集中供热项目环境效益分析——以某市集中供热项目为例

介绍了某市新区供热现状,并对预测模型AERMOD的运行参数及数据来源进行了简要说明,根据区内供热现状及采取集中供热方式后新区冬季采暖集中供热锅炉烟气污染物排放源强的变化情况,采用AERMOD模型分别进行了预测。在此基础上,通过对比分析,得出了大型集中供热工程具有明显环境效益的结论。     

连续流序批式活性污泥法

连续流序批式活性污泥法是一种新型污水生物处理工艺，介绍了该工艺的结构组成、流程控制、生物脱氮除磷基本原理、自动化管理以及与其它处理工艺的比较。     

某铁路站区供热系统节能技术改造效果评估

针对某车站供暖成本升高和污染物排放等问题,从热源改造和建筑维护结构改造2个方面提出节能技术改造方案,通过对机组运行情况和围护结构改造情况的现场测试,得到节能技术改造效果良好的结论,并从节能效益、经济效益和环保效益3个方面对站区节能技术改造方案效果进行分析.     

Generation and Quantification of Hazardous Dusts from Coal Mining in the Indian Context

The increasing trend of opencast coal mining in India tends to release huge amounts of dust. But there is no well-defined method of estimating dust emission due to different coal mining activities. This paper examines the sources of dust emission due to coal mining activities, and focuses on the quantification of dust emission with the development and use of emission factors. Because of their site-specific nature, emission factors developed for one site may not give the correct results for another site. In the present investigation, prediction equations are utilized for the development of emission factors. For the applications of this concept, one large opencast coal project of Bharat Coking Coal Ltd. (BCCL) was investigated, and the total amount of dust emitted due to different mining activities was calculated by the utilization of emission factor data, which was estimated to be 9368.2 kg/day. This paper also focuses on the significance of this study in the field of environmental protection and likely impacts of such study. The paper concludes that once the amount of dust generation is estimated, the impact on air quality can be assessed appropriately and a proper air-pollution control strategy can be developed.     

暖风机的可靠性分析与改进

本文介绍了我国出口室内加热器类产品中暖风机在型式试验过程中常见的安全问题,指出其普遍存在的不符合标准的条款和产生的原因,并提出了解决问题的技术途径和预防措施.     

Improving sustainability through effective reuse of product returns: minimizing waste in a batch blending process environment

A case study of a successful reuse program in a batch blending production environment is presented. This program involves not only addressing the company's own potential waste, but also working with distributors and customers to take back and reuse product, thus eliminating the customers' burden of disposal. Implications of the program for downstream supply chain partners are identified and a structured approach for implementation is presented. Modification for use in similar production environments is possible, enhancing sustainability, while providing environmental as well as economic benefits.     

Temperature and feed strategy effects on sulfate and organic matter removal in an AnSBB

The objective of this work was to analyze the interaction effects between temperature, feed strategy and COD/[SO(4)(2-)] levels, maintaining the same ratio, on sulfate and organic matter removal efficiency from a synthetic wastewater. This work is thus a continuation of Archilha et al. (2010) who studied the effect of feed strategy at 30 °C using different COD/[SO(4)(2-)] ratios and levels. A 3.7-L anaerobic sequencing batch reactor with recirculation of the liquid phase and which contained immobilized biomass on polyurethane foam (AnSBBR) was used to treat 2.0 L synthetic wastewater in 8 h cycles. The temperatures of 15, 22.5 and 30 °C with two feed strategies were assessed: (a) batch and (b) batch followed by fed-batch. In strategy (a) the reactor was fed in 10 min with 2 L wastewater containing sulfate and carbon sources. In strategy (b) 1.2 L wastewater (containing only the sulfate source) was fed during the first 10 min of the cycle and the remaining 0.8 L (containing only the carbon source) in 240 min. Based on COD/[SO(4)(2-)] = 1 and on the organic matter (0.5 and 1.5 gCOD/L) and sulfate (0.5 and 1.5 gSO(4)(2-)/L) concentrations, the sulfate and organic matter loading rates applied were 1.5 and 4.5 g/L.d, i.e., same COD/[SO(4)(2-)] ratio (=1) but different levels (1.5/1.5 and 4.5/4.5 gCOD/gSO(4)(2-)). When reactor feed was 1.5 gCOD/L.d and 1.5 gSO(4)(2-)/L.d, gradual feeding (strategy b) showed to favor sulfate and organic matter removal in the investigated temperature range, indicating improved utilization of the electron donor for sulfate reduction. Sulfate removal efficiencies were 87.9; 86.3 and 84.4%, and organic matter removal efficiencies 95.2; 86.5 and 80.8% at operation temperatures of 30; 22.5 and 15 °C, respectively. On the other hand, when feeding was 4.5 gCOD/L.d and 4.5 gSO(4)(2-)/L.d, gradual feeding did not favor sulfate removal, indicating that gradual feeding of the electron donor did not improve sulfate reduction.     

高锰酸盐指数测定方法的探讨

本文对高锰酸盐指数的测定，用直火加热法和水浴加热法两种方法同时进行了对比测定．结果表明，两种方法的精密度和准确度基本一致．     

异养硝化细菌处理氨氮废水及影响因素研究

从生物陶粒反应器中筛选出6株异养硝化细菌,将异养硝化细菌扩大培养后,建立SBR反应器并进行了氨氮去除的试验研究。在SBR反应器进入稳定运行阶段时,可以观察到系统对于氨氮的去除率稳定在82．96％左右,表现出较好的氨氮去除效果;出水亚硝酸盐含量一直维持在较低的水平,其最大值不超过3．84mg·L-1;COD的平均去除率为54．72％,基本实现了同一反应器中的有机物和氨氮的共同去除。异养硝化SBR反应器温度为29℃时,反应器对氨氮和总氮的去除能力最大为82．28％和47．27％;在pH值为8．0时,氨氮去除率最高达到80．15％。C／N〈4．5时,随着C／N比的增加,氨氮和总氮的去除率快速增加;在C/N为6时,氨氮去除率最高达到87．62％。     

城市集中供热联片取暖的效益分析与评价

在对大连市凌水地区实施集中供热前后的环境效益进行定性分析比较的基础上,应用环境经济学的费用效益分析方法,对集中供热的环境效益进行了效益定量化估算,结果表明:实行区域集中供热联片取暖10年后投资费效比为1∶3.3。