期刊文献+

车用天然气储罐脱附放气过程热力特性

Thermodynamic Properties Analysis of Natural Gas Vehicle Tank in Desorption
下载PDF
导出
摘要 车用吸附天然气储罐在脱附放气过程中产生的热效应,严重影响了储罐的脱附效率和汽车行驶速度.建立了天然气、活性炭吸附剂和天然气储罐的热质交换模型,模拟计算了脱附过程中储罐内温度、压力和脱附量的变化,分析了温度、压力等热力参数对脱附速度和脱附量的影响.计算结果表明:储罐的自然脱附过程是吸热过程,在脱附过程中,储罐内的平均温度由293.15K降到了250.46K;储罐中心处温降最大,由293.15K降至244K,降幅达到了49.15K;自然对流下的脱附效率比等温脱附降低了24.49%;在自然对流条件下,壁面所提供的热量越少,脱附速度越小,脱附效率也就越低. Thermal effect produced in desorption of natural gas vehicle tank seriously affects desorption efficiency and vehicle velocity.The variation of storage tank temperature,pressure and desorption amount are simulated and the influence of storage tank temperature and pressure on the desorption rate and the desorption amount are analyzed based on the newly-erected heat and mass transfer model of natural gas,activated carbon adsorbents and gas tank.The results show that desorption process is an endothermic process;the average temperature of adsorbent in the storage tank reduces from 293.15 K to 250.46 K and the maximum temperature at the center of the storage tank reduces from 293.15 K to 244 K with a margin of 49.15 K.At the same time,the desorption rate in natural convection is lower than that of the isotherm desorption by 24.49%.Under natural convection,the desorption rate and efficiency varies with the heat of the wall.
出处 《同济大学学报(自然科学版)》 EI CAS CSCD 北大核心 2012年第3期446-451,共6页 Journal of Tongji University:Natural Science
基金 吉林省教育厅资助项目(2006102)
关键词 车用吸附罐 热质交换模型 脱附热效应 脱附速度 adsorbed natural gas vehicle tanks heat and mass transfer model desorption thermal desorption rate
  • 相关文献

参考文献11

  • 1欧成华,李朝纯,杜建芬,陈娟,赵永富.吸附天然气汽车技术研究与对策[J].天然气工业,2002,22(2):90-92. 被引量:3
  • 2钱焕群,陈宝明,张建,宋辉.天然气吸附床脱附过程的传热实验研究[J].山东建筑大学学报,2008,23(5):394-397. 被引量:1
  • 3Najibi H,Chapoy A,Tohidi B. Methane/natural gas storage and delivered capacity for activated carbons in dry and wet conditions[J].Fuel,2008,(01):7.doi:10.1016/j.fuel.2007.03.044.
  • 4刘保华,赵乃勤,李家俊,姜召阳.用活性炭纤维吸附天然气的研究[J].中山大学学报(自然科学版),2003,42(A19):126-129. 被引量:5
  • 5Zhang T,Walawender W P,Fan L T. Grain-hased activated carbons for natural gas storage[J].Bioresource Technology,2010,(06):1983.doi:10.1016/j.biortech.2009.10.046.
  • 6王皆腾,孙俊芳,刘中良.天然气吸附储存容器的结构优化分析[J].工程热物理学报,2009,30(10):1729-1731. 被引量:3
  • 7孙俊芳,刘中良,蒋文明,庞会中.天然气吸附储存过程的数值模拟研究[J].热科学与技术,2009,8(3):231-235. 被引量:1
  • 8Gadalla M A. Simulation of intermittent thermal compression processes using adsorption technology[J].Journal of the Franklin Institute,2007,(05):725.doi:10.1016/j.jfranklin.2005.12.007.
  • 9Wojcik A M W,Jansen J C,Maschmeyer Th. Thermodynamically consistent thermal energy equation for an adsorbent/fluid system[J].International Journal of Heat and Mass Transfer,2001,(12):2379.doi:10.1016/S0017-9310(00)00255-6.
  • 10Tseng R,Wu F. Analyzing concurrent multi-stage adsorption process of activated carbon with a favorable parameter of Langmuir equation[J].Journal of the Taiwan Institute of Chemical Engineers,2009,(02):197.

二级参考文献22

共引文献8

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部