烟气排放连续监测系统存在问题及建议

介绍了烟气排放连续监测系统（CEMS）中气态污染物监测子系统、烟尘监测子系统、烟气排放参数监测子系统的配置现状。针对现场CEMS的安装、运营、环保检查、质控比对监测中常见的问题,进行了研究与分析,对分析、校准、测量等关键单元进行了优化,提出了合理改进建议和对策。     

烟气连续监测系统可靠性分析

系统地介绍了200型烟气连续监测系统的对比试验方法，烟气连续监测系统的可靠性等.     

烟尘对光谱法烟气在线监测系统的影响分析

介绍了紫外吸收光谱法烟气在线监测的原理和数据处理方法，分析了烟尘对不同光谱数据处理结果的影响及各方法的优缺点，利用紫外光谱法不仅可以进行烟气排放的在线监测，同时能进行烟尘检测，与其他光谱法相比，差分吸收光谱法计算结果受烟尘的干扰最小，比较适合用于烟气排放在线监测系统。     

燃煤电厂烟气排放连续监测系统验收测试方法

简述了ISO标准和美国EPA关于烟气排放连续监测系统验收测试的相关规定，并详细介绍了我国燃煤电厂烟气排放连续监测系统验收测试方法。     

燃煤电厂烟气污染物连续监测系统的标定与校验

对烟气污染物连续监测系统与车载烟气监测仪进行了同步测试和校验。结果表明：烟气污染物连续监测系统和车载仪器所测数据吻合程度较好,能反映污染的实际排放状况,可供环保管理部门参考。     

浙江省火电厂烟气连续监测系统运行现状及运管方式

介绍了火电厂烟气连续监测系统(CEMS)的类型及系统组成，分析了浙江省火电厂已安装CEMS的现状和存在问题，对系统的运行管理方式进行了探讨，并提出建议。     

对我国火电厂烟气自动监测系统应用情况的分析

本文对烟气自动监测系统在10个电厂的安装、运行情况进行了综合评述，针对引进系统作了详细地收资、调查。     

MSI COMPACT分析仪在火电厂烟气监测中的应用

介绍了ＭＳＩＣＯＭＰＡＣＴ烟气分析仪的性能及该仪器在火电厂烟气ＳＯ２监测中的应用。     

烟气排放连续监测系统在420t/h燃煤锅炉上的应用

铜陵发电厂在1台420t／h燃煤锅炉上应用烟气排放连续监测系统(CEMS)，对锅炉烟气SO2、NOx、颗粒物及相关烟气参数进行在线监测。该系统工作可靠，安装简便，无需专人值守，运行维护量较小，性能指标通过了环境监测部门的标定测试，达到了国家环保总局行业标准的要求。同时，该系统具有实时数据传送功能，提高了环境监测工作的信息化管理水平。     

浅议大型湿法脱硫工程烟气挡板门制造中的问题及对策

烟气挡板门是大型火力发电厂湿法脱硫工程中的重要设备，它通过控制锅炉烟气的流通来实现脱硫装置的投运或退出，其性能好坏直接影响烟气脱硫系统的正常运行。通过分析烟气挡板门在制造过程中存在的主要问题，提出了提高烟气挡板门制造质量的相关措施。     

工业火炬气NOx排放的模拟实验

为准确核定石化企业火炬气NO_x的排放情况,采用模拟火炬燃烧装置对现场采集的不同种类火炬气进行燃烧,取得了燃烧温度及NO_x排放数据。实验结果表明：火炬气的燃烧温度及燃烧烟气中的NO_x质量浓度与火炬气组分中H₂的体积分数呈正相关;兰炭荒煤气、煤甲醇合成驰放气、合成氨变换气和合成氨合成解析气的燃烧温度分别为410,430,560,650℃。通过计算得到4种火炬气的NO_x排放系数分别为：合成氨合成解析气0.3154~0.5406kg/t,煤甲醇合成驰放气0.1245~0.2263kg/t,合成氨变换气0.0591~0.0813kg/t,兰炭荒煤气0.0801~0.1762kg/t。     

