期刊文献+

环保型吸附制冷工质对及其制冷性能 被引量:5

Studies on Environmentally Benign Adsorption Refrigeration Working Pairs and their Refrigeration Performance
下载PDF
导出
摘要 选取13X分子筛、凹凸棒土和氯化锶等为主要吸附材料,制备了一系列有着优良吸附性能的复合吸附剂(M4-0132、M1-9906、M1-0001和M2-0003).测定了水、乙醇在自制复合吸附剂上的吸附等温线.根据吸附等温线拟合参数对水、乙醇与自制复合吸附剂组成的吸附工质对的特征吸附功计算表明:复合吸附剂-水吸附工质对的特征吸附功约为13X分子筛-水的12%~29%;复合吸附剂-乙醇吸附工质对的特征吸附功约为活性炭-乙醇的10%~20%.采用吸附制冷体系(液体-气体-吸附剂)的稳态平衡方程,对水和乙醇与复合吸附剂组成的吸附工质对适合的制冷场合分析表明:M4-0132-水和M1-0001-水工质对可用于大循环量的制冷体系,例如空调系统的场合;M1-9906-乙醇和M2-0003-乙醇工质对可用于低温制冷体系,例如制冰和冷冻系统的场合.M1-9906-水工质对的吸附制冷量是13X-水的2.0~2.5倍;在60~120C再生条件下,M4-0132-水工质对的吸附制冷量为441~924kJ·kg-1.40~100℃再生条件下,M1-0001-乙醇工质对的吸附制冷量315~909kJ·kg-1,是活性炭-乙醇的2.2~5.9倍. Composite adsorbents (M4-0132, MI-9906, MI-0001 and M2-0003), which demonstrate favorable adsorption refrigeration performance, were prepared through combining a series of main adsorptive materials, such as 13X molecular sieve, concavo-convex stick stone and strontium chloride. Adsorption isotherms of water or ethanol on composite adsorbents were determined. According to the fitting parameters of the adsorption isotherms, the calculations show that the characteristic adsorption work of self-prepared composite adsorbents-water adsorption working pairs is about 12%-29% that of 13X molecular sieve-water pair, and that of composite adsorbents-ethanol pairs is approximately 10%-20% that of activated carbon-ethanol pair. The stable state equilibrium equation for adsorption refrigeration system (liquid-vapor-adsorbent) was set up. The favorable refrigeration systems (situations) of working pairs, consisted of water and ethanol with composite adsorbents, were discussed, and the results show that: M4-0132-water and Ml-0001-water pairs can be utilized for refrigeration system requiring larger cooling cycle volume, i.e air conditioning system, while Ml-9906-ethanol and M2-0003-ethanol pairs are more preferable to low-temperature refrigeration system, i.e ice-making and chilling system. Adsorption refrigeration volume of Ml-9906-water pairs is 2.0-2.5 times that of 13X-water. Regenerated at temperature of 60-120°C, adsorption refrigeration volume of M4-0132-water pairs is 441-924kJ&middotkg-1, while regenerated at 40-100°C, said cooling volume of Ml-0001-alcohol pairs is 315-909kJ&middotkg-1, which is 2.2-5.9 times that of activated carbon-ethanol pairs.
出处 《高校化学工程学报》 EI CAS CSCD 北大核心 2005年第2期175-180,共6页 Journal of Chemical Engineering of Chinese Universities
基金 江苏省应用基础项目(BJ97067) 已获得科技成果鉴定(苏科鉴字[2002]第960号)。
关键词 吸附制冷 复合吸附剂 特征吸附功 吸附工质对 吸附制冷量 Adsorbents Adsorption Adsorption isotherms Cooling systems Ethanol
  • 相关文献

参考文献12

  • 1方利国,汪立军,朱冬生,谭盈科.吸附式制冷中吸附剂传热传质的强化[J].高校化学工程学报,1998,12(1):17-22. 被引量:9
  • 2叶振华.吸附分离过程基础[M].北京:化学工业出版社,1988..
  • 3陆泉,苏跃红,刘震炎,葛新石,王永堂.几种吸附式致冷新工质对的性能预测[J].太阳能学报,1996,17(2):184-188. 被引量:6
  • 4Aistov Yu I, Restuccia G, Cacciola G, Parmon V N. A family of new working materials for solid sorption air conditioning systems [J]. Applied Thermal Engineering, 2002, 22(2): 191-204.
  • 5Vasiliev L L, Mishkinis D A, Antukh, AA. Solar-gas solid sorption refrigerator [J]. Adsorption, 2001, 7(2): 149-161.
  • 6LI Ming, WANG Ru-zhu, XU Yi-xiong, et al. Experimental study on dynamic performance analysis of a flat-plate solar-adsorption refrigeration for ice maker [J]. Renewable Energy, 2002, 27(2): 211-221.
  • 7Cacciola G, Restuccia G, Giordano N. Economic comparison between adsorption and compression heat pumps [J]. Heat Recovery Systems & CHP, 1990, 10(6): 499-507.
  • 8Anyanwu E E. Review of solid adsorption solar refrigerator I: an overview of the refrigeration cycle [J]. Energy Conversion and Management, 2003, 44(2): 301-312.
  • 9朱冬生,林琳,侯轶,程锐敏.吸附器中导热胶热传导系数的研究[J].高校化学工程学报,2001,15(5):476-480. 被引量:7
  • 10崔群,陈海军,姚虎卿.吸附制冷用复合吸附剂的制备[J].南京工业大学学报(自然科学版),2002,24(6):6-10. 被引量:8

二级参考文献20

  • 1方利国,冯毅,谭盈科.国内外环保型制冷方法的性能分析及新动态[J].环境保护科学,1996,22(3):1-3. 被引量:2
  • 2[1]Tchernev D I, EmersonDT. High-Efficiency Regenerative Zeolite Heat Pump. ASHRAE Trans, 1988, 94: 2024~2032
  • 3[2]Meunier F E, Sun Lian-ming. Predictive Model and Experimental Results for a Two-Adsorber Solid Adsorption Heat Pump. Ind Eng Chem Res., 1988, 27: 310~316
  • 4[3]Cacciola G, Restuccia G, Giordano N. Economic Comparison Between Adsorption and Compression Heat Pumps. Heat Recovery Systems & CHP, 1990, 10(6): 499~507
  • 5[4]Tamainoit-Telto Z, Critoph R E. Adsorption Refrigerator Using Monolithic Carbon-Ammonia Pair. Int J Refrig, 1997, 20(2): 146~155
  • 6[5]Cui Qun, Chen Haijun, Yao Huqing. Properties of Advanced Adsorbent for Solid Desiccant Cooling. Journal of Southeast University (English Edition), 2001,17(2):91~94
  • 7严爱珍,制冷学报,1983年,1期,35页
  • 8鹿政理,吸附的基础与设计,1983年
  • 9严爱珍,制冷学报,1982年,4期,28页
  • 10汪大--,化工学报,1989年,6期,655页

共引文献31

同被引文献48

引证文献5

二级引证文献14

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