Phosphorus recovery from biogas fermentation liquid by Ca–Mg loaded biochar

Shortage in phosphorus (P) resources and P wastewater pollution is considered as a serious problem worldwide. The application of modified biochar for P recovery from wastewater and reuse of recovered P as agricultural fertilizer is a preferred process. This work aims to develop a calcium and magnesium loaded biochar (Ca–Mg/biochar) application for P recovery from biogas fermentation liquid. The physico-chemical characterization, adsorption efficiency, adsorption selectivity, and postsorption availability of Ca-Mg/biochar were investigated. The synthesized Ca–Mg/biochar was rich in organic functional groups and in CaO and MgO nanoparticles. With the increase in synthesis temperature, the yield decreased, C content increased, H content decreased, N content remained the same basically, and BET surface area increased. The P adsorption of Ca–Mg/biochar could be accelerated by nano-CaO and nano-MgO particles and reached equilibrium after 360 min. The process was endothermic, spontaneous, and showed an increase in the disorder of the solid–liquid interface. Moreover, it could be fitted by the Freundlich model. The maximum P adsorption amounts were 294.22, 315.33, and 326.63 mg/g. The P adsorption selectivity of Ca–Mg/biochar could not be significantly influenced by the typical pH level of biogas fermentation liquid. The nano-CaO and nano-MgO particles of Ca–Mg/biochar could reduce the negative interaction effects of coexisting ions. The P releasing amounts of postsorption Ca–Mg/biochar were in the order of Ca–Mg/B600 > Ca–Mg/B450 > Ca–Mg/B300. Results revealed that postsorption Ca–Mg/biochar can continually release P and is more suitable for an acid environment.     

Mercury levels and estimated total daily intakes for children and adults from an electronic waste recycling area in Taizhou, China: Key role of rice and fish consumption

In order to assess the potential health risks of Hg pollution, total mercury (T–Hg) and methyl mercury (MeHg) concentrations were determined in air, dust, surface soil, crops, poultry, fish and human hair samples from an electronic waste (e-waste) recycling area in Taizhou, China. High concentrations of T–Hg and MeHg were found in these multiple matrices, and the mean concentration was 30.7 ng/m³ of T–Hg for atmosphere samples, 3.1 μg/g of T–Hg for soil, 37.6 μg/g of T–Hg for dust, 20.3 ng/g of MeHg for rice and 178.1 ng/g of MeHg for fish, suggesting that the e-waste recycling facility was a significant source of Hg. The inorganic Hg (I–Hg) levels (0.84 μg/g) in hair samples of e-waste workers were much higher than that in the reference samples. Pearson''s correlation coefficients showed that strong positive correlations (p < 0.01) between hair I–Hg and time staying in industrial area (r = 0.81) and between MeHg and fish consumption frequency (r = 0.91), imply that workers were mainly exposed to Hg vapor through long-time inhalation of contaminated air and dust, while other population mainly exposed to MeHg through high-frequency fish consumption. The estimated daily intakes of Hg showed that dietary intake was the major Hg exposure source, and Hg intakes from rice and fish were significantly higher than from any other foods. The estimated total daily intakes (TDIs) of MeHg for both children (696.8 ng/(kg·day)) and adults (381.3 ng/(kg·day)) greatly exceeded the dietary reference dose (RfD) of 230 ng/(kg·day), implying greater health risk for humans from Hg exposures around e-waste recycling facilities.     

Analysis of trace dicyandiamide in stream water using solid phase extraction and liquid chromatography UV spectrometry

An improved method for trace level quantification of dicyandiamide in stream water has been developed. This method includes sample pretreatment using solid phase extraction. The extraction procedure (including loading, washing, and eluting) used a flow rate of 1.0 mL/min, and dicyandiamide was eluted with 20 mL of a methanol/acetonitrile mixture (V/V = 2:3), followed by pre-concentration using nitrogen evaporation and analysis with high performance liquid chromatography–ultraviolet spectroscopy (HPLC–UV). Sample extraction was carried out using a Waters Sep-Pak AC-2 Cartridge (with activated carbon). Separation was achieved on a ZIC^®-Hydrophilic Interaction Liquid Chromatography (ZIC-HILIC) (50 mm × 2.1 mm, 3.5 μm) chromatography column and quantification was accomplished based on UV absorbance. A reliable linear relationship was obtained for the calibration curve using standard solutions (R² > 0.999). Recoveries for dicyandiamide ranged from 84.6% to 96.8%, and the relative standard deviations (RSDs, n = 3) were below 6.1% with a detection limit of 5.0 ng/mL for stream water samples.     

Preparation of steel slag porous sound-absorbing material using coal powder as pore former

The aim of the study was to prepare a porous sound-absorbing material using steel slag and fly ash as the main raw material, with coal powder and sodium silicate used as a pore former and binder respectively. The influence of the experimental conditions such as the ratio of fly ash, sintering temperature, sintering time, and porosity regulation on the performance of the porous sound-absorbing material was investigated. The results showed that the specimens prepared by this method had high sound absorption performance and good mechanical properties, and the noise reduction coefficient and compressive strength could reach 0.50 and 6.5 MPa, respectively. The compressive strength increased when the dosage of fly ash and sintering temperature were raised. The noise reduction coefficient decreased with increasing ratio of fly ash and reducing pore former, and first increased and then decreased with the increase of sintering temperature and time. The optimum preparation conditions for the porous sound-absorbing material were a proportion of fly ash of 50% (wt.%), percentage of coal powder of 30% (wt.%), sintering temperature of 1130°C, and sintering time of 6.0 hr, which were determined by analyzing the properties of the sound-absorbing material.     

