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改性酒糟生物炭对水体氨氮吸附特性影响

Effects of modified distiller’s grains biochar on the adsorption characteristics of ammonia nitrogen in water

  • 摘要: 生物炭吸附是解决水体氨氮污染的重要手段,而常规生物炭(BC)对氨氮吸附性能有限。该研究提出了两种具有高效吸附性的浸渍改性酒糟生物炭(磷酸改性生物炭PBC、氯化锌改性生物炭ZBC),并采用傅里叶变换红外光谱(Fourier transform infrared spectroscopy,FTIR)、比表面积分析(Brunauer-Emmett-Teller,BET)、X射线衍射(X-ray diffraction,XRD)、扫描电子显微镜( scanning electron microscope,SEM)等表征手段及静态吸附试验,探究了改性酒糟生物炭对水体氨氮吸附行为和动力学驱动机制影响。结果表明:相较传统BC生物炭,经磷酸和氯化锌改性后,显著提高了生物炭O/C与(O+N)/C,丰富含氧官能团,提升亲水性,增大比表面积,并促进孔隙结构发育,显著增强了对NH4+的吸附能力。经PBC和ZBC处理的模拟氨氮废水中吸附动态过程呈现初期快速增长并趋于稳定的趋势,符合准二级动力学模型,以化学吸附起主导作用。PBC与ZBC对模拟氨氮废水的吸附均在240 min内达到平衡,其最大吸附容量(qe)分别可达232.66 mg/g与224.18 mg/g,显著高于BC处理的吸附容量,增幅达50倍。相较于模拟氨氮废水,PBC与ZBC对实际猪粪废水的氨氮最大吸附容量分别下降了 19.22%和39.66%,归因于实际猪粪废水中Ca2+、Mg2+等共存离子与NH4+竞争吸附点位,从而抑制了生物炭对专一氨氮的吸附作用。正交试验表明,温度为35℃和pH值为7的条件下,经360 min的接触吸附,生物炭对猪粪废水中氨氮的去除效果最佳,PBC和ZBC吸附量分别达197.49和146.71 mg/g。PBC吸附机制主要包括表面物理吸附,静电吸附及离子交换实现对氨氮的吸附增强;ZBC依赖离子交换作用提升化学吸附,并通过改善孔隙结构强化物理吸附。此外,两者均存在阳离子-π作用的辅助吸附机制。研究结果可为酒糟废弃物资源化制备高效氨氮吸附剂提供了可行路径。

     

    Abstract: Excessive discharge of ammonium nitrogen (NH4+-N)-laden wastewater from agricultural and industrial activities has become a critical threat to aquatic ecosystems and human health, necessitating the development of efficient, low-cost adsorbents. Biochar derived from agricultural residues offers a sustainable remediation strategy, yet its pristine form suffers from limited adsorption capacity. This study proposes a novel pre-impregnation coupled with slow pyrolysis strategy to fabricate two modified biochars using distillers’ grains—a widely available, underutilized by-product of the liquor industry—as the feedstock, with phosphoric acid (H3PO4) and zinc chloride (ZnCl2) employed as impregnation agents to produce PBC and ZBC, respectively. The physicochemical properties of the biochars were comprehensively characterized by elemental analysis, Fourier transform infrared spectroscopy (FTIR), Brunauer–Emmett–Teller (BET) surface area measurement, X-ray diffraction (XRD), scanning electron microscopy (SEM), and zeta potential analysis, while batch adsorption experiments were conducted under varying conditions (contact time, initial concentration, pH, temperature) using both synthetic NH4Cl solutions and real swine wastewater to evaluate adsorption kinetics, isotherms, and the interference of coexisting ions. Compared with unmodified biochar (BC), both PBC and ZBC exhibited substantially enhanced O/C and (O+N)/C atomic ratios (0.48–0.51 vs. 0.09; 0.49-0.56 vs. 0.15), indicating greater hydrophilicity and surface polarity, with FTIR spectra revealing the successful grafting of phosphorus-containing groups (P-O, P-O-P, PO43−) on PBC and Zn-OH moieties on ZBC. BET analysis showed that PBC and ZBC achieved specific surface areas of 781.34 and 557.46 m2/g, respectively—77 and 55 times higher than that of BC (10.09 m2/g)—while total pore volume increased from 0.03 cm3/g (BC) to 0.43 cm3/g (PBC) and 0.31 cm3/g (ZBC), with average pore diameters of 2.20-2.25 nm characteristic of mesoporous structures; XRD patterns further confirmed the presence of phosphate crystals (PDF#25-0408) on PBC and ZnCl2 phases (PDF#74-0517) on ZBC, providing structural bases for electrostatic attraction and ion exchange. Adsorption kinetics revealed that NH4+ uptake on both modified biochars proceeded rapidly within the first 60 min and reached equilibrium at 240 min, with the pseudo-second-order model providing superior fits (R2 > 0.95) compared to the pseudo-first-order model and yielding calculated equilibrium adsorption capacities (231.35 mg/g for PBC, 218.31 mg/g for ZBC) that closely matched experimental values (232.66 and 224.18 mg/g, respectively)—approximately 50-fold higher than that of BC (4.51 mg/g)—thereby confirming chemisorption as the dominant rate-controlling mechanism. When applied to real swine wastewater containing coexisting cations (Na+, K+, Ca2+, Mg2+), the NH4+ adsorption capacities of PBC and ZBC decreased by 19.22% and 39.66%, respectively, under optimal conditions (35℃, pH 7, 360 min), with competitive adsorption and surface site coverage by coexisting ions—particularly the precipitation of phosphates with Ca2+/Mg2+ for PBC and the preferential exchange of Na+/K+ at Zn–OH sites for ZBC—identified as the primary inhibitory mechanisms via ion concentration monitoring and speciation analysis. Mechanistic analysis indicates that PBC enhances NH4+ adsorption through: 1) physical pore filling enabled by its highly developed porosity; 2) electrostatic attraction between negatively charged phosphate groups (PO) and NH4+;3) ion exchange via H+ release from –OH and –COOH groups; and (iv) cation–π interactions with the aromatic carbon skeleton, whereas ZBC primarily relies on: 1) ion exchange between Zn-OH and NH4+; 2) improved physical adsorption due to ZnCl2-induced pore development; and 3) supplementary cation–π interactions. A preliminary cost assessment based on laboratory-scale production estimates the unit cost of modified biochar at 62.85–64.85 CNY/kg, significantly lower than commercial activated carbon (200-300 CNY/kg) and ion-exchange resins (>1000 CNY/kg), highlighting its economic viability. This study demonstrates that distillers’ grains-derived biochar modified via H3PO4 or ZnCl2 impregnation is a highly efficient, low-cost, and environmentally sustainable adsorbent for NH4+ removal from both synthetic and real wastewater, providing a waste-to-resource strategy that valorizes an industrial by-product while addressing the pressing challenge of aquatic nitrogen pollution; future research should focus on column adsorption performance, adsorbent regeneration, and field-scale validation in integrated wastewater treatment systems.

     

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