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Constructed wetlands (CWs) are characterized by low construction cost, convenient maintenance and management, and environmentally friendly features. They have emerged as promising technologies for decentralized sewage treatment across rural areas. Source separation of black water and gray water can facilitate sewage recycling and reuse of reclaimed water, reduce the size of treatment facilities, and lower infrastructure investment and operating cost. This is consistent with the concept of sustainable development. However, black water contains high concentrations of ammonia nitrogen, and the denitrification capacity of CWs is not excellent due to insufficient carbon source. Therefore, application of CWs for black water treatment faces challenges. This article provides a review on the progress in CWs for treatment of the sewage with high-influent nitrogen load, with emphasis on the commonly used strengthening means and the role of plants in nitrogen removal via CWs. The current issues of rural sewage treatment with high-influent nitrogen load by CWs are also assessed. Finally, the challenges and perspectives are discussed for the optimization of CWs-enhanced denitrification strategies., (© 2021. The Author(s), under exclusive licence to Springer Nature B.V.)

Dewatering of waste activated sludge (WAS) is of major interest in its volume reduction, transportation and ultimate disposal. Persulfate-based oxidation process is a newly developed option for enhancing WAS dewaterability through the generation of powerful sulfate radicals (SO 4 - ·). However, the enhancement in WAS dewaterability by persulfate differs with the species of iron catalysts used. In this study, two types of iron catalysts (i.e. Fe 2+ vs. Fe 0 ) were employed to initiate the persulfate (S 2 O 8 2- ), and the catalyzing behaviors and the underlying principles in enhancing WAS dewaterability were investigated and compared. The Fe 2+ exhibited the high effectiveness in catalyzing the decomposition of persulfate to sulfate radicals (SO 4 - ·), inducing the greater improvement in WAS dewatering. The WAS dewaterability (indicated by dry solids content after filtration) increased with the added S 2 O 8 2- /Fe 2+ dosages, with the dry solids content reaching up to 5.1 ± 0.8 wt% at S 2 O 8 2- /Fe 2+ dosages of 1.2/1.5 mmol/g-VS after only 30 s' filtration, roughly 1.8-fold increase than raw WAS (1.8 ± 0.1 wt%). In contrast, the influence of the persulfate oxidation when activated with Fe 0 on WAS dewaterability was statistically insignificant. The WAS dewaterability remained nearly unchanged (i.e. dry solids content of 2.0 ± 0.0 wt%), irrespective of the employed S 2 O 8 2- /Fe 0 dosages. Further analysis demonstrated that the WAS dewaterability negatively corresponded to loosely bound extracellular polymeric substances (LB-EPS) and tightly bound EPS (TB-EPS). The abundant SO 4 - · from S 2 O 8 2- /Fe 2+ system could effectively disrupt the gel-like EPS matrix, break apart the cells and subsequently arouse the release of the water inside EPS and cells, facilitating water-solid separation. In the case of S 2 O 8 2- /Fe 0 , the dissolution of Fe 0 oxidation could concurrently degrade COD and ammonia from WAS filtrate, lighten the burden of the subsequent sewage treatment facilities and reduce operational expense. Hence, from an environmental and economic perspective, the S 0 metallic surface, which resulted in the slow SO 4 - · production and thus hardly promoted WAS dewaterability. The pH adjustment could accelerate Fe 0 dissolution and enhance the dewatering performance of S 2 O 8 2- /Fe 0 process to a certain degree, but the effect was unsatisfactory. Additionally, the observations regarding the dissolved organic matters and ammonium collectively revealed that except for enhancing WAS dewatering, S 2 O 8 2- /Fe 2+ oxidation could concurrently degrade COD and ammonia from WAS filtrate, lighten the burden of the subsequent sewage treatment facilities and reduce operational expense. Hence, from an environmental and economic perspective, the S 2 O 8 2- /Fe 2+ system possesses much greater promise for WAS dewatering., (Copyright © 2018 Elsevier Ltd. All rights reserved.)

• The novel SE-M-R co-compost could potentially lower nitrogenous gas emission. • TN, NH 4 +-N and NO 3 --N nutrients were enhanced by the novel SE-M-R co-compost. • Controlled co-composting of SM and LM can simultaneously achieve LM recycling. • Compared to M-R, total N, P, K, cu and zn were enriched in SE-M-R final compost. Co-composting of solid manure (SM) and liquid manure (LM) is a new practice in livestock wastes recycling process and management. However, this practice is laced with various challenges including undesired leachate production, greenhouse gas emissions and characteristics poor nutrient quality of the final compost. Pragmatic utilization of the resource potential availed by combined LM and SM co-composting will be a game changer strategy for direct recycling of livestock wastes and reducing environmental contamination. By adapting a recently proposed LM addition model, we systematically investigated the promoting factors (thermophilic duration, organic matter (OM) degradation, and so on) necessary for successful co-composting of SM and LM, and for the first time examined the nutrient enrichment model essential to achieving final compost recyclability. Compared to the conventional SM co-compost, the proposed SM and LM controlled co-composting process elongated the thermophilic duration, reduced leachate generation, enhanced OM degradation, and simultaneously induced potential nutrients enrichment as evidenced by the nutrient balance analysis. The concentrations of TN, TP, TK, Cu and Zn in the controlled final compost were relatively enriched by 21.7 ± 2.16%, 12.1 ± 0.14%, 12.6 ± 0.16%, 11.0 ± 0.16% and 11.3 ± 1.24%, respectively. In addition, the controlled co-composting technique allowed for reduction in nutrients loss due to volatile N, estimated at 28.8% decrease in N loss rate relative to the conventional SM co-compost, and approximately 1.8 t/day of livestock wastewater can be effectively managed. The study conclusively demonstrated that concomitant utilization of liquid and solid manure presents an environmental friendly and unique advantage for simultaneous management and recycling of livestock wastes. [ABSTRACT FROM AUTHOR]

