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燃煤烟气脱硝技术研究进展 总被引:2,自引:0,他引:2
在查阅大量相关文献的基础上,对选择性催化还原法(SCR)、非选择性催化还原法(SNCR)、SNCR-SCR联合脱硝法、光催化氧化法、非平衡等离子体法、干法低温脱硫脱硝法和循环流化床联合脱硫脱氮技术等工艺的脱硝原理、脱除效率、应用条件、经济性等方面进行了阐述分析,并根据实际情况对我国不同地区燃煤电厂烟气脱硝提出合理可行的工艺。 相似文献
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《安全.健康和环境》2020,(7)
介绍了国内炼厂烟气脱硝工艺现状,包括NOx相关排放标准和烟气排放特点以及常用的烟气脱硝技术,烟气选择性催化还原(SCR)技术是最有效、应用范围最广的脱硝技术。重点分析了炼化企业主要的含NOx烟气治理情况和脱硝装置运行的情况。 相似文献
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选择性催化还原脱硝法(SCR)是当前世界上主流的烟气脱硝技术工艺,具有脱硝效率高、成熟可靠、应用广泛、经济合理和适应性强等特点。本文就影响燃煤电厂SCR烟气脱硝设计的几个主要因素如入口NOx浓度、还原剂和催化剂形式及其布置方式进行了分析与讨论,并指出各燃煤电厂在进行SCR烟气脱硝设计时应结合自身烟气条件、煤质资料及其当地环境保护法律法规等合理选择烟气参数,以保证SCR系统运行的安全性和经济性。 相似文献
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研究了某大型焦化厂的选择性催化还原(SCR)装置对焦炉煤气燃烧废气中典型非故意产生持久性有机污染物(UPPOPs)的脱除效果,对SCR装置入口和出口废气和SCR装置降尘中二英(PCDD/Fs)、多氯联苯(PCBs)和多氯萘(PCNs)的全部异构体进行了分析.结果表明,SCR装置对总PCDD/Fs的脱除效率最高,为94.6%,对总PCBs和总PCNs的脱除率分别为74.7%和78.4%.SCR装置入口和出口废气中UP-POPs同系物的分布模式明显不同,入口处以高氯取代为主,出口处以低氯取代为主.SCR装置对高氯取代UP-POPs有更好的脱除效果.催化还原和催化氧化降解同时发生是SCR装置脱除废气中UP-POPs的重要机制. 相似文献
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Asad Naeem Shah Yunshan Ge Jianwei Tan Zhihua Liu Chao He Tao Zeng 《环境科学学报(英文版)》2012,24(8):1449-1456
Two after treatment units, selective catalytic reduction (SCR) and continuously regenerating trap (CRT), were independently retrofitted to a diesel engine, with the objective to investigate their impact on the conversion/reduction (CR) of polycyclic aromatic hydrocarbons (PAHs). The experiments were conducted under the European steady state cycle (ESC) first without any retrofits to get baseline emissions, and then with SCR and CRT respectively, on the same engine. The particulate matter (PM)-phase PAHs were trapped in fiberglass filters, whereas gas-phase PAHs were collected in cartridges, and then analyzed using a gas chromatograph-mass spectrometer (GC-MS). Both PM-phase and gas-phase PAHs were greatly reduced with CRT showing respective CR of 90.7% and above 80%, whereas only gas-phase PAHs were abated in the case of SCR, with CR of above 75%. Lower molecular weight (LMW) PAHs were in abundance, while naphthalene exhibited a maximum relative contribution (RC) to LMW-PAHs for all three cases. Further, the CR of naphthalene and anthracene were increased with increasing catalyst temperature of SCR, most likely due to their conversion to solid particles. Moreover, the Benzo[a]Pyrene equivalent (BaPeq) of PAHs was greatly reduced with CRT, owing to substantial reduction of total PAHs. 相似文献
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为定量地综合评价燃煤电厂氮氧化物控制技术,建立了包括环境、技术、经济3个方面共11项指标的多因素多级评价指标体系.采用模糊评价方法,选择低氮燃烧器(LNB)、燃尽风(OFA)、再燃(Reburning)、选择性催化还原(SCR)、选择性非催化还原(SNCR)和SCR/SNCR联合6种典型的氮氧化物控制技术,定量评估其技术、经济和环境性能,以筛选出燃煤电厂最佳适用控制技术组合.案例分析结果表明,对于燃烧贫煤或无烟煤的墙式锅炉,要求脱硝效率70%,SCR与LNB联用技术是最优选择;对于使用烟煤或褐煤的W火焰和切圆燃烧锅炉,脱硝效率30%即可达标排放,LNB和再燃等燃烧中脱硝技术是最佳选择.因此,在经济较发达、生态环境脆弱的重点地区,建议燃用无烟煤和贫煤的大型机组安装LNB和SCR,燃用烟煤和褐煤的机组或者100MW机组可考虑LNB和SNCR联用来减少NOx排放;在其它尚有环境容量的地区,建议燃无烟煤和贫煤的机组安装LNB和SNCR,其它机组通过安装LNB减少NOx排放. 相似文献
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烟气中氮氧化物污染的治理 总被引:10,自引:0,他引:10
对最新的一些烟气NOx脱除技术进行了综述,对于主要的两种燃烧后烟气NOx脱除工艺技术─选择性催化还原(SCR)及选择性非催化还原(SNCR)进行了较为详细的讨论,并对这两种方法的优缺点进行了对比.还对其它的一些工艺技术如碳氢化合物选择性催化还原(HC—SCR)及NOx直接催化分解作了简要介绍. 相似文献
