孙翠华：我国将采取10大措施实现2020年减排目标

国家发改委应对气候变化司副司长孙翠华6月27日在应对气候变化与绿色低碳发展高级别国际研讨会上说,为实现到2020年单位国内生产总值（GDP）二氧化碳排放比2005年下降40％至45％的目标,促进经济社会可持续发展,我国将在10个方面采取措施。     

Genotoxicity removal of reclaimed water during ozonation

Genotoxicity in wastewater and reclaimed water now is gaining increased attention because of genotoxins' potential damage to the ecosystem and human health. The effect of ozonation on genotoxicity in reclaimed water was investigated. It was found that ozonation decreased the genotoxicy dramatically in three tertiary treatment plants. In the further batch ozonation experiment in laboratory,secondary effluent sample used exhibited the genotoxicity of(41.1 ± 4.1) μg 4NQO/L. Ozonation with a dose of 10 mg O3/L completely removed the genotoxicity in secondary effluent. However,after ozonation, the dissolved organic carbonvalue of the sample didn't change much but the specific ultraviolet absorbance(SUVA) value dropped sharply. With the help of Fourier transform infrared spectroscopy, ozonation was found to change chemical aliphatic carbon and C–O of the dissolved arganic matter, which might be the reason of the significant decreases of SUVA and genotoxicity.     

Fouling distribution in forward osmosis membrane process

Fouling behavior along the length of membrane module was systematically investigated by performing simple modeling and lab-scale experiments of forward osmosis （FO） membrane process. The flux distribution model developed in this study showed a good agreement with experimental results, validating the robustness of the model. This model demonstrated, as expected, that the permeate flux decreased along the membrane channel due to decreasing osmotic pressure differential across the FO membrane. A series of fouling experiments were conducted under the draw and feed solutions at various recoveries simulated by the model. The simulated fouling experiments revealed that higher organic （alginate） fouling and thus more flux decline were observed at the last section of a membrane channel, as foulants in feed solution became more concentrated. Furthermore, the water flux in FO process declined more severely as the recovery increased due to more foulants transported to membrane surface with elevated solute concentrations at higher recovery, which created favorable solution environments for organic adsorption. The fouling reversibility also decreased at the last section of the membrane channel, suggesting that fouling distribution on FO membrane along the module should be carefully examined to improve overall cleaning efficiency. Lastly, it was found that such fouling distribution observed with co-current flow operation became less pronounced in counter- current flow operation of FO membrane process.     

Two-step accelerated mineral carbonation and decomposition analysis for the reduction of CO2 emission in the eco-industrial parks

Carbon dioxide（CO2） emissions are a leading contributor to the negative effects of global warming. Globally, research has focused on effective means of reducing and mitigating CO2 emissions. In this study, we examined the efficacy of eco-industrial parks（EIPs） and accelerated mineral carbonation techniques in reducing CO2 emissions in South Korea.First, we used Logarithmic Mean Divisia Index（LMDI） analysis to determine the trends in carbon production and mitigation at the existing EIPs. We found that, although CO2 was generated as byproducts and wastes of production at these EIPs, improved energy intensity effects occurred at all EIPs, and we strongly believe that EIPs are a strong alternative to traditional industrial complexes for reducing net carbon emissions. We also examined the optimal conditions for using accelerated mineral carbonation to dispose of hazardous fly ash produced through the incineration of municipal solid wastes at these EIPs. We determined that this technique most efficiently sequestered CO2 when micro-bubbling, low flow rate inlet gas, and ammonia additives were employed.     

Review of the progress in preparing nano Ti02： An important environmental engineering material

TiO2 nanomaterial is promising with its high potential and outstanding performance in photocatalytic environmental applications, such as CO2 conversion, water treatment, and air quality control. For many of these applications, the particle size, crystal structure and phase, porosity, and surface area influence the activity of TiO2 dramatically. TiO2 nanomaterials with special structures and morphologies, such as nanospheres, nanowires, nanotubes, nanorods, and nanoflowers are thus synthesized due to their desired characteristics. With an emphasis on the different morphologies of TiO2 and the influence factors in the synthesis, this review summarizes fourteen TiO2 preparation methods, such as the sol-gel method, solvothermal method, and reverse micelle method. The TiO2 formation mechanisms, the advantages and disadvantages of the preparation methods, and the photocatalytic environmental application examples are proposed as well.     

钦州湾无机氮入海通量及其富营养化症状分析

根据对环钦州湾区域的入海河流、直排海污染源及养殖废水无机氮入海通量的估算,2011年钦州湾无机氮入海通量约为7 655 t,其中入海河流无机氮入海通量占总量的96.4%,直排海污染源次之。入海无机氮占钦州湾无机氮总量的比重为36.7%,说明钦州湾已属中等强度人为影响海域。根据对钦州湾富营养化症状——叶绿素a含量的分析,钦州湾富营养化症状不明显,钦州湾整体的富营养化程度较低。因而仅以营养盐含量评价目标海域的富营养化程度,易失之偏颇,宜结合富营养化症状来判断目标海域的富营养化程度。     

