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间接空冷系统

间接空冷系统的相关文献在1993年到2022年内共计229篇,主要集中在电工技术、能源与动力工程、建筑科学 等领域,其中期刊论文70篇、会议论文32篇、专利文献3809502篇;相关期刊44种,包括动力工程学报、汽轮机技术、华电技术等; 相关会议18种,包括2016年中国电机工程学会年会、2015年“技术创新与信息化驱动电力土建发展”学术交流会、2015国际空冷凝汽器会议等;间接空冷系统的相关文献由515位作者贡献,包括李海、冯璟、赵慧文等。

间接空冷系统—发文量

期刊论文>

论文:70 占比:0.00%

会议论文>

论文:32 占比:0.00%

专利文献>

论文:3809502 占比:100.00%

总计:3809604篇

间接空冷系统—发文趋势图

间接空冷系统

-研究学者

  • 李海
  • 冯璟
  • 赵慧文
  • 李丽梅
  • 杨晓军
  • 张伟
  • 张莱新
  • 丁利
  • 彭继业
  • 李日鑫
  • 期刊论文
  • 会议论文
  • 专利文献

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    • 张垚鹏; 蒋以山; 赵欣
    • 摘要: 在我国北方干旱地区的火力发电厂中,间接空冷系统由于其优越的节水性能得到了广泛应用。第五代福哥型间接空冷散热器(下文福哥型散热器亦指此)作为一种主要的空冷散热器型号,研究其流动传热特性,对于电站间接空冷系统的选型及高效运行具有重要意义。该文采用数值模拟的方法,计算获得了福哥型散热器冷却空气流动阻力和平均对流换热系数随迎面风速的变化关系。通过与同尺寸、没有开扰流孔散热器翅片管束的流动换热数据进行比较,结果表明:随着入口风速的不断增加,两种散热器翅片管束的空气流动压降和对流换热系数逐渐上升,摩擦因子则随之降低。空气在通过福哥型散热器时,扰流孔处的流动边界层和热边界层都遭到破坏,在增大流动损失的同时,也使传热得到显著强化。当来流风速uf为5m/s,Re为4800时,福哥型散热器翅片管束的综合性能达到最优。
    • 贾斌; 李晓波; 张维蔚
    • 摘要: 以表面式间接空冷系统空冷塔为研究对象,建立了间冷塔散热器传热性能数学模型,研究了零风速条件下间冷塔内冷却水和空气间的传热性能,以及机组负荷、环境温度对冷却水量的影响和冷却水量可调节的温度范围的影响.计算结果显示,机组负荷越高,冷却水量最低值越大,冷却水量可调节的温度范围越大;冷却水进口温度最低值越高,冷却水量最低值越小,可调节温度范围越大;冷却水出口温度最低值越高,冷却水量最低值是越大,可调节温度范围越小.得到的冷却水量优化调节的结论可为间冷机组优化运行提供理论依据及方法.
    • 魏小强
    • 摘要: 近年来因特高压外送建设的需求,我国北方地区新增较多间接空冷燃煤发电机组,尤其是1000Mw级大容量间接空冷机组如雨后春笋,而间接空冷系统散热器铝翅片腐蚀、泄露及防护一直是电力人探索研究的重点.本文介绍间接空冷系统散热器铝翅片运行现状、腐蚀原因和采取的相应措施.长城发电公司在设计初期新增一套间冷旁流处理系统,以控制间冷水pH、电导率,确保间冷系统安全稳定运行.
    • 贾世勋
    • 摘要: 直接空冷系统运行的性能好坏主要反映在凝汽器的压力上,压力过大会对直接空冷系统的运行产生影响,而凝汽器的压力又受环境变化的影响,所以说环境因素是影响直接空冷系统运行的关键要素。本文主要是直接空冷系统的基本情况、环境风对直接空冷系统的影响及如何进行优化进行分析论述。
    • 张维蔚; 王甲斌; 田瑞; 程龙; 巴旭阳
    • 摘要: 以表面式间接空冷散热器为例,建立了间接空冷散热器冷却单元的一维传热数学模型.通过该模型,计算并分析了冷却水流量、温度及空气进口温度(环境温度)、流速等对空冷散热器传热性能的影响.计算结果显示,随着冷却水流量、温度和空气流速、温度的增大,散热器总传热系数逐渐增大;散热器总传热系数更接近于空气侧表面传热系数,其中空气流速对总传热系数的影响尤为明显;积灰对散热器传热性能的负面影响较大,积灰越厚,散热器总传热系数越小.另外,利用本文模型,得到了一定条件下间接空冷系统冷却水最佳流量,为间接空冷机组的运行了提供一定的理论依据.%Taking the air cooled radiator of surface indirect air cooling system as an example, a one-dimensional heat transfer mathematical model for cooling unit of indirect air cooled radiator were established. By this model, the influence of cooling water flow rate, temperature, air inlet temperature ( ambient temperature) and flow velocity on the heat transfer performance of air-cooled radiator were calculated and analyzed. Results show that,the overall heat transfer coefficient of the radiator increases with the increase of cooling water flow rate, temperature, air flow rate and temperature; the overall heat transfer coefficient of the radiator is closer to the convective heat transfer coefficient of the air side, especially the influence of the air velocity on the overall heat transfer coefficient;the negative influence of dust accumulation on the heat transfer performance of radiator is greater, and the thicker the dust accumulation is, the smaller the total heat transfer coefficient of the radiator is. In addition, the optimal cooling water flow rate of indirect air cooling system under certain conditions was obtained by using this model, which provides a theoretical basis for the operation of indirect air cooling unit.
    • 邹庆江; 张义江; 郭民臣; 储德全
