Phenanthrene biodegradation in a fed-batch reactor treating a spent sediment washing solution: Techno-economic implications for the recovery of ethanol as extracting agent

被引:25
作者
Bianco, Francesco [1 ]
Race, Marco [1 ]
Papirio, Stefano [2 ]
Esposito, Giovanni [2 ]
机构
[1] Univ Cassino & Southern Lazio, Dept Civil & Mech Engn, Via Biasio 43, I-03043 Cassino, Italy
[2] Univ Napoli Federico II, Dept Civil Architectural & Environm Engn, Via Claudio 21, I-80125 Naples, Italy
关键词
Polycyclic aromatic hydrocarbons; Ethanol; Sediment washing; Biological treatment; Degradation kinetics; Cost assessment; POLYCYCLIC AROMATIC-HYDROCARBONS; PAH-DEGRADING BACTERIA; SP STRAIN PN/Y; 2-HYDROXY-1-NAPHTHOIC ACID; CONTAMINATED SOIL; SPHINGOMONAS SP; ANAEROBIC BIODEGRADATION; MANGROVE SEDIMENTS; META-CLEAVAGE; WASTE-WATER;
D O I
10.1016/j.chemosphere.2021.131361
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The continuous dredging of sediments contaminated by polycyclic aromatic hydrocarbons such as phenanthrene (PHE) has required the employment of high-efficiency technologies, including sediment washing (SW). However, the large amount of generated spent SW effluents requires the development of effective, eco-friendly and cost-saving approaches, which can tackle the waste formation in favor of the recovery of chemicals. This study proposes the treatment of a spent SW solution containing ethanol (EtOH) as extracting agent, by testing different initial PHE concentrations (i.e. 20-140 mg L-1) within six consecutive cycles in a fed-batch bioreactor under aerobic conditions. The biological process achieved a PHE removal of 63-91% after the enrichment of PHE-degrading bacteria and the proper supplementation of nutrients, and was mainly affected by the initial PHE concentration value and the excessive decrease of pH and dissolved oxygen. Achromobacter, Sphingobacterium and Dysgonomonas genera were mainly involved in PHE degradation, which followed a first-order kinetic model (R2 = 0.652-0.928) with a degradation rate and half-life time of 0.127-1.177 d-1 and 0.589-2.912 d, respectively. A techno-economic assessment revealed that a virtuous operation of SW, EtOH recovery and biodegradation of the SW solution can allow the recovery of up to 1.35 tons of EtOH per ton of remediated sediment and the decrease of the overall costs by 50%.
引用
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页数:13
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