[1] Shi J. Handbook of Chemical Engineering[M]. 1996:10-2.
[2] Ding X, Tan Q. Industrial Crystallization[M]. Chemical Industry Press,1985:26.
[3] Giulietti M, Seckler M M, Derenzo S, et al. Industrial Crystallization and Precipitation from Solutions: State of the Technique[J]. Brazilian Journal of Chemical Engineering, 2001, 18 (4):423-440.
[4] Darmali C, Mansouri S, Yazdanpanah N, et al. Mechanisms and Control of Impurities in Continuous Crystallization: A Review[J]. Industrial & Engineering Chemistry Research, 2018, 58 (4):1463-1479.
[5] J. W. Mullin. Crystallization [M]. London:Elsevier,2001:3.
[6] Allan S. Myerson, Deniz Erdemir, Lee A Y. Handbook of Industrial Crystallization[M]. 2002.
[7] Zhang D, Wang X, Ulrich J, et al. Control of Crystal Properties in a Mixed-Suspension Mixed-Product Removal Crystallizer: General Methods and the Effects of Secondary Nucleation[J]. Crystal Growth & Design, 2019, 19 (5):3070-3084.
[8] Wang Q, Xi L, Wang L, et al. Kinetics of P-Xylene Liquid-Phase Catalytic Oxidation to Terephthalic Acid[J]. Industrial & Engineering Chemistry Research, 2004, 44 (2):261-266.
[9] Wang Q-b, Xu H-b, Li X. Solubility of Terephthalic Acid in Aqueous Acetic Acid from 423.15 to 513.15k[J]. Fluid Phase Equilibria, 2005, 233 (1):81-85.
[10] Wang Q, Cheng Y, Wang L, et al. Isothermal Seeded Semicontinuous Reactive Crystallization of Crude Terephthalic Acid Crystals[J]. Industrial & Engineering Chemistry Research, 2008, 47 (16):5861-5870.
[11] Brown P M, Myerson A S. The Growth, Dissolution and Aging of Terephthalic Acid Crystals[J]. AIChE Journal, 1989, 35 (10):1749-1752.
[12] Wang Q, Cheng Y, Xu H, et al. Aging of Crude Terephthalic Acid Crystals at High Temperatures[J]. Industrial & Engineering Chemistry Research, 2007, 46 (22):7367-7377.
[13] Fisher J A. Terephthalic Acid Recovery by Continuous Flash Crystallization: US, US 3931305 A[P], 1976.
[14] Olsen G P, Towle P H, Baldwin R H. Terephthalic Acid Recovery: US, US 3452088[P], 1969.
[15] Lin R, O'Meadhra R S, Kingsport R B. Process for the Production of Purified Terephthalic Acid: US, US 20020198405A1[P], 2002.
[16] Beckham G T, Peters B, Starbuck C, et al. Surface-Mediated Nucleation in the Solid-State Polymorph Transformation of Terephthalic Acid[J]. J Am Chem Soc, 2007, 129 (15):4714-4723.
[17] Davey R J, Maginn S J, Andrews S J, et al. Morphology and Polymorphism in Molecular Crystals: Terephthalic Acid[J]. Journal of the Chemical Society Faraday Transactions, 1994, 90 (7):1003-1009.
[18] Karothu D P, Weston J, Desta I T, et al. Shape-Memory and Self-Healing Effects in Mechanosalient Molecular Crystals[J]. J Am Chem Soc, 2016, 138 (40):13298-13306.
[19] Deming Y, ITO Y, Yamazaki K. Method for Manufacturing Purified Terephthalic Acid: Japen, CN 104817454B[P], 2015.
[20] YOSHIAKI I, TUKASA K, AKIHIKO T. Process for Producing Terephthalic Acid: US, US 5567842A[P], 1996.
[21] DEMING Y, TOSHITSUGU I, HATSUTARO Y. Method for Manufacturing Refined Terephthalic Acid: China, CN 104817454A[P], 2009.
[22] Wang H, Zhang D, Fan Y, et al. Research Progress in Refining Process for Production of Caprolactam by Beckman Rearrangement Reaction[J]. China Petroleum Processing & Petrochemical Technology, 2019, 21 (2):10-18.
[23] Chianese A, Santilli N. Modelling of the Solid Layer Growth from Melt Crystallization—the Integral Formulation Approach[J]. 1998, 53 (1):107-111.
[24] Poschmann M, Ulrich J. Fractional Suspension Crystallization with Additional Purification Steps[J]. Journal of Crystal Growth, 1996, 167 (1-2):248-252.
[25] Jansens P J, Langen Y, Berg E, et al. Morphology of -Caprolactam Crystals Dependent on the Crystallization Conditions[J]. Journal of Crystal Growth, 1995, 155 (1-2):126-134.
[26] Diepen P J, Bruinsma O, Rosmalen G. Melt Crystallization by Controlled Evaporative Cooling. The Caprolactam–Water System in Batch Operation[J]. Chemical Engineering Science, 2000, 55 (18):3575-3584.
[27] Guo S, Su W, Hao H, et al. Solution Thermodynamics of Caprolactam in Different Monosolvents[J]. Journal of Chemical & Engineering Data, 2020, 66 (1):494-503.