油气生产过程中放空燃烧气的检测与回收利用现状

本文对油气生产中放空燃烧气的检测方法进行了总结,并对国内外放空气回收利用的主要技术进行了比较分析。指出:利用遥感监测数据计算放空燃烧气量具有较好的应用前景,但需同地面常规实测数据结合,改进反演算法,以减少不确定性;采用油气混输、天然气发电、压缩天然气（CNG）、液化天然气（LNG）、液态产品转化等回收利用手段将显著减少放空燃烧气带来的温室气体排放。     

湿法烟气脱硫系统中烟气换热器的灰色综合评价

将灰色综合评价分析法引入湿法脱硫系统的烟气换热器综合评价,从技术和经济两个方面探讨了综合评价、优选烟气换热器的方法和过程,并以3种典型的烟气换热器技术为例进行了实际计算,给出了评价结果。     

Air and landfill gas movement through passive gas vents installed in closed landfills

In a closed landfill, Japan, remedial actions have been undertaken to address the inadequate leachate collection and drainage systems. Part of this process included installing many passive gas vents in the landfill to promote stabilization of landfilled waste. This study focused on the gas velocity in vents by conducting tracer tests to elucidate the gas flow via passive gas vents. The gas composition and gas temperature in the vents was also measured.As the gas vents pass through the waste layer, both landfill gas and air flows through the vents. Therefore, passive gas vents can be used to aerate landfilled waste as well as to collect and release landfill gas. Aerobic biodegradation occurs when air migrates through the waste layer if organic matter is present; this increases the temperature of the waste layer. Inflow of air into the gas vents can occur at a wide range of depths, even 10–20 m below ground level. Air is induced not from the surface of the landfill, but horizontally along the waste layer. The driving force of air induction from outside is a buoyancy effect caused by the temperature rise due to aerobic biodegradation.     

Passive drainage and biofiltration of landfill gas: Australian field trial

In Australia a significant number of landfill waste disposal sites do not incorporate measures for the collection and treatment of landfill gas. This includes many old/former landfill sites, rural landfill sites, non-putrescible solid waste and inert waste landfill sites, where landfill gas generation is low and it is not commercially viable to extract and beneficially utilize the landfill gas. Previous research has demonstrated that biofiltration has the potential to degrade methane in landfill gas, however, the microbial processes can be affected by many local conditions and factors including moisture content, temperature, nutrient supply, including the availability of oxygen and methane, and the movement of gas (oxygen and methane) to/from the micro-organisms. A field scale trial is being undertaken at a landfill site in Sydney, Australia, to investigate passive drainage and biofiltration of landfill gas as a means of managing landfill gas emissions at low to moderate gas generation landfill sites. The design and construction of the trial is described and the experimental results will provide in-depth knowledge on the application of passive gas drainage and landfill gas biofiltration under Sydney (Australian) conditions, including the performance of recycled materials for the management of landfill gas emissions.     

Energy recovery from solid waste fuels using advanced gasification technology

Since the mid-1980s, TPS Termiska Processer AB has been working on the development of an atmospheric-pressure gasification process. A major aim at the start of this work was the generation of fuel gas from indigenous fuels to Sweden (i.e. biomass). As the economic climate changed and awareness of the damage to the environment caused by the use of fossil fuels in power generation equipment increased, the aim of the development work at TPS was changed to applying the process to heat and power generation from feedstocks such as biomass and solid wastes. Compared with modern waste incineration with heat recovery, the gasification process will permit an increase in electricity output of up to 50%. The gasification process being developed is based on an atmospheric-pressure circulating fluidised bed gasifier coupled to a tar-cracking vessel. The gas produced from this process is then cooled and cleaned in conventional equipment. The energy-rich gas produced is clean enough to be fired in a gas boiler (and, in the longer term, in an engine or gas turbine) without requiring extensive flue gas cleaning, as is normally required in conventional waste incineration plants. Producing clean fuel gas in this manner, which facilitates the use of efficient gas-fired boilers, means that overall plant electrical efficiencies of close to 30% can be achieved. TPS has performed a considerable amount of pilot plant testing on waste fuels in their gasification/gas cleaning pilot plant in Sweden. Two gasifiers of TPS design have been in operation in Grève-in-Chianti, Italy since 1992. This plant processes 200 tonnes of RDF (refuse-derived fuel) per day. It is planned that the complete TPS gasification process (including the complete fuel gas cleaning system) be demonstrated in several gas turbine-based biomass-fuelled power generating plants in different parts of the world. It is the aim of TPS to prove, at commercial scale, the technical feasibility and economic advantages of the gasification process when it is applied to solid waste fuels. This aim shall be achieved, in the short-term, by employing the cold clean product gas in a gas boiler and, in the longer-term, by firing the gas in engines and gas turbines. A study for a 90 MWth waste-fuelled co-generation plant in Sweden has shown that, already today, gasification of solid waste can compete economically with conventional incineration technologies.     

