Regenerable Sorbents for High-Temperature Desulfurization of Syngas from Biomass Gasification

Single-metal high-temperature solid sorbents for syngas cleaning using Mn, Ca, Fe, Cu, or Mo supported on γ-Al₂O₃ were synthesized, characterized, and tested in a fixed-bed reactor. H₂S and SO₂ concentrations in the gas after treatment at T = 400 to 700 °C were compared with thermodynamic calculations. The Mn-based sorbent showed the best ability to achieve a low sulfur residual in the gas, especially at temperatures above 600 °C. Sorbents with Fe, Cu, and Mo gave SO₂ formation in the initial phase, but this could be avoided by a pre-reduction treatment of the sorbent material.     

配加预处理脱硫灰对铁矿烧结基础特性的影响

 半干法脱硫灰堆弃处理占用土地且容易造成二次污染,将脱硫灰预处理后替代CaO熔剂配入烧结有望充分利用其中的熔剂组分,实现脱硫灰在钢铁企业的闭路资源化利用。研究了脱硫灰配加焦粉加热分解特性及替代CaO熔剂配加对铁矿粉烧结基础特性的影响。结果表明,配加1%焦粉可以有效提高脱硫灰分解率,减少CaSO₄的生成。随着预处理脱硫灰替代CaO比例的增加,铁矿粉同化温度和黏结相强度呈现先增加后减小的趋势;液相流动性呈现单调增加趋势,当替代比超过40%时,液相流动性形成了流动性很大的“假象”;黏结相微观结构表明,替代比例小于40%时,有利于烧结试样中铁酸钙的生成;综合考虑,最佳的替代比例应小于40%。     

复合外加剂改性盐石膏的研究

盐石膏的主要成分为无水硫酸钙,其活性差、凝结硬化慢、强度低,需要添加活性剂来激发盐石膏的活性。通过复合外加剂对盐石膏加以改性,并通过XRD和SEM对其作用机理做了分析。结果表明,单掺脱硫石膏和建筑石膏均能缩短盐石膏的凝结时间,建筑石膏的效果较好,但掺量不宜过高。复掺建筑石膏和缓凝剂时,两者比例要控制得当,适宜的建筑石膏和缓凝剂掺量分别为50%和0.10%~0.12%（质量分数）。分析可知,大掺量建筑石膏会增加盐石膏硬化体中二水相和针棒状晶体的含量;缓凝剂掺量的增加,会降低盐石膏硬化体中二水相的含量,棱形晶体增多,从而降低了盐石膏的强度。     

窑灰作脱硫剂的水泥窑湿法脱硫系统优化

针对水泥窑生产工艺中生料磨启停工序引起的烟气温度、二氧化硫浓度对湿法脱硫系统的影响以及杂质对湿法脱硫系统设备和浆液储罐的影响,提出了优化设计方法和运行措施,以便达到较好的烟气脱硫效果。实践表明,该工艺综合循环利用窑灰作脱硫剂,不仅可将烟气中二氧化硫能够达标排放,而且脱硫副产物石膏可作为水泥缓凝剂添加料,有较好的工程应用价值。     

关于电石炉散点除尘灰在热电脱硫装置的应用研究

通过对散点除尘灰的成分进行分析,并结合生产实际,提出将散点除尘灰在干法及湿法脱硫系统使用,既有效利用了生产固废,又节省了生产成本。     

循环流化床脱硫灰用于水泥生产的研究

褐煤作燃料热电厂产生的循环流化床脱硫灰应用于我公司2 500 t/d新型干法窑生产线水泥生产，由于褐煤中全硫含量偏高且波动大，由此致使脱硫过程中脱硫剂比例变化波动也大，将熟料、矿渣、脱硫灰分别用小磨粉磨后进行试验，在试验基础上，除了对该脱硫灰超细粉磨外，同时必须要解决脱硫灰的均化和f-CaO消解问题，通过技术改造使系统设备、工艺更加适合采用脱硫灰复掺技术。     