Fouling of membranes continues to be a prominent challenge in the membrane distillation (MD) treatment of high salinity organic wastewater (HSOW). Although membrane electrochemical reactor (MER) can effectively inhibit the membrane fouling of MD, the high cost of the proton exchange membrane (PEM) used in MER limits its widespread application. In this study, cost-effective pressure-driven membranes were employed as a substitute for PEM to establish pressure-driven membrane electrochemical reactors for HSOW pre-treatment. By using ultrafiltration membrane (UFM) and reverse osmosis membrane (ROM), UFMER and ROMER were developed, respectively. Due to the superior electrochemical performance of UFM, UFMER saved 43 % of energy compared to PEMER with the highest removal rate of organics (~85 %) in the simulated HSOW treatment. In practical applications, using UFMER significantly reduced the amount and size of complexes in the real nanofiltration concentrate (NC) of landfill leachate. This contributed to the superior specific flux maintenance (97 %) with a salt rejection (>99 %) and the highest recovered specific water flux (99.6 %) in MD cases. UFMER reduced ~27 % of energy compared to PEMER in MER pre-treatment, and saved the most energy (~39.6 %) in MD post-treatment. Hence, this strategy is potential for forthcoming applications, notably in lowering the membrane cost of MER and energy consumption of both MER and MD. [Display omitted] • UFM exhibited the highest current and the fastest response to the applied voltage. • UFMER maintained good ionic permeability without organics permeation. • MER significantly reduced the amount and size of complexes in the NC. • 97 % of MD specific flux could be maintained after UFMER pretreatment. • Using UFM saved 27 % of SEC in MER, and UFMER saved 39.6 % of SEC in MD. [ABSTRACT FROM AUTHOR]

The dispersion of granules in upflow anaerobic sludge blanket (UASB) reactor represents a critical technical issue in methanolic wastewater treatment. In this study, the potentials of coupling a microbial electrolysis cell (MEC) into an UASB reactor for improving methanolic wastewater biodegradation, long-term process stability and biomethane recovery were evaluated. The results indicated that coupling a MEC system was capable of improving the overall performance of UASB reactor for methanolic wastewater treatment. The combined system maintained the comparatively higher methane yield and COD removal efficiency over the single UASB process through the entire process, with the methane production at the steady-state conditions approaching 1504.7 ± 92.2 mL-CH 4 L − 1 -reactor d − 1 , around 10.1% higher than the control UASB (i.e. 1366.4 ± 71.0 mL-CH 4 L − 1 -reactor d − 1 ). The further characterizations verified that the input of external power source could stimulate the metabolic activity of microbes and reinforced the EPS secretion. The produced EPS interacted with Fe 2+/3+ liberated during anodic corrosion of iron electrode to create a gel-like three-dimensional [-Fe-EPS-] n matrix, which promoted cell-cell cohesion and maintained the structural integrity of granules. Further observations via SEM and FISH analysis demonstrated that the use of bioelectrochemical stimulation promoted the growth and proliferation of microorganisms, which diversified the degradation routes of methanol, convert the wasted CO 2 into methane and accordingly increased the process stability and methane productivity. [ABSTRACT FROM AUTHOR]

The use of liquid fraction of pressed municipal solid waste (LPW) for hydrogen production was evaluated via electrohydrogenesis in a single-chamber microbial electrolysis cell (MEC). The highest hydrogen production (0.38 ± 0.09 m 3 m −3 d −1 and 30.94 ± 7.03 mmol g −1 COD added ) was achieved at an applied voltage of 3.0 V and pH 5.5, increasing by 2.17-fold than those done at the same voltage without pH adjustment (pH 7.0). Electrohydrogenesis was accomplished by anodic oxidation of fermentative end-products (i.e. acetate, as well as propionate and butyrate after their acetification), with overall hydrogen recovery of 49.5 ± 11.3% of COD added . These results affirm for the first time that electrohydrogenesis can be a noteworthy alternative for hydrogen recovery from LPW and simultaneous organics removal. Electrohydrogenesis efficiency of this system has potential to improve provided that electron recycling, electromethanogenesis and deposition of non-conductive aggregates on cathode surface, etc. are effectively controlled. [ABSTRACT FROM AUTHOR]