饱和器进出口湿空气的相对湿度、温度和水的温度,而且也测量了饱和器内部几个高度截面上湿空气的相对湿度和气相、液相的温度。根据实验测量的湿空气的相对湿度和温度,计算出了饱和器内湿空气的含湿量和测量高度间湿空气的加湿量。由实验结果可见,随水气质量比的增大,饱和器出口湿空气的温度和温升也相应增大。湿空气的含湿量和水的蒸发量、出口温度随进口水温升高、水气质量比增大而增大。在所有实验工况下,饱和器出口湿空气接近或达到饱和。随空气速度增大水滴逃逸量增大。总体上饱和器内部下部主要是加湿进口空气,上部是加湿和加热空气。 相似文献
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针对偏远缺水地区提出一种新型竖管式蒸馏太阳能苦咸水淡化装置,利用嵌套圆管之间小空间形成苦咸水受热蒸发冷凝腔从而生成淡水,该装置具有结构紧凑、节省空间、承压性能好等特点。介绍了竖管式蒸馏太阳能苦咸水淡化装置的结构原理,对装置在不同加热功率下淡水产量及蒸发冷凝温度进行了试验研究,得到了不同运行工况下装置的性能系数,探索了提高装置淡水产量的方法,分别研究了在负压运行工况和套筒外壁面水冷负压运行工况下的装置淡水产量和温度变化。结果表明:装置在输入功率为200 W时,性能系数可以达到0.80;工作压力为75kPa,加热温度为80.00℃时,装置淡水产量为0.259kg/h,比相同加热温度下常压时装置淡水产量提高23.90%;当装置套筒外壁面进行水冷强化,工作压力为75kPa,加热温度为70.00℃时,装置淡水产量为0.690kg/h,是非水冷相同运行工况下装置淡水产量的3.62倍。 相似文献
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A heat pump process is proposed for the recovery of the latent heat of water vapour in waste heat gases. The process includes a humidifier where the moist waste gas is additionally humidified. The moist gas leaving the humidifier is pressurized in a turbocompressor. The dew point temperature of the gas is increased by the humidification and the compression. This is utilized by indirect heat exchange for the production of low pressure steam and for the required heat of vaporization in the humidifier. It should be possible to use the process for waste heat recovery from moist flue gases and from process gases such as dryer exhaust air. Performance data have been calculated for production of low pressure steam at 1.2 bar from moist air at atmospheric pressure, dry temperature 100°C and the absolute humidity 0.19 kg water vapour per kg dry air. With these data a coefficient of performance for the heat pump process has been calculated to be 2.8. 85% (m/m) of the waste heat has been recovered from the moisture content. For these calculations the pressurization in the compressor has been set to 4.0 bar. The process should be further investigated to find performance data under optimal operating conditions. 相似文献
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An experimental investigation of the thermodynamic performance of a counter-flow spray humidifier was conducted on the basis of theoretical analysis of the heat and mass transfer mechanism inside the humidifier. Critical parameters such as the temperature and relative humidity of air and the temperature of water at the inlet and outlet were measured. The influence of every measured parameter on the thermal performance of the humidifier was obtained under different experimental conditions. The cooling number, whose variation was also obtained, was calculated according to the measured data. The experimental results show that both the temperature and the temperature increment of outlet humid air and the temperature of outlet water increase with an increase of the water-gas ratio, whereas the cooling number decreases. Under all experimental conditions, the outlet humid air reaches or is close to the saturation level. The lower cooling number is favorable for the system, but it has an optimal value for a certain humidifier. 相似文献
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Yuzhang WANG Yixing LI Shilie WENG Yonghong WANG 《Frontiers of Energy and Power Engineering in China》2008,2(1):43-47
An experimental investigation of the thermodynamic performance of a counter-flow spray humidifier was conducted on the basis
of theoretical analysis of the heat and mass transfer mechanism inside the humidifier. Critical parameters such as the temperature
and relative humidity of air and the temperature of water at the inlet and outlet were measured. The influence of every measured
parameter on the thermal performance of the humidifier was obtained under different experimental conditions. The cooling number,
whose variation was also obtained, was calculated according to the measured data. The experimental results show that both
the temperature and the temperature increment of outlet humid air and the temperature of outlet water increase with an increase
of the water-gas ratio, whereas the cooling number decreases. Under all experimental conditions, the outlet humid air reaches
or is close to the saturation level. The lower cooling number is favorable for the system, but it has an optimal value for
a certain humidifier.
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Translated from Journal of Power Engineering, 2006, 40(9): 1263–1267 [译自: 动力工程] 相似文献
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A study of the performance enhancement of a humidification-dehumidification (HDH) system integrated with multiple evaporators/condensers heat pump (HP) and heat recovery units is presented. The HP unit is intended to deliver necessary heating for humidifier and heating/cooling for dehumidifier in a new strategy. The proposed integrated system is capable to produce fresh water from the HDH system and HP unit. Four different configurations of the system formed by excluding/adding condensers and evaporators were investigated; mode-A (seawater precooling and reheating), mode-B (seawater reheating), mode-C (seawater precooling and humid air reheating), and mode-D (humid air reheating). Fresh water productivity, fresh water ratio, system water recovery, gain output ratio, specific work consumption, and fresh water production cost were used as performance measuring parameters of the system. The influences of operating parameters on the system performance were analytically studied and experimentally validated for different system configurations. The results indicate the enhancement of the systems' performance with increasing ambient air temperature and humidity, seawater and air flow rates, and with decreasing seawater temperature. The system configuration of mode-B shows the best performance with fresh water production of 61.94 kg/h and gain output ratio of 4.97 which are higher than those of the other configurations by 13%, 55%, 85% and 11%, 48%, and 75%, respectively. Comparisons of the proposed configurations with the other HDH desalination systems available in the literature were presented and better performance of the proposed systems was noticed. 相似文献
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在理论分析湿化器内部传热传质机理的基础上,进行了湿化器总体热力性能试验,得出了在不同实验工况下,各测量参数对湿化器热力性能的影响规律,同时计算了冷却数,得出了其变化规律。结果表明:随水气质量比的增大,湿化器出口湿空气的温度、温升和出口水温都增大,而冷却数减少。在同一水气质量比下,随进口水温升高,出口湿空气温度、温升和出口水温都增大,冷却数减少。在各实验工况下,湿化器的出口湿空气都具有很高的相对湿度,达到或接近饱和状态。冷却数降低对系统有利,但不是越低越好,应该优化选择最佳值。 相似文献
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以陕西地区苹果树修剪枝为原料,采用自制的生物质成型燃料多参数调控试验系统,分析单颗粒成型过程中的压力-位移曲线,考察基质含水率(5%~20%)、成型温度(70~150℃)和压力(80~120 MPa)对颗粒燃料成型能耗的影响。结果表明:随着压具位移的增加,挤压过程的压力变化呈3个阶段:松散段、过渡段和压紧段;推出过程的压力变化总体呈波动下滑的趋势,且初期压力波动范围较大。试验范围内,随着温度的升高,挤压能耗降低、推出能耗升高;随着压力的增大,二者均升高;基质含水率影响趋势相同,15%均达到最低值(29.47、4.79 J/g)。 相似文献