Effect of fibres on fluidized bed expansion parameters

被引:5
作者
Loranger, Eric [1 ]
Canonne, Melissa [1 ]
Daneault, Claude [1 ]
Chabot, Bruno [1 ]
机构
[1] Univ Quebec Trois Rivieres, Ctr Integre Pates & Papiers, Trois Rivieres, PQ G9A 5H7, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Fluidized bed; Fibres; Flocculation; Adsorption; Dissolved and colloidal substances; Crowding factor; LIQUID; VELOCITY; SEDIMENTATION; SUSPENSIONS; REMOVAL; WATER;
D O I
10.1016/j.cej.2009.05.022
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Better ways to protect water resources and the environment must be implemented in the papermaking industry to help Canada achieve its strategic target in maintaining a healthy environment and ecosystems. Closing down paper machine whitewater systems is the only way to reach that goal. However, under such conditions, a build-up of dissolved and colloidal substances in whitewater occurs. This results in lower paper quality and paper machine runnability problems. A fluidized bed reactor with modified solid sorbents is proposed to remove contaminants from paper machine whitewater prior to recycling. However, the whitewater fibre content significantly modifies bed expansion creating a major impact on the terminal particle velocity and the Richardson and Zaki expansion coefficient. Fibre flocculation was identified as a key characteristic that must be included in the classical equations describing fluidization A modification. for Newton's terminal velocity law and a new model for the expansion coefficient have been developed. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:530 / 536
页数:7
相关论文
共 27 条
  • [1] Settling velocity of sediments at high concentrations
    Baldock, TE
    Tomkins, MR
    Nielsen, P
    Hughes, MG
    [J]. COASTAL ENGINEERING, 2004, 51 (01) : 91 - 100
  • [2] Recent modelling of sedimentation of suspended particles: A survey
    Boogerd, P
    Scarlett, B
    Brouwer, R
    [J]. IRRIGATION AND DRAINAGE, 2001, 50 (02) : 109 - 128
  • [3] Measuring techniques in gas-liquid and gas-liquid-solid reactors
    Boyer, C
    Duquenne, AM
    Wild, G
    [J]. CHEMICAL ENGINEERING SCIENCE, 2002, 57 (16) : 3185 - 3215
  • [4] Coulombe G., 2004, Commission d'etude sur la gestion de la foret publique quebecoise (Rapport Coulombe)
  • [5] NEW INTERPRETATION OF EXPANSION IN BIOFILM-COATED PARTICLE FLUIDIZATION
    CSIKOR, Z
    MIHALTZ, P
    CZAKO, L
    HOLLO, J
    [J]. APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1994, 41 (05) : 608 - 614
  • [6] The sedimentation velocity of dilute suspensions of nearly monosized spheres
    Di Felice, R
    [J]. INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1999, 25 (04) : 559 - 574
  • [7] *ENV CAN, 2004, NWRI SCI ASS REP SER, V3
  • [8] VELOCITY-VOIDAGE RELATIONSHIPS FOR FLUIDIZATION AND SEDIMENTATION IN SOLID-LIQUID SYSTEMS
    GARSIDE, J
    ALDIBOUNI, MR
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1977, 16 (02): : 206 - 214
  • [9] GELLER A, 1982, TAPPI J, V65, P97
  • [10] INTERACTIONS OF 2 SETTLING SPHERES - SETTLING RATES AND COLLISION EFFICIENCY
    HAN, MY
    LAWLER, DF
    [J]. JOURNAL OF HYDRAULIC ENGINEERING-ASCE, 1991, 117 (10): : 1269 - 1289