树脂相分光光度法测定水中痕量苦味酸

建立了树脂相分光光度法测定水中痕量苦味酸的新方法。该法灵敏度高,表观摩尔吸光系数为1.08×105L/(mol·cm);精密度理想(测定苦味酸质量浓度为5μg/mL的实验5次,相对标准偏差为1.0%);线性范围为0～7.0μg/mL;以3σ衡量,检出限为0.14μg/mL;加标回收率为97%～103%。采用该法直接测定水样中的苦味酸、间接测定烟草中的烟碱,结果令人满意。     

BaO/γ-Al2O3同时吸附脱除一氧化氮和二氧化硫

利用固定床连续流动反应器研究了BaO／γ—Al2O，同时吸附模拟烟气中NO和SO2的工艺条件和再生循环使用性能，对BaO／γ—Al2O3进行了比表面积和程序升温表面反应（TPSR）等表征分析。结果表明，BaO／γ—Al2O3的适宜工艺条件是SO2与NO体积比为2．9～8．4、原料气中O2体积分数大于4．5％、吸附温度448～523K。BaO／γ—Al2O3在循环使用过程中吸附能力下降。与NOXSO吸附催化剂Na2CO3／γ—Al2O3相比，BaO／γ-Al2O3同时吸附SO2和NO的能力大、再生循环使用性能好、适宜的SO2与NO体积比范围宽、热稳定性好。将BaO／γ—Al2O3应用于NOXSO工艺可望提高该工艺的脱硫、脱氮效率。     

厌氧-好氧一体化反应器处理高浓度有机废水的运行特性研究

本实验采用新型厌氧—好氧一体化反应器处理高浓度有机废水,主要研究了系统的启动与运行性能,并对系统的NH3 N去除效果作了初步考察。实验结果表明:在16℃～24℃的自然温度下,采用递增负荷、厌氧和好氧分期启动的方式,系统可在38天内达到较好的启动效果;在系统负荷运行期内,当系统总进水COD浓度平均值为3601 8mg/L,总出水COD浓度平均值为384 0mg/L,系统容积负荷平均值为2 54kgCOD/(m3·d),系统总HRT平均值为35 1h时,系统总COD去除率平均值达90 6%。实验还发现:当进水NH3 N浓度为280 3～350 7mg/L,整个系统的NH3 N去除率在68 5%～91 7%,平均为81 0%。由此说明,本反应器具有很好的COD去除性能和NH3 N去除效果,适合于处理COD浓度高且含有中等NH3 N浓度的有机废水。     

二安替比林甲烷分光光度法测定氯化镁中钛的含量

用盐酸溶解氯化镁样品,以抗坏血酸和焦磷酸钠共同作掩蔽剂,在酸性介质中用二安替比林甲烷分光光度法测定氯化镁中钛的含量,给出了合理的实验条件.     

毛细管柱气相色谱法测定工作场所空气中的丙烯腈

为了建立采用毛细管柱测定工作场所空气中丙烯腈浓度的方法,使用活性炭管采集工作场所空气中的丙烯腈,二硫化碳溶液解吸,毛细管柱分离后,用氢火焰离子化检测器检测。结果显示:丙烯腈的检出限为0.73μg/ml,相关系数为0.9998,解吸效率94.3%～104.7%,相对标准偏差为0.41%～1.0%。因此,该方法灵敏度高、检测准确、操作性强,可提高丙烯腈的检测效率,适用于工作场所空气中丙烯腈的分析。     

Reaction kinetics of waste sulfuric acid using H2O2 catalytic oxidation

The process of recovering waste sulfuric acids using H₂O₂ catalytic oxidation is studied in this paper. Activated carbon was used as catalyst. Main operating parameters, such as temperature, feed rate of H₂O₂, and catalyst dosage, have effects on the removal of impurities from waste sulfuric acids. The reaction kinetics of H₂O₂ catalytic oxidation on impurities are discussed. At a temperature of 90°C, H₂O₂ feeding rate of 50 g (kg waste acid)^?1 per hour, and catalyst dosage of 0.2 wt% (waste acid weight), the removal efficiencies of COD and chrominance were both more than 99%, the recovery ratio of sulfuric acid was more than 95%, and the utilization ratio of H₂O₂ was 88.57%.

