首页> 外文学位 >Development of techniques for in-situ measurement of heat and mass transfer in ammonia-water absorption systems.
【24h】

Development of techniques for in-situ measurement of heat and mass transfer in ammonia-water absorption systems.

机译:氨水吸收系统中传热和传质现场测量技术的发展。

获取原文
获取原文并翻译 | 示例

摘要

An experimental investigation of heat and mass transfer in a horizontal tube falling-film ammonia-water absorber was conducted. A tube bank consisting of four columns of six 9.5 mm (3/8") nominal OD, 0.292 m (11.5") long tubes was installed in an absorber shell that allowed heat and mass transfer measurements and optical access. A test facility consisting of all the components of a functional absorption chiller was fabricated specifically for this investigation. Several variations of the basic system set up were fabricated to enable testing over the wide range of conditions (nominally, desorber solution outlet concentrations of 5--40% for three nominal absorber pressures of 150, 345 and 500 kPa, over solution flow rates of 0.019--0.034 kg/s.) Measurements at the absorber were used to determine heat transfer rates, overall thermal conductances, solution-side heat and vapor-side mass transfer coefficients for each test condition.; For the range of experiments conducted, the solution heat transfer coefficient varied from 923 to 2857 W/m2-K while the vapor mass transfer coefficient varied from 0.0026 to 0.25 m/s and the liquid mass transfer coefficient varied from 5.51 x 10-6 to 3.31 x 10-5 m/s depending on the test condition. The solution heat transfer coefficient increased with increasing solution flow rate; however, the vapor and liquid mass transfer coefficients seem to remain unaffected with the variations in solution flow rate and were found to be primarily determined by the vapor and solution properties. The experimental heat and mass transfer coefficients were compared with the relevant studies from the literature.; Based on the observed trends, heat transfer correlations and mass transfer correlations in the vapor and liquid phases were developed to predict heat and mass transfer coefficients for the range of experimental conditions tested. These correlations can be used to design horizontal tube falling-film absorbers for ammonia-water absorption systems.
机译:在水平管降膜式氨水吸收器中进行了传热和传质的实验研究。在吸收器外壳中安装了由四根六列9.5 mm(3/8“)标称外径,0.292 m(11.5”)长管组成的管束,该管壳允许进行传热和传质测量以及光学访问。专为这项研究而建造的功能性吸收式冷却器的所有组件组成的测试设施。制作了几种基本系统设置的变体,以便能够在各种条件下进行测试(名义上,对于150、345和500 kPa的三个标称吸收器压力,解吸器溶液出口浓度为5--40%,在溶液流速范围为0.019--0.034 kg / s。)在吸收器上的测量用于确定每种测试条件下的传热速率,总热导率,溶液侧传热和蒸汽侧传质系数;在所进行的实验范围内,溶液的传热系数在923至2857 W / m2-K之间变化,而蒸汽的传质系数在0.0026至0.25 m / s之间变化,液体的传质系数在5.51 x 10-6之间变化。 3.31 x 10-5 m / s,取决于测试条件。溶液的传热系数随溶液流量的增加而增加。然而,蒸汽和液体的传质系数似乎不受溶液流速变化的影响,并且主要由蒸汽和溶液的性质决定。实验传热和传质系数与文献中的相关研究进行了比较。基于观察到的趋势,开发了气相和液相中的传热相关性和传质相关性,以预测在所测试的实验条件范围内的传热和传质系数。这些关联可用于设计用于氨水吸收系统的水平管降膜吸收器。

著录项

  • 作者

    Lee, Sangsoo.;

  • 作者单位

    Georgia Institute of Technology.;

  • 授予单位 Georgia Institute of Technology.;
  • 学科 Engineering Mechanical.
  • 学位 Ph.D.
  • 年度 2007
  • 页码 310 p.
  • 总页数 310
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 机械、仪表工业;
  • 关键词

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号