脉冲放电烟气脱硫脱硝技术研究进展

综述了脉冲放电等离子体烟气脱硫脱硝技术的发展历史、研究现状、进展及其存在的问题.     

用硫酸渣制备铁基颜料铁黄

以硫酸渣为原料，用黄铁矿粉作还原剂，采用湿式空气氧化法制备铁基颜料铁黄。试验得出的适宜工艺条件为：Fe^2 浓度0．25—0．40mol/L，氧化温度70℃，用氢氧化钠或氨水调节反应液的pH，氧化过程溶液的pH控制在3—4。依照该工艺制得的铁基颜料铁黄，其各项指标符合HG／T2249—91标准。     

湿法脱硫系统中液相二价汞的还原抑制

湿法脱硫系统协同脱汞是当前燃煤烟气脱汞的重要方法,而进入脱硫系统的二价汞还原问题会降低汞的脱除效率,从而限制该方法的使用。在脱硫浆液中添加添加剂捕集和稳定二价汞能有效抑制二价汞的还原。在模拟浆液条件下考察多硫化钙、TMT、乙基黄原酸钠、EDTA和腐殖酸对液相二价汞的还原抑制效果。结果表明,多硫化钙和TMT能极大的抑制二价汞的还原,当其添加量分别为0.004%(体积分数)和0.002%(体积分数)时,汞还原量仅为未添加条件下的3.3%和0.8%,而乙基黄原酸钠、EDTA和腐殖酸在一定条件下不仅不会抑制二价汞的还原,反而会一定程度促进二价汞的还原。这表明乙基黄原酸钠、EDTA和腐殖酸并不适合于作为液相二价汞的还原抑制剂。     

Long Term Trends in Sulphur and Nitrogen Deposition in Europe and the Cause of Non-linearities

Emissions of sulphur and oxidized nitrogen compounds in Europe have been reduced following a series of control measures during the last two decades. These changes have taken place during a period in which the primary gases and the wet deposition throughout Europe were extensively monitored. Since the end of the 1970s, for example land based sulphur emissions declined by between 90 and 70% depending on the region. Over the same period the total deposition of sulphur and its partitioning into wet and dry deposition have declined, but the spatial pattern in the reduction in deposition differs from that of emission and has changed with time. Such non-linearities in the emission-deposition relationship are important to understand as they complicate the process of assessing the effects of emission reduction strategies. Observed non-linearities in terrestrial sulphur emission-deposition patterns have been identified in north west Europe due to increases in marine emissions, and are currently slowing the recovery of freshwater ecosystems. Changes in the relative amounts of SO₂ and NH₃ in air over the last two decades have also changed the affinity of terrestrial surfaces for SO₂ and have therefore changed the deposition velocity of SO₂ over substantial areas. The consequence of this effect has been the very rapid reduction in ambient SO₂ concentration in some of the major source areas of Europe, where NH₃ did not change much. Interactions between the different pollutants, generating non-linearities are now being incorporated in long-range transport models to simulate the effects of historical emission trends and to provide projections into the future. This paper identifies non-linearities in emission deposition relationships for sulphur and nitrogen compounds in Europe using data from the EMEP long-rang transport model and measured concentration fields of the major ions in precipitation and of SO₂ and NO₂ in surface air.     

烟气脱硫系统调试方法

介绍了风洞式烟气脱硫系统的工艺流程及原理,重点对烟气脱硫系统调试过程进行了阐述,为相关工程测试人员提供参考。     

冲击水浴喷雾式除尘器的应用

介绍了冲击水浴喷雾式除尘器在柳钢焦化厂的应用试验情况，制作安装，调试运行后检测鉴定表明，冲击水浴喷雾式除尘器应用在冶金焦末粉尘上，不但操作简单，维护方便，除尘效率高，效果好，而且成本低廉，只有电除尘器或布袋除尘器的20%左右。     

烧结烟气应用电子束脱硫脱硝技术之利弊

介绍了电子束辐照烟气脱硫技术的原理、工艺流程、主要设备及其作用;中国工程物理研究院1.2万m^3/h电子束脱硫脱硝试验装置及试验结论;成都热电厂30万m^3/h脱硫示范装置的设计参数、运行情况;综合分析了烧结烟气脱硫应用电子束辐照烟气脱硫脱硝技术之利弊,认为烧结烟气脱硫应用电子束辐照烟气脱硫技术不失为一个可供选择且可行的技术.     

燃煤锅炉脱硫工艺浅谈

简述了燃煤锅炉常用烟气脱硫方法和烟气脱硫工艺选择原则，介绍一种简易脱硫工艺。     

亚甲蓝湿式氧化影响因素研究

以湿式氧化技术对亚甲蓝水溶液进行处理,用水样COD去除率评价处理效果.考察了反应时间、温度、氧分压、搅拌速度、进水pH值以及进水浓度对处理效果的影响,并进行机理分析.实验确定的最佳操作工艺条件为:反应温度210℃、氧分压2.0 MPa、搅拌速度880 r/min、进水pH=11.30.在此条件下,COD为2 000mg/L的亚甲蓝水溶液,反应90min时COD去除率达93.2%.     

Cu(NO3)2在亚甲蓝湿式氧化处理中的应用

用CWAO技术处理COD为2 000 mg/L的亚甲蓝水溶液.以Cu(NO3)2为催化剂,考察了催化剂投加量、反应温度、压力及进水pH值对亚甲蓝水样COD去除率、脱色率、出水pH值的影响.实验表明,亚甲蓝的氧化效率随催化剂投加量的增加,反应温度及压力的升高而升高.然而,综合考虑亚甲蓝的氧化效率、试剂费用、设备成本及能量消耗,实验确定Cu(NO3)2的投加量以Cu2 计为150 mg/L,反应温度及压力分别为200℃和2.0 MPa.在酸性进水条件下,COD去除率随进水pH值的降低而升高;而在碱性进水条件下,COD去除率随进水pH值的升高而升高.pH值按COD去除率由高到低的排列顺序是:3.87、11.23、5.50、7.25、9.47,实验确定最佳进水pH值是3.87.在以上最佳的操作条件下,反应150 min,水样COD去除率达97.4%,脱色率达99.97%,出水pH值3.63.