SUSTAINABILITY AT THE LOCAL LEVEL: MANAGEMENT TOOLS AND MUNICIPAL TAX INCENTIVE MODEL

The implementation of sustainable development may seem a simple concept when written on paper. However to carry-out long term actions put forward by the Agenda 21 (AG21) at the local level represents one of the main challenges as municipal governments in general do not have the capacity to effectively implement the process. Regional environmental assessment (REA) has shown to be effective in supporting decision-making not only to correct environmental problems due to past unsustainable social-economic developments but also help local governments to implement sustainable actions. However this requires long-term investments of AG21 plans and projects. The allocation of regular and consistent financial resources is one of the main ingredients for the sustainable development process. But traditional plans and projects financed by national and/or international funds may not be sustainable in the long-term because they become dependent on external funding. Research demonstrate that innovative economic instruments such as ecotaxes represent a feasible alternative to sponsor local sustainability because taxes are collected permanently by the government and could be invested in continuous actions. Ecotaxes experiences have provided important reference to structure a municipal incentive model (MIM) to sponsor AG21’s environmental plans and projects on a long-term (permanent) basis. However sustainable development cannot be solely through economic investments. A comprehensive municipal environmental management scheme (MEMS) has been established to support the incentive model. The scheme seeks not only to improve local institutional framework but also incentive continuous participation of local stakeholders at all levels of society. Participatory events and the provision of incentives (educational and financial) are key to motivate society to protect the environment and support actively the sustainable development process as emphasised in the RIO-92 Conference.     

漓江流域δD和δ18O对蒸发的指示作用

以漓江流域为例查明不同水体之间氢氧稳定同位素组成特征,并探讨氢氧稳定同位素对漓江流域的蒸发过程指示作用.结果表明：流域内不同水体之间,氢氧稳定同位素表现出不同的组成特征,地表水和地下水,在丰水期δD值和δ¹⁸O值要比枯水期更容易富集,地下水的δD值和δ¹⁸O值分布范围较地表水小;随着水温的升高,δ¹⁸O的变化趋势比d-excess明显.从漓江上游到下游高程逐渐下降,河水线的斜率和截距也在逐渐减小,其中漓江下游河水线的斜率和截距要低于当地大气降水线,表明下游受到蒸发作用较强烈;地下河水线、地表河水线在一定程度上偏离当地大气降水线,但偏离程度较小,表明三者之间有很好的水力联系.受温度和湿度的共同影响,漓江干流丰水期河水的蒸发量占最初水体总量的0.7%~9.1%,枯水期河水的蒸发量占最初水体总量的2.6%~9.7%,丰水期的蒸发比例低于枯水期,从上游到下游蒸发比例在逐渐上升.研究区蒸发量估算值为959.40mm,与多年实测值少43.11mm,相对误差4.70%.氢氧稳定同位素对研究区降水、地表水、地下水之间的转换规律具有重要的实际意义,在今后的漓江流域水文研究中有着更加广阔的空间.     

离子液体吸收废印刷线路板热拆解过程中挥发性有机物——基于COSMO-RS模型

模拟废印刷线路板（WPCB）的热拆解过程,分析热拆解过程中的挥发性有机物（VOCs）组分;利用真实溶剂似导体屏蔽（COSMO-RS）模型对浓度较高的污染物进行量子力学模拟,研究离子液体（ILs）组成单元对目标污染物溶解度的影响差异,分析溶解过程中主导分子间作用力类型,确定优选吸收剂;测定不同溶剂进行溶解性,验证模型适用性.结果表明：①乙酸乙酯和环戊酮是浓度较高的VOCs组分,在240和250℃时浓度分别为43.1,153mg/m³和105,252mg/m³,质量百分比总和分别为76.3%和67.3%.②高表面屏蔽电荷密度分布峰、长烷基链阴阳离子和亲电基团的存在可提高乙酸乙酯和环戊酮在ILs中的溶解度.双三氟甲磺酰基亚胺盐（NTf₂^-）类ILs是一类优良吸收剂.静电力和范德华力对溶解过程起主导作用.③COSMO-RS模型可定性和半定量用于预测乙酸乙酯和环戊酮的溶解度.     

