固体废弃物轮胎的热解技术

综述了国内外对废轮胎的处理状况，并详细地讨论了废轮胎热解技术的发展、分类以及典型工艺流程。热解技术主要包括油化技术、气化技术和炭化技术三种，并可制得衍生油、燃料气、碳黑等产品。分析了废轮胎热解工艺存在的问题，指出了如何开发环境友好的集成工艺是废轮胎热解工艺的发展方向。     

高活性脱硫剂脱硫工艺的实验研究

对以粉煤灰为原料制备的高活性脱硫剂进行了半干法烟气脱硫实验研究,考虑添加剂、脱硫剂加入量、反应温度、烟气流量工艺因素的影响时该活性脱硫剂的脱硫性能;实验结果表明,加入添加剂后,脱硫效率提高1.5%～8.1%;当烟气流量＜2 m3/min,钙硫比取1.5～2.0范围时,脱硫效率较高;一定范围内反应温度变化对脱硫效率影响不大.     

高活性脱硫剂脱硫工艺的实验研究

对以粉煤灰为原料制备的高活性脱硫剂进行了半干法烟气脱硫实验研究，考虑添加剂、脱硫剂加入量、反应温度、烟气流量工艺因素的影响时该活性脱硫剂的脱硫性能；实验结果表明，加入添加剂后，脱硫效率提高1．5％～8．1％；当烟气流量〈2m^3／min，钙硫比取1．5—2．0范围时，脱硫效率较高；一定范围内反应温度变化对脱硫效率影响不大。     

基于密相半干法脱硫工艺的生石灰消化及改性

以某公司生产的生石灰作为脱硫剂,密相半干法脱硫工艺在某炼铁厂烧结烟气脱硫工程的应用为例,对生石灰的消化反应和调质改性进行实验,考察其满足脱硫要求的最佳消化条件和烧结机头灰作为改性剂的比重。实验表明,当水灰比在1.5～1.7、生石灰粒径在200μm以下、消化温度在55℃左右、搅拌轴转速在15～25 r/min的范围内,可以保证生石灰有最佳的转化率,烧结机头灰占比重的5%时为最佳改性剂量;同时对实验的工程运行成本和脱硫效果进行分析,使用自制改性脱硫剂即可以节约运行成本和水电资源,又能提高脱硫效果,为脱硫设备的长期稳定运行提供了可靠依据。     

烧结烟气脱硫剂性能的研究

为了提高脱硫效率和合理利用烧结过程中产生的机头灰,在半干法烟气脱硫剂生石灰中,加入一定量的烧结机头灰作为脱硫催化剂。在测定机头灰与生石灰化学成分、粒度和比表面积的基础上,研究和分析了机头灰与生石灰的质量配比对于脱硫效率的影响。结果表明,脱硫剂与机头灰在粒径分布和比表面积上都较接近,但经过消化活化后的混合脱硫剂的比表面积明显增大。当机头灰添加量为脱硫剂质量的2%～5%时,脱硫效率提高了2%～3%。机头灰与生石灰的胶凝反应以及机头灰中Fe2O3的催化作用是主要的作用机理。     

石灰石高温煤气脱硫的试验研究

采用天然石灰石做脱硫剂，在固定床上进行硫化氢高温脱除的试验研究，考察了脱硫剂粒径、反应温度、气速及高温煤气中H2对石灰石脱硫性能的影响，同时还用热重分析(TG)、扫描电镜(SEM)、X-射线衍射(XRD)等测试手段对脱硫剂的物相组成和结构等进行了表征。结果表明，脱硫剂的粒径对脱硫效果的影响很大，0.38～0.83 mm的石灰石脱硫效果最佳；温度对脱硫效果的影响比较复杂，最佳的操作温度为850℃；气速对脱硫效果的影响较明显，脱硫剂的穿透时间随气速的减小而加长；H₂对脱硫过程起阻碍作用，气速越小，这种阻碍作用越明显。     

