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添加剂强化石灰石湿法烟气脱硫实验研究 总被引:7,自引:0,他引:7
以Na2SO4和MgSO4等无机盐添加荆加入石灰石浆液中,测定了不同浆液中CaCO3溶解度.结果表明,Na2SO4和MgSO4均能提高CaCO3溶解度,其中Na2SO4的促溶效果更好.通过平流泵定量滴定稀硫酸溶液,测定了不同浆液组成的CaCO3溶解速度.结果表明,加入0.05 mol/L柠檬酸钾可使浆液中生成柠檬酸,从而提高CaCO3的溶解速度,并增强浆液缓冲能力,其强化效果优于Na2SO4和MgSO4.在配有无机盐添加剂的浆液中通入由N2和SO2模拟的含不同ρ(SO2)的烟气(ρ(SO2)为2000~3 000mg/m3),分别研究了SO2吸收率随着初始pH,通气时间和浆液成分的变化规律.结果表明,在浆液中加入0.05 mol/l的Na2SO4或MgSO4,可以强化CaCO3溶解和SO2吸收,同时可以增强浆液的缓冲能力. 相似文献
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添加剂在石灰石湿法烟气脱硫工艺中的应用与分析 总被引:2,自引:0,他引:2
本文主要介绍了添加剂在石灰石湿法烟气脱硫工艺中的应用和国内外研究现状,并对其作用机理进行了探讨。脱硫添加剂可以改善吸收剂的液相传质性能,缓冲浆液的pH值,从而提高脱硫效率,降低运行成本,在我国燃煤电厂烟气脱硫工艺中有着广阔的应用前景。 相似文献
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模糊控制在湿法脱硫烟气系统中的应用 总被引:1,自引:1,他引:1
介绍了石灰石-石膏湿法脱硫装置烟气系统的设计情况,重点讲述了增压风机动叶的控制,针对增压风机动叶系统时滞、非线性等特点,常规PID控制效果并不理想,设计出模糊控制器,仿真后证明了理论的正确性。 相似文献
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目前,大型燃煤发电锅炉和工业燃煤锅炉排烟的SO_2控制,多采用湿法烟气脱硫(WFGD)系统。该系统技术成熟,操作简单,SO_2脱除效率高,但也存在着酸性废水排放等缺点。因此,近年来WFGD遇到了新开发成功的干法烟气脱硫(DFGD)的挑战并有被取代之势。本文介绍的美国能源部(DOE)匹斯堡能源技术中心(PETC)开发的流化床氧化铜DFGD系统和日本电力开发公司(EPDC)开发的活性炭DFGD系统就是希望取代WFGD的两种代表性系统。 相似文献
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湿法烟气脱硫的烟气排放 总被引:5,自引:0,他引:5
目前国内燃煤电厂多采用石灰石-石膏湿法烟气脱硫技术,而通过该工艺脱硫后的净烟气在排放时是否进行再热处理-直困扰着产业界.我国湿法烟气脱硫系统在引进之初均采用再热系统,但在实际运行中,再热系统的日常维护和运行问题较多,运行成本高,所以有些电厂不再设置再热系统.就我国普遍采用的FGD系统对脱硫后烟气的两种排放方式和具体的设备进行了分析. 相似文献
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石灰石湿法烟气脱硫添加剂的实验研究 总被引:9,自引:0,他引:9
利用双搅拌釜,作石灰石浆液脱硫的实验,测定添加剂强化前后石灰石浆液脱硫过程中气液两相传质系数的变化,对比气液两相传质系数的大小。并结合国内外脱硫技术现状,提出了以石灰石作为脱硫剂,以硫酸镁、硫酸钠、腐残酸钠为添加剂,应用双搅拌釜为主设备的湿法脱硫方法,对添加剂的脱硫机理进行了基础性研究。 相似文献
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石灰石湿法烟气脱硫试验研究 总被引:5,自引:0,他引:5
介绍了湍球塔石灰石湿法烟气脱硫系统,通过试验,研究分析了床层阻力,脱硫效率,CaCO3利用率等因素,试验证明烟气脱硫的效率可达50% ̄85%,是一种简易的烟气脱硫方法。 相似文献
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研究表明,湿法烟气脱硫装置(WFGD)可去除烟气中绝大部分Hg^2+,但对单质汞的吸收效果不明显,因此研究提高湿法烟气脱硫系统中单质汞的氧化率的方法对控制汞的排放具有重要意义。综述了WFGD及在此系统中各种添加剂的脱汞性能,认为在添加剂中,气态的臭氧、液态的次氯酸和氯化钠稀溶液、黄磷乳浊液、氢硫化钠溶液及EDTA的汞去除效果较好,且不会被SO2大量消耗,可在WFGD系统实现同时脱硫脱汞;而气态的氯气,液态的K2S2O8溶液虽然也有较好的汞去除效果,但因易被SO2或亚硫酸盐溶液消耗,当在WFGD系统中用其氧化单质汞时,需要对脱硫塔进行分层或其他改造,使烟气中的SO2被吸收后再控制汞,提高经济性。 相似文献
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Selective catalytic reduction (SCR) denitration may increase the emission of NH4+ and NH3. The removal and transformation characteristics of ammonium sulfate aerosols and ammonia slip during the wet flue gas desulfurization (WFGD) process, as well as the effect of desulfurization parameters, were investigated in an experimental system equipped with a simulated SCR flue gas generation system and a limestone-based WFGD system. The results indicate that the ammonium sulfate aerosols and ammonia slip in the flue gas from SCR can be partly removed by slurry scrubbing, while the entrainment and evaporation of desulfurization slurry with accumulated NH4+ will generate new ammonium-containing particles and gaseous ammonia. The ammonium-containing particles formed by desulfurization are not only derived from