循环流化床锅炉脱硫的影响因素分析

较为系统的分析了影响循环流化床锅炉脱硫的各因素,其中包括运行床温、Ca与S物质的量、床料粒度、流化速度、以及SO_2在炉膛停留时间等,提出在不同运行条件下利用拟合曲线找出最佳脱硫工况。     

垃圾焚烧烟气中二(噁)英零排放技术实践

介绍了绍兴新民热电有限公司用煤和垃圾混烧循环流化床技术处理城市生活垃圾，焚烧烟气经活性炭吸附、半干法和布袋除尘器净化工艺处理后，烟气中二噁英接近零排放。     

Emissions of SO2, NO and N2O in a circulating fluidized bed combustor during co-firing coal and biomass

This paper presents the experimental investigations of the emissions of SO2, NO and N2O in a bench scale circulating fluidized bed combustor for coal combustion and co-firing coal and biomass. The thermal capacity of the combustor is 30 kW. The setup is electrically heated during startup. The influence of the excess air, the degree of the air staging, the biomass share and the feeding position of the fuels on the emissions of SO2, NO and N2O were studied. The results showed that an increase in the biomass shares resulted in an increase of the CO concentration in the flue gas, probably due to the high volatile content of the biomass. In co-firing, the emission of SO2 increased with increasing biomass share slightly, however, non-linear increase relationship between SO2 emission and fuel sulfur content was observed. Air staging significantly decreased the NO emission without raising the SO2 level. Although the change of the fuel feeding position from riser to downer resulted in a decrease in the NO emission level, no obvious change was observed for the SO2 level. Taking the coal feeding position R as a reference, the relative NO emission could significantly decrease during co-firing coal and biomass when feeding fuel at position D and keeping the first stage stoichiometry greater than 0.95. The possible mechanisms of the sulfur and nitrogen chemistry at these conditions were discussed and the ways of simultaneous reduction of SO2, NO and N2O were proposed.     

循环流化床锅炉燃煤技术热电厂生命周期评价

运用生命周期评价方法,应用Gabi5.0软件对采用循环流化床锅炉燃煤技术的热电企业进行资源耗竭和环境影响分析,计算各生产单元生命周期清单的全球变暖潜值、酸化效应潜值、富营养化潜值、非生物资源耗竭潜值、人体毒性潜值以及光化学烟雾和臭氧生成潜值等主要环境影响类型,对燃煤发电过程进行生命周期评价。结果表明,全球变暖和非生物资源耗竭为发电运行过程中主要的环境影响因素,分别占53%和15.05%;锅炉燃烧阶段的环境影响最重,占整个生命周期影响值的77.12%,并且除生物耗竭潜值外的其他5项指标均为发电运行阶段各个单元中最高。采用SNCR脱硝技术减少燃烧过程中NOx的排放量,并对该技术方案进行生命周期评价,比较方案实施前后的环境影响。     

CFB锅炉环保项目SNCR工艺优化提效研究

某炼化企业自备电厂循环流化床锅炉(简称CFB锅炉)环保项目所采用的脱硝方法为选择性非催化还原脱硝(简称SNCR),使用的还原剂为尿素,SNCR系统投用后,虽然能使NOX排放量显著下降,但尿素用量明显过度,增加了企业脱硝成本,并导致脱硫废水氨氮含量超标。为了应对这一情况,本研究主要通过现场调节锅炉运行参数,以及基于CFD建模的方法研究出高效可靠的SNCR工艺优化调整策略及方法,结果表明:在锅炉燃料煤∶焦=4∶1掺烧比例下,氧含量不宜超过3%,有利于降低NOX生成量;控制减少石灰石量有助于提升NOX的脱除效率;通过模拟计算发现下半部喷枪起到主要的脱硝作用,可适当减少上半部喷枪、提升环下半部喷枪的尿素喷入量来提高脱硝效率。为煤焦混烧CFB锅炉脱硝系统的优化提供指导和借鉴作用。     

循环流化床锅炉脱硫效率分析及监测实例

分析总结了循环流化床（CFB）锅炉的脱硫机理以及影响其脱硫效率的各种因素,对某燃煤热电厂和某生物质环保热电厂的循环流化床锅炉脱硫效果（加石灰石前后二氧化硫的排放情况）进行了实测,结果表明：采用循环流化床添加石灰石炉内脱硫后的烟气排放完全满足中国相关排放标准的要求。通过加强对循环流化床锅炉运行的管理,可具有广阔的应用前景。     

大型CFB锅炉安全问题与对策

根据CFB锅炉运行的特点,重点分析了大型CFB锅炉存在的锅炉磨损、冷渣器故障、给煤系统故障、浇注料破坏脱落以及锅炉膨胀等安全问题,提出对策措施。     

330MW循环流化床机组协调控制系统的特点分析与应用实例

循环流化床机组在动态特征上不同于煤粉炉,其燃料煤粒较粗,燃烧过程复杂,并且因为其燃烧室内的床料具有相当大的热惯性和蓄热能力,是以当给煤量改变后,主蒸汽压力的变化相应比煤粉锅炉的迟延和惯性要大得多,造成了循环流化床机组燃烧过程实现自动协调控制的困难。以京海煤矸石发电有限责任公司凤凰岭电厂新建工程2×330 MW循环流化床机组控制系统为例,从变参数的应用、前馈的应用、主压力与给水的解耦控制、煤质修正控制等多方面阐述了循环流化床机组的控制特点,分析探讨了应用中存在的问题并提出了解决方法。     

垃圾焚烧烟气中二恶英零排放技术的实践

介绍了绍兴新民热电有限公司煤和垃圾混烧循环流化床技术处理城市生活垃圾,焚烧烟气经活性炭吸附、半干法和布袋除尘器净化工艺处理后,烟气中二恶英接近零排放。     

烧结机头烟气脱硫脱硝技术比较分析

本文提出了目前常见的两种烧结机头烟气脱硫脱硝超低排放工艺技术:CFB脱硫+SCR脱硝工艺和活性焦脱硫脱硝一体化工艺,并对两种脱硫脱硝技术的工艺过程和工艺特点进行了比较和分析。