城市生活垃圾、污泥和煤粉混合燃料热值的研究

为了寻求生活垃圾和污泥的高效资源化、能源化方法.选取生活垃圾、污泥和煤粉的混合,枯枝落叶,助燃剂MnO2,脱硫剂 CaO 为控制因子,安排正交试验,成型加工为混合燃料.测定其热值,并通过正交分析,筛选出燃料最大热值组合,即混合时垃圾、污泥、煤粉的比例为 1:1:2,枯枝落叶所占比例为 0%,助燃剂 MnO2 含量为 0.18%,脱硫剂 CaO 含量为 1.5/(100 g),该燃料的热值为 17.8898 kJ/g.为该混合燃料的推广与应用提供理论依据.     

钢渣脱除烧结烟气中二氧化硫的实验研究

通过对钢渣的分析,确定了其作为脱硫剂的可能性.从钢渣在不同操作条件下脱硫的实验研究看,钢渣能有效地脱除烟气中的SO2,在湿润状态、低流速条件下,微细钢渣的脱硫能力较强,钢渣作为脱硫剂使用将具有良好的经济效益和环境效益.     

FeSO4/Ac脱硫剂脱硫性能的研究

为寻找经济适用且具有较高效率的烟气脱硫方法．研制了FeSO4／Ac脱硫剂。并对FeSO4／Ac脱硫剂的脱硫性能进行了实验研究。实验研究结果显示,烟气中O2、水蒸气含量的多少及脱硫温度的高低会影响FeSO4／Ac脱硫剂的脱硫性能。实验证明,当n(O2):n(SO2)=7～10、n(H2O)：n(SO2)=3～5、脱硫温度取120℃时,FeSO4／Ac脱硫剂具有良好的脱硫性能,脱硫效率可达92．1％～96．8％。FeSO4／Ac脱硫剂能够再生重复使用。采用水蒸气加热再生法对FeSO4／Ac脱硫剂进行再生,实验结果显示,经4次加热法再生的FeSO4／Ac脱硫剂的脱硫效率仍能达到91％。     

粗媒体颗粒流化床半干法烟气脱硫

开发了粗媒体颗粒流化床半干法烟气脱硫技术.在流化床内加入惰性粗媒体颗粒,改善脱硫剂与烟气的接触,延长脱硫剂在床内的停留时间,促进脱硫反应进行,提高脱硫效率和脱硫剂利用率.以工业用石灰石为脱硫剂,实验研究了粗媒体颗粒的加入量及其他操作条件对此过程脱硫效率的影响.结果表明:随着粗媒体颗粒粒径减小及床内加入量增加,烟气脱硫效率提高;随着Ca/S增大、饱和接近度降低、空速及脱硫剂颗粒粒径减小,脱硫效率提高.当粗媒体颗粒的静止床高为122 mm,饱和接近度为15～18℃、空速为2850 h-1、钙硫比为1.0～1.1、脱硫剂粒径为64μm时,脱硫效率可达90%以上.     

空速和二氧化碳对沼气脱硫剂硫容确定的影响

为了弄清空速与二氧化碳含量对氧化铁脱硫剂硫容确定的影响,分别在实验气源为纯硫化氢,空速为40、80、120和160 h-1以及实验气源为二氧化碳含量分别在0%、20%、40%和80%,其余为硫化氢,空速为80 h-1条件下,对T502(粗脱硫剂)和HXT-2(精脱硫剂)2种氧化铁脱硫剂进行了不同测试条件对氧化铁硫容确定影响的研究。研究结果表明,T502和HXT-2氧化铁脱硫剂硫容测试结果随着空速和二氧化碳含量增加而减少,结果显示了在空速较低条件下(120h-1),二氧化碳含量在40%以下时对氧化铁脱硫剂硫容测试结果影响不大,但二氧化碳含量在40%以上时,对氧化铁脱硫剂硫容测试结果影响显著。     