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LI Zhe SHEN Lin-tao HUANG Wei~* XIE Ke-chang Key Laboratory of Coal Science Technology Ministry of Education Shanxi Province Taiyuan University of Technology Taiyuan China. 《环境科学学报(英文版)》2007,19(12)
The catalyst of Fe-Mo/ZSM-5 has been found to be more active than Fe-ZSM-5 and Mo/ZSM-5 separately for selective catalytic reduction (SCR) of nitric oxide (NO) with NH_3.The kinetics of the SCR reaction in the presence of O_2 was studied in this work.The results showed that the observed reaction orders were 0.74-0.99,0.01-0.13,and 0 for NO,O_2 and NH_3 at 350-450℃,respectively. And the apparent activation energy of the SCR was 65 kJ/mol on the Fe-Mo/ZSM-5 catalyst.The SCR mechanism was also deduced. Adsorbed NO species can react directly with adsorbed ammonia species on the active sites to form N_2 and H_2O.Gaseous O_2 might serve as a reoxidizing agent for the active sites that have undergone reduction in the SCR process.It is also important to note that a certain amount of NO was decomposed directly over the Fe-Mo/ZSM-5 catalyst in the absence of NH_3. 相似文献
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The catalyst of Fe-Mo/ZSM-5 has been found to be more active than Fe-ZSM-5 and Mo/ZSM-5 separately for selective catalytic reduction (SCR) of nitric oxide (NO) with NH3. The kinetics of the SCR reaction in the presence of O2 was studied in this work. The results show that the observed reaction orders were 0.74-0.99, 0.01-0.13, and 0 for NO, O2 and NH3, respectively, at 350-450℃. And the apparent activation energy of the SCR was 65 kJ/mol on the Fe-Mo/ZSM-5 catalyst. The SCR mechanism was also deduced. Adsorbed NO species can react directly with adsorbed ammonia species on the active sites to form N2 and H2O. Gaseous O2 might serve as a reoxidizing agent for the active sites that have undergone reduction in the SCR process. It is also important to note that a certain amount of NO was decomposed directly over the Fe-Mo/ZSM-5 catalyst in the absence of NH3. 相似文献
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Coal-fired utility boilers are now identified as the largest source of mercury in the United States. There is speculation that the installation of selective catalytic reduction (SCR) system for reduction of NOx can also prompt the oxidation and removal of mercury. In this paper, tests at six full-scale power plants with similar type of the SCR systems are conducted to investigate the effect of the SCR on the transformation of mercury speciation. The results show that the SCR system can achieve more than 70%-80% oxidation of elemental mercury and enhance the mercury removal ability in these units. The oxidation of elemental mercury in the SCR system strongly depends on the coal properties and the operation conditions of the SCR systems. The content of chloride in the coal is the key factor for the oxidization process and the maximum oxidation of elemental mercury is found when chloride content changes from 400 to 600 ppm. The sulfur content is no significant impact on oxidation of elemental mercury. 相似文献