Impact of supersaturation ratio on phosphorus recovery from synthetic anaerobic digester supernatant through a struvite crystallization fluidized bed reactor

被引:7
|
作者
Ghosh, Shayok [1 ,2 ]
Lobanov, Sergey [1 ]
Lo, Victor K. [1 ]
机构
[1] Univ British Columbia, Dept Civil Engn, 2002-6250 Appl Sci Lane, Vancouver, BC V6T 1Z4, Canada
[2] East West Univ, Dept Civil Engn, Dhaka 1000, Bangladesh
基金
加拿大自然科学与工程研究理事会;
关键词
Anaerobic digester supernatant; P-removal; P-recovery; struvite pellets; pH; supersaturation ratio; REMOVING PHOSPHORUS; WASTE-WATER;
D O I
10.1080/09593330.2018.1435734
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Over the past few decades, several technologies have been developed to recover phosphorus (P) as struvite from wastewater. Although these technologies have achieved reasonable P-removal efficiencies, these technologies are associated with several shortcomings such as high capital and operating costs, longer crystallization time and production of low-quality product. This study focussed on the development of an efficient technology by designing a new fluidized bed reactor (FBR) and determining its optimum operating conditions. The supersaturation ratio is the most important process parameter for struvite recovery. This study exerted effort to establish a range of supersaturation ratios in order to achieve optimum P-removal and recovery with a lesser amount of fine crystals produced. Bench-scale FBR used in this study was able to accomplish 90% P-removal with 18% P-recovery. P-removal efficiency was observed to be increasing with an increase in the initial supersaturation ratio up to a value of 6.5. On the other hand, an increase in the supersaturation ratio resulted in a lower P-recovery efficiency with an increase in fines production. The supersaturation ratio from 5.5 to 6.0 was found to be optimum for efficient operation of the reactor.
引用
收藏
页码:2000 / 2010
页数:11
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