Some Technical and Economic Aspects of Residual Fuel Oil Desulfurization

Combustion of residual, the most common type of fuel oil used in industrial and commercial steam generating plants, accounts for about 600,000 tons or 37 percent of the sulfur oxide emissions in New York state. On the average, residual oil available in New York state contains about 2.2 percent sulfur and is consumed at an annual rate of approximately 85 million barrels. The removal of sulfur from many types of residuals should become economically feasible as a result of the development of the HDS and H-Oil hydrodesulfurization processes. From studies recently made, these methods of desulfurization have been estimated to vary from a minimum of no appreciable increase in overall cost to a maximum of about one cent per gallon. The by-product distillates produced in hydrodesulfurization are a very significant factor in making the process economical and the demand for these is increasing at a greater rate than residual.     

Desulfurization of Caribbean Fuel

An American Petroleum Institute study of desulfurization of Caribbean fuel oil was completed in February 1967. The report is unique in that proprietary information was made available to the contractor, the Bechtel Corp., by task force members and licensors of desulfurization processes. Thus confidential information never before available to a single organization was used to develop feasibility and incremental costs of various processes for desulfurization. The report provides needed guideposts for decision-making by governmental units as well as by industry. Incremental costs are presented for intermediate levels of desulfurization from the normal level for Caribbean heavy fuel oil of 2.6% down to 0.5%, as well as the sensitivity of costs to sulfur credits and to rate of recovery of invested capital. Degree of justifiable confidence in the various data is discussed. Effects of desulfurization on other characterisics of the fuel oil are also discussed.     

Spray-dry desulfurization of flue gas from heavy oil combustion

An experimental investigation on sulfur dioxide removal in a pilot-scale spray dryer from the flue gas generated by combustion of low-sulfur (S) heavy oil is reported. A limewater slurry was sprayed through an ultrasonic two-fluid atomizer in the spray-dry chamber, and the spent sorbent was collected downstream in a pulse-jet baghouse together with fly ash. Flue gas was sampled at different points to measure the desulfurization efficiency after both the spray-dry chamber and the baghouse. Parametric tests were performed to study the effect of the following variables: gas inlet temperature, difference between gas outlet temperature and adiabatic saturation temperature, lime-to-S ratio, and average size of lime particles in the slurry. Results indicated that spray drying is an effective technology for the desulfurization of low-S fuel oil flue gas, provided operating conditions are chosen carefully. In particular, the lowest gas inlet and outlet temperatures compatible with baghouse operation should be selected, as should a sufficiently high lime-to-S ratio. The attainment of a small lime particle size in the slurry is critical for obtaining a high desulfurization efficiency. A previously presented spray-dry flue gas desulfurization model was used to simulate the pilot-scale desulfurization tests, to check the ability of the model to predict the S capture data and its usefulness as a design tool, minimizing the need for pilot-scale experimentation. Comparison between model and experimental results was fairly good for the whole range of calcium/S ratios considered.     

油田含油污泥热解制备烟气脱硫剂

为实现油田含油污泥深度资源化,针对高含油的孤岛采油厂含油污泥采用热解处理,回收油气资源的同时将热解残渣制备成烟气脱硫剂。以苯吸附值和热解残渣含油率为基准对热解工艺进行了优化,对热解油品和残渣进行分析,热解残渣经过后续处理进行了烟气脱硫性能评价。通过正交实验得到热解最佳工艺条件为:氮气保护下,热解温度550℃,热解时间4h,升温速率10℃/min。此时苯吸附值为60.12mg/g,热解残渣含油率为0.29%。最佳工艺条件下,热解油品产率可达10%左右,回收率大于65%,热裂解作用明显,热解油品的品质较好,产生的不凝气体可以作为洁净燃料气;热解残渣经过后续处理,可用于脱除烟气中的SO2,吸附脱硫能力较好,穿透硫容达到3%以上。     

