Improved calcium sulfate recovery from a reverse osmosis retentate using eutectic freeze crystallization

被引:10
|
作者
Randall, D. G. [1 ]
Mohamed, R. [2 ]
Nathoo, J. [3 ]
Rossenrode, H. [1 ]
Lewis, A. E. [1 ]
机构
[1] Univ Cape Town, Dept Chem Engn, ZA-7925 Cape Town, South Africa
[2] Unilever, Johannesburg, South Africa
[3] NuWater, Res & Dev, Cape Town, South Africa
关键词
calcium sulfate; crystallization; desalination; environment; eutectic freeze crystallization; separations; TEMPERATURE;
D O I
10.2166/wst.2012.540
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A novel low temperature crystallization process called eutectic freeze crystallization (EFC) can produce both salt(s) and ice from a reverse osmosis (RO) stream by operating at the eutectic temperature of a solution. The EFC reject stream, which is de-supersaturated with respect to the scaling component, can subsequently be recycled back to the RO process for increased water recovery. This paper looks at the feasibility of using EFC to remove calcium sulfate from an RO retentate stream and compares the results to recovery rates at 0 and 20 degrees C. The results showed that there was a greater yield of calcium sulfate obtained at 0 degrees C as compared with 20 degrees C. Operation under eutectic conditions, with only a 20% ice recovery, resulted in an even greater yield of calcium sulfate (48%) when compared with yields obtained at operating temperatures of 0 and 20 degrees C (15% at 0 degrees C and 13% at 20 degrees C). The theoretical calcium recoveries were found to be 75 and 70% at 0 and 20 degrees C respectively which was higher than the experimentally determined values. The EFC process has the added advantage of producing water along with a salt.
引用
收藏
页码:139 / 146
页数:8
相关论文
共 50 条
  • [1] Recovery of Na2SO4•10H2O from a reverse osmosis retentate by eutectic freeze crystallisation technology
    Reddy, S. T.
    Lewis, A. E.
    Witkamp, G. J.
    Kramer, H. J. M.
    van Spronsen, J.
    [J]. CHEMICAL ENGINEERING RESEARCH & DESIGN, 2010, 88 (9A): : 1153 - 1157
  • [2] CRYSTALLIZATION OF CALCIUM-SULFATE ON REVERSE-OSMOSIS MEMBRANES
    FOUNTOUKIDIS, E
    MAROULIS, ZB
    MARINOSKOURIS, D
    [J]. DESALINATION, 1990, 79 (01) : 47 - 63
  • [3] Rennet coagulation and calcium distribution of raw milk reverse osmosis retentate
    Sorensen, Ida
    Le, Thao T.
    Larsen, Lotte Bach
    Wiking, Lars
    [J]. INTERNATIONAL DAIRY JOURNAL, 2019, 95 : 71 - 77
  • [4] Precipitation of calcium carbonate in reverse osmosis retentate flow by means of seeded techniques - A tool to increase recovery
    Pervov, A. G.
    [J]. DESALINATION, 2015, 368 : 140 - 151
  • [5] A succinct review of the treatment of Reverse Osmosis brines using Freeze Crystallization
    Randall, D. G.
    Nathoo, J.
    [J]. JOURNAL OF WATER PROCESS ENGINEERING, 2015, 8 : 186 - 194
  • [6] Reverse osmosis of the retentate from the nanofiltration of secondary effluents
    Garcia-Figueruelo, C.
    Bes-Pia, A.
    Mendoza-Roca, J. A.
    Lora-Garcia, J.
    Cuartas-Uribe, B.
    [J]. DESALINATION, 2009, 240 (1-3) : 274 - 279
  • [7] A case study for treating a reverse osmosis brine using Eutectic Freeze Crystallization-Approaching a zero waste process
    Randall, D. G.
    Nathoo, J.
    Lewis, A. E.
    [J]. DESALINATION, 2011, 266 (1-3) : 256 - 262
  • [8] Effect of chemical and physical factors on the crystallization of calcium sulfate in seawater reverse osmosis brine
    Choi, Youngkwon
    Naidu, Gayathri
    Jeong, Sanghyun
    Lee, Sangho
    Vigneswaran, Saravanamuthu
    [J]. DESALINATION, 2018, 426 : 78 - 87
  • [9] Fluoride Removal and Recovery from Water Using Reverse Osmosis and Osmotic Membrane Crystallization
    Ousman, Wuhib Zeine
    Alemayehu, Esayas
    Luis, Patricia
    [J]. CLEAN TECHNOLOGIES, 2023, 5 (03): : 973 - 996
  • [10] Eutectic freeze crystallization for recovery of NiSO4 and CoSO4 hydrates from sulfate solutions
    Ma, Yiqian
    Svard, Michael
    Xiao, Xiong
    Sahadevan, Suchithra Ashoka
    Gardner, James
    Olsson, Richard T.
    Forsberg, Kerstin
    [J]. SEPARATION AND PURIFICATION TECHNOLOGY, 2022, 286