污泥流化床焚烧产物的重金属排放特性研究

采用小型流化床装置对西湖底泥和四堡污泥进行燃烧实验。用原子吸收法测量污泥及不同温度燃烧产物中Cu、Cr、Cd、Hg等重金属元素,分析金属元素在燃烧过程中的排放特性。     

Methodological and Practical Considerations for Developing Multiproject Baselines for Electric Power and Cement Industry Projects in Central America

The Lawrence Berkeley National Laboratory (Berkeley Lab) and the Center for Sustainable Development in the Americas (CSDA) conducted technical studies and organized two training workshops to develop capacity in Central America for the evaluation of climate change projects. This paper describes the results of two baseline case studies conducted for these workshops, one for the power sector and one for the cement industry, that were devised to illustrate certain approaches to baseline setting. Multiproject baseline emission rates (BERs) for the main Guatemalan electricity grid were calculated from 2001 data. In recent years, the Guatemalan power sector has experienced rapid growth; thus, a sufficient number of new plants have been built to estimate viable BERs. We found that BERs for baseload plants offsetting additional baseload capacity ranged from 0.702 kgCO2/kWh (using a weighted average stringency) to 0.507 kgCO2/kWh (using a 10th percentile stringency), while the baseline for plants offsetting load-following capacity is lower at 0.567 kgCO2/kWh. For power displaced from existing load-following plants, the rate is higher, 0.735 kgCO2/kWh, as a result of the age of some plants used for meeting peak loads and the infrequency of their use. The approved consolidated methodology for the Clean Development Mechanism yields a single rate of 0.753 kgCO2/kWh. Due to the relatively small number of cement plants in the region and the regional nature of the cement market, all of Central America was chosen as the geographic boundary for setting cement industry BERs. Unfortunately, actual operations and output data were unobtainable for most of the plants in the region, and many data were estimated. Cement industry BERs ranged from 205 kgCO2 to 225 kgCO2 per metric ton of cement.     

医院污水处理系统工艺改进的研究初探

通过对昆明某医院污水处理系统工艺两次改造的实验研究表明：医院污水经深化处理后比未经深化处理污水的COD、SS、氨氮、色度、粪大肠菌群数都大幅度降低，达到了GB18466-2005《医疗机构水污染物排放标准》和GB18920-2002《城市污水再生利用城市杂用水水质》中冲厕及绿化用水。建议循环再利用。     

流化床电偶反应器

探讨了流化床电偶反应器的工作原理 ,阐述了流化床电偶反应器的结构特点及工艺性能 ,重点介绍了该反应器对多种有机废水和重金属离子废水净化的作用。     

厌氧酸化-二级PSB流化床工艺处理高浓度有机废水

采用厌氧酸化+二级光合细菌(PSB)流化床的组合工艺对植物压榨发酵废水进行降解实验,一级流化床(PSB1)中填料为轻质多孔炭渣,二级流化床(PSB2)为活性炭,扰动方式分别采用机械流化和机械气动组合流化,稳定运行40d。结果表明,进水酸化12h后CODCr由80000~120000mg/L降至63000~95000mg/L,进而由系统出水回流稀释至8000~12000mg/L,进入二级流化床反应器,PSB1白天厌氧光照、夜间微好氧,PSB2白天微好氧、夜间好氧,停留48h,CODCr降至295.8~384mg/L,稳定实现96.2%以上的CODCr去除率,TN去除率为71.3%。     

双循环流化床烟气悬浮脱硫技术工业化试验研究

在一台75t/h电站燃煤锅炉上，设计建造了基于双循环流化床烟气悬浮脱硫技术工艺的脱硫装置，烟气处理量为140000m^3/h，该脱硫装置主要特征是循环灰采用两经分离，内外双重循环方式和石灰浆液采用多层喷浆方式。介绍了该装置的系统组成、工作原理、工艺流程、工业化实验结果。实际表明：当Ca/S=1.3,△T=10℃时，脱硫效率达90%；固体颗粒物的循环使脱硫效率提高15%左右。     

Mechanisms of granular activated carbon anaerobic fluidized-bed process for treating phenols wastewater

ＩｎｔｒｏｄｕｃｔｉｏｎＢｅｆｏｒｅｔｈｅ 1 980ｓｃｏｎｖｅｎｔｉｏｎａｌｔｒｅａｔｍｅｎｔｐｒｏｃｅｓｓｅｓｏｆｐｈｅｎｏｌｓｗａｓｔｅｗａｔｅｒａｒｅｓｏｌｖｅｎｔｅｘｔｒａｃｔｉｏｎ ,ｐｈｙｓｉｃａｌａｄｓｏｒｐｔｉｏｎ ,ｃｈｅｍｉｃａｌｏｘｉｄａｔｉｏｎａｎｄａｅｒｏｂｉｃｂｉｏｌｏｇｉｃａｌｐｒｏｃｅｓｓ.Ａｍｏｎｇｔｈｅｂｉｏｌｏｇｉｃａｌｕｎｉｔｐｒｏｃｅｓｓｅｓａｃｔｉｖａｔｅｄｓｌｕｄｇｅｐｒｏｃｅｓｓｉｓｍａｉｎｏｎｅ.Ａｆｔｅｒｔｈｅ 1 980ｓａｎａｅｒｏｂｉｃｂｉｏｌｏｇｉｃ…     

废旧家电产品回收性能评价指标体系的建立

针对家电产品回收工艺流程决策评价的多阶段、多目标的特点,以及不同类型家电产品和不同回收工艺过程的动态特性,采用层次分类方法建立了以经济指标和环境指标为主要内容的回收工艺流程评价指标体系,对指标体系的组成进行了较为详细的分析,讨论了应该考虑的因素及有关计算方法。以电冰箱为例,用改进的模糊层次分析法与遗传算法相结合,介绍了回收工艺流程的优化决策方法。建立的指标体系不仅可以根据评价对象进行动态修改,而且具有较强的可操作性。     

三唑磷农药废水厌氧处理可行性研究

采用厌氧流化率工艺处理在唑磷农药废水，必须降低原水中ＮＨ３－Ｎ含量，调整营养比例，当ＣＯＤ：Ｎ：Ｐ＝（１８０～２００）：５：１时，在中温厌氧消化条件下，ＣＯＤ含量可从４１７０ｍｇ／ｌ，去除率约５０％，沼气产率达到０．２５６ｍ＾３／ｍ＾３．ｄ。因此，把厌氧处理作为好氧处理的预处理单元，能确保整个处理系统出水达标。     

电场耦合高效液相色谱柱改善极性芳烃分离的研究

从燃烧的煤和油中排放出来的极性污染物,包含有多种含氮、氧和硫的极性多环芳烃(PAH),这些极性组分比非极性组分常具有更强的致癌和致突变性。目前,正相高效液相色谱(NP-HPLC)常被用来分离分析这类极性组分。 但是,要提高这些极性组分分离的选择性,现大多采用梯度洗脱的方法。也就是改变流动相极性的方法。本文介绍了一种高压电场耦合色谱柱的新方法。这种技术除了具