Filtration ability of hollow fiber membrane for production of magnesium ammonium phosphate crystals by reaction crystallization
H. Watamura, H. Marukawa, I. Hirasawa
Filtration ability of hollow fiber membrane for production of magnesium ammonium phosphate crystals by reaction crystallization
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.
membrane separation / crystallization / MAP
[1] |
Seyhan D, Weikard H P, van Ierland E. An economic model of long-term phosphorus extraction and recycling. Resources, Conservation and Recycling, 2012, 61: 103–108
CrossRef
Google scholar
|
[2] |
Ott C, Rechberger H. The European phosphorus balance. Resources, Conservation and Recycling, 2012, 60: 159–172
CrossRef
Google scholar
|
[3] |
Jarvie H P, Neal C, Withers P J A. Sewage-effluent phosphorus: a greater risk to river eutrophication than agricultural phosphorus? Science of the Total Environment, 2006, 360(1-3): 246–253
CrossRef
Google scholar
|
[4] |
Bechmann M E, Berge D, Eggestad H O, Vandsemb S M. Phosphorus transfer from agricultural areas and its impact on the eutrophication of lakes-two long-term integrated studies from Norway. Journal of Hydrology (Amsterdam), 2005, 304(1-4): 238–250
CrossRef
Google scholar
|
[5] |
Jaffer Y, Clark T A, Pearce P, Parsons S A. Potential phosphorus by struvite formation. Recovery Water Research, 2002, 36: 1834–1842
|
[6] |
Bradford-Hartke Z, Lant P, Leslie G. Phosphorus recovery from centralised municipal water recycling plants. Chemical Engineering Research & Design, 2012, 90(1): 78–85
CrossRef
Google scholar
|
[7] |
Hirasawa, Kaneko S, Kanai Y, Hosoya S, Okuyama K. Crystallization phenomena of magnesium ammonium phosphate (MAP) in a fluidized-bed-type crystallizer. Journal of Crystal Growth, 2002, 237–239: 2183–2187
|
[8] |
Shimamura K, Hirasawa I, Ishikawa H, Tanaka T. Phosphorus recovery in a fluidized bed crystallization reactor. Journal of Chemical Engineering of Japan, 2006, 39(10): 1119–1127
CrossRef
Google scholar
|
[9] |
Hirasawa, Nakagawa H, Yoshikawa O, Itoh M. Phosphate recovery by reactive crystallization of magnesium ammonium phosphate: application to wastewater. American Chemical Society, 1997, 667: 267–276
|
[10] |
Hirasawa, Toya Y. Fluidized-bed process for phosphate removal by calcium phosphate, crystallization as a separations process. American Chemical Society, 1990, 438: 355–363
|
[11] |
Shimamura K, Ishikawa H, Tanaka T, Hirasawa I. Use of a seeder reactor to manage crystal growth in the fluidized bed reactor for phosphorus recovery. Water Environment Research, 2007, 79(4): 406–413
CrossRef
Google scholar
|
[12] |
Ruth B F, Montillon G H, Montonna R E. Studies in filtration. 1. Critical analysis of filtraion theory. Industrial & Engineering Chemistry, 1933, 25(1): 76–82
CrossRef
Google scholar
|
[13] |
Ruth B F, Montillon G H, Montonna R E. Studies in filtration. 2. Fundamental axiom of constant-pressure filtraion. Industrial & Engineering Chemistry, 1933, 25(2): 153–161
CrossRef
Google scholar
|
C0 | Suspension concentration (kg∙m-3) |
J | Filtration flux (m∙s-1) |
K | Filtration constant (m2∙s-1) |
⊿P | Filtration pressure (Pa) |
V | Filtrated volume per membrane area (m) |
Vm | Filtration volume till cake formed (m) |
αc | Specific filtration resistance (m∙kg-1) |
μ | Filtrate viscosity (Pa∙s) |
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