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[1]NHDÍÑ̼ϵͳ½ÚÄܸĽø, »¯·ÊÉè¼Æ£¬ 30(6), 51-52£¬2004
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[5]the operation of draining column holdup for slop cut withdrawal in batch distillation, chinese journal of chemical engineering£¬ 14(3), 337-342£¬2006
[6]»¬Æ¬Ê½ÌÝÐε¼Ïò¸¡·§µÄÁ÷ÌåÁ¦Ñ§ÐÔÄÜÑо¿,»¯Ñ§¹¤³Ì£¬ 36(10), 25-28£¬2008
[7]ÐÂÐÍËþÄÚ¼þÔÚTDIµÚÒ»ÍÑODCBËþÀ©²ú¸ÄÔìÖеÄÓ¦ÓÃ, ¾Û°±õ¥¹¤Òµ£¬ 24(2), 35-38£¬2009
[8]Development on the Technique of Total Recovery of Benzoic Acid Residue, chinese journal of chemical engineering£¬ 17(14), 608-612£¬2009
[9]Experimental study and process simulation of n-butyl acetate produced by transesterification in a catalytic distillation column, chemical engineering and processing£¬ 49(1), 132-137£¬2010
[10]Hydrodynamic characters of co-current operation for SO2 absorption in a laboratory packed column, Korean J. Chem. Eng£¬28(11), 2190-2195£¬2011
[11]ÌîÁÏËþÆøÒº²¢Á÷½Ó´¥Ê±Ñ¹½µµÄÑо¿, »¯Ñ§¹¤ÒµÓ빤³Ì£¬29(4), 45-49£¬2012
[12]Æø̬ĤÎüÊÕ·ÖÀë¶þ¼×°·Ë®ÈÜÒºµÄÑо¿, »·¾³¿Æѧѧ±¨£¬32(10), 2360-2365£¬2012
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[14] Isobaric vapor¨Cliquid equilibrium for ternary system of sec-butyl alcohol + sec-butyl acetate + N,N-dimethyl acetamide at 101.3 kPa, Fluid Phase Equilibria, Volume 394, 25 May 2015, Pages 83-87
[15]µÍÎíĵ¼ÏòÌÝÐι̶¨·§Ëþ°åÁ÷ÌåÁ¦Ñ§ÐÔÄÜ[J]. »¯Ñ§¹¤³Ì,2015,07:39-43.
[16] ÝÍÈ¡¾«Áó·ÖÀë»·¼ºÍé-»·¼ºÏ©ÈܼÁµÄɸѡ[J]. »¯Ñ§¹¤³Ì,2015,08:23-26.
[17]Experimental isobaric vapor liquid equilibrium for the ternary system of sec-butyl alcohol + sec-butyl acetate + dimethyl sulfoxide at 101.3 kPa, Fluid Phase Equilibria, Volume 406, 25 November 2015, Pages 55-60
[18]Supported-gas-membrane process for removal and recovery of aliphatic amines from aqueous streams, Chemical Engineering Science, Volume 141, 17 February 2016, Pages 330-341.
[19] Concentrating aqueous urea solution by using continuous-effect membrane distillation, Chemical Engineering Research and Design, Volume 104, December 2015, Pages 589-604,
[20] Supported-gas-membrane process for removal and recovery of aliphatic amines from aqueous streams, Chemical Engineering Science, Volume 141, 17 February 2016, Pages 330-341.
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