A three-mechanism (intermediate pore blocking, standard pore blocking and cake filtration) model considering correction of effective filtration area

被引:2
|
作者
Zhong, Chenyin [1 ]
Wang, Zhan [1 ,2 ]
机构
[1] Beijing Univ Technol, Dept Environm & Chem Engn, Beijing Key Lab Green Catalysis & Separat, Beijing 100124, Peoples R China
[2] Changzhou Vocat Inst Engn, Changzhou 213164, Peoples R China
来源
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING | 2024年 / 12卷 / 05期
基金
中国国家自然科学基金;
关键词
Filtration; Constant flowrate; Cross-flow; Model; DEAD-END MICROFILTRATION; MEMBRANE BIOREACTOR; CONSTANT-PRESSURE; WASTE-WATER; INTERFACIAL INTERACTIONS; INTERACTION ENERGY; BOUNDARY-LAYER; LAWS; ULTRAFILTRATION; INITIATION;
D O I
10.1016/j.jece.2024.113654
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A general three-mechanism (intermediate pore blocking, standard pore blocking and cake filtration) model considering correction of the effective filtration area based on Darcy's law, Hagen-Poiseuille equation and Hermes' law was firstly developed to describe the variation of trans-membrane pressure (Delta p(t)) in the constant flowrate cross-flow filtration mode by using EPS model solutions (bovine serum albumin (BSA), sodium alginate (SA) and humic acid (HA)). Results showed that the model predictions fitted well with the experimental data (the single EPS model solution (R2 >= 0.904), the binary EPS model solution (R2 >= 0.910) and the ternary EPS model solution (R2 >= 0.878)). For all model solution, the domination mechanism in the first stage was intermediate pore blocking, while that in the second stage was cake filtration. Meanwhile, higher flux or concentration would led to the transition point appear earlier, while higher cross-flow velocity made it appear later. Moreover, the predictive accuracy of the proposed model improved by 1.25 % compared with that without considering the correction of the effective filtration area. Also, the proposed model was also validated using other membranes (polyvinylidene fluoride (PVDF) and polyether sulfone (PES) membranes) (R2 >= 0.953) and other feed suspensions (yeast, kaolin and activated sludge suspensions) (R2 >= 0.981).
引用
收藏
页数:15
相关论文
共 32 条
  • [21] Ultrafiltration of whey: membrane performance and modelling using a combined pore blocking-cake formation model
    Corbaton-Baguena, Maria-Jose
    Alvarez-Blanco, Silvia
    Vincent-Vela, Maria-Cinta
    JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2018, 93 (07) : 1891 - 1900
  • [22] Analysis of humic acid fouling during microfiltration using a pore blockage-cake filtration model
    Yuan, W
    Kocic, A
    Zydney, AL
    JOURNAL OF MEMBRANE SCIENCE, 2002, 198 (01) : 51 - 62
  • [23] An Evaluation of the Relationship between Membrane Properties and the Fouling Mechanism Based on a Blocking Filtration Model
    Katagiri, Nobuyuki
    Uchida, Takehiro
    Takahashi, Hironori
    Iritani, Eiji
    SEPARATIONS, 2024, 11 (03)
  • [24] A new approach to model asphaltene induced permeability damage with emphasis on pore blocking mechanism
    Ghadimi, Marzieh
    Ghaedi, Mojtaba
    Malayeri, Mohammad R.
    Amani, Mohammad J.
    JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2020, 184
  • [25] Modified intermediate pore blockage model describes fouling behavior during sterile filtration of glycoconjugate vaccines
    Emami, Parinaz
    Fallahianbijan, Fatemeh
    Dinse, Erica
    Motevalian, Seyed Pouria
    Conde, Brenda Carrillo
    Reilly, Kelvin
    Zydney, Andrew L.
    JOURNAL OF MEMBRANE SCIENCE, 2020, 613
  • [26] A combined pore blockage, osmotic pressure, and cake filtration model for crossflow nanofiltration of natural organic matter and inorganic salts
    Mattaraj, Supatpong
    Jarusutthirak, Chalor
    Charoensuk, Chareopon
    Jiraratananon, Ratana
    DESALINATION, 2011, 274 (1-3) : 182 - 191
  • [27] Size separation of silver nanoparticles by dead-end ultrafiltration: Description of fouling mechanism by pore blocking model
    Palencia, Manuel
    Rivas, Bernabe L.
    Valle, Hernan
    JOURNAL OF MEMBRANE SCIENCE, 2014, 455 : 7 - 14
  • [28] Membrane fouling mechanism of biofilm-membrane bioreactor (BF-MBR): Pore blocking model and membrane cleaning
    Zheng, Yi
    Zhang, Wenxiang
    Tang, Bing
    Ding, Jie
    Zheng, Yi
    Zhang, Zhien
    BIORESOURCE TECHNOLOGY, 2018, 250 : 398 - 405
  • [29] Fluid loss from the peritoneal cavity by back-filtration through the small pores of the three-pore model
    Rippe, B.
    Venturoli, D.
    KIDNEY INTERNATIONAL, 2008, 73 (09) : 985 - 986
  • [30] Filtration of the catalyst suspension in hydrogenated oil through the woven cloth: Mathematical model of the process accounting for dynamics of the cake growth and filter pore blockage
    Vernikovskaya, N. V.
    Chumachenko, V. A.
    Romanenko, A. V.
    Dobrynkin, N. M.
    SEPARATION AND PURIFICATION TECHNOLOGY, 2019, 212 : 355 - 367