Passive drainage and biofiltration of landfill gas: results of Australian field trial

A field scale trial was undertaken at a landfill site in Sydney, Australia (2004-2008), to investigate passive drainage and biofiltration of landfill gas as a means of managing landfill gas emissions from low to moderate gas generation landfill sites. The objective of the trial was to evaluate the effectiveness of a passive landfill gas drainage and biofiltration system at treating landfill gas under field conditions, and to identify and evaluate the factors that affect the behaviour and performance of the system.The trial results showed that passively aerated biofilters operating in a temperate climate can effectively oxidise methane in landfill gas, and demonstrated that maximum methane oxidation efficiencies greater than 90% and average oxidation efficiencies greater than 50% were achieved over the 4 years of operation. The trial results also showed that landfill gas loading was the primary factor that determined the behaviour and performance of the passively aerated biofilters. The landfill gas loading rate was found to control the diffusion of atmospheric oxygen into the biofilter media, limiting the microbial methane oxidation process. The temperature and moisture conditions within the biofilter were found to be affected by local climatic conditions and were also found to affect the behaviour and performance of the biofilter, but to a lesser degree than the landfill gas loading.     

Treating landfill gas hydrogen sulphide with mineral wool waste (MWW) and rod mill waste (RMW)

Hydrogen sulphide (H₂S) gas is a major odorant at municipal landfills. The gas can be generated from different waste fractions, for example demolition waste containing gypsum based plaster board. The removal of H₂S from landfill gas was investigated by filtering it through mineral wool waste products. The flow of gas varied from 0.3 l/min to 3.0 l/min. The gas was typical for landfill gas with a mean H₂S concentration of ca. 4500 ppm. The results show that the sulphide gas can effectively be removed by mineral wool waste products. The ratios of the estimated potential for sulphide precipitation were 19:1 for rod mill waste (RMW) and mineral wool waste (MWW). A filter consisting of a mixture of MWW and RMW, with a vertical perforated gas tube through the center of filter material and with a downward gas flow, removed 98% of the sulfide gas over a period of 80 days. A downward gas flow was more efficient in contacting the filter materials. Mineral wool waste products are effective in removing hydrogen sulphide from landfill gas given an adequate contact time and water content in the filter material. Based on the estimated sulphide removal potential of mineral wool and rod mill waste of 14 g/kg and 261 g/kg, and assuming an average sulphide gas concentration of 4500 ppm, the removal capacity in the filter materials has been estimated to last between 11 and 308 days. At the studied location the experimental gas flow was 100 times less than the actual gas flow. We believe that the system described here can be upscaled in order to treat this gas flow.     

我国石化行业温室气体排放源识别

依据《2006年IPCC（政府间气候变化专门委员会）国家温室气体清单指南》及《温室气体协议》,对我国石化行业温室气体排放源进行了识别。结合温室气体排放源范围的两种划分方法,为石化行业的主要生产部门--油气开采、原油炼制与加工、石化原料与制品制造编制了初步的温室气体排放源清单,并简要介绍了石化行业温室气体排放量的核算方法,为石化行业温室气体排放量核算体系的构建奠定基础。     

水合物法分离CO2研究

混合气体在形成水合物时,水合物内的气体组分与气相内不同。CO2溶解度远高于N2、O2、H2等气体,因此水合物法可分离燃煤电厂烟气中的CO2。分析了气体组成、压力、温度、促进剂和多孔介质等因素对水合物法分离CO2的影响,指出采用耦合技术降低操作压力和提高水合速度是今后改进和努力的方向。