控制煤中SO2排放的技术对策分析

在分析我国煤炭资源状况、煤中硫的赋存状态和燃煤引起的SO2污染状况的基础上，探讨了国内外控制SO2排放的研究现状，研究了燃烧前、燃烧中和燃烧后三大类脱硫方法的可行性与适用范围。研究认为，对洗选脱硫要先对煤中硫的赋存状态进行研究，否则效率难以得到保证；固硫剂脱硫比较适合我国国情，但脱硫效率有待提高。固硫剂脱硫和洗选脱硫可结合使用，以提高脱硫率。     

砷污染稻作区发展旱稻控制稻米砷暴露风险探讨

农田砷污染是我国中南、西南稻作区面临的重要环境问题之一。水稻淹水种植条件下,土壤砷的溶解度较高,其移动性和生物有效性较大,水稻根系易吸收并向地上部转移砷。而在非淹水富氧条件下,土壤砷的移动性、生物有效性及稻米砷累积量显著降低。本文在综述水分管理影响水稻砷吸收基础上,提出：砷污染稻作区可通过水改旱、发展旱稻种植,显著降低土壤砷的生物有效性;在非淹水种植、降低土壤砷活性基础上,可通过筛选砷低吸收基因型旱稻,进一步控制水稻砷吸收和稻米砷累积,实现砷污染稻作区农产品质量安全保障与水危机缓解的双赢。目前,关于旱稻对砷的胁迫响应及对砷的吸收、转运与代谢研究鲜见报道,无疑,相关工作值得深入开展。     

环境砷污染与健康

本文论述了环境砷污染对健康的影响,包括砷中毒、机理、危害及分析方法。     

黄河上游水体中砷的来源及迁移初探

在对黄河上游水体及沿岸表层土壤、底泥中的砷进行监测分析的基础上,对水体中砷的来源、迁移过程进行了初步探索。结果表明:黄河上游沿岸土壤中砷的含量偏高,水体中的砷来源于沿岸的土壤。     

饮用水中砷去除技术综述

自从1996年孟加拉国和印度报道慢性砷中毒事件以来，饮用水砷污染和砷中毒问题就受到全世界的关注。如何解决这一难题，研究人员进行了大量研究。本文综述了饮用水中砷的去除方法，包括混凝／沉淀、吸附、离子交换技术等，对各种除砷技术进行了总结和比较。     

HPLC—ICP—MS法测定农业废水中有机砷与无机砷的方法研究

建立了应用高效液相色谱（HPLC）和电感耦合等离子质谱（ICP—Ms）联用技术测定农业水环境样品中三价砷（Aslll）、一甲基砷（MMA）、二甲基砷（DMA）、五价砷（AsV）4种砷形态的分析方法。试验表明,4种砷形态的线性范围宽（1-300μg·L-1）,相关系数（r）均大于0．9990,方法检出限低（0．7～0．98μg·L-1）,精密度好,重复测定7次结果的RSD均小于5％。通过计算加标回收率验证方法的准确性,加标回收率为94％～112％。实际样品的测定结果显示,农田废水中砷的主要存在形态为As（V）,其次为As（Ⅲ）。     

准确测定水中砷应注意的问题

砷的化合物在自然界普遍存在且均有剧毒，在环境监测中，砷是常规化验项目之一。本文对砷的测定方法、样品的预处理、干扰物的排除等有关问题进行了探讨。     

成都地区典型土壤与农作物中砷含量研究

成都地区土壤和农作物中砷污染研究资料不多，本文以成都地区7类典型土壤和该土壤上生长的10余种常见农作物中的砷含量为研究对象，通过对监测数据的整理、分析，应用正态分布、方差分析、线性相关检验等方法对土壤和农作物中砷的分布规律以及两者的关系进行了比较详尽的分析和研究，并对比了国内相关研究结果，说明了成都地区土壤和农作物中砷污染的规律和相关性。     

SCR 催化剂的砷中毒研究

催化剂是SCP系统的重要组成部分,研究催化剂中毒的原因,对延长催化剂的使用寿命及降低SCR系统的运行费用意义重大.本文介绍了煤燃烧过程中砷的迁移规律,利用实验的方法测定出氧化砷浓度与催化剂中毒的关系,建立了砷中毒后NOX反应速率的动力学方程,并利用国外几组SCR数据对方程进行了验证,计算值和实际值相吻合.文章并对如何降低砷的危害提出了建议.     

