Influence of solution and operating conditions on the treatment of aquaculture wastewater using direct contact membrane distillation: Ammonia rejection and membrane fouling

被引:12
|
作者
Zhang, Bing [1 ,2 ,4 ]
Shen, Jing [1 ]
Xiong, Jianhui [3 ]
Shen, Yu [1 ,2 ]
Zhang, Bing [1 ,2 ,4 ]
Shi, Wenxin [4 ]
机构
[1] Chongqing Technol & Business Univ, Natl Res Base Intelligent Mfg Serv, Chongqing 400067, Peoples R China
[2] Chongqing Yujiang Intelligent Technol Co Ltd, Chongqing 409003, Peoples R China
[3] Cent South Architectural Design Inst Co Ltd, Wuhan 430071, Peoples R China
[4] Chongqing Univ, Sch Environm & Ecol, Chongqing 400044, Peoples R China
基金
中国国家自然科学基金;
关键词
Ammonia rejection; Membrane fouling; DCMD; BSA; Temperature; pH; MASS-TRANSFER; ATTENTION; REMOVAL; BSA; MD;
D O I
10.1016/j.cej.2023.147326
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In the context of recirculating aquaculture, the timely and efficient treatment of ammonia nitrogen, which is a key factor influencing the survival of aquaculture organisms, has become a critical issue that must be addressed. This study aimed to comparatively investigate the interactive effects of bovine serum albumin (BSA) concentration, ammonia concentration, pH, temperature, and flow rate on the efficiency and membrane fouling during ammonia rejection by direct contact membrane distillation (DCMD) in the presence or absence of BSA. The results showed that the elevation of ammonia nitrogen concentration, regardless of the presence of BSA in the solution, led to an increase in concentration polarization, resulting in elevated rejection for ammonia nitrogen and aggravated membrane fouling. Moreover, the conditions of ammonia rejection that were found to be more favorable included lower temperature, pH, and flow rate. Among them, temperature and pH change primarily impacted ammonia solubility, which were the two factors with the significant influence on DCMD's ability to reject ammonia. In the presence of BSA, significant alterations were observed in the rejection of ammonia nitrogen and membrane fouling. The inclusion of 5 mg/L BSA resulted in a remarkable 97.5 % rejection of ammonia through hydration force. The elevation of pH led to a notable mitigation of membrane fouling owing to the augmentation of electrostatic force. Furthermore, a strong correlation was found between ammonia concentration, BSA concentration, and DCMD's rejection of ammonia. This study provides valuable insights for the future implementation of DCMD in treating actual ammonia wastewater and mitigating membrane fouling.
引用
收藏
页数:11
相关论文
共 50 条
  • [21] Spent caustic wastewater treatment using direct contact membrane distillation with electroblown styrene-acrylonitrile membrane
    A. S. Niknejad
    S. Bazgir
    M. Ardjmand
    M. M. A. Shirazi
    International Journal of Environmental Science and Technology, 2021, 18 : 2283 - 2294
  • [22] A comparison of vacuum and direct contact membrane distillation for phosphorus and ammonia recovery from wastewater
    Simoni, Gustav
    Kirkebaek, Bastian Stiem
    Quist-Jensen, Cejna Anna
    Christensen, Morten Lykkegaard
    Ali, Aamer
    JOURNAL OF WATER PROCESS ENGINEERING, 2021, 44
  • [23] Fouling behavior of calcium phosphate in direct contact membrane distillation
    Zhang, Jianhua
    Qin, Wenli
    Ng, Derrick
    Ji, Xiaosheng
    Zhang, Xiaozhuan
    Ye, Ying
    Xie, Zongli
    ENVIRONMENTAL TECHNOLOGY & INNOVATION, 2021, 21
  • [24] Dye synthetic solution treatment by direct contact membrane distillation using commercial membranes
    Ramlow, Heloisa
    Machado, Ricardo Antonio Francisco
    Bierhalz, Andrea Cristiane Krause
    Marangoni, Cintia
    ENVIRONMENTAL TECHNOLOGY, 2020, 41 (17) : 2253 - 2265
  • [25] Treatment of ammonia nitrogen wastewater by membrane distillation using PVDF membranes
    Xia, Qiang
    Yun, Yanbin
    Chen, Jinjin
    Qu, Dan
    Li, Chunli
    Zhu, Shouwei
    DESALINATION AND WATER TREATMENT, 2017, 61 : 126 - 135
  • [26] Treatment of radioactive wastewater solutions by direct contact membrane distillation using surface modified membranes
    Khayet, M.
    DESALINATION, 2013, 321 : 60 - 66
  • [27] Sugarcane Stillage Treatment Using Direct Contact Membrane Distillation
    Omayra B. Ferreiro
    Frederico A. Kronemberger
    Cristiano P. Borges
    Waste and Biomass Valorization, 2021, 12 : 3987 - 3999
  • [28] Sugarcane Stillage Treatment Using Direct Contact Membrane Distillation
    Ferreiro, Omayra B.
    Kronemberger, Frederico A.
    Borges, Cristiano P.
    WASTE AND BIOMASS VALORIZATION, 2021, 12 (07) : 3987 - 3999
  • [29] Direct contact membrane distillation for the treatment of industrial dyeing wastewater and characteristic pollutants
    Li, Fang
    Huang, Jiahui
    Xia, Qin
    Lou, Mengmeng
    Yang, Bo
    Tian, Qing
    Liu, Yanbiao
    SEPARATION AND PURIFICATION TECHNOLOGY, 2018, 195 : 83 - 91
  • [30] Direct contact membrane distillation for the treatment of wastewater for a cooling tower in the power industry
    Ali, A.
    Criscuoli, A.
    Macedonio, F.
    Argurio, P.
    Figoli, A.
    Drioli, E.
    H2OPEN JOURNAL, 2018, 1 (01) : 57 - 68