Wang J, Smith R. Dephlegmator design in low temperature gas separation[J].Chemical Engineering Research and Design, 2005, 83(9): 1133-1144.
[4]
Howard L J, Rowles H C, Nickel R J, et al. Dephlegmator system and process: US,6349566[P].2002-02-26.
[5]
Fischer B, Viltard J C. Fractionation of preferential gases; cool gases, separate first gas phase from first liquid phase, send gas phase to expansion stage, send first phase to heat exchangers, heat, cool, separate gas and liquid phases by distillation: US, 6318119[P].2001-11-20.
Tuchlenski A, Beckmann A, Reusch D, et al. Reactive distillation——Industrial applications, process design & scale-up[J]. Chemical Engineering Science, 2001, 56(2): 387-394.
[13]
Nappa M J, Rao V N M, Sievert A C, et al. Process and methods of purification for the manufacture fluorocarbons: US, 7 981 311[P].2011-07-19.
Engelien H K, Larsson T, Skogested S. Implementation of optimal operation for heat-integrated distillation columns[J]. Chemical Engineering Research and Design, 2003, 81(2): 277-281.
O'brien J V. Dephlegmator process with liquid additive: US, 6336344[P].2002-01-08.
[23]
潘晓磊, 朱绍芬. ARS 技术在乙烯装置上的应用现状及探讨[J].石油化工技术经济, 1996, 12(4): 56-58.
[24]
Lokshin E P. Production of high-purity potassium by vacuum distillation with dephlegmation[J].Russian Journal of Applied Chemistry, 2001, 74(7): 1069-1075.
Dennis P.Bernhard. Process for recovering C4+ hydrocarbons using a dephlegmator:US,451925[P].1985-05-28.
[40]
沈波. 氨水吸收式制冷系统氨水分离特性的研究[D].大连:大连海事大学, 2013.
[41]
Siddiqui M U, Said S A M. A review of solar powered absorption systems[J].Renewable and Sustainable Energy Reviews, 2015,42: 93-115.
[42]
Said S A M, El-Shaarawi M A I, Siddiqui M U. Alternative designs for a 24h operating solar-powered absorption refrigeration technology [J].International Journal of Refrigeration, 2012, 35(7): 1967-1977.
[43]
Sieres J, Fernández-Seara J. Evaluation of the column components size on the vapour enrichment and system performance in small power NH3-H2O absorption refrigeration machines[J]. International Journal of Refrigeration, 2006, 29(4): 579-588.
[44]
Sieres J, Fernandez Seara J, Uhia F J. Experimental characterization of the fractionating process in ammonia water absorption systems with a large-specific area corrugated sheet structured packing[J].International Journal of Refrigeration, 2009,32:1230-1240.
[45]
Sieres J, Fernandez-Seara J. Mass transfer characteristics of a structured packing for ammonia rectification in ammonia-water absorption refrigeration systems[J]. International Journal of Refrigeration, 2007,30:58-67.
[46]
Darwish N A, Al-Hashimi S H,Al-Mansoori A S. Performance analysis and evaluation of a commercial absorption refrigeration water-ammonia (ARWA) system[J].International Journal of Refrigeration, 2008, 31:1214-1223.
吴剑峰, 公茂琼, 董学强,等. 带二级分凝分离回热混合工质节流制冷的低温冷冻贮存箱:中国,102494467 B [P]. 2012-06-13.
[49]
Zhang Y, Gong M, Wu J. Vapor-liquid equilibrium measurement and correlation for R23+R116 system[J]. Journal of Chemical Industry and Engineering(China), 2008, 59(2): 269.
Leland M Vane. Separation of vapor-phase alcohol/water mixtures via fractional condensation using a pilot-scale dephlegmator: Enhancement of the pervaporation process separation factor [J].Ind. Eng. Chem. Res, 2004, 43(1): 173-183.