Control of Crystal Size Distribution Using a mL-Scale Continuous Crystallizer Equipped with a High Speed Agitator
Author:
Affiliation:
1. Department of Applied Chemistry and Bioengineering, Graduate School of Engineering, Osaka City University
Publisher
Society of Chemical Engineers, Japan
Subject
General Chemical Engineering,General Chemistry
Link
http://www.jstage.jst.go.jp/article/jcej/45/1/45_11we158/_pdf
Reference6 articles.
1. Seeding Effect on Batch Crystallization of Potassium Sulfate under Natural Cooling Mode and a Simple Design Method of Crystallizer.
2. FINES DESTRUCTION DURING BATCH CRYSTALLIZATION
3. The influence of additives on the growth kinetics and mechanism of l-alanine crystals
4. Mullin, J. W. and J. Nyvlt; “Programmed Cooling of Batch Crystallizer,” Chem. Eng. Sci., 26, 369–377 (1997)
5. Ooshima, H., K. Igarashi, Y. Sasaki, M. Azuma and H. Noda; “Production of Large Crystals of Glycine with a Narrow Size Distribution Using WWDJ-Batch Crystallizer,” Chem. Eng. Trans., 1, 981–986 (2002)
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1. Pharmaceutical Microcrystal Formation by Supersaturation Control with an Electrolyte;JOURNAL OF CHEMICAL ENGINEERING OF JAPAN;2018-07-20
2. Continuous Pharmaceutical Crystallization from Solution;Engineering Crystallography: From Molecule to Crystal to Functional Form;2017
3. Cooling Crystallization Using a mL-Scale Continuous Crystallizer Equipped with a High Speed Agitator for Production of Uniform Small Crystals;Journal of Chemical Engineering of Japan;2016
4. MoOx-promoted Pt catalysts for the water gas shift reaction at low temperatures;Chinese Journal of Catalysis;2015-05
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