加压活性炭生物膜法处理DSD有机废水

采用加压活性炭生物膜法处理以对硝基甲苯磺酸盐为主的难降解的有机废水的研究,是在活性炭生物膜法处理有机废水基础上发展起来的新技术。本实验结果表明,在加压9.8×10~4Pa(1kgt/cm~2)的条件下,COD_(Cr)去除率为62％～70％,比常压活性炭生物膜法高20％～25％;其容积负荷Nv=1.7～2.9kgCOD/m~3·d,比一般活性污泥法高3～6倍。     

污水处理厂污泥中磷的回收

磷是一种不可再生而又面临枯竭的重要资源。为控制水体富营养化,污水处理厂采用生物除磷脱氮工艺把污水中的磷转移到污泥中以除去;由此形成富磷污泥,为实现污泥磷回收创造了条件。并介绍了三种从污水处理厂剩余污泥中回收磷的工艺:污泥水解回收磷的工艺(KREPROProcess和Cambi-KREPROProcess)和从污泥焚烧灰中回收磷的工艺(BioConProcess)。这些工艺可以以磷酸铁或磷酸的形式回收污泥中约75%的磷。     

汽车内二氧化碳污染与通风模式

不同车速下,对四种通风模式(A关闭通风口和风扇、B关闭通风口打开风扇、C打开通风口关闭风扇、D打开通风口和风扇)车内二氧化碳浓度进行分析研究。通风口关闭的状态,无论是否打开风扇及车速快慢,车内CO2浓度严重超标。通风口打开:不开风扇,以50km/h速度行驶,车内CO2浓度高于标准限量;速度提高到80km/h,车内CO2浓度可低于标准限量,通风口和缝隙的换气可以保障车内的空气质量;而打开风扇可以有效排除车内污染物。车速提高,各种通风模式的换气量都增加,属于缝隙换气贡献的比例增加,属于风扇换气贡献的比例减小,属于通风口换气贡献比例变化不大。基于研究结果,提出了一些减少车内污染的通风方式建议。     

黄土高原人工刺槐林土壤团聚体中不同活性有机碳从南到北的变化特征

不同粒径团聚体中的不同活性有机碳对人工林土壤质量改善及碳库动态平衡有重要的作用.本研究在黄土高原地区,从南向北沿着降雨和温度降低梯度选择淳化、安塞、绥德和神木共4个地区,比较研究了人工刺槐林土壤团聚体不同的活性有机碳含量变化及其影响因素.通过湿筛法将土壤团聚体分级为粉黏粒（<0.053 mm）、微团聚体（0.25~0.053 mm）和大团聚体（>0.25 mm）,用Leffory法测定3种粒径土壤团聚体低、中、高活性有机碳含量.结果表明：①4个样区大团聚体（>0.25 mm）含量由南至北呈先降低后增加趋势,微团聚体（0.25~0.053 mm）含量逐渐增加,粉黏粒（<0.053 mm）含量则先增后减.②4个样区中土壤团聚体3种活性有机碳含量大小顺序为低活性 > 中活性 > 高活性,其中,粉黏粒（<0.053 mm）低活性有机碳含量为1.02~1.52 g·kg^-1,中活性有机碳含量为0.53~0.91 g·kg^-1,高活性有机碳含量为0.28~0.43 g·kg^-1;而微团聚体（0.25~0.053 mm）低活性有机碳含量为1.02~2.02 g·kg^-1,中活性有机碳含量为0.46~1.20 g·kg^-1,高活性有机碳含量为0.31~0.85 g·kg^-1;大团聚体（>0.25 mm）低活性有机碳含量为1.08~3.07 g·kg^-1,中活性有机碳含量为0.70~1.96 g·kg^-1,高活性有机碳含量为0.48~1.24 g·kg^-1.③黄土高原人工刺槐林3种粒径团聚体的低、中、高活性有机碳含量主要与年均气温（MAT）、年均降雨量（MAP）、土壤SOC、TN和含水率显著相关（p<0.05）,且在同一活性下,活性有机碳含量与MAT、MAP、土壤TN、SOC、含水率的相关性随着土壤团聚体粒径的增大而越显著.研究结果对理解黄土高原土壤团聚体活性有机碳含量在空间尺度上的变化特征和影响因素具有重要意义.     