半干法烟气脱硫脱硝除尘一体化技术在焦化厂中的应用

介绍了焦化厂半干法烟气脱硫脱硝除尘一体化技术在焦化厂中的应用,描述了半干法烟气脱硫、低温选择性催化还原法(SCR)脱硝+除尘一体化工艺流程,该工艺运行效果、运行参数、工艺技术的特点,运行中常见问题及解决方法和未来需要进一步思考和解决的问题等。实践证明,该工艺技术在焦化厂能够长期稳定运行,脱硫脱硝及除尘效果较好,烟气指标可达到环保要求。     

Catalytic oxidative desulfurization of gasoline using phosphotungstic acid supported on MWW zeolite

Catalysts for the desulfurization of gasoline samples were synthesized via the immobilization of well-dispersed phosphotungstic acid (HPW) on Mobil composition of matter-twenty-two (MWW) zeolite. Characterization results indicated that these catalysts possess a mesoporous structure with the retention of the Keggin structure of immobilized HPW. Relevant reaction parameters influencing sulfur removal were systematically investigated, including HPW loading, catalyst dosage, temperature, initial S-concentration, molar ratio of oxidant to sulfide (O/S), volume ratio of MeCN to model oil (Ext./oil), and sulfide species. The 40 wt-% HPW/MWW catalyst exhibited the highest catalytic activity with 99.6% dibenzothiophene sulfur removal from prepared samples. The 40 wt-% HPW/MWW catalyst was recycled four times and could be easily regenerated. Finally, as an exploratory study, straight-run-gasoline and fluid catalytic cracking gasoline were employed to accurately evaluate the desulfurization performance of 40 wt-% HPW/MWW. Our research provides new insights into the development and application of catalysts for desulfurization of gasoline.     

煤粉锅炉脱硫系统中除尘器压差过高原因及解决方案

高倍率灰钙循环烟气脱硫技术在神东矿区的煤粉锅炉环保改造项目中已投入建设并成功运行,脱硫率可达95%以上。在NGD系统的运行调试期,布袋除尘器压差的数值及其上升速度均较改造前有大幅提高,影响了锅炉系统的正常运行并降低了布袋除尘器的运行效率。为了解决此问题,先分析滤料透气性降低而导致布袋除尘器压差上升的根本原因,再结合现场调研情况对NGD系统工况下的烟气含湿量、烟气温度、烟气灰浓度、除尘器本体的问题以及上游锅炉系统问题逐一进行对比和分析,并找出问题产生的各主要因素。NGD系统中布袋除尘器差压升高的原因包括多方面,为了使NGD系统的运行更加稳定,需要使除尘器适应NGD系统的工况并对系统中部分设备进行改造。在未来NGD系统的设计中,布袋除尘器需按高浓度烟气设计,且针对煤粉工业锅炉的运行、维护特性应加入对烟气中含水量的监测及对布袋除尘器的相应保护措施。     

Catalytic oxidative desulfurization of dibenzothiophene utilizing molybdenum and vanadium oxides supported on MCM-41

As a series of bimetallic nanocatalysts, molybdenum/vanadium oxides supported on the silica (MoO₃/V₂O₅/MCM-41) were prepared by the impregnation. Their catalytic activity in the oxidation of dibenzothiophene was investigated using H₂O₂ as an oxidant. Textures and surface properties of the prepared catalysts were characterized using FT-IR, XRD, FESEM-EDX and N₂ adsorption/desorption techniques. The effects of main process variables including H₂O₂/DBT molar ratio, catalyst dosage, reaction temperature and reaction time were analyzed by employing the response surface methodology (RSM). The effect of the MoO₃/V₂O₅ loading on the catalytic performance of the catalysts was also investigated. The results indicated that the catalytic activity of the catalyst was increased by enhancing the MoO₃/V₂O₅ content. Thus, the catalyst with high MoO₃/V₂O₅ loading (20%MoO₃/20%V₂O₅/60%MCM-41) indicated the highest catalytic activity and could convert 99.06% of dibenzothiophene under the optimum conditions. Mass and FT-IR analysis demonstrated that the major product of dibenzothiophene oxidation was its corresponding sulfone. The catalyst could be recycled five times without any considerable reduction in its catalytic activity. The kinetics of the reaction fitted the pseudo-first-order equation pretty well. Eventually, a reaction mechanism for the catalytic oxidation of DBT in the presence of MoO₃/V₂O₅/MCM-41 was proposed.