Investigation on the relationship between the fine particle emission and crystallization characteristics of gypsum during wet flue gas desulfurization process

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 Fe^3 + 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 Fe^3 + 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.     

Effect of SiO2 addition on NH4HSO4 decomposition and SO2 poisoning over V2O5–MoO3/TiO2–CeO2 catalyst

The deposition of NH₄HSO₄ and the poisoning effect of SO₂ on SCR catalyst are the main obstacles that restrict the industrial application of CeO₂-doped SCR catalysts. In this work, deposited NH₄HSO₄ decomposition behavior and SO₂ poisoning over V₂O₅–MoO₃/TiO₂ catalysts modified with CeO₂ and SiO₂ were investigated. By the means of characterization analysis, it was found that the addition of SiO₂ into VMo/Ti–Ce had an impact on the interaction existed between catalyst surface atoms and NH₄HSO₄. Temperature-programmed methods and in situ diffused reflectance infrared Fourier transform spectroscopy (DRIFTS) experiments indicated that the doping of SiO₂ promoted the decomposition of deposited NH₄HSO₄ on VMo/Ti–Ce catalyst surface by reducing the thermal stability of NH₄HSO₄ and enhancing the NH₄HSO₄ reactivity with NO in low temperature. And this improvement may be the reason for the better catalytic activity than VMo/Ti–Ce in the case of NH₄HSO₄ deposition. Accompanied with cerium sulfate species generated over catalyst surface, the conversion of SO₂ to SO₃ was inhibited in SiCe mixed catalyst. The addition of SiO₂ could promote the decomposition of cerium sulfate, which may be a potential strategy to enhance the resistance of SO₂ poisoning over CeO₂-modifed catalysts.     

Brominated dioxins and furans in a cement kiln co-processing municipal solid waste

A field study and theoretical calculations were performed to clarify the levels, profiles, and distributions of polybrominated dibenzo-p-dioxins and dibenzofurans(PBDD/Fs) in a cement kiln co-processing solid waste, with a focus on the PBDF formation mechanism.The raw materials contributed greatly to input of PBDD/Fs into the cement kiln. The PBDD/F concentrations in the raw materials were much higher than those in particle samples from different process stages in the cement kiln. The PBDD/F concentrations in the clinkers were1.40% of the concentrations in the raw materials, which indicated that the high destruction efficiencies for PBDD/Fs by cement kiln. PBDD/F distribution patterns in particle samples collected from different process stages indicated the cement kiln backend was a major site for PBDD/F formation. PBDFs with high levels of halogenation, such as heptabrominated furans(Hp BDF), were the dominant contributors to the total PBDD/F concentrations and accounted for 42%–73% of the total PBDD/F concentrations in the particle samples. Our results showed that co-processing of municipal solid waste in a cement kiln may influence the congener profile of PBDD/Fs, especially for the higher halogenated PBDD fraction. In addition, there were significant correlations between the decabromodiphenyl ether and heptabrominated furan concentrations, which is an indicator of transformation from polybrominated diphenyl ethers to PBDD/Fs. Theoretical calculations were performed and demonstrated that elimination of HBr and Br_2 from polybrominated diphenyl ethers were the dominant formation pathways for PBDD/Fs. These pathways differed from that for polychlorinated dibenzo-p-dioxins and dibenzofurans(PCDD/Fs).     

基于凝聚函数的电力系统经济负荷分配

经济负荷分配(Economic Load Dispatch,ELD)是提高电力系统运行经济性的重要措施之一。基于ELD优化问题一般数学模型,针对传统数学方法难以处理不可微非线性问题,借助于最大熵理论,利用其推导出的凝聚函数来处理不可微的约束条件,构建了基于凝聚函数的负荷经济分配优化模型,并采用光滑化的方法将所建立的模型转化为一般非线性优化问题,采用原对偶内点法进行求解。仿真结果表明:该算法能有效地处理不可微的非线性规划问题,在算法的计算效率以及目标优化的结果中显示出了优越性,为解决电力系统经济负荷分配问题提供了有效手段。     

