PERFORMANCE OF CONE-SHAPED FLUIDIZED BED STRUVITE CRYSTALLIZERS IN REMOVING PHOSPHORUS FROM WASTEWATER
PERFORMANCE OF CONE-SHAPED FLUIDIZED BED STRUVITE CRYSTALLIZERS IN REMOVING PHOSPHORUS FROM WASTEWATER
复制标题
锥形流化床鸟粪石结晶器去除废水中磷的性能
DOI:
10.13031/2013.18523
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发表时间:
2005
影响因子:
1.5
通讯作者:
P. Westerman
中科院分区:
文献类型:
--
作者:
K. Bowers;P. Westerman
A struvite crystallizer design consisting of a continuously operating, cone-shaped fluidized bed was tested for its
ability to remove phosphorus from swine lagoon liquid. A laboratory-scale apparatus was first tested, operating at 41 and
57 L h-1 of lagoon liquid, and then a field-scale apparatus was tested, operating at 341 and 568 L h-1. Tests were arranged
in a randomized complete block design, with the two cited lagoon liquid flow rates and three levels each of magnesium (Mg)
supplementation and pH increase as independent variables. Levels of Mg supplementation were 0, 30, and 60 ppm. Ammonia
was used to increase pH, and in the laboratory-scale tests, levels of this variable were set at 0, 100, and 200 ppm as nitrogen
(N) of ammonia. In the field-scale tests, pH was controlled directly, and increased by 0, 0.5, and 1.0 pH units. In the
laboratory-scale tests, orthophosphate phosphorus (OP) removal ranged from 1% to 80%, and total phosphorus (TP) removal
ranged from -5% to 56%. In the field-scale tests, OP removal was 13% to 82%, and TP removal was 0% to 80%. The
laboratory-scale apparatus exhibited greater removal with increasing Mg supplementation and pH augmentation, but flow
rate showed no significant effect. The effects of the independent variables were similar in the field-scale apparatus, except
that decreasing flow rate was associated with greater removal.