北部湾南流江流域土地覆盖及生物多样性模拟

以北部湾独流入海河流南流江流域为研究对象,基于研究区2000年和2015年遥感数据解译的土地利用数据以及社会经济等数据,采用CLUE-S模型对未来2030年生态保护情景、自然增长情景以及粮食安全情景的土地利用格局进行了模拟预测,在此基础上采用InVEST模型对流域过去和未来不同情景的生物多样性进行了评估,探讨了流域生物多样性的生境质量和生境退化程度.结果表明：2000~2015年南流江流域建设用地、园地、水域和未利用地呈现出增加趋势,其中建设用地的增幅最大,而耕地和林地减幅最大.流域土地系统中共存在着34种土地网络转移流关系,上游存在24种,中游20种,下游28种,耕地与建设用地、耕地与林地以及林地与园地之间的转换占到流域总土地利用变化的70.74%.CLUE-S模型模拟未来土地利用的Kappa系数达到0.86,表明模型模拟未来情景的土地利用精度满足要求.2000年、2015年、2030年生态保护情景、2030年自然增长情景以及2030年粮食安全情景流域生境质量总得分和平均得分分别为866630,900357,921055,876231,865370和0.7457,0.7747,0.7925,0.7539,0.7466.2030年3种情景的中上游和下游地区生物多样性都呈现出不同程度的改善趋势,而中游地区则表现出退化趋势.     

Morphology-dependent interfacial interactions of Fe2O3 with Ag nanoparticles for determining the catalytic reduction of p-nitrophenol

In this work,we fabricated three kinds of Ag/Fe_2O_3 model catalysts with different morphologies to study the interfacial interactions between Ag and Fe_2O_3,and how they affected the catalytic activity in hydrogenation of p-nitrophenol was explored.The hydrothermal method was used to synthesize the metal oxide supported silver catalyst,with various morphologies including nanoplates(NPs),nanospheres(NSs),and nanocubes(NCs).The crystal structure,morphology and surface elements of the composite were investigated by various measurements,such as X-ray diffraction(XRD),scanning electron microscopy(SEM),transmission electron microscopy(TEM) and X-ray photoelectron spectroscopy(XPS).The catalytic activity was also evaluated by the reduction of p-nitrophenol to p-aminophenol.It was found that the activities of the above catalysts varied with the morphology of the support.Among them,Ag/Fe_2O_3 NPs promoted the highest performance,Ag/Fe_2O_3 NSs were slightly inferior,and Ag/Fe_2O_3 NCs were the worst.At last,we ascribed the remarkable activity of Ag/Fe_2O_3 NPs to the strong metal-support interactions between Ag and Fe_2O_3.     

Coupling mechanism of activated carbon mixed with dust for flue gas desulfurization and denitrification

To clarify the effect of coking dust, sintering dust and fly ash on the activity of activated carbon for various industrial flue gas desulfurization and denitrification, the coupling mechanism of the mixed activated carbon and dust was investigated to provide theoretical reference for the stable operation. The results show that coking dust had 34% desulfurization efficiency and 10% denitrification efficiency; correspondingly, sintering dust and fly ash had no obvious desulfurization and denitrification activities. For the mixture of activated carbon and dust, the coking dust reduced the desulfurization and denitrification efficiencies by blocking the pores of activated carbon, and its inhibiting effect on activated carbon was larger than its own desulfurization and denitrification activity. The sintering dust also reduced the desulfurization efficiency on the activated carbon while enhancing the denitrification efficiency. Fly ash blocked the pores of activated carbon and reduced its reaction activity. The reaction activity of coking dust mainly came from the surface functional groups, similar to that of activated carbon. The reaction activity of sintering dust mainly came from the oxidative property of Fe₂O₃, which oxidized NO to NO₂ and promoted the fast selectively catalytic reduction (SCR) of NO to form N₂. Sintering dust was activated by the joint action of activated carbon, and both had a coupling function. Sintering dust enhanced the adsorption and oxidation of NO, and activated carbon further promoted the reduction of NO_x by NH₃; thus, the denitrification efficiency increased by 5%-7% on the activated carbon.     

