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結(jié)晶分離方法碩士學(xué)位論文(更新版)

  

【正文】 Solution with a Nonsolvent[J].AIChE Journal,2013,46(4):857~865.[7] Gallagher P M, Coffey M P, Krukonis V J,et al. Supercritical Fluid Science and Technology[C]. ACS Symp. Series 406, Washngton D C: ACS, 2013. 334~336 .[8] Werling J O, Debenedetti P G. Numerical Modeling of Mass Transfer in the Supercritical Antisolvent Process: Miscible CondI tions[J]. J. Supercritical Fluids, 2012, 18 (1): 11~24.[9] Serge R Bitemo,洪鐳,劉昆,[J].華東理工大學(xué)學(xué)報(bào)(自然科學(xué)版),2011, 27(4): 338~340.[10] Shekunov B Yu, Baldyga J, York P. Particle fromby Mixingwith Supercritical Antisolvent at High Reynolds Numbers[J]. Chemical Engineering Science, 2013,56:2421~2433.[11] Chattopadhyay P, Gupta R B. Supercritical CO2Based Production of Fullerene Nanoparticles[J]. Ind. Eng. Chem. Res., 2010, 39 (7): 2281~2289.[12] Reverchon E, Porta G Della, Falivene M G. Process Parameters and Morphology in Amoxicillin Micro and Submicro Particles Generation by Supercritical Antisolvetn Precipitation[J]. J. Supercritical Fluids, 2010, 17 (3): 239~248.[13] Sarkari M, Darrat I, Knutson B L. Generation of Microparticles Using CO2and CO2Philic Antisolvents [J]. AIChE Journal,2000, 46 (9): 1850~1859.[14] Thiering R, Dehghani F, Dillow A, et al. Solvent Effects on the Controlled Dense Gas Precipitation of Model Proteins[J]. J. ChemTechnol Biotechnol, 2000,75: 42~53.[15]潘見(jiàn),[P].CN:1220906, 1999630.[16]合肥工大首創(chuàng)萃取結(jié)晶組合分離工藝[N].科技日?qǐng)?bào),20130104(1).[17] Ukai K et al1Wang J K ed1Proceedings of International Symposium on Industrial Crystallization,Beijing:Academic Press,1998:65[18] Tung HH et al1Wang J K ed1Proceedings of International Symposium on Industrial Crystallization,Beijing:Academic Press,2009:138[19] Li Lin1JSouth China University of Technology,2009
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