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.     

Anaerobic tapered fluidized bed reactor for starch wastewater treatment and modeling using multilayer perceptron neural network

Anaerobic treatability of synthetic sago wastewater was investigated in a laboratory anaerobic tapered fluidized bed reactor(ATFBR) with a mesoporous granular activated carbon(GAC)as a support material.The experimental protocol was defined to examine the effect of the maximum organic loading rate(OLR),hydraulic retention time(HRT),the efficiency of the reactor and to report on its steady- state performance.The reactor was subjected to a steady-state operation over a range of OLR up to 85.44 kg COD/(m~3.d).The COD removal efficiency was found to be 92% in the reactor while the biogas produced in the digester reached 25.38 m~3/(m~3·d) of the reactor. With the increase of OLR from 83.7 kg COD/(m~3.d),the COD removal efficiency decreased.Also an artificial neural network(ANN) model using multilayer perceptron(MLP)has been developed for a system of two input variable and five output dependent variables. For the training of the input-output data,the experimental values obtained have been used.The output parameters predicted have been found to be much closer to the corresponding experimental ones and the model was validated for 30% of the untrained data.The mean square error(MSE)was found to be only 0.0146.     

基于CFD的内构件强化内循环流化床流场结构分析

针对流化床内部流体结构的复杂性和缺乏有效放大设计理论的问题,以漏斗型导流内构件强化的内循环流化床的气液运动为研究对象,利用欧拉-欧拉双流体模型构建了能描述其复杂流动的CFD数学模型,通过宏观流场、气含率分布、液体速度分布解析内构件对气液混合传质的作用原理.数值模拟结果表明:双流体模型能较好地揭示流化床内气液流场结构,流...     

Modification of Ce02-ZrO2 catalyst by potassium for NOx-assisted soot oxidation

Potassium-modified ceria-zirconia catalyst was synthesized by wetness impregnation method. The ageing treatment was performed in static air at 800℃ for 20 hr to evaluate the thermal stability of the catalyst. The catalysts were characterized by X-ray diffraction,BET surface area, oxygen storage capacity, NOx-temperature programmed desorption and soot-temperature programmed oxidation measurements. By introduction of potassium, the maximum soot oxidation rate temperature (Tm) of the ceria-zirconia based catalyst decreased from 525 to 428℃ in the presence of NO under a loose contact mode. The shift of Tm of the K-modified catalyst after ageing is only 15℃. The enhanced activity of the aged catalyst mainly lies in the promotional effect of potassium on the NOx/oxygen storage cacity as well as the soot-catalyst contact.     

小型燃煤工业锅炉NO_x形成与释放规律模拟研究

NOx是我国十二五期间重点控制的污染物,燃煤工业锅炉是其重要来源。为了研究燃煤工业锅炉NOx的形成与释放规律,在实验室模拟了不同煤种的燃烧过程。采用原煤/焦炭燃烧法分别研究挥发分氮和焦炭氮生成NOx的反应,探讨燃料型NOx的形成与释放规律,并解释试验模拟条件下燃煤NOx产污系数和现场实测值的差异。结果表明,试验中烟煤、无烟煤、煤焦的NO转化率平均值分别为25.77%,22.17%和11.98%,产污系数平均值分别为4.31,5.08和2.00kg/t,高于现场实测结果核算值。燃煤工业锅炉NOx以燃料型为主,燃料型NOx的形成和释放是一个复杂的多相反应过程,由挥发分氮的氧化还原反应和焦炭氮的氧化还原反应组成,煤种、温度、空气流量、粒径、氧含量等因素对4种反应各自影响及影响程度并不相同。     

La-Co-Fe-Cu/HZSM-5在尾气碳颗粒燃烧中的催化性能

采用柠檬酸络合低温浸渍法制备分子筛负载钙钛矿型复合氧化物催化剂。采用XRD、SEM和H2-TPR等手段对催化剂性能进行表征,并在微型固定床反应器中对催化剂进行活性评价。结果表明,在钙钛矿型复合氧化物中进行B位离子掺杂,可以改善催化活性,碳颗粒燃烧温度降低。在20%LaCoO3/HZSM-5催化剂中用铁离子部分取代钴离子可以改善碳颗粒的燃烧性能,取代量增加碳颗粒燃烧温度降低,但是生成CO2的选择性也降低,以20%LaCo0.2Fe0.8O3/HZSM-5为催化剂,Tig、Tm和Tf分别为256℃、399℃和403℃,但生成CO2的选择性只有72.5%。在20%LaCo1-xFexO3/HZSM-5中的钙钛矿型复合氧化物B位离子中加入铜离子后,在碳颗粒燃烧反应中生成CO2的选择性得到明显改善,Sco2提高10个单位以上。以20%LaCo0.2Fe0.6Cu0.2O3/HZSM-5为催化剂,在碳颗粒燃烧反应中生成CO2的选择性可以达到94.7%,Tig、Tm和Tf分别为242℃、427℃和445℃。     

