Dynamic release of siloxanes in the form of biogas from simulated municipal-solid-waste landfill and the corresponding driving mechanism.

Simulated landfill bioreactors were established and operated for 635 days to investigate the dynamic release of seven siloxanes in landfill biogas (denoted by octamethyltrisiloxane (L3), decamethyltetrasiloxane (L4), dodecamethylpentasiloxane (L5), hexamethylcyclotrisiloxane (D3), octamethylcyclotetrasiloxane (D4) and decamethylcyclopentasiloxane (D5) and dodecamethylcyclohexasiloxane (D6)). In total, 259.45, 252.73, 233.30, 80.40, 4.35, 1.67 and 1.10 mg of D5, D3, D4, D6, L4, L5 and L3 were discharged from 57 kg of municipal solid waste (MSW). More than 70 % of the siloxanes were released before day 119, indicating that the peak period of siloxane discharge occurred during the hydrolysis and acid production stage. The cyclosiloxanes (D3, D4, D5 and D6) were the dominant siloxane species in the biogas. The mass load of discharged cyclosiloxanes was more than 98 % of that of the total siloxanes. In addition to the variation in the concentration distribution profiles of the different siloxane species in the MSW, transformations among species may have an important effect on the release of siloxanes. The main transformation products were D3 and D4 with high release rates (>20 %) and high measured contents of trimethylsilanol (TMSOH) and functional microorganisms (Pseudomonas) were observed during landfilling. These results suggested that MSW degradation and transformation of siloxanes both drive the dynamic release of siloxanes during long-term landfilling.

Insight into the impact of industrial waste co-disposal with MSW on groundwater contamination at the open solid waste dumping sites.

Due to the lack of normalized management, industrial waste is often co-disposed at open solid waste dumping sites, which could aggravate the groundwater pollution. In this study, 5 practical open solid waste dumping sites dealing with municipal solid wastes (MSW) (2 of 5) and industrial wastes mixed with MSW (3 of 5) were chosen to investigate the effect of waste co-disposal on the groundwater contamination. The industrial waste was mainly from rubber production, leather production, machinery industry, pharmaceutical industry and plastic production. 3 to 6 groundwater wells were excavated from each dumping site and 148 indices were analyzed, including regular chemicals, heavy metals, biological pollutants, volatile organic compounds (VOCs), semi-volatile organic compounds (SVOCs) and pesticide residues. Nemerow index analysis showed that 5 indices were severely polluted in the groundwater from every industrial waste co-disposal landfill, while only 0 and 1 severely polluted index was found for the two MSW landfill, respectively. The principal component analysis (PCA) analysis indicated that 2 biological pollutant (plate-counting bacteria (TPB) and total coliforms (TCs)), 4 chemical pollutants (permanganate index, ammonia, S2- and petroleum) were closely connected with the disposal of industrial waste. Besides, co-disposal of industrial waste also brought in series of PAHs and dichloromethane, with di(2-ethylhexyl)phthalate exceeding the standard limit (10.5 mg L-1). Attention should be paid to TPB and TCs, whose maximal concentrations exceeded the standard limit by extraordinary 3200 and 1600 times, respectively. The distribution pattern of the pollutants showed that the biological pollutants at the downstream area, and chemical pollutants at the leakage points exhibited the highest concentration, which indicated the downstream area and seepage points should be specially concerned for the industry waste co-disposed dumping sites.

The effects of magnetite on anammox performance: Phenomena to mechanisms.

Low temperature is adverse to anaerobic ammonium oxidation (anammox) reaction while proper Fe addition can enhance anammox performance. Therefore, batch assays were conducted to investigate the potential effects of magnetite (100 µm, 20 µm and 200 nm) on anammox performance which were achieved from the reactor operated at 10-25 °C. After 3 runs, the results indicated that nano-scale magnetite improved the nitrogen elimination significantly. The specific anammox activity (SAA) of the group with nano-magnetite amendments was greater than the other groups after 3 runs (13.5, 12.9, 14.3, 15.4 and 15.7 mgTN/(gVSS·h)), reaching 18.0 mgTN/(gVSS·h). The distribution of magnetite in the granules were then analyzed using X-ray diffraction (XRD) and energy dispersive X-ray spectroscopy (EDS). The results indicated that nano-magnetite was more feasible to attached to the surface of the granules which might accelerate the release of Fe(II) or Fe(III) to enhance anammox performance.