冬季东海、南黄海中DMS和DMSP浓度分布及影响因素研究

于2011年12月~2012年1月现场测定了东海、南黄海表层海水中二甲基硫(DMS)及其前体物质二甲巯基丙酸内盐(DMSP分为溶解态DMSPd和颗粒态DMSPp)的含量,研究了它们的浓度分布规律及其影响因素,并对DMSPp的粒级分布和DMS的海-气通量进行了探讨.结果表明,表层海水中DMS、DMSPd和DMSPp的浓度分别在0.58~4.14、0.37~7.86和4.29~25.76 nmol·L-1之间,平均值分别为(2.20±0.82)、(2.12±1.66)和(11.98±6.23)nmol·L-1.DMS、DMSPp与叶绿素a(Chl-a)呈现明显的正相关关系,并且它们的周日变化趋势基本一致,说明浮游植物生物量是影响研究海域内DMS和DMSP生产分布的关键因素.另外,DMSPd浓度和总细菌丰度表现出一定的负相关,这可能是在细菌释放的DMSP裂解酶的作用下DMSPd会发生裂解生成DMS.研究发现,5~20μm的微型浮游植物是海区内Chl-a和DMSPp的主要贡献者.此外,冬季东海、南黄海表层海水DMS的海-气通量在0.61~25.52μmol·(m2·d)-1之间,平均值为(8.30±5.92)μmol·(m2·d)-1.     

生物活性炭投加量对垃圾渗滤液处理效果的影响

试验对比了不同生物活性炭(biological activated carbon,BAC)投加量对垃圾渗滤液去除COD效果的影响.每升活性污泥中活性炭投加量为0、100、300 g的反应器处理垃圾渗滤液100个周期平均COD去除率分别为12.9%、19.6%、27.7%,表明BAC可以去除部分难降解有机物,并且COD去除率与投加量呈正相关关系.曝气8 h反应器中二氧化碳(CO2)产生量依次为109、193、306 mg,表明生物分解量也与投加量呈正相关关系.分析认为COD去除率与投加量的正相关关系是由于吸附与生物再生的共同作用导致,生物再生是BAC能够生物分解难降解有机物的根本原因.     

1980~2010年浙江某典型河流硝态氮通量对净人类活动氮输入的动态响应

以浙江某典型流域为研究对象,基于1980～2010年的水质水量和氮源数据及LOADEST模型,估算了逐年河流NO-3-N通量和净人类活动氮输入(NANI),分析了河流NO-3-N通量和NANI的年际演化特征及其动态响应关系,探讨了每年NANI、滞留氮库、自然背景源对河流NO-3-N通量的贡献.结果表明,1980～2010年,河流NO-3-N通量和NANI总体上都呈现出先增后减的抛物线型变化趋势,均在1998年左右分别达到峰值5.74 kg·(hm2·a)-1和77.5 kg·(hm2·a)-1;过去31 a,河流NO-3-N通量和NANI分别净增加了～42%和～77%.化肥氮和大气氮沉降是NANI的主要来源,分别占了NANI的～48%和～40%.河流NO-3-N通量的年际变化不仅与NAIN(R2=0.27**)和化肥氮输入量(R2=0.32**)显著相关,而且与河流年均流量(R2=0.79**)或降雨量(R2=0.63**)具有更强的相关性,意味着河流NO-3-N的来源除了当年的NAIN,还受滞留氮库的影响.所建立的以NANI和流量为自变量的回归模型能很好地模拟河流NO-3-N通量变化(R2=0.94**).该模型预测结果显示,在NANI和流量分别降低30%的情况下,河流年均NO-3-N通量将分别减少～21%和～30%;每年的NANI、滞留氮库、自然背景源对河流当年NO-3-N通量的贡献率分别为～53%、～24%、～23%.河流NO-3-N通量长期的年际变化是NANI和水文要素共同作用的结果;但是,由于滞留氮库的影响,与源控制方式相比,增加"汇"景观应该能更加快速地削减河流NO-3-N通量.     

京津冀区域生产和消费CO2排放的时空特点分析

区分消费和生产二氧化碳排放是对开放的经济区域进行排放责任划分的基础,日渐受到政策制定者的关注.利用经济投入产出-生命周期分析模型,对京津冀区域1997年、2002年和2007年的消费和生产二氧化碳排放时空特征及二氧化碳排放平衡进行分析.结果表明,京津冀区域消费和生产二氧化碳排放呈约4%的年均增长;贸易隐含二氧化碳排放比例为30%~83%,并以国内贸易隐含二氧化碳排放为主;河北的消费和生产二氧化碳排放占区域主导,增速和二氧化碳排放强度高于北京和天津;京津冀区域为二氧化碳排放净流入区域,存在部分排放责任转移;京津为二氧化碳排放净转入地区,冀为二氧化碳排放净转出地区;京津冀三地二氧化碳排放关键部门分布集中且相似度较高,可以考虑区域联合控制.其中,电力、蒸汽、热水生产和供应业和金属冶炼及压延加工业对二氧化碳排放的依赖性最大,承担较大的其他部门的二氧化碳排放责任.投入产出分析解析了地区生产和消费二氧化碳排放情况,有利于区域减排的精细化管理和制定相应对策,并促进区域减排合作.