Emergy algebra: Improving matrix methods for calculating transformities

Transformity is one of the core concepts in Energy Systems Theory and it is fundamental to the calculation of emergy. Accurate evaluation of transformities and other emergy per unit values is essential for the broad acceptance, application and further development of emergy methods. Since the rules for the calculation of emergy are different from those for energy, particular calculation methods and models have been developed for use in the emergy analysis of networks, but double counting errors still occur because of errors in applying these rules when estimating the emergies of feedbacks and co-products. In this paper, configurations of network energy flows were classified into seven types based on commonly occurring combinations of feedbacks, splits, and co-products. A method of structuring the network equations for each type using the rules of emergy algebra, which we called “preconditioning” prior to calculating transformities, was developed to avoid double counting errors in determining the emergy basis for energy flows in the network. The results obtained from previous approaches, the Track Summing Method, the Minimum Eigenvalue Model and the Linear Optimization Model, were reviewed in detail by evaluating a hypothetical system, which included several types of interactions and two inputs. A Matrix Model was introduced to simplify the calculation of transformities and it was also tested using the same hypothetical system. In addition, the Matrix Model was applied to two real case studies, which previously had been analyzed using the existing method and models. Comparison of the three case studies showed that if the preconditioning step to structure the equations was missing, double counting would lead to large errors in the transformity estimates, up to 275 percent for complex flows with feedback and co-product interactions. After preconditioning, the same results were obtained from all methods and models. The Matrix Model reduces the complexity of the Track Summing Method for the analysis of complex systems, and offers a more direct and understandable link between the network diagram and the matrix algebra, compared with the Minimum Eigenvalue Model or the Linear Optimization Model.     

京津冀及周边地区采暖季PM2.5化学组分变化特征

利用京津冀及周边地区大气污染综合立体监测网,在京津冀大气污染传输通道城市（“2+26”城市）开展了PM_2.5及其化学组分长期连续观测,并对数据进行深入分析.结果表明:①2017年、2018年和2019年采暖季“2+26”城市PM_2.5浓度平均值分别为（84±62）（95±63）和（80±61）μg/m3,达到了京津冀及周边地区2019—2020年秋冬季PM_2.5平均浓度同比下降4%的目标;与PM_2.5浓度变化相似,其主要化学组分——有机物（OM）浓度最大值出现在2018年采暖季,但二次无机盐（硝酸盐、硫酸盐和铵盐）浓度呈逐年上升趋势,而元素碳、氯盐、地壳物质和微量元素浓度均呈逐年下降趋势.②OM、硝酸盐、硫酸盐、铵盐、地壳物质、元素碳、氯盐和微量元素浓度空间分布存在明显差异.受污染物排放、气象条件以及地形因素的共同影响,PM_2.5及其化学组分浓度高值区主要出现在太行山传输通道城市（保定市、石家庄市、邢台市、邯郸市、安阳市和新乡市）.③不同空气质量状况下,“2+26”城市PM_2.5化学组分浓度年际变化相似,即随空气污染的加重,硝酸盐、硫酸盐和铵盐占PM_2.5的比例均上升,而OM占比下降.研究显示,采暖季“2+26”城市空气质量总体得到改善,但需进一步加强对PM_2.5中二次组分的科学管控.      

京津冀地区臭氧污染特征与来源分析

2013—2014年京津冀地区13个城市O_3日最大8 h平均值第90百分位数平均为155~162μg/m3,京津冀地区已成为全国O_3污染最严重的地区之一,京津冀地区O_3污染程度有所加重。京津冀地区夏季O_3浓度高,冬季浓度低,O_3质量浓度较高的月份集中在5—9月,12月—次年1月浓度最低。在O_3污染较重的夏季,每日6:00~7:00,O_3质量浓度最低,15:00~16:00 O_3浓度最高。在空间分布上郊区点位的O_3质量浓度往往高于主城区点位。京津冀区域夏季O_3小时浓度和NO2浓度呈高度负相关关系,和其他污染物无明显的相关性。O_3质量浓度和气温呈显著的正相关关系,和大气相对湿度呈显著的负相关关系。京津冀区域O_3的主要来源为NOX和VOC等一次污染物在日光照射下发生光化学反应而产生,控制O_3前体物的源排放,尤其是控制好VOC的排放是控制O_3污染的有效途径。     

粘土制砖过程中固氟剂的研究

基于制砖时氟易与钙结合生成高温下较稳定的ＣａＦ２,从而降低氯化物逸出量,在试验分析２４种钙基物料固氟效果的基础上,选取效果较佳的６种分别在实验室和砖瓦厂进行优化添加比例试验,对其中途中 作了砖质检验,以研究其可能对成品砖质量的影响,并进行了相应的理论分析。     

Transformation and removal of ammonium sulfate aerosols and ammonia slip from selective catalytic reduction in wet flue gas desulfurization system

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.