脉动频率对低浓度瓦斯脉动燃烧的影响研究

本文将低浓度瓦斯与脉动燃烧结合,主要研究了脉动频率对低浓度瓦斯燃烧的影响。实验结果发现：频率为99Hz至120Hz之间的脉动燃烧不仅可以降低贫燃极限．实现瓦斯在5％浓度下稳定而充分的燃烧,而且在相同温度下提高了瓦斯燃烧效率,污染物的排放也得到了改善。     

Turbosorp湍流吸收循环流化床烟气脱硫技术在改造工程中的应用

循环流化床半干法烟气脱硫技术是目前世界上主流脱硫工艺技术之一,主要适用于大中型燃煤电厂的烟气脱硫,在国内外拥有大量成功运行的工程案例。本文章基于本公司实践论述Turbosorp湍流吸收循环流化床脱硫技术的技术特点、关键工艺控制要点以及在机组改造工程中的技术优势,为同类型机组改造工程中的方案选择提供参考。     

Enhanced struvite recovery from wastewater using a novel cone-inserted fluidized bed reactor

The feasibility of struvite recovery at low （12.5 mg/L） and high （120 mg[L） phosphorus concentrations was studied by constructing a novel fluidized bed reactor with cones （FBRwc） and without cones （FBRwoc）. The crystallization process was continuously operated for 133 days under different hydraulic retention times （HRT = 1-10 hr）, pH （7.5-10）, and molar ratios of Mg/P （0.75-1.75）, N/P （1-10） and Ca/Mg （0-2）. The optimum operating conditions of HRT, pH, Mg/P and N/P molar ratios were found to be 2 hr, 9, 1.25, and 7.5, respectively. Under these optimum conditions, the phosphorus precipitation efficiencies of FBRwc were 93% for low and 98% for high phosphorus influent; however, the efficiencies were 78% and 81% for FBRwoc, respectively. Due to crystal losses at each junction （17%-31%）, the crystal recovery efficiency of FBRwoc was relatively low （47%-65%） for both influent concentrations. However, the losses were minimal in FBRwc, which showed 75% and 92% crystal recovery for low and high phosphorus concentrations, respectively. At low calcium concentration, crystal chemical analysis showed the product to be pure struvite （〉 99%）. The scanning electron microscope and X-ray diffraction results further confirmed that the crystal recovered from FBRwc contained pure struvite, which could be considered a high quality fertilizer. Except HRT, all parameters （pH, Mg/P, N/P and Ca/Mg） were found to be influencing factors for FBRwc performance. Overall, inserting cones in each part of the reactor played a significant role in enhancing struvite recovery from a wide range of phosphorus-containing wastewater.     

A restoration-promoting integrated floating bed and its experimental performance in eutrophication remediation

Numerous studies on eutrophication remediation have mainly focused on purifying water first, then restoring submerged macrophytes. A restoration-promoting integrated floating bed （RPIFB） was designed to combine the processes of water purification and macrophyte restoration simultaneously. Two outdoor experiments were conducted to evaluate the ecological functions of the RP1FB. Trial 1 was conducted to compare the eutrophication purification among floating bed, gradual-submerging bed （GSB） and RPIFB technologies. The results illustrated that RPIFB has the best purification capacity. Removal efficiencies of RPIFB for TN, TP,NH4＋-N, NO3-N, CODcr, Chlorophyll-a and turbidity were 74.45%, 98.31%, 74.71%, 88.81%, 71.42%, 90.17% and 85%, respectively. In trial 2, influences of depth of GSB and photic area in RPIFB on biota were investigated. When the depth of GSB decreased and the photic area of RPIFB grew, the height of Potamogeton crispus Linn. increased, but the biomass of Canna indica Linn. was reduced. The mortalities of Misgurnus anguillicaudatus and Bellamya aeruginosa in each group were all less than 7%. All results indicated that when the RPIFB was embedded into the eutrophic water, the regime shift from phytoplankton-dominated to macrophyte-dominated state could be promoted. Thus, the RPIFB is a promising remediation technology for eutrophication and submerged macrophyte restoration.