    • 摘要: Indirect dry cooling systems are widely used in coal-fired power plants.However,high environmental temperatures affect the heat dissipation performance of the dry cooling tower,causing the increase of the back pressure of the steam turbine.In this work,the evaporative cooler operating with the dry cooling tower is adopted to reduce the circulating water temperature and the exhaust steam pressure,and improve the thermal efficiency of the power unit.Taking a 600-MW steam turbine unit as the study object,an indirect dry-cooled system with evaporative cooler is designed and a mathematical model is established.The matching characteristics of the heat load distribution between the evaporative cooler and the dry cooling tower are analyzed.The back pressure,the water consumption and the pump power consumption are analyzed for various heat loads.The results show that at the rated load,when the ratio of the water flow rate for the evaporative cooler to the total circulating water flow rate is between 0.21 and 0.31,and the generation standard coal consumption rate decreases by about 7.4 g/(kW·h).%间接空冷系统在中国的应川越来越广泛,但是高温天气影响空冷塔散热,导致汽轮机背压升高.采用蒸发式冷却器与闭式空冷塔并联运行,可以降低循环水温度,进而降低汽轮机的排汽压力,提高机组的热经济性.针对某600 MW汽轮机组,设计了一种采用蒸发式冷却器的问接空冷系统,构建了数学模型,分析了蒸发式冷却器与闭式空冷塔的热负荷匹配特性,探讨了额定工况下蒸发式冷却器热负荷改变时,汽轮机背压、系统耗水量和冷却系统功耗的变化规律.计算结果表明,额定工况下,分流比为0.21~0.31时,发电标准煤耗率可降低7.4 g/(kW·h).
    • 刘学亮; 陈胜利; 万超; 李高潮
    • 摘要: 以某600 MW间接空冷汽轮机组为例,利用EBSILON软件建立了汽轮机和凝汽器模型,结合空冷塔模型完成三者耦合计算,通过正交试验方法研究了多种变工况特性,获得了不同环境温度、循环水流量和机组负荷下背压和热耗率的变化规律.结果表明:机组在相同负荷和循环水流量下,随着环境温度上升,背压和热耗率不断升高,在高温段上升速率明显快于低温段;机组负荷一定,在同样的循环水流量变化幅度下,环境温度越高,背压和热耗率的变化速率越大;在一定环境温度和循环水流量下,随着负荷增大,背压升高,热耗率下降;在机组负荷和循环水流量不变时,空冷塔出口水温上升速率大于环境温度上升速率,在100%循环水流量下,前者为后者的1.11~1.15倍,导致凝汽器进口水温迅速升高,机组运行经济性下降.%Taking a 600-MW indirect air-cooling steam turbine unit for example, the calculation model of steam turbine, condenser and air-cooling tower is established on the basis of EBSILON software. Characteristics regarding to a variety of operation conditions are studied through the orthogonal test method, such that the variations of back pressure with respect to heat rate under the conditions of different ambient temperatures, circulating water flows and steam turbine loadings are obtained. The results show that, with constant circulating water flow and steam turbine load, as the ambient temperature goes up, the back pressure and the heat rate will keep rising. In particular the increasing rate in the high-temperature section is apparently higher than that in the low-temperature section. If the steam turbine load remains constant, the higher the ambient temperature, the higher the changing rate of the back pressure and the heat consumption rate under the same cyclic water flow. In the case of constant ambient temperature and the circulating water flow, with the raise of steam turbine load, the back pressure will increase while the heat rate will drop down. In the case of constant steam turbine load and circulating water flow, the rising rate of the outlet water temperature for the air-cooling tower is greater than that of the ambient temperature rise. Specifically, the former will be 1.11-1.15 times of the latter if the circulating water flow reaches full volume limit, which will lead to the rapid increase of the inlet water temperature at the condenser and the decline of the system economy performance.
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