Sources of underground CO: Crushing and ambient temperature oxidation of coal

As a harmful gas in underground coal mine, CO seriously threatened the safety of miners. Currently, the spontaneous combustion of residual coal in goaf is generally considered as the main source of underground CO. CO gas is also widely used as an indicator gas in fire prediction in mines. However, high concentrations of CO are also detected in some mines without spontaneous combustion of coal. Therefore, in the paper, with four ranks of coal, we studied other two potential CO sources: crushing and oxidation at ambient temperature. The more completely crushed coal produces more CO. The concentration of generated CO is inversely proportional to moisture content in coal. Therefore, the addition of water can inhibit the generation process of CO during the crushing process of coal. Lignite with low metamorphic grade can be oxidized to produce CO at ambient temperature (25 °C), and anthracite with high coal rank can be only oxidized to produce CO at 60 °C. Infrared spectra indicated that the coal with rich aliphatic hydrocarbons and oxygen-containing functional groups are more susceptible to oxidation at room temperature. Moreover, the smaller particle size of coal is more beneficial to the oxidation at ambient temperature to generate CO. CO generation during coal oxidation is also closely related to the ventilation rate.     

微生物絮凝剂M-C11处理高岭土悬浊液的响应曲面优化

采用响应曲面法对微生物絮凝剂M-C11处理高岭土悬浊液的过程参数进行优化,选取中心复合实验设计(CCD),以p H、M-C11投加量和Ca Cl2投加量等因素为自变量,以处理后的高岭土悬浊液絮凝率(Fr)为响应值,并借助扫描电镜对絮凝剂的作用机理进行初步探讨。结果表明,微生物絮凝剂M-C11可显著改善高岭土悬浊液的絮凝性能,且选取的3种单因素水平均可影响絮凝剂活性。经多元回归拟合分析,在M-C11投加量为2.56 m L,Ca Cl2投加量为0.37 g/L的最优条件下,微生物絮凝活性实验值可达92.37%,接近模型预测值(92.30%)。Ca Cl2投加量对絮凝效果的影响高于M-C11投加量(PCa Cl2相似文献   

不同混凝剂处理松花江低温水

东北松花江地区冬季有将近6个月的冰封期,低温季节水源水处理难度大。为了保证东北地区冬季饮用水供应,研究几种混凝剂在处理冬季松花江低温水时的混凝效果。实验结果表明,NPAC1和NPAC2水解产物中具有较高的Alb和Alc成分,拥有较高的电中和、吸附和网捕卷扫性能,高效聚铝铁(PAF)水解产物Fe(OH)3具有比表面积大、吸附架桥作用较强的优点。这3种混凝剂无论是在控制出水浊度还是在对水体有机物去除能力方面均优于目前水厂所使用的PAC和聚合氯化铝铁(水厂PAF);NPAC2的投加量达到50 mg/L时,出水浊度达到最优;当混凝剂投加量达到50 mg/L时,NPAC1的浊度去除率逐渐超过NPAC2,剩余浊度低于3.0 NTU;NPAC1、NPAC2和PAF 3种混凝剂对有机物的去除能力大致相当,当混凝剂投加量为50 mg/L时,这3种混凝剂处理后的水的UV254的值均低于0.06,而水厂使用的2种混凝剂处理后的水的UV254仍高于0.1;结合其对浊度去除的情况,可以判断55 mg/L的投药量为NPAC1的最优投药点,PAF的最佳投药量为65 mg/L;投加适量的粉末活性碳可以有效地提高氨氮的去除率,当粉末活性炭的投加量为30 mg/L时,氨氮的去除率基本达到最大(51.27%)。表面负荷对混凝效果具有重要的影响,合理降低沉淀池的表面负荷对于提高出水水质具有重要作用。     

固相萃取-高效液相色谱法测地表水中11种酚类化合物

建立了固相萃取-高效液相色谱法同时测定地表水中11种酚类化合物的方法。水样经过全自动固相萃取仪富集,以HLB柱为萃取柱,乙腈(含1%乙酸)为洗脱剂,用高效液相色谱仪分析定量。该方法在0.5~5.0 mg/L范围内线性良好,相关系数为0.999 6~0.999 9,11种酚类化合物的纯水加标回收率为82.0%~111%,地表水加标回收率为98.5%~116%,精密度为3.58%~4.67%,检出限为1×10-4~5×10-4mg/L,该方法简单实用、准确可靠,可用于地表水中酚类化合物的同时测定。     

“十三五”期间中国生态环境质量变化特征

以国家生态环境监测网监测结果为基础,总结归纳了"十三五"时期中国生态环境质量变化特征和主要环境问题。结果表明:"十三五"期间,全国生态环境质量全面好转,2020年环境空气优良天数比例比"十二五"末期上升5.8个百分点;地表水总体水质由轻度污染转为良好,Ⅰ～Ⅲ类水质断面比例上升17.4个百分点,劣V类断面比例下降9.0个百分点;酸雨污染程度减轻,海洋等环境要素质量稳中向好。但与此同时,后续改善难度加大,全国仍有40%地级及以上城市空气质量超标,4.8%的国土面积发生酸雨,辽河和海河流域仍是轻度污染,部分河流污染较重,地下水以IV类水质为主,农村饮用水源地和地表水水质均受到不同程度污染,近三分之一国土面积县域生态质量为较差和差。总体来看,当前生态环境质量与人民对美好生态环境的需求和美丽中国目标的实现还有较大差距。逐年上升的能源消费总量和不断增长的汽车保有量,增加了生态环境质量继续改善的压力。     