Will Simplified Modalities and Procedures Make More Small-Scale Forestry Projects Viable Under the Clean Development Mechanism?

Simplified modalities and procedures (M&P) are expected to increase the viability of small-scale project activities under the Clean Development Mechanism (CDM). A small-scale afforestation or reforestation (AR) project is defined as a project removing less than 8 kilotons of carbon dioxide equivalent (CO₂e) per year. Depending on the project type and the method for measuring scale, 8 kilotons of CO₂e per year correspond to highly diverse areas, possibly ranging from 200 to 6000 ha. Using a model to calculate the minimum project scale above which the CDM is a positive financial incentive for eligible AR project activities, the paper analyzes whether a reduction of transaction costs under simplified M&P will be a sufficient incentive to motivate small-scale participation in the CDM. Model results show that, even under optimistic assumptions on carbon market conditions and transaction costs, small-scale project activities will not benefit from simplified M&P. Results also show that project activities removing more than 8 kilotons of CO₂e per year and registered as small-scale would be the ones that could benefit the most from simplified M&P. It is concluded that the participation of small-scale project activities to the CDM requires more than simplified M&P, the price of expiring Certified Emission Reductions being one of the most critical parameters.     

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.     

Carbon Dioxide Balance of Wood Substitution: Comparing Concrete- and Wood-Framed Buildings

In this study a method is suggested to compare the net carbon dioxide (CO₂) emission from the construction of concrete- and wood-framed buildings. The method is then applied to two buildings in Sweden and Finland constructed with wood frames, compared with functionally equivalent buildings constructed with concrete frames. Carbon accounting includes: emissions due to fossil fuel use in the production of building materials; the replacement of fossil fuels by biomass residues from logging, wood processing, construction and demolition; carbon stock changes in forests and buildings; and cement process reactions. The results show that wood-framed construction requires less energy, and emits less CO₂ to the atmosphere, than concrete-framed construction. The lifecycle emission difference between the wood- and concrete-framed buildings ranges from 30 to 130 kg C per m² of floor area. Hence, a net reduction of CO₂ emission can be obtained by increasing the proportion of wood-based building materials, relative to concrete materials. The benefits would be greatest if the biomass residues resulting from the production of the wood building materials were fully used in energy supply systems. The carbon mitigation efficiency, expressed in terms of biomass used per unit of reduced carbon emission, is considerably better if the wood is used to replace concrete building material than if the wood is used directly as biofuel.     

Preparation and performance of photocatalytic regenerationable activated carbon prepared via sol-gel TiO2

Preparation of photocatalytic regenerationable activated carbon （AC） is the key step for the practical application of in situ regeneration of exhausted AC. A novel photocatalytic regenerationable AC was prepared by sol-gel TiO2 in this work. The adsorption and regeneration performance of TiO2/AC were evaluated using phenol as model compound. Scanning electron microscope （SEM） and nitrogen （77 K） adsorption isotherm were used to determine the surface area, pore structure and the distribution of TiO2. The results showed that with the increase of TiO2 loading, adsorption capacity of TiO2/AC decreased and the regeneration efficiency increased. The photocatalytic regenerationable AC with suitable TiO2 loading （2 wt%） exhibited suitable adsorption capacity and regeneration efficiency. TiO2 located mainly in the entrance of macro-pore of carbon. The prepared TiO2/AC exhibited similar surface structure and pore structure with material carbon.     

Photocatalytic degradation of L-acid by TiO2 supported on the activated carbon

Introduction Aromatic sulfonic acid, which is produced in large amounts in chemical industry since the end of 19th century, has been widely applied in many industrial processes, including the various steps of procedure (Alonso and Barcelo, 2000). Naphthalene- sulfonic acids are of importance as dye intermediates and commonly used in the textile auxiliary industry employing many azo dyes and pigments. Among them, 1-naphthol-5-sulphonic acid (L-acid) is widely used in the printing as the raw ma…     

载甲苯活性炭微波脱附再生试验

研究了利用微波对载甲苯饱和活性炭的辐照再生。从甲苯的脱附和回收率2个方面探讨了活性炭再生的工艺条件。得出工艺的最佳条件：微波功率为500W、载气流速为300mL／min、辐射时间3min、活性炭量为10g。