土壤中砷的污染控制技术研究

土壤砷污染修复是世界性的难题,日益受到人们的密切关注。本文阐述了土壤砷污染的现状、危害及其来源,探讨土壤砷污染的传统物理化学和生物修复技术的研究现状及特点的同时,重点阐述了纳米材料修复技术,尤其是纳米铁技术,并对土壤砷污染修复研究方向进行了展望。     

Coal Combustion Product: Nonhazardous Material for Mine Fill

As is the case in many other countries around the world, India's main source of electricity is coal‐fired power plants. In addition to providing energy, the burning of coal also results in large amounts of coal combustion products (CCP), the incombustible material, such as fly ash, left after the coal is burned. These materials are produced in large volume, and if they are not managed or utilized properly, they can pose a danger to the environment. This article discusses the uses of CCP, with a special emphasis on fly ash, and the role that it is currently playing and can continue to play as a mine filler for India's depleted opencast and underground coal mines.     

Utilization of coal combustion by-products in sustainable construction materials

Solid waste management is gaining significant importance with the ever-increasing quantities of industrial by-products and wastes. With the environmental awareness and scarcity of space for landfilling, wastes/by-product utilization has become an attractive alternative to disposal. Several industrial by-products are produced from manufacturing processes, service industries and municipal solid wastes. Some of these industrial by-products/waste materials could possibility be used in cement-based materials.Coal combustion by-products (CCBs) represent incombustible materials left after combustion of coal in conventional and/or advanced clean-coal technology combustors. These include fly ash, bottom ash, boiler slag, and flue gas desulfurization (FGD) by-products from advanced clean-coal technology combustors. This paper briefly describes various coal combustion products produced, as well as current best recycling use options for these materials. Materials, productions, properties, potential applications in manufacture of emerging materials for sustainable construction, as well as environmental impact are also briefly discussed.     

Oxy-fuel coal combustion—A review of the current state-of-the-art

Carbon dioxide emissions will continue being a major environmental concern due to the fact that coal will remain a major fossil-fuel energy resource for the next few decades. To meet future targets for the reduction of greenhouse gas (GHG) emissions, capture and storage of CO₂ is required. Carbon capture and storage technologies that are currently the focus of research centres and industry include: pre-combustion capture, post-combustion capture, and oxy-fuel combustion. This review deals with the oxy-fuel coal combustion process, primarily focusing on pulverised coal (PC) combustion, and its related research and development topics. In addition, research results related to oxy-fuel combustion in a circulating fluidised bed (CFB) will be briefly dealt with.During oxy-fuel combustion, a combination of oxygen, with a purity of more than 95 vol.%, and recycled flue gas (RFG) referred to as oxidant is used for combusting the fuel producing a gas consisting of mainly CO₂ and water vapour, which after purification and compression, is ready for storage. The high oxygen demand is supplied by a cryogenic air separation process, which is the only commercially available mature technology. The separation of oxygen from air as well as the purification and liquefaction of the CO₂-enriched flue gas consumes significant auxiliary power. Therefore, the overall net efficiency is expected to be decreased by 8–12% points, corresponding to a 21–35% increase in fuel consumption. Alternatively, ion transport membranes (ITMs) are proposed for oxygen separation, which might be more energy efficient. However, since ITMs are far away from becoming a mature technology, it is widely expected that cryogenic air separation will be the selected technology in the near future. Oxygen combustion is associated with higher temperatures compared with conventional air combustion. Both fuel properties as well as limitations of steam and metal temperatures of the various heat exchanger sections of the boiler require a moderation of the temperatures in the combustion zone and in the heat-transfer sections. This moderation in temperature is accomplished by means of recycled flue gas. The interdependencies between the fuel properties, the amount and temperature of the recycled flue gas, and the resulting oxygen concentration in the combustion atmosphere are reviewed.The different gas atmosphere resulting from oxy-fuel combustion gives rise to various questions related to firing, in particular, with respect to the combustion mechanism, pollutant reduction, the risk of corrosion, and the properties of the fly ash or its resulting deposits. In this review, detailed nitrogen and sulphur chemistry was investigated in a laboratory-scale facility under oxy-fuel combustion conditions. Oxidant staging succeeded in reducing NO formation with effectiveness comparable to that typically observed in conventional air combustion. With regard to sulphur, a considerable increase in the SO₂ concentration was measured, as expected. However, the H₂S concentration in the combustion atmosphere in the near-flame zone increased as well. Further results were obtained in a pilot-scale test facility, whereby acid dew points were measured and deposition probes were exposed to the combustion environment. Slagging, fouling and corrosion issues have so far been addressed via short-term exposure and require further investigation.Modelling of PC combustion processes by computational fluid dynamics (CFD) has become state-of-the-art for conventional air combustion. Nevertheless, the application of these models for oxy-fuel combustion conditions needs adaptation since the combustion chemistry and radiative heat transfer is altered due to the different combustion gas atmosphere.CFB technology can be considered mature for conventional air combustion. In addition to its inherent advantages like good environmental performance and fuel flexibility, it offers the possibility of additional heat exchanger arrangements in the solid recirculation system, i.e. the ability to control combustion temperatures despite relatively low flue gas recycle ratios even when combusting in the presence of high oxygen concentrations.     

