Process Intensification of Continuous Antisolvent Crystallization Using a Coiled Flow Inverter

被引:24
|
作者
Benitez-Chapa, Andrea G. [1 ]
Nigam, Krishna D. P. [1 ,2 ]
Alvarez, Alejandro J. [1 ]
机构
[1] Tecnol Monterrey, Sch Engn & Sci, Av Eugenio Garza Sada 2501, Monterrey 64849, NL, Mexico
[2] Indian Inst Technol Delhi, Dept Chem Engn, Hauz Khas, New Delhi 110016, India
关键词
RESIDENCE TIME DISTRIBUTION; DESIGN; DISPERSION; OPTIMIZATION; OPERATION; REMOVAL; GROWTH; BATCH; TUBE;
D O I
10.1021/acs.iecr.9b04160
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The present work experimentally studies the antisolvent continuous crystallization of flufenamic acid using the coiled flow inverter (CFI) as a novel crystallization device. A multistage antisolvent addition strategy was evaluated. The experimental results show that the mean crystal size increased with the number of antisolvent addition points in the CFI. The continuous CFI crystallizer produced crystals of a smaller size with narrower size distributions as compared to the Kenics crystallizer and tube crystallizer without mixing elements at the same process conditions. The effect of the number of flow inversions on the size distribution of the flufenamic acid crystals was studied. The mean crystal size and the coefficient of variation decreased as the number of equally spaced 90 degrees bends increased. Using the population balance equation, it was found that an ideal plug flow model can accurately describe the CFI continuous crystallization process. Overall, this work shows that the CFI crystallizer successfully intensifies the continuous antisolvent crystallization process.
引用
收藏
页码:3934 / 3942
页数:9
相关论文
共 50 条
  • [21] Process Intensification for the Continuous Flow Hydrogenation of Ethyl Nicotinate
    Ouchi, Takashi
    Battilocchio, Claudio
    Hawkins, Joel M.
    Ley, Steven V.
    ORGANIC PROCESS RESEARCH & DEVELOPMENT, 2014, 18 (11) : 1560 - 1566
  • [22] Rapid Continuous Antisolvent Crystallization of Multicomponent Systems
    Raza, Syed A.
    Schacht, Ulrich
    Svoboda, Vaclav
    Edwards, Darren P.
    Florence, Alastair J.
    Pulham, Colin R.
    Sefcik, Jan
    Oswald, Iain D. H.
    CRYSTAL GROWTH & DESIGN, 2018, 18 (01) : 210 - 218
  • [23] Green engineering approach with microstructured coiled flow inverter for CMF and HMF continuous flow synthesis
    Schael, Frank
    Nigam, Krishna
    Rojahn, Patrick
    JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 2022, 99 : 100 - 100
  • [24] Shining Light on the Coiled-Flow Inverter-Continuous-Flow Photochemistry in a Static Mixer
    Tiwari, Chinmay P.
    Delgado-Licona, Fernando
    Valencia-Llompart, Maria
    Nunez-Correa, Sara
    Nigam, Krishna D. P.
    Montesinos-Castellanos, Alejandro
    Lopez-Guajardo, Enrique A.
    Aguirre-Soto, Alan
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2020, 59 (09) : 3865 - 3872
  • [25] Continuous Antisolvent Crystallization of L-Histidine: Impact of Process Parameters and Kinetic Estimation
    Liu, Peng
    Yang, Li
    Ma, Yixin
    Zhang, Yan
    Wang, Haoliang
    Cheng, Jingcai
    Yang, Chao
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2024, 63 (06) : 2831 - 2841
  • [26] Coiled flow inverter as a heat exchanger
    Kumar, Vimal
    Mridha, Monisha
    Gupta, A. K.
    Nigam, K. D. P.
    CHEMICAL ENGINEERING SCIENCE, 2007, 62 (09) : 2386 - 2396
  • [27] Coiled flow inverter as an inline mixer
    Mrldha, Monisha
    Nigam, K. D. P.
    CHEMICAL ENGINEERING SCIENCE, 2008, 63 (06) : 1724 - 1732
  • [28] Continuous aqueous two-phase extraction of microalgal C-phycocyanin using a coiled flow inverter
    Ruiz-Ruiz, Federico
    Lopez-Guajardo, Enrique
    Vazquez-Villegas, Patricia
    del Angel-Chong, Martha E.
    Nigam, K. D. P.
    Willson, Richard C.
    Rito-Palomares, Marco
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2019, 142
  • [29] SUGAR CRYSTALLIZATION AS A CONTINUOUS-FLOW PROCESS
    BROADFOOT, R
    WHITE, ET
    INTERNATIONAL SUGAR JOURNAL, 1978, 80 (953): : 135 - 139
  • [30] Process intensification of solution crystallization
    Feng Y.
    Chen K.
    Zhao J.
    Wang N.
    Wang T.
    Huang X.
    Zhou L.
    Hao H.
    Huagong Jinzhan/Chemical Industry and Engineering Progress, 2024, 43 (01): : 87 - 99