Heat Transfer and Residence Time Distribution in Plug Flow Continuous Oscillatory Baffled Crystallizers

被引:12
|
作者
Briggs, Naomi E. B. [1 ]
McGinty, John [1 ]
McCabe, Callum [1 ]
Raval, Vishal [1 ]
Sefcik, Jan [1 ]
Florence, Alastair J. [1 ]
机构
[1] Univ Strathclyde, Strathclyde Inst Pharm & Biomed Sci, EPSRC Continuous Mfg & Adv Crystallisat Future Mf, Glasgow G4 0RE, Lanark, Scotland
来源
ACS OMEGA | 2021年 / 6卷 / 28期
基金
英国工程与自然科学研究理事会;
关键词
AXIAL-DISPERSION; FLUID DISPERSION; SCALE-UP; TUBE; PERFORMANCE; DESIGN; NUMBER; BATCH;
D O I
10.1021/acsomega.1c02215
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Heat transfer coefficients in a continuous oscillatory baffled crystallizer (COBC) with a nominal internal diameter of 15 mm have been determined as a function of flow and oscillatory conditions typically used under processing conditions. Residence time distribution measurements show a near-plug flow with high Peclet numbers on the order of 100-1000 s, although there was significant oscillation damping in longer COBC setups. Very rapid heat transfer was found under typical conditions, with overall heat transfer coefficients on the order of 100 s W m(-2) K-1. Furthermore, poor mixing in the COBC cooling jacket was observed when lower jacket flow rates were implemented in an attempt to decrease the rate of heat transfer in order to achieve more gradual temperature profile along the crystallizer length. Utilizing the experimentally determined overall heat transfer coefficients, a theoretical case study is presented to investigate the effects of the heat transfer rate on temperature and supersaturation profiles and to highlight potential fouling issues during a continuous plug flow cooling crystallization.
引用
收藏
页码:18352 / 18363
页数:12
相关论文
共 50 条
  • [21] Heat transfer and residence time distribution of liquid flow in direct contact evaporation heat exchanger
    Fu, Hailing
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2020, 149
  • [22] RESIDENCE TIME MEASUREMENTS ON CONTINUOUS EVAPORATING CRYSTALLIZERS .5.
    BRUHNS, M
    SITTEL, G
    SCHULZ, T
    ZUCKERINDUSTRIE, 1992, 117 (06): : 461 - 465
  • [23] HEAT-TRANSFER AND ASSOCIATED ENERGY-DISSIPATION FOR OSCILLATORY FLOW IN BAFFLED TUBES
    MACKLEY, MR
    STONESTREET, P
    CHEMICAL ENGINEERING SCIENCE, 1995, 50 (14) : 2211 - 2224
  • [24] RESIDENCE TIME DISTRIBUTION IN AN AXIALLY-DISPERSED PLUG FLOW WITH CAPACITY
    STEPANEK, JB
    SHILIMKAN, RV
    TRANSACTIONS OF THE INSTITUTION OF CHEMICAL ENGINEERS, 1973, 51 (02): : 112 - 115
  • [25] Continuous flow residence time distribution function characterization
    Haas, CN
    Joffe, J
    Heath, MS
    Jacangelo, J
    JOURNAL OF ENVIRONMENTAL ENGINEERING-ASCE, 1997, 123 (02): : 107 - 114
  • [27] Effect of Inclination Angle of Baffled Reactor at Up-Flow on Residence Time Distribution
    Bouakaz, Nadji
    Bendjama, Zoubida
    Hamitouche, Adh'ya-eddine
    Amrane, Abdeltif
    Trari, Mohamed
    ARABIAN JOURNAL FOR SCIENCE AND ENGINEERING, 2018, 43 (11) : 5723 - 5731
  • [28] Effect of Inclination Angle of Baffled Reactor at Up-Flow on Residence Time Distribution
    Nadji Bouakaz
    Zoubida Bendjama
    Adh’ya-eddine Hamitouche
    Abdeltif Amrane
    Mohamed Trari
    Arabian Journal for Science and Engineering, 2018, 43 : 5723 - 5731
  • [29] Liquid flow field and residence time distribution in a baffleless oscillatory flow coil reactor
    Fadaee, Mohammad Mahdi
    Doyle, Brendon J.
    Roberge, Dominique M.
    Macchi, Arturo
    Haelssig, Jan B.
    Chemical Engineering Journal, 2024, 492
  • [30] Continuous flow synthesis of zeolite FAU in an oscillatory baffled reactor
    Ramirez Mendoza H.
    Valdez Lancinha Pereira M.
    Van Gerven T.
    Lutz C.
    Journal of Advanced Manufacturing and Processing, 2020, 2 (02)