土地复垦投资的政策法规建议

土地复垦投资的政策法规是为了克服市场经济本身的缺陷和不足,规范生产建设者（当事者）的行为以及强化其社会意识和责任,确保土地复垦投资机制的形成和运作。本文分析了我国土地复垦投资的相关政策和法规的现状和问题,有针对性地提出了一些政策和法规建议,且对《土地复垦规定》提出了具体的修改建议。     

植物遗传资源保护与利用的市场化机制和国际制度

随着植物物种资源的不断减少和因生物技术迅猛发展对植物遗传资源需求的不断增加 ,植物遗传资源正逐步由公共物品转变为稀缺物品。坚持《生物多样性公约》所确立的遗传资源效益公平分享原则 ,完善现有国际多边体系 ,促进以“遗传编码功能”价值概念和遗传资源保护效应“内部化”与“补偿”方案为基础的植物遗传资源市场化保护与利用机制的形成 ,建立“植物遗传资源交易所”和“生物多样性合作社” ,将有助于提高世界各国尤其是发展中国家保护植物遗传资源的积极性 ,实现全球植物遗传资源的可持续利用     

排放系数法估算污染物排放总量

掌握污染物总量动态变化情况，采用排放系统法进行估算是有效的方法。利用１９９５年上海乡镇工业污染调查数据对排放系数进行验证，说明应如何选用排放系数。     

多环芳烃的几种理化参数与LC_(50)的相关性研究

对多环芳烃(PAHS)4种理化参数(K;W、Sw。X Vv。)与 LCO的相关关系进行了研究,建立了 4种一元线性回归方程。结果表明,4种参数的相关系数分别为:0.刀66、08083、09488、0.9570,经r检验,后两种属高度显著相关.用所建立的一元线性回归方程对7种PAHS的LC。进行估算,估算值与实测值相比,平均相对误差分别为58.84％、32.23％、1761％、198％,用l和V＊.H对LClj进行估算的估算精度也较高。经比较,提出用(。估算P＊比对麦穗鱼＊CO的新方法。     

黔中地区二级阶地堆积物边坡稳定性对工程建设的影响

结合在建工程清水河大花水电站实例,本文对黔中地区二级阶地堆积物边坡成因、堆积物物质成份、结构与其物理力学特性作了分析、总结,初步探讨了贵州省二级阶地堆积物边坡稳定性对工程建设的影响,望能给正在进行工程建设的同行以一定的参考,并对工程建设区的二级地堆积物边坡稳定性引起重视。     

NBIAS中污泥龄对脱氮除磷效果的影响

探讨无回流间歇曝气系统 (简称 NBIAS) ,处理城市污水的污泥龄 ( SRT)对脱氮除磷及有机物去除效果的影响。通过原污水流程试验和人工合成污水静态模拟实验 ,试验结果表明 :在水温为 2 0℃～ 30℃ ,污泥负荷为 0 .2 5～0 .45kg CODcr/ kg MLSS· d,SRT为 1 8～ 2 2 d,HRT为 8～ 1 0 h时 ,利用原污水作为碳源 ,NBIAS在保持较高的 CODcr去除率的同时 ,总氮和总磷的去除率均在 80 %以上。     

钢铁企业富余煤气制甲醇与二甲醚的研究

利用钢铁联合企业的富余煤气,制甲醇与二甲醚.提出合理可行的工艺方案,进行主要物料消耗计算和成本估算,得出在工艺上和经济上可行的结论.项目的实施,能实现钢铁联合企业资源综合利用,提高企业的经济效益,同时对实现能源的多样化、发展新型清洁能源、改善生态环境都具有重要意义,其经济效益和社会效益显著.     

Removal of high concentrated ammonia nitrogen from landfill leachate by landfilled waste layer

The landfill of municipal solid waste(MSW) could be regarded as denitrification reactor and involved in ammonia nitrogen biological removal process. In this research, the process was applied to municipal solid waste collected in Shanghai, China, which was characterized by high food waste content. The NH4^ removal efficiency in the system of SBR nitrifying reactor followed by fresh and matured landfilled waste layer in series was studied. In the nitrifying reactor, above 90% of NH4^ in leachate was oxidized to NO2^- and NO3^- . Then high concentrated NO2^- and NO3^- were removed in the way of denitrification process in fresh landfilled waste layer. At the same time, degradation of fresh landfilled waste was accelerated. Up to the day 120, 136.5 gC/(kg dry waste) and 17.9 gN/(kg dry waste) were converted from waste layer. It accounted for 50.15 % and 86.89 % of the total carbon and nitrogen content of preliminary fresh waste, which was 4.42 times and 5.17 times higher than that of reference column respectively. After filtering through matured landfilled waste, BOD5 concentration in leachate dropped to below 100 mg/L, which would not affect following nitrification adversely. Because the matured landfilled waste acted as a well methanogenic reactor, 23% of carbon produced accumulatively from fresh landfilled waste degradation was converted into CH4.     

Kinetics of continuous biodegradation of pesticide organic wastewater by activated carbon-activated sludge

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LPWCO method for the treatment of high concentrated organic wastewater

Based on wet air oxidation (WAO) and Fenton reagent, thispaper raises a new low pressure wet catalytic oxidation(LPWCO)which requires low pressure for the treatment of highlyconcentrated and refractory organic wastewater. Compared withgeneral wet air oxidation, the pressure of the treatment(0.1-0.6MPa) is only one of tens to percentage of latter(3.5-10MPa). Inaddition, its temperature is no more than 180℃.Compared withFenton reagent, while H2O2/COD(weight ratio) less than 1.2, theremoval of COD in the treatment is over twenty percents more thanFenton's even the value of COD is more than 14000mg/L. In thispaper, we study the effect factor of COD removal and the mechanismof this treatment. The existence of synergistic effect (catalytic oxidation and carbonization) for COD removal in H2SO4-Fenton reagent system under the condition of applied pressure and heating (0.1-0.6MPa, 104-165℃) was verified. The best condition of this disposal are as follows:H2O2/COD(weight ratio)=0.2-1.0, Fe2+ 0.6×10-3 mol, H2SO4 0.5mol, COD>1×104mg/L, the operating pressure is 0.1-0.6MPa and temperature is 104-165℃. This method suit to dispose the high-concentrated refractory wastewater, especially to the wastewater containing H2SO produced in the manufacture of pesticide, dyestuff and petrochemical works.