不同有机废水厌氧产酸过程的研究

主要研究了不同类废弃有机物厌氧产酸过程中产生的挥发性脂肪酸的产量和组成比例。研究发现,废糖蜜溶液、蛋白废液和淀粉废液在达到最高产酸量时,超过50%的VFAs是乙酸,其次是丙酸,还含有少量的丁酸和戊酸。废甘油溶液在达到最高产酸量时,产生的VFAs的主要成分是丙酸。4种有机废液中,相同初始COD浓度条件下,淀粉废液产生的VFAs产量最多,初始COD为5000mg/L时最高产量为2.321g/L,其次是废甘油溶液,最高产量是2.244g/L。     

水和废水中化学需氧量测定方法的改进研究

在水的CODcr测定中,将30 ml回流量确定为常规检测回流量,可节省浓硫酸和硫酸银用量50%;将消解回流时间从120 min缩短为30 min,已满足对地表水和各类废水中CODcr的准确测定,可节省水电费用75%以上,含氯水样中Cl-的掩蔽研究表明:按国标法用10倍Cl-重量的HgSO4 掩蔽Cl-,加标(CODcr =100 mg/L)回收率为110%~120%左右,用30~40倍Cl -重量的HgSO4 掩蔽Cl-,加标回收率为100%左右,对HgSO4 掩蔽Cl-的条件和机理作了适当探讨.另外,采用加入H2 SO4-后加入HgSO4 的方法可减少HgSO4 的耗用量70%以上.     

餐厨垃圾处理设备的现状与发展趋势研究

针对人类社会在日常运转中产生的大量餐厨垃圾,当下最有效的应对措施是发展相关的餐厨垃圾处理产业,以相关的工作模式和工作设备来应对餐厨垃圾的处理工作。由于餐厨垃圾的特殊性,不同于一般的日常生活垃圾,因此餐厨垃圾的处理设备自然也就有独特的特点与性质。当下社会中餐厨垃圾处理设备行业的发展可谓如火如荼,各种各样的餐厨垃圾处理设备应运而生,针对餐厨垃圾处理设备的发展现状与发展趋势详细的探讨,对促进中国餐饮垃圾处理行业的发展具有借鉴意义。     

含氯化工废水TOC和COD的相关性研究

COD和TOC均是表征水体有机污染程度的综合性指标,选取含氯有机化工废水和含氯有机无机混合化工废水2种废水,通过准确测定水样的COD与TOC数值,采用一元线性回归方程对所得数据进行拟合,判定高氯废水中COD与TOC的相关性,建立COD对TOC的转换方程.数据表明,样本水样的TOC与COD之间可以建立相应的线性回归方程,TOC与COD之间存在显著的相关性,证明采用TOC值对COD进行转换是可行的.定量关系验证结果表明,TOC对COD的转换系数是可以准确测定的,确定转换系数后,结果是可靠的.     

高效液相色谱-电感耦合等离子体质谱联用测定生物样品中的有机汞

建立了酸提取-高效液相色谱-电感耦合等离子体质谱联用技术(HPLC-ICP-MS)测定生物样品中甲基汞、乙基汞、苯基汞等3种有机汞的分析方法。鱼肉和贝类样品经盐酸消解,苯萃取,硫代硫酸钠溶液反萃取后,采用醋酸铵/L-半胱氨酸缓冲盐及甲醇体系组成的流动相按一定比例进行梯度洗脱,经前处理的生物样品在液相色谱中经C18柱分离后,进入电感耦合等离子体质谱检测其甲基汞、乙基汞和苯基汞的浓度。3种有机汞化合物均在0.50~50.0μg/L范围内呈现良好的线性关系,线性相关系数(r)均大于0.9998。方法检出限为0.010~0.038mg/kg;3种有机汞样品加标的RSD均小于12.2%;两个水平的加标回收率在50.8~129%。     

有机化学品不同温度下(过冷)液体蒸气压预测模型的建立与评价

(过冷)液体蒸气压(PL)是评价化学品在环境中分配、迁移和归趋行为的重要参数。PL具有较强的温度依附性。发展一种能够精确预测不同环境温度下化学品PL的方法,有助于填补化学品生态风险评估的大量数据缺失。本研究收集整理了661种有机化合物在不同温度下(200~830 K)共计10 478个log PL值。在此基础上,采用偏最小二乘(PLS)回归和支持向量机(SVM)方法,构建了PL的线性和非线性预测模型。结果表明:2种模型均具有良好的拟合度、稳健性及预测能力,SVM模型的预测性能略高于PLS模型(PLS:R2adj.tra=0.912,RMSEtra=0.477,Q2ext=0.910;SVM:R2adj.tra=0.997,RMSEtra=0.092,Q2ext=0.967)。机理分析表明,温度是影响PL的主要因素,温度越高,蒸气压越大;其次,X1sol也影响PL大小,X1sol用来描述分子间的色散作用,分子间色散力越小,蒸气压越大;此外,化合物的氢键个数、极性和分子构型等因素也影响PL大小。采用Wiliams plot方法表征了PLS模型应用域。所建立的模型可用来预测烷烃、烯烃、醇、酮、羧酸、苯、酚、联苯、卤代芳香烃、含N化合物及含S化合物在不同温度下的PL数据。