病毒在土壤中的存活时间与传播能力及其影响因素

土壤是病毒在自然界主要的分布场所,也是病毒传播的一种媒介.对流感病毒、肠道病毒、甲型肝炎病毒和冠状病毒在土壤中的存活与传播进行了系统分析,并探究了病毒在土壤中吸附与存活的主要影响因素.结果表明:流感病毒、肠道病毒、甲型肝炎病毒和冠状病毒均能在土壤中存活较长时间,并能以土壤为介质进行传播,进而导致人体暴露;土壤微生物、含水量、土壤类型及温度是影响病毒在土壤中吸附与存活的主要因素,土壤微生物的存在、含水量的降低以及温度的升高可能阻碍病毒在土壤中的存活,黏粒含量及pH较高的土壤中病毒的吸附量与存活率较高,而金属氧化物及有机质含量较高的土壤中病毒的吸附量与存活率较低.基于上述分析,对病毒在土壤中存活与传播的研究提出了有针对性的建议,如系统开展我国土壤病毒的调查研究,加强病毒在土壤中存活、传播规律及影响因素的研究等.研究显示,土壤在病毒的环境传播过程中具有重要作用,不可忽视病毒经土壤传播产生的风险.      

病毒在无生命物体表面存活时间及其影响因素分析

2020年3月11日,世界卫生组织宣布新型冠状病毒肺炎（COVID-19,简称“新冠肺炎”）疫情全球大流行.病毒性传染病在人群中的发生需具备3个相互关联的条件,即传染源、传播途径和易感人群,其中传播途径是一个关键环节.从环境传播的角度,综述了包括SARS（重症急性呼吸综合征）病毒、MERS（中东呼吸综合征）病毒等病毒在无生命物体表面的存活时间及影响因素.结果表明:包括冠状病毒在内的一些具有传染性的病毒能在多种无生命物体表面存活一定时间,进而可能通过物体表面进行环境传播,造成潜在的健康风险;物体材质、温度、湿度以及病毒载量等因素是影响病毒在无生命物体表面存活的主要因素.在上述分析的基础上,对医疗废物和生活垃圾的收集、运输、处理等过程提出了针对性的防控措施,以期对新型冠状病毒（2019-nCoV）以及未来可能出现的其他病毒的环境传播防控对策提供参考.      

洱海北部入湖河流水质特征及其对北部湖区的影响

基于2016—2018年罗时江、弥苴河、永安江及洱海北部湖区监测数据分析,探讨洱海北部入湖河流污染变化特征及对北部湖区的影响。结果表明:1）"北三江"监测断面总磷、COD、氨氮浓度整体稳定在GB 3838—2002《地表水环境质量标准》Ⅱ—Ⅲ类标准限值内,年内污染物浓度变化表现出典型的农业面源污染特征,且受流域内产业模式等的综合影响;2）研究期间,河流首要污染物为TN,旱季次要污染物为COD,雨季为TP。雨季入湖负荷高于旱季,弥苴河污染负荷大于罗时江、永安江。"北三江"入湖TN和TP污染负荷分别占洱海允许负荷的50.1%和59.7%;3）入湖河流的磷元素输入是洱海北部湖区磷污染的重要来源。北部湖区污染物浓度对氮、磷入湖污染负荷相关性次月强于当月,响应存在延迟。筛选环境友好型种植模式,控制"北三江"氮磷入湖负荷,有利于保护洱海水环境。     

CeO2形貌结构对催化湿式空气氧化苯酚性能的影响

采用水热法、沉淀法和溶胶凝胶法制备了3种不同形貌的CeO₂催化材料,并将其用于湿式空气氧化苯酚水溶液过程中,探讨了CeO₂形貌结构对催化湿式氧化苯酚水溶液性能的影响.采用扫描电子显微镜（SEM）、透射电子显微镜（TEM）、X射线衍射（XRD）、程序升温还原（TPR）等手段对CeO₂催化材料进行了表征.结果表明,水热法制备的CeO₂催化材料表现出较好催化性能,主要原因是水热法合成的CeO₂呈现交错的纳米棒状结构,主要暴露（220）晶面,且沿着（220）晶向生长.在反应温度为200℃、空气压力为2MPa、苯酚初始浓度500mg/L的条件下,最终（240min）COD的去除率为95.5%.