RESEARCH ARTICLE

Filtration ability of hollow fiber membrane for production of magnesium ammonium phosphate crystals by reaction crystallization

  • H. Watamura ,
  • H. Marukawa ,
  • I. Hirasawa
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  • Applied Chemistry, Advanced Science and Engineering, Waseda University, Tokyo 169-8555, Japan

Received date: 30 Oct 2012

Accepted date: 25 Dec 2012

Published date: 05 Mar 2013

Copyright

2014 Higher Education Press and Springer-Verlag Berlin Heidelberg

Abstract

Relationship between magnesium ammonium phosphate (MAP) crystal properties and the filtration ability of hollow fiber membrane (HFM) were investigated. Phosphorus recovery process by crystallization has a problem that it produces a large amount of fine crystals. So improvement of the crystallization process by combining with filtration was discussed. MAP crystals were obtained by batch reaction crystallization and the filtration characteristics were investigated. The filtration was evaluated by the specific filtration resistance (αc) on HFM. Filtered slurry was prepared with each suspension density and crystal size distribution. The solution was filtered at constant pressure of 0.02 MPa and the filtration time on each filtrated volume was recorded. As a result, αc decreases exponentially with suspension density increasing from 0.25 g/L to 0.5 g/L and αc decreases moderately with suspension density increasing from 0.5 g/L to 1.5 g/L. αc of large crystals decreases exponentially at less suspension density than αc of small crystals does. Also, αc increases as the ratio of the fractured crystals increases.

Cite this article

H. Watamura , H. Marukawa , I. Hirasawa . Filtration ability of hollow fiber membrane for production of magnesium ammonium phosphate crystals by reaction crystallization[J]. Frontiers of Chemical Science and Engineering, 2013 , 7(1) : 55 -59 . DOI: 10.1007/s11705-013-1312-y

Acknowledgments

Authors thank KURARAY Co. Ltd. for financial support.
Nomenclature
C0Suspension concentration (kg∙m-3)
JFiltration flux (m∙s-1)
KFiltration constant (m2∙s-1)
PFiltration pressure (Pa)
VFiltrated volume per membrane area (m)
VmFiltration volume till cake formed (m)
αcSpecific filtration resistance (m∙kg-1)
μFiltrate viscosity (Pa∙s)
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