期刊文献+

空气预纯化吸附过程模拟 被引量:1

Simulation of Adsorption Process of Air-Prepurification
下载PDF
导出
摘要 采用一种改进型的多组分等温线模型,运用Aspen Adsorption软件模拟空分过程中吸附塔内13X分子筛吸附空气中微量水蒸气和二氧化碳的过程。考察了操作压力、温度变化对穿透时间的影响以及水蒸气、二氧化碳在床层中的负载分布。研究结果表明:当压力从120 kPa增大到350 kPa,H2O和CO2的穿透时间分别增加32%和116%;在10~30℃,随着温度的升高,穿透时间点逐渐前移,但变化幅度较小;在CO2和H2O的竞争吸附中,CO2吸附能力明显弱于H2O,其饱和吸附量仅为H2O饱和吸附量的0.34%。 The modified adsorption isotherm model and Aspen Adsorption software were used to simulate for air-prepurification in zeolite 13X bed where CO2 and H2O were adsorbed and the effects of operation pressure and temperature on breakthrough time were studied.Moreover,the variations of the concentrations of CO2 and H2O with adsorption time and the distributions of CO2、H2O adsorption quantity in the Z direction were obtained.The results showed that the breakthrough time of CO2 and H2O increase 32% and 116% respectively with the pressure increase from 120 kPa to 350 kPa but the effect of temperature on the breakthrough curve is very small within the range of 10~30 ℃.In the competitive adsorption of CO2 and H2O,the saturated adsorption quantity of CO2 is significantly less than that of H2O and only makes up 0.34 percent of H2O′s saturated adsorption quantity.
作者 程烦 王煤
出处 《低温与特气》 CAS 2013年第3期19-24,共6页 Low Temperature and Specialty Gases
关键词 吸附 ASPEN ADSORPTION 吸附等温线模型 水蒸气 二氧化碳 adsorption Aspen Adsorption adsorption isotherm model water vapor CO2
  • 相关文献

参考文献7

  • 1KIM JH, LEE CH , KIM WS, LEE JS , K1M JT , SUH JK, LEE JM. Adsorption equilibria of water vapor on alumina, zeolite 13X, and a zeolite 13X/activated carbon composite [ J ]. J Chem Eng Data, 2003,48 ( 1 ) : 137-141.
  • 2AHN H, LEE CH. Effects of capillary condensation on ad- sorption and thermal desorption dynamics of water in zeolite 13X and layered beds[J]. Chem Eng Sci,2004,59(13) : 2727-2743.
  • 3张培昆,王立,刘桂芹,李正强,杨秉彪,郭桂彬.空分装置三吸附器TSA纯化系统及其节能效果分析[J].过程工程学报,2009,9(5):932-939. 被引量:10
  • 4ZHANG Peikun, WANG Li . Extended Langmuir equation for correlating multilayer adsorption equilibrium data [J]. Sep Purif Technol ,2010,70(3) : 367-371.
  • 5LEE JS,KIM JH, KIM JT,SUH JK,LEE JM, LEE CH. Ad- sorption equilibria of CO: on zeolite 13X and zeolite 13X/ activated carbon composite [ J ]. J Chem Eng Data, 2002,47 (5) : 1237-1242.
  • 6REGE SU, YANG RT, BUZANOWSKI MA. Sorbents for air prepurification in air separation[ J]. Chem Eng Sci ,2000,55 (21) :4827- 4838.
  • 7近藤精一.吸附科学[M].石川达雄,安部郁夫,李国希译.北京:化学工业出版社,2006.227~264

二级参考文献15

  • 1Tatsushi U, Tooru N, Morimitsu N. Development of Air-purification TSA Simulator for Cryogenic Air Separation Unit [J]. Nippon Sanso Engineering Report, 2003, (22): 13-18.
  • 2Ahn H W, Lee C H. Adsorption Dynamics of Water in Layered Bed for Air-drying TSA Process [J]. AIChE J., 2003, 49(6): 1601-1609.
  • 3Kim J H, Lee C H, Kim W S. Adsorption Equilibria of Water Vapor on Alumina, Zeolite 13X, and a Zeolite X/Activated Carbon Composite [J]. J. Chem. Eng. Data, 2003, 48(1): 137-141.
  • 4Ahn H W, Lee C H. Effects of Capillary Condensation on Adsorption and Thermal Desorption Dynamics of Water in Zeolite 13X and Layered Beds [J]. Chem. Eng. Sci., 2004, 59(13): 2727-2743.
  • 5Yang R T. Gas Separation by Adsorption Process [M]. Boston: Butterworth's, 1987. 51,178.
  • 6Ruthven D M. Principle of Adsorption and Adsorption Process [M]. New York: Wiley, 1984. 320.
  • 7Harwell J H, Liapis A I, Litchfield R. A Non-equilibrium Model for Fixed-bed Multi-component Adiabatic Adsorption [J]. Chem. Eng. Sci., 1980, 35(11): 2287-2296.
  • 8Carter J W, Husain H. The Simultaneous Adsorption of Carbon Dioxide and Water Vapor by Fixed Beds of Molecular Sieves [J]. Chem. Eng. Sci., 1974, 29(1): 267-273.
  • 9Pan C Y, Basmadjian D. An Analysis of Adiabatic Sorption of Single Solutes in Fixed Beds: Equilibrium Theory [J]. Chem. Eng. Sci., 1971, 26(1): 45-57.
  • 10Ko D, Kim M, Moon I. Analysis of Purge Gas Temperature in Cyclic TSAProcess [J]. Chem. Eng. Sci., 2002, 57(1): 179-195.

共引文献96

同被引文献3

引证文献1

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