Large eddy simulation of oxy-coal combustion in an industrial combustion test facility

Oxy-fuel combustion is considered as one of the most promising technologies for carbon capture and storage (CCS). In this study, a commercial computational fluid dynamics (CFD) code has been employed for the simulation of an air-fired coal combustion and an oxy-fired coal combustion with recycled flue gas in a 1 MW_th combustion test facility. Reynolds–averaged Navier–Stokes (RANS) solutions have been obtained for both cases. Results indicate that the CFD code with existing physical sub-models can provide a reasonable prediction for the air-fired combustion. However, the prediction for the oxy-fired case has not been as satisfactory as expected. In order to assess the impact of the turbulence treatment in CFD on the predictions, large eddy simulation (LES) has been performed for oxy-fired case and compared with the results from the RANS simulation and the available experimental data. Although the results suggest that LES can provide a more realistic prediction of the shape and the physical properties of the flame, there has not been significant improvement in the prediction of the temperature. In addition, the complexity of the problem requires more detailed experimental data for the validation of the LES. In order to improve the validity of numerical simulations for design purposes, further modelling improvements for oxy-coal combustion that are necessary for more accurate predictions are addressed. Based on this study, it is envisaged that the complexity in the oxy-coal combustion process requires more detailed analyses of the available physical sub-models.     

A novel process integration,optimization and design approach for large-scale implementation of oxy-fired coal power plants with CO2 capture

The widespread use of fossil fuels within the current energy infrastructure is considered as the largest source of anthropogenic emissions of carbon dioxide, which is largely blamed for global warming and climate change. At the current state of development, the risks and costs of non-fossil energy alternatives, such as nuclear, biomass, solar, and wind energy, are so high that they cannot replace the entire share of fossil fuels in the near future timeframe. Additionally, any rapid change towards non-fossil energy sources, even if possible, would result in large disruptions to the existing energy supply infrastructure. As an alternative, the existing and new fossil fuel-based plants can be modified or designed to be either “capture” or “capture-ready” plants in order to reduce their emission intensity through the capture and permanent storage of carbon dioxide in geological formations. This would give the coal-fired power generation units the option to sustain their operations for longer time, while meeting the stringent environmental regulations on air pollutants and carbon emissions in years to come.Currently, there are three main approaches to capturing CO₂ from the combustion of fossil fuels, namely, pre-combustion capture, post-combustion capture, and oxy-fuel combustion. Among these technology options, oxy-fuel combustion provides an elegant approach to CO₂ capture. In this approach, by replacing air with oxygen in the combustion process, a CO₂-rich flue gas stream is produced that can be readily compressed for pipeline transport and storage. In this paper, we propose a new approach that allows air to be partially used in the oxy-fired coal power plants. In this novel approach, the air can be used to carry the coal from the mills to the boiler (similar to the conventional air-fired coal power plants), while O₂ is added to the secondary recycle flow as well as directly to the combustion zone (if needed). From a practical point of view, this approach eliminates problems with the primary recycle and also lessens concerns about the air leakage into the system. At the same time, it allows the boiler and its back-end piping to operate under slight suction; this avoids the potential danger to the plant operators and equipment due to possible exposure to hot combustion gases, CO₂ and particulates. As well, by integrating oxy-fuel system components and optimizing the overall process over a wide range of operating conditions, an optimum or near-optimum design can be achieved that is both cost-effective and practical for large-scale implementation of oxy-fired coal power plants.     

