Carbon reclamation from biogas plant flue gas for immobilizing lead and neutralizing alkalis in municipal solid waste incineration fly ash
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1. Introduction
Due to the growing output of municipal solid waste (MSW), the by- product, namely MSW incineration fly ash (MSWI-FA), has increased explosively in the last five years [1–2] . Statistics has predicted that the annual production of MSWI-FA in China would exceed 10 million tons by the end of 2020 [3] . The dominant disposal method of MSWI-FA is still landfill treatment, but a range of hazardous properties should be noted, of which the excessive heavy metal concentration and strong basicity in leachate are the worst [4–5] . Previous study of our group reported that lead (Pb) in MSWI-FA was measured as the only heavy metal element, whose leaching toxicity was about eleven fold of the limiting value stipulated in the latest regulations of hazardous waste landfill in China [6–7] . It would be attributed to the presence of exchangeable fraction (8%–9%) [8] . If the prestabilization is lacking, the highly toxic Pb probably endangered the soil, crops, and even human beings [9–10] . On the other hand, raw FA sample is rich in alkaline oxides and hydroxides, whose mass ratio account for more than half of FA, leaving a strong alkalinity of its leaching solution (pH > 12) [11] . This property might impose negative effects on the landfill soil, resulting in the deterioration of its physical characteristics and following inhibi- tion of crop growth [12–13] . On the basis of the landfill standard, a limited pH range (6–9) of effluent must be obeyed. Hence, pursuing pretreatment method for simultaneously stabilizing Pb and neutralizing alkalis is required. The current Pb stabilization methods in China include washing, separation and extraction, melting in high temperature, and solidifica- tion/stabilization [14–17] . Chelating agent (CA) stabilization, equipped with the advantages of strong reliability and availability, is wildly recognized as the leading technology. Previous studies found that inorganic agents (e.g., sulfides, phosphates, and molysite) are unable to stabilize Pb that up to standard until supplying huge dosage of more than 13%, meanwhile, this Pb speciation would be easily destructed under acidic and parlkaline conditions [7,14] . To handle the above limitations, stabilization using organic CA including thiourea de- rivatives, chitosan, dithiocarbamates was put forward as an alternative method [7–8,18–19] . These chelates could achieve standardized leach- ing of Pb with a less dosage and reinforced stability in extreme * Corresponding author at: The State Key Laboratory of Pollution Control and Resource Reuse, School of Environmental Science and Engineering, Tongji Uni- versity, 1239 Siping Road, Shanghai 200092, China. E-mail addresses: 15957106196@163.com (Z. Zhu), 1410421@tongji.edu.cn (T. Zhou). Contents lists available at ScienceDirect Chemical Engineering Journal journal homepage: www.elsevier.com/locate/cej https://doi.org/10.1016/j.cej.2022.134812 Received 5 November 2021; Received in revised form 24 December 2021; Accepted 17 January 2022 Chemical Engineering Journal 435 (2022) 134812 2 environments, but the high cost and potential biotoxicity remains a burning question. To prevent the soil alkalization, chemical amelioration, phytor- emediation, colloidal flocculation, and water washing were used as main treatment methods [20–21] . Calcium sulfate serve as the primary inor- ganic conditioner, providing Ca in replacing exchangeable Na mean- while reducing soil bulk density and promoting saturated hydraulic conductivity [22] . However, a long-term supplement of inorganic conditioner would result in the disruption of soil fertility [23] . Applying organic amendment would effectively handle the soil alkalization as well as increase the capacity of soil organisms [21] . Nevertheless, such amelioration could not simultaneously chelate Pb up to standard, causing unpleasant cost and operation complexity. Accelerated carbonation is defined as the reaction between alkaline metal oxides and CO 2 in high concentration, which forms relatively stable carbonates. This promising process had already been investigated for immobilizing heavy metals in MSWI-FA [24] , and current research mainly focuses on the optimization of reacting factors, including gas component and concentration, liquid to solid ratio (L/S), solution pH, etc [25–27] . Results indicated that carbonation immobilized Pb, Cu, Zn, and As in MSWI-FA, but exerted an adverse influence on Cd and Sb [26] . The introduction of SO 2 into reaction gas weakened the immobilization effect on MSWI-FA, and the CO 2 content was a negligible factor with increasing content from 12% to 100% [25] . 0.25 and 9.5–10.5 were investigated as the optimum L/S ratio and solution pH towards MSWI- FA carbonation [26,28] . Currently, some blanks about MSWI-FA carbonation should be noticed and handled: (i) All previous studies only considered carbon dioxide (CO 2 ) in different volume fractions as the reactant gas, or uti- lized the mixture of CO 2 and sulfur dioxide to simulate the typical components of incineration flus gas [25,29–30] . But there is still a blank for effect assessment with an actual flue gas; (ii) Previous work revealed that the Pb leaching, treated by single carbonation, hardly satisfied the latest regulation, making the incorporation with other pre-stabilization methods vital [31] . Moreover, the cost analysis of incorporated stabili- zation was essential for further application. However, the involved research is limited; (iii) Previous research confirmed the carbonation could reduce the alkaline capacity while sequestering CO 2 in MSWI-FA [24] . However, the relationship between carbonation time and leachate pH or CO 2 capture capacity is lacked. Hence, it’s quite necessary and promising to investigate whether the combination between carbonation with actual flue gas and agent treatment could concurrently realize the Pb immobilization, alkali neutralization, carbon emission reduction, and economic benefit improvement. In this study, the investigates were as follows: i) to determine the Pb leaching behavior under different carbonation time while varying the agent type, leaching pH and curing durations; ii) to obtain the rela- tionship between carbonation time and acid-base neutralization; iii) to summarize the carbonation mechanisms through the characterization of raw and carbonated FA; iv) to calculate the maximum values of carbonation conversion and cost reduction rate compared with the uncarbonated. Download 2.53 Mb. Do'stlaringiz bilan baham: |
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