Implications: Waste sulfuric acid is a big environmental problem in China. The amount of waste sulfuric acid is huge every year. Many small and medium-sized businesses produced lots of waste acids, but they don’t have an appropriate method to treat and recover them. H₂O₂ catalytic oxidation has been used to treat and recover waste sulfuric acid and activated carbon is the catalyst here. Main parameters, such as temperature, feed rate of H₂O₂, and catalyst dosage, have been investigated. The reaction kinetics are discussed. This method can be economical and feasible for most small and medium-sized businesses.     

Facile Preparation of Chitosan Films for High Performance Removal of Reactive Blue 19 Dye from Aqueous Solution

This study aimed at finding effective strategies for high-performance removal of reactive blue 19 (RB19) dye from aqueous solution. Chitosan (CS) films had been prepared by using solvent casting with mild drying for this purpose. The CS films were characterized by X-ray diffraction, field-emission scanning electron microscopy, and Fourier transform infrared (FTIR) spectroscopy. The performance of RB19 removal using CS were evaluated by varying contact time, solution pH, initial dye concentration, and adsorbent dosage. Adsorption isotherms, kinetics, and desorption were investigated by batch experiments. Results showed that CS films exhibited the optimal adsorption performance for RB19 removal and high maximum adsorption capacities of RB19, which were 799 and 822.4 mg g^?1 at 20 and 40 °C, respectively. Adsorption kinetic data were well described by the pseudo-second-order kinetic model. FTIR analyses further indicated that interactions between RB19 and the CS film occurred during adsorption. The CS films also exhibited satisfactory desorption of RB19 at about 80 % after 30 min of desorption at pH 11. Our study demonstrated that the CS films can be easily prepared and applied for effective removal of RB19 in treatment of wastewater.     

Study on NOx removal from simulated flue gas by an electrobiofilm reactor: EDTA-ferrous regeneration and biological kinetics mechanism

Environmental Science and Pollution Research - The regeneration of EDTA-FeII is a key step in electrobiofilm reduction-integrated systems for NOx removal from industrial boiler flue gas. The...     

Research status,challenges and future prospects of renewable synthetic fuel catalysts for CO2 photocatalytic reduction conversion

Environmental Science and Pollution Research - In recent years, with global climate change, the utilization of carbon dioxide as a resource has become an important goal of human society to achieve...     

Pyrolysis technologies for municipal solid waste: A review

Pyrolysis has been examined as an attractive alternative to incineration for municipal solid waste (MSW) disposal that allows energy and resource recovery; however, it has seldom been applied independently with the output of pyrolysis products as end products. This review addresses the state-of-the-art of MSW pyrolysis in regards to its technologies and reactors, products and environmental impacts. In this review, first, the influence of important operating parameters such as final temperature, heating rate (HR) and residence time in the reaction zone on the pyrolysis behaviours and products is reviewed; then the pyrolysis technologies and reactors adopted in literatures and scale-up plants are evaluated. Third, the yields and main properties of the pyrolytic products from individual MSW components, refuse-derived fuel (RDF) made from MSW, and MSW are summarised. In the fourth section, in addition to emissions from pyrolysis processes, such as HCl, SO₂ and NH₃, contaminants in the products, including PCDD/F and heavy metals, are also reviewed, and available measures for improving the environmental impacts of pyrolysis are surveyed. It can be concluded that the single pyrolysis process is an effective waste-to-energy convertor but is not a guaranteed clean solution for MSW disposal. Based on this information, the prospects of applying pyrolysis technologies to dealing with MSW are evaluated and suggested.