多环芳烃污染与防治对策

多环芳烃是一类已被证实具有致癌作用的碳氢化合物，它不仅可以诱发皮肤癌，还可诱发肺癌。列出１６种多环芳烃的化学性质和致癌的强弱程度，并且从燃煤和油田开发角度出发分析了多环芳烃的污染情况，提出了具体防治对策。     

锅炉燃煤的最佳方式

从节能、环保、资源开发并重并举的高度,探讨了锅炉燃煤的最佳方式和技术经济的可行性,认为先热解后燃烧,特别是以廉价氢源进行加氢热解后再燃烧是锅炉燃煤的最佳方式。     

China: Energy and environment

Some of China's most prominent environmental problems are related to energy The air pollution of the cities and industrial centers is caused by the inefficient combustion of coal. Deforestation is due to a certain extent to the procurement of firewood. Further problems are caused by the ash and slag from coal combustion and the oil pollution of the sea. While most of China's air is still clean, pollution levels in the cities surpass by far those of German industrial towns, and the health effects are becoming apparent The problem of deforestation must be considered still more serious because it affects whole regions. Short-term effective solutions to the problems presented are not available     

Thermodynamic and Economic Aspects of the Hard Coal Based Oxyfuel Cycle

The present study shows a new approach in modelling the hard coal fired Oxyfuel Cycle on the whole. The static process model comprises an Oxyfuel combustion principle applied to an existing state-of-the-art hard coal power plant located in Rostock, Germany. It includes the air separation unit and the flue gas liquefaction unit, which are modelled in detail. As one of the main advances to previous work, the closed simulation of all components in one model delivers a coherent solution with a significantly reduced number of assumptions. The model needs no interfaces between different stand alone simulation tools or manual iteration and transfer of internal variables. Results from a thermodynamic and economic feasibility study on this process are shown and areas relevant for future research are identified.

The present study shows the feasibility and prospective key figures of the technology under realistic, comparable and reproducible assumptions and boundary conditions. The basic engineering of the process with a detailed study of the necessary gas separation and flue gas handling technologies is undertaken in the effort to a first stage optimisation of the process.

The flowsheet tool Aspen Plus (TM) was used to simulate the overall process. This particular tool was chosen because it offers an advanced data library on chemical substances and allows the calculation of phase equilibria and real gas behaviour during air separation and flue gas liquefaction. Emissions, coal consumption and investment costs of the Oxyfuel power plant are compared to those of the original state-of-the-art hard coal power plant which is used as the reference case.     

我国煤炭开采和燃烧过程中的硫污染对土壤环境的影响

我国煤炭在开采和燃烧过程中形成的硫污染物主要是酸性矿井水和二氧化硫,由煤炭燃烧造成的硫的干湿沉降以及煤炭开采过程中形成的酸性矿井水使土壤的物理化学性质发生变化,从而对土壤造成严重的破坏。主要表现在造成土壤中可溶性硫酸盐的大幅度升高;引起土壤的pH值下降;植物营养元素特别是K、Na、Ca、Mg等产生淋失;活性铝溶出量增加;有毒重金属活化;抑制土壤酶的活性等方面。可以通过脱硫除尘、加强绿化、建立合理的工业布局、加入土壤改良剂等措施来减少硫污染物的排放量和改善其对土壤环境的影响,但总量控制是关键,是最根本的途径。