竹制填料生物接触氧化工艺处理污染河水简

针对受污染的湖溪河水质特征，以传统弹性塑料填料做对比，研究以竹球和竹丝为填料的生物接触氧化工艺，考察填料的挂膜时间、生物量和污水处理效果；确定连续曝气和间歇曝气时反应器的最优运行工况：连续曝气时为HRT=7.5 h，DO=3 mg/L；间歇曝气时为厌氧1.2 h、好氧6.3 h交替运行。实验结果表明，与弹性塑料填料相比，竹制填料挂膜速度快，竹球填料的水处理效果最好；连续曝气最优工况下竹球填料反应器中COD、TN、NH₃-N和TP的平均去除率分别为66.7%、47.9%、57.1%和30.6%；间歇曝气最优工况下竹球填料反应器中COD、TN、NH₃-N和TP的平均去除率分别64.08%、39.95%、60.7%和54.68%；竹制填料可替代传统的塑料填料作为生物接触氧化工艺的载体填料。     

微磁场条件下pH冲击对微氧活性污泥表面性质的影响

研究了微磁场条件下pH冲击对处理低负荷葡萄糖废水的微氧活性污泥表面性质的影响。在pH=6.0和9.0的条件下对添加磁粉和无磁粉反应器微氧活性污泥进行15 d的冲击,而后调整pH=7.5进行5 d的恢复实验。对pH冲击下污泥絮凝能力FA、疏水性RH和表面电荷SC的变化情况进行考察,结果表明,有磁粉反应器的各项指标均优于无磁粉反应器。经过5 d的恢复实验,添加磁粉反应器污泥的各指标均能恢复到接近初始值,而无磁粉反应器污泥难以恢复到接近初始值。     

石英砂滤料表面润湿改性

采用硅烷偶联剂、钛酸酯偶联剂和铝酸酯偶联剂对石英砂进行表面改性,以制备亲油疏水性滤料。研究得出,钛酸酯偶联剂改性石英砂的最佳工艺条件为:偶联剂用量15%,反应温度90℃,搅拌时间15 min;硅烷偶联剂和铝酸酯偶联剂改性石英砂的最佳工艺条件均为:偶联剂用量15%,反应温度110℃,搅拌时间15 min。水对钛酸酯偶联剂改性石英砂滤料的润湿重量由改性前的1.5589 g降低到0.0282 g,水对硅烷偶联剂改性石英砂滤料的润湿重量降低到0.0607 g,水对铝酸酯改性石英砂滤料的润湿重量降低到0.2664 g。静态吸附实验表明,硅烷偶联剂、钛酸酯偶联剂和铝酸酯偶联剂改性石英砂滤料对油的吸附容量分别增加了33.67%、42.87%和22.30%。XPS和FT-IR分析表明,偶联剂均以化学键的方式包覆在石英砂滤料表面,结合稳定。     

Multi-response optimization of Fenton process for applicability assessment in landfill leachate treatment

Fenton process, as a pretreatment method, was found to be effective in the primary treatment of mature/medium landfill leachate. However, the main problem of the process is the large amount of produced sludge that requires an accurate feasibility evaluation for operational applications. In this study, the response surface methodology was applied for the modeling and optimization of Fenton process in three target responses, (1) overall COD removal, (2) sludge to iron ratio (SIR) and (3) organics removal to sludge ratio (ORSR), where the latter two were new self-defined responses for prediction of sludge generation and applicability assessment of the process, respectively. The effective variables included the initial pH, [H₂O₂]/[Fe²⁺] ratio and Fe²⁺ dosage. According to the statistical analysis, all the proposed models were adequate (with adjusted R² of 0.9116–0.9512) and had considerable predictive capability (with prediction R² up to 0.9092 and appropriate adequate precision). It was found that all the variables had significant effects on the responses, specifically by their observed role in dominant oxidation mechanism. The optimum operational conditions obtained by overlay plot, were found to be initial pH of 5.7, [H₂O₂]/[Fe²⁺] ratio of 17.72 and [Fe²⁺] of 195 mM, which led to 69% COD removal, 2.4 (l sludge/consumed mole Fe²⁺) of SIR and 16.5 (gCOD removed/l produced sludge) for ORSR in verification test, in accordance with models-predicted values. Finally, it was observed that [H₂O₂]/[Fe²⁺] ratio and Fe²⁺ dosage had significant influence on COD removal, while Fe²⁺ dosage and [H₂O₂]/[Fe²⁺] ratio had remarkable effects on SIR and ORSR responses, respectively.     

燃煤电厂在线监测系统颗粒物浓度排放系数影响因素的探讨

选取上海市7家未安装气-气换热器的国控燃煤电厂作为研究对象，从煤质、除尘器、脱硫协同脱除作用以及锅炉工况负荷等方面探讨对颗粒物浓度排放系数 K值产生的影响，得出上述因素通过改变脱硫进口颗粒物浓度值影响 K值，当脱硫进口颗粒物浓度较低、波动范围较小时，其 K值也维持相对稳定的状态；当脱硫进口颗粒物浓度较高、波动范围较大时，其 K值也会发生较大的变化等结论。