The effect of organic matter on the removal of phosphorus through precipitation as struvite and calcium phosphate in synthetic dairy wastewater

被引:9
作者
Aleta, Prince [1 ]
Parikh, Sanjai J. [2 ]
Silchuk, Amy P. [2 ]
Scow, Kate M. [2 ]
Park, Minseung [1 ]
Kim, Sungpyo [1 ]
机构
[1] Korea Univ, Dept Environm Syst Engn, Sejong City 339770, South Korea
[2] Univ Calif Davis, Dept Land Air & Water Resources, Davis, CA 95616 USA
来源
MEMBRANE AND WATER TREATMENT | 2018年 / 9卷 / 03期
关键词
phosphorus recovery; struvite; calcium phosphate; HUMIC SUBSTANCES; AMMONIA NITROGEN; RECOVERY; CRYSTALLIZATION; CHALLENGES; XYLAN; IONS;
D O I
10.12989/mwt.2018.9.3.163
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This study investigated the effect of organic matter on the precipitation of struvite and calcium phosphate for phosphorus recovery from synthetic dairy wastewater. Batch precipitation experiments were performed to precipitate phosphorus from solutions containing PO43- and NH4+ by the addition of Mg2+ and Ca2+, separately, at varying pH, Mg/P and Ca/P molar ratios, and organic matter concentrations. Soluble total organic solids exhibited more inhibition to precipitation due to potential interaction with other dissolved ionic species involved in phosphorus precipitation. Xylan with low total acidity only exhibited significant inhibition at very high concentrations in synthetic wastewater (at up to 100 g/L). No significant inhibition was observed for Mg2+ and Ca2+ precipitation at relatively lower concentrations (at up to 1.2 g/L). MINTEQ simulations show that dissolved organic matter (DOM) as humic substances (HS) can cause significant inhibition even at relatively low concentrations of 0.165 g/L fulvic acid. However, scanning electron microscopy (SEM) and X-ray diffraction (XRD) analysis suggested that xylan altered the crystal structure of both precipitates and had caused the formation of smaller sized struvite crystals with slightly rougher surfaces This could be due to xylan molecules adhering on the surface of the crystal potentially blocking active sites and limit further crystal growth. Smaller particle sizes will have negative practical impact because of poorer settleability.
引用
收藏
页码:163 / 172
页数:10
相关论文
共 41 条
  • [1] Phosphorus recovery through struvite precipitation from wastewater: effect of the competitive ions
    Acelas, Nancy Y.
    Florez, Elizabeth
    Lopez, Diana
    [J]. DESALINATION AND WATER TREATMENT, 2015, 54 (09) : 2468 - 2479
  • [2] Multi-Impurity Adsorption Model for Modeling Crystal Purity and Shape Evolution during Crystallization Processes in Impure Media
    Borsos, Akos
    Majumder, Aniruddha
    Nagy, Zoltan K.
    [J]. CRYSTAL GROWTH & DESIGN, 2016, 16 (02) : 555 - 568
  • [3] Britz T.J., 2006, TREATMENT DAIRY PROC, P1
  • [4] Burke G., 2005, Handbook of Environmental Management and Technology, V2nd
  • [5] Sustainability Challenges of Phosphorus and Food: Solutions from Closing the Human Phosphorus Cycle
    Childers, Daniel L.
    Corman, Jessica
    Edwards, Mark
    Elser, James J.
    [J]. BIOSCIENCE, 2011, 61 (02) : 117 - 124
  • [6] The story of phosphorus: Global food security and food for thought
    Cordell, Dana
    Drangert, Jan-Olof
    White, Stuart
    [J]. GLOBAL ENVIRONMENTAL CHANGE-HUMAN AND POLICY DIMENSIONS, 2009, 19 (02): : 292 - 305
  • [7] Phosphorus recovery from wastewater: needs, technologies and costs
    Cornel, P.
    Schaum, C.
    [J]. WATER SCIENCE AND TECHNOLOGY, 2009, 59 (06) : 1069 - 1076
  • [8] Recent advances in removing phosphorus from wastewater and its future use as fertilizer (1997-2003)
    de-Bashan, LE
    Bashan, Y
    [J]. WATER RESEARCH, 2004, 38 (19) : 4222 - 4246
  • [9] Overview and description of technologies for recovering phosphorus from municipal wastewater
    Egle, Lukas
    Rechberger, Helmut
    Zessner, Matthias
    [J]. RESOURCES CONSERVATION AND RECYCLING, 2015, 105 : 325 - 346
  • [10] Recovery of ammonia nitrogen from industrial wastewater treatment as Struvite slow releasing fertilizer
    El Diwani, G.
    El Rafie, Sh.
    El Ibiari, N. N.
    El-Aila, H. I.
    [J]. DESALINATION, 2007, 214 (1-3) : 200 - 214