Natural desulfurization in coal-fired units using Greek lignite

This paper analyzes the natural desulfurization process taking place in coal-fired units using Greek lignite. The dry scrubbing capability of Greek lignite appears to be extremely high under special conditions, which can make it possible for the units to operate within the legislative limits of sulfur dioxide (SO2) emissions. According to this study on several lignite-fired power stations in northern Greece, it was found that sulfur oxide emissions depend on coal rank, sulfur content, and calorific value. On the other hand, SO2 emission is inversely proportional to the parameter gammaCO2(max), which is equal to the maximum carbon dioxide (CO2) content by volume of dry flue gas under stoichiometric combustion. The desulfurization efficiency is positively correlated to the molar ratio of decomposed calcium carbonate to sulfur and negatively correlated to the free calcium oxide content of fly ash.     

氧化镁烟气脱硫反应特性研究

利用实验室规模的鼓泡式反应装置,对比了碳酸钙、氧化镁和氧化镁/硫酸镁脱硫剂的反应活性,证实脱硫液中高浓度硫酸镁的存在是保证镁法脱硫效率高于钙法的重要因素,并考察了硫酸镁浓度、脱硫剂(氧化镁)浓度、烟气量、SO2浓度和吸收液温度等因素对脱硫效率的影响。结果表明,脱硫反应可以根据pH分为2个不同阶段;反应过程中脱硫效率随着硫酸镁浓度的增加而显著升高;烟气量增加将会导致脱硫效率有所下降;入口SO2浓度升高,脱硫效率下降;氧化镁浓度、温度对脱硫效率影响不显著。结合实验现象进行推断,氧化镁脱硫的反应过程受SO2在气液两相界面的传质扩散和其水解产物在液相的扩散控制。     

锌、铁等离子对氧化锌烟气脱硫工艺中亚硫酸锌氧化的影响

在氧化锌法脱除烟气SO2工艺中，脱硫产物亚硫酸锌的氧化是实现锌、硫资源回收的关键环节。在pH为4～5，25℃等条件下，考察了锌、铁、镉离子对亚硫酸锌氧化过程的影响。结果发现，铁离子对亚硫酸锌氧化过程有较强的催化作用，锌离子有一定的催化作用，而低浓度的镉离子几乎不影响氧化过程。进一步的研究表明，锌、铁离子的独自催化氧化速率对各自的浓度均为0．5级响应，但在混合状态下，锌离子对铁离子的催化过程有抑制作用。     

酸碱改性对氧化铁脱硫剂脱硫性能影响的研究

通过酸碱改性制备了酸式和碱式2种不同表面性质的常温氧化铁脱硫剂,并采用FT-IR技术对其表面酸碱性质和净化硫化氢废气活性进行了研究.结果表明,表面酸碱件质不同的脱硫剂其脱硫反应行为也不同,在脱硫过程中硫化氢氧化生成的硫酸及亚硫酸会影响脱硫剂的表面酸碱性质,造成酸式脱硫剂的表面酸性更强,从而抑制了硫化氢分子在酸式脱硫剂表...     

From Air Repair to EM: A&WMA’s Publications through a Century of Change

Abstract

This paper analyzes the natural desulfurization process taking place in coal-fired units using Greek lignite. The dry scrubbing capability of Greek lignite appears to be extremely high under special conditions, which can make it possible for the units to operate within the legislative limits of sulfur dioxide (SO₂) emissions. According to this study on several lignite-fired power stations in northern Greece, it was found that sulfur oxide emissions depend on coal rank, sulfur content, and calorific value. On the other hand, SO₂ emission is inversely proportional to the parameter y _CO2max, which is equal to the maximum carbon dioxide (CO₂) content by vol ume of dry flue gas under stoichiometric combustion. The desulfurization efficiency is positively correlated to the molar ratio of decomposed calcium carbonate to sulfur and negatively correlated to the free calcium oxide content of fly ash.