[28] NAOKI T, TATSUYA O. Method for Producing Epsilon-Caprolactam: China, CN 104011017 B[P], 2016.
[29] Chen S, Xie L, Zhang S, et al. Method for Crystallizing Ε-Caprolactam Crude Product and Method for Preparing Caprolactam: China, CN 103420912 B[P], 2016.
[30] Mohameed H A, Jdayil B A, Takrouri K. Separation of Para-Xylene from Xylene Mixture Via Crystallization[J]. Chemical Engineering and Processing: Process Intensification, 2007, 46 (1):25-36.
[31] Swift J D. Crystallization Process for Para-Xylene Recovery Using Two-Stage Recovery Section: US, US 5329061[P], 1994.
[32] Patience D B, Rawlings J B, Mohameed H A. Crystallization of Para-Xylene in Scraped-Surface Crystallizers[J]. AIChE Journal, 2001, 47 (11):2441-2451.
[33] Lima R M, Grossmann I E. Optimal Synthesis Ofp-Xylene Separation Processes Based on Crystallization Technology[J]. AIChE Journal, 2009, 55 (2):354-373.
[34] Xiao J, Kong D, Yang W, et al. Combined Method for Production of P-Xylene: China, CN 101735003 A[P], 2010.
[35] Suren S, Sunsandee N, Stolcova M, et al. Measurement on the Solubility of Adipic Acid in Various Solvents at High Temperature and Its Thermodynamics Parameters[J]. Fluid Phase Equilibria, 2013, 360:332-337.
[36] David R, Villermaux J, Marchal P, et al. Crystallization and Precipitation Engineering—Iv. Kinetic Model of Adipic Acid Crystallization[J]. Chemical Engineering Science, 1991, 46 (4):1129-1136.
[37] Costa C, Costa A, Filho R M. Mathematical Modeling and Optimal Control Strategy Development for an Adipic Acid Crystallization Process[J]. Chemical Engineering & Processing Process Intensification, 2005, 44 (7):737-753.
[38] Narducci O, Jones A G, Kougoulos E. An Assessment of the Use of Ultrasound in the Particle Engineering of Micrometer-Scale Adipic Acid Crystals[J]. Crystal Growth & Design, 2011, 11 (5):1742-1749.
[39] Narducci O, Jones A G, Kougoulos E. Continuous Crystallization of Adipic Acid with Ultrasound[J]. Chemical Engineering Science, 2011, 66 (6):1069-1076.
[40] Wohlgemuth K, Ruether F, Schembecker G. Sonocrystallization and Crystallization with Gassing of Adipic Acid[J]. Chemical Engineering Science, 2010, 65 (2):1016-1027.
[41] Kuhn J, Lakerveld R, Kramer H, et al. Characterization and Dynamic Optimization of Membrane-Assisted Crystallization of Adipic Acid[J]. Industrial & Engineering Chemistry Research, 2009, 48 (11):5360-5369.
[42] HENRIET E, B., LECONTE P, PATOIS C, et al. Method for Purifying Adipic Acid by Crystallization: Franch, WO 1997046510 A1[P], 1997.
[43] STEPANSKI M, JANS B J. Process for Fractional Crystallization of Substances, a Crystallizer Suitable for Working the Process, and Use of the Process: US, US 6145340A[P], 2000.
[44] Jancic S, Sakellariou E. Process and Apparatus for Separating Substances by Crystallization: US, US 5230769 A[P], 1993.
[45] Hengstermann A, Cameretti L. Solvent Screening and Measurement of Phase Diagrams for the Yield Maximization of an Acrylic Acid Crystallization[J]. Journal of Chemical & Engineering Data, 2010, 55 (11):4597-4606.
[46] Le Page Mostefa M, Muhr H, Plasari E, et al. Determination of the Solid–Liquid Phase Diagram of the Binary System Acrylic Acid + Propionic Acid[J]. Journal of Chemical & Engineering Data, 2012, 57 (4):1209-1212.
[47] Beilles S, Franke R, Nordhoff S. Influence of Water as an Impurity on Acrylic Acid Melt Crystallization[J]. Chem. Eng. Trans., 2002, 1:725-730.
[48] Hengstermann A, Kadam S, Jansens P J. Influence of Supercooling and Water Content on Crystal Morphology of Acrylic Acid[J]. Crystal Growth & Design, 2009, 9 (4):2000-2007.
[49] Le Page Mostefa M, Muhr H, Plasari E, et al. A Purification Route of Bio-Acrylic Acid by Melt Crystallization Respectful of Environmental Constraints[J]. Powder Technology, 2014, 255:98-102.
[50] Cheng Y S, Lam K W, Ng K M, et al. Workflow for Managing Impurities in an Integrated Crystallization Process[J]. AIChE Journal, 2009, 56 (3):633-649.
[51] Urwin S J, Levilain G, Marziano I, et al. A Structured Approach to Cope with Impurities During Industrial Crystallization Development[J]. Org Process Res Dev, 2020, 24 (8):1443-1456.
[52] Hertrampf A, Muller H, Menezes J C, et al. A Pat-Based Qualification of Pharmaceutical Excipients Produced by Batch or Continuous Processing[J]. J Pharm Biomed Anal, 2015, 114:208-215. |