the entrainment of slurry droplets, but also from the re-condensation of gaseous ammonia generated by slurry evaporation. Therefore, even if the concentration of NH4+ in the desulfurization slurry is quite low, a high level of NH4+ was still contained in the fine particles at the outlet of the scrubber. When the accumulated NH4+ in the desulfurization slurry was high enough, the WFGD system promoted the conversion of NH3 to NH4+ and increased the additional emission of primary NH4+ aerosols. With the decline of the liquid/gas ratio and flue gas temperature, the removal efficiency of ammonia sulfate aerosols increased, and the NH4+ emitted from entrainment and evaporation of the desulfurization slurry decreased. In addition, the volatile ammonia concentration after the WFGD system was reduced with the decrease of the NH4+ concentration and pH values of the slurry. 相似文献
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IntroductionInstallationofscrubbersortheuseoflowsulfur containingcoalaretwooptionsusedbypowerplantstoreduceSO2 emissions.ThemajorityofpowerplantscontrolSO2 emissionsusinglimebasedscrubbing ,althoughthisdesulfurizationprocesshasanumberofadvantages,italsoh… 相似文献
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The relationship between the fine particles emitted after desulfurization and gypsum crystals in the desulfurization slurry was investigated, and the crystallization characteristics varying with the operation parameters and compositions of the desulfurization slurry were discussed. The results showed that the fine particles generated during the desulfurization process were closely related to the crystal characteristics in the desulfurization slurry by comparison of their morphology and elements. With the higher proportion of fine crystals in the desulfurization slurry, the number concentration of fine particles after desulfurization was increased and their particle sizes were smaller, indicating that the optimization of gypsum crystallization was beneficial for the reduction of the fine particle emission. The lower pH value and an optimal temperature of the desulfurization slurry were beneficial to restrain the generation of fine crystals in the desulfurization slurry. In addition, the higher concentrations of the Fe3 + ions and the F− ions in the desulfurization slurry both promoted the generation of fine crystals with corresponding change of the morphology and the effect of the Fe3 + ions was more obvious. With the application of the desulfurization synergist additive, it was beneficial for the inhibition of fine crystals while the thinner crystals were generated. 相似文献
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以元素硫的地球化学循环为指导,系统研究硫酸盐还原菌(SRB)生化代谢产物还原性硫化物与亚硫酸根的反应过程机理及产物形态.结果表明,在生化烟气脱硫及硫回收反应体系中,pH=(4.04±0.10)、ORP=(-134±17mV)时硫磺产量最大,硫磺产率大于40%;SO2(aq)-S2-(aq)体系证明pH=(3.99±0.21)、ORP=(-159±40)mV、SO32-/ΣS2-物质的量比约1:1时为产硫磺最佳条件区间;S2O32-与S2-的产硫磺反应为副反应,有利于硫磺的产生;近中性条件下硫磺的消耗归因于产多硫化物和连多硫酸盐反应的进行;SO2(aq)-S2-(aq)体系和生化体系的固体产物表征分析为球状高纯斜方硫,生化体系产生的硫磺被胞外多聚物粘附裹挟. 相似文献