Mixotrophic algal system for centrate treatment and resource recovery

被引:16
作者
Abeysiriwardana-Arachchige, I. S. A. [1 ]
Chapman, G. W. [1 ]
Rosalez, R. [2 ]
Soliz, N. [2 ]
Cui, Z. [2 ]
Munasinghe-Arachchige, S. P. [1 ]
Delanka-Pedige, H. M. K. [1 ]
Brewer, C. E. [2 ]
Lammers, P. J. [3 ]
Nirmalakhandan, N. [1 ]
机构
[1] New Mexico State Univ, Civil Engn Dept, Las Cruces, NM 88003 USA
[2] New Mexico State Univ, Chem & Mat Engn Dept, Las Cruces, NM 88003 USA
[3] Arizona State Univ, Arizona Ctr Algae Technol & Innovat, Phoenix, AZ USA
来源
ALGAL RESEARCH-BIOMASS BIOFUELS AND BIOPRODUCTS | 2020年 / 52卷
基金
美国国家科学基金会;
关键词
Centrate treatment; Nitrogen recovery; Phosphorus recovery; Energy recovery; Algal sewage treatment; DOMESTIC WASTE-WATER; HYDROTHERMAL LIQUEFACTION; GALDIERIA-SULPHURARIA; NUTRIENT RECOVERY; NITROGEN REMOVAL; ENERGY; AMMONIA; PRECIPITATION; PHOSPHATE; AMYLASE;
D O I
10.1016/j.algal.2020.102087
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
In traditional activated sludge-based wastewater treatment plants equipped with anaerobic digesters, the nutrient-rich centrate from the digester is typically recirculated to the headworks of the plant exerting a parasitic load. As an alternative, mixotrophic algal cultivation in a blend of the centrate and primary effluent is proposed to yield energy- and nutrient-rich biomass from which, liquid biofuel and fertilizers could be recovered. Core components in the proposed sewage treatment and resource recovery (STaRR) system include i) algal sewage treatment/biomass cultivation; ii) hydrothermal liquefaction of algal biomass for energy recovery, and iii) recovery of struvite and concentrated ammonia from the hydrothermal liquefaction byproducts. Results from a 700 l pilot-scale STaRR system run with four different blends of centrate and primary effluent are presented to validate the proposed approach. A 20: 80 centrate-to-primary effluent blend enabled discharge standards for ammoniacal-nitrogen, phosphate phosphorus, and biochemical oxygen demand to be met in < 7 days; volumetric removal rates at this blending ratio were 4.0 mg/l-d, 0.70 mg/l-d and, 10.50 mg/l-d, respectively. Hydrothermal liquefaction of the resulting biomass (20% solids content, 350 degrees C, and 60 min holding time) yielded 77.5 g light bio-crude oil and 108.0 g heavy bio-crude oil per kg of dry algae. It is estimated that the STaRR system can produce 6.75 kg of struvite and 3.42 kg of concentrated ammoniacal nitrogen per 100 m(3) of blended wastewater.
引用
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页数:8
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