农村水环境保护与经济可持续发展

我国的生态环境问题 ,如水土流失、草场退化、沙漠化、盐渍化等问题 ,归根到底还是农村水环境问题。本文分析了农村水环境保护、高效利用水资源的紧迫性 ,以及影响农村生态系统可持续性的因素和保护、改善农村水环境的主要措施 ;认为加强农村水环境保护及其持续发展能力的建设是我国整个社会特别是农村经济可持续发展的基本保障     

Carbon Emission by Soils in Forests Damaged by the Siberian Moth

In the southern-taiga low grass–green moss fir forest completely defoliated by the Siberian moth, the rate of soil respiration in the third year after the pest population outbreak was 1.5 times higher than in an undisturbed tree stand. This was explained by a significant increase in the abundance and activity of soil microorganisms in the pest-defoliated forest, which occurred due to the qualitative changes in the litter composition and the increased temperature and moisture in the upper soil layers. The rate of carbon emission from the soil in the defoliated forest was 41.7 kg/ha per day, compared to 28.3 kg/ha per day in the undisturbed fir forest.     

中国城镇化道路的反思与对策

改革开放加速了我国的城镇化进程。从1978年至2010年,城镇化率由17.92%迅速提高到49.95%,形成了长三角、珠三角、京津冀三大城市群,一批区域性城市群正在加速形成。城镇化的快速发展特别是城市群的形成为推动我国经济社会发展和增强国际竞争力发挥了重要作用。但与此同时,城镇化也带来了突出的可持续发展问题。主要表现在:人口过度膨胀,城市病集中爆发,经济增长与宜居性背道而驰;城市面貌千篇一律,野蛮拆迁横行,土地型资本运作难以持续;进城易,定居难,城乡"二元社会"问题正演变为城市内定居群体与流动群体"二元社会"问题;城市间恶性竞争,产业同构,建立分工协作的机制任重道远。基于此,本文提出了未来10年推进我国城镇化的对策思路:坚持积极发展小城市和小城镇方针,缓解地域中心城市人口压力;创新农村居民点用地管理制度,实现城镇化与新农村建设有机统一;加强城市规划与管理的科学化,全力提升城市品位;建立跨区域城市协调机制,破解恶性竞争与产业同构困局;促进公共服务均等化,消除新老"二元社会"问题。     

Study of nitrogen oxide absorption in the calcium sulfite slurry

Experiments were conducted using a bubbling reactor to investigate nitrogen oxide absorption in the calcium sulfite slurry. The effects of CaSO₃ concentration, NO₂/NO mole ratio and O₂ concentrations on NO₂ and SO₂ absorption efficiencies were investigated. Five types of additives, including MgSO₄, Na₂SO₄, FeSO₄, MgSO₄/Na₂SO₄ and FeSO₄/Na₂SO₄, had been evaluated for enhancing NO₂ absorption in CaSO₃ slurry. Results showed that CaSO₃ concentration had significant impact on NO₂ and SO₂ absorption efficiencies, and the highest absorption efficiencies of SO₂ and NO₂ could reach about 99.5 and 75.0 %, respectively. Furthermore, the NO₂ absorption was closely related to the NO₂/NO mole ratio, and the existence of NO₂ in flue gas may promote NO absorption. The presence of O₂ in simulated flue gas was disadvantage for NO _x removal because it can oxidize sulfite to sulfate. It was worth pointing out that FeSO₄/Na₂SO₄ was the best additive among those investigated additives, as the NO₂ removal efficiency was significantly increased from 74.8 to 95.0 %. IC and in situ FTIR results suggest that the main products were NO₃ ^? and NO₂ ^? in liquid phase and N₂O, N₂O₅ and HNO₃ in gas phase during the CaSO₃ absorption process.     

生物絮凝剂MBFGA1预处理乳制品加工废水

用生物絮凝剂MBFGA1预处理乳制品加工废水（简称废水）。实验结果表明,废水处理的水力条件为：以150r／min的转速搅拌30S,再以30r／min的转速搅拌20min;MBFGA1的最佳加入量为15mg／L;废水pH为4．0时,MBFGA1对废水的絮凝处理效果最好;废水温度对浊度、COD去除率有一定的影响,在20～45℃时,废水浊度的去除率始终保持在85％以上;30℃时,COD去除率达到最大值65．0％。     

流动注射分光光度法测定水中铝的含量

以桑色素作显色剂,采用流动注射分光光度法测定水中铝的含量。在桑色素质量浓度为0．8g／L、聚氧乙烯辛基苯基醚体积分数为1．0％、进样环体积为400μL、检测波长420nm的条件下,采用流动注射分光光度法对水中铝的含量进行测定,本方法的线性范围为2～300μg／L,检出限（信噪比为3）为0．124μg／L,相对标准偏差为2．9％,加标回收率为96．4％～101．8％。     

Fe_2O_3/膨润土微波诱导氧化处理染料废水

以膨润土为载体,采用直接沉淀法制备了Fe2O3/膨润土负载型催化剂。制备催化剂的最佳工艺条件:硝酸铁质量浓度为8.08g/L,硝酸铁与膨润土质量比为1.0,焙烧温度为350℃,焙烧时间为3h。用Fe2O3/膨润土负载型催化剂微波诱导氧化处理50mL质量浓度为50mg/L的模拟活性嫩黄废水的最佳工艺条件:催化剂加入量为0.5g,微波功率为900W,微波作用时间为5min。在此条件下模拟活性嫩黄废水脱色率达96.40%。微波诱导氧化处理模拟活性嫩黄废水的反应符合一级反应动力学方程。     

流动注射催化光度法测定环境水样中的痕量亚硝酸根

基于在pH为2.7的一氯乙酸缓冲溶液中亚硝酸根对溴酸钾氧化亮绿具有催化作用,建立了测定环境水样中痕量亚硝酸根的流动注射催化光度法。在室温下,当溴酸钾浓度为0.15mol/L、亮绿溶液浓度为1.12×10-3mol/L时,该方法的线性范围为0.04～0.36mg/L,检出限为7.44×10-4mg/L,测定频率为60次/h,相对标准偏差为1.1%(n=11)。     

Energy recovery from grass using two-phase anaerobic digestion

Municipal solid wastes are major sources of air, water and soil contamination. There is a need for alternative waste management techniques to better utilize the waste and minimize its adverse environmental impact. A two-phase pilot-scale bio-fermentation system was used to evaluate the feasibility of producing methane from grass waste, a major constituent of solid wastes. The bi-phasic system consists of a solid phase and a methane phase. Leachate is re-circulated through the solid phase until a desired level of volatile fatty acid (VFA) is accumulated in the leachate. The leachate is then transferred to the methane reactor where the VFA is converted to methane. The results showed that 67% of the volatile solids in the waste can be converted into soluble chemical oxygen demand in a period of six months. The system produced an average of 0.15 m3 of methane per kg of grass. The average methane concentration in the produced gas was 71%. A mathematical model was developed to estimate the methane and carbon dioxide concentrations in the gas phase as a function of reactor properties.