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101.
阐述了利用柠檬酸钠溶液循环脱硫工艺对克劳斯制硫尾气进行脱硫处理的效果。工业试验结果表明,把克劳斯制硫尾气焚烧、洗涤降温后,用柠檬酸钠溶液循环吸收脱硫,脱硫效果好,排烟中二氧化硫体积质量低于50 mg/m3。该工艺将脱硫过程中回收的二氧化硫再返回克劳斯制硫装置回收硫黄。脱硫系统工程投资小,运行费用低,脱除二氧化硫的成本为1 172.5 RMB$/t,工艺简单,操作方便,排放的废液量少。 相似文献
102.
In this study, Claus reaction was applied for the selective removal of H2S contained in the gasified coal gas, and the characteristics of Claus reaction over the Ce-based catalysts were investigated to propose the reaction mechanism. The Ce-based catalysts showed a high activity on Claus reaction. Specially, Ce0.8Zr0.2O2 catalyst had a higher activity than CeO. On the basis of our experimental results, it was proposed that the selective oxidation of H2S was carried out by the lattice oxygen in the Ce-based catalysts and that the reduction of SO2 was performed by the lattice oxygen vacancy in the reduced catalyst. Since the mobility of the lattice oxygen in Ce0.8Zr0.2O2 composite catalyst was better than the one in CeO2, Ce0.8Zr0.2O2 provided more lattice oxygen for the selective oxidation of H2S. It was presumed that the reaction mechanism to convert H2S and SO2 into elemental sulphur over our prepared catalysts was different from the mechanism over the solid-acid catalysts. It is believed that Claus reaction over the Ce-based catalysts was carried out by the redox mechanism. Since the moisture was contained in the major components, CO and H, of the gasified fuel gas, the effects of CO and H2O on the catalytic reaction were investigated over a Ce-based catalyst. The conversion of H2S and SO2 was decreased in Claus reaction over the Ce-based catalysts as the concentration of either H2O or CO in the gasified coal gas was increased. Under the circumstances of the coexistence of both moisture and CO, however, the conversion was increased as the concentration of CO was increased. The reactivity of Claus reaction was varied in terms of the concentration ratio of CO to H2O. The maximum conversion of H2S and SO2 was achieved in the condition of that the concentration of CO contained in the reacting gas was higher than the one of H2O. The conversions of H2S and SO2 did not match to the stoichiometric ratios of Claus reaction. The higher conversion of H2S was obtained in the higher concentration of H2O, while the higher conversion of SO2 was achieved in the higher concentration of CO. It was another evidence to indicate that the Claus reaction over the Ce-based catalysts was carried out by the redox mechanism. 相似文献
103.
介绍改良的Claus工艺加Clinsulf工艺的硫回收系统的工艺流程,总结系统的运行状况,分析系统运行不正常的原因,提出改造措施,经过改造后系统运行效果良好. 相似文献
104.
105.
对降低尾气处理装置SO_2排放的认识与建议 总被引:6,自引:6,他引:0
针对将硫磺回收装置排放尾气中SO2质量浓度从960mg/m3降至500mg/m3以下的技术方案,提出通过降低贫液进入SCOT工艺选吸塔的温度及贫液中H2S浓度,可有效地将总硫回收率提高至99.9%以上;若再辅以配方型溶剂的应用,则有望进一步改善选吸效果与总硫回收率。但现有工业数据表明,目前,属于氧化-吸收型的Cansolv总硫回收率低于常规SCOT工艺。因此,对采用Cansolv工艺处理Claus硫磺回收装置尾气的方案宜采取慎重态度。 相似文献
106.
Mitchell J. Stashick Gabriel O. Sofekun Robert A. Marriott 《American Institute of Chemical Engineers》2020,66(6):e16225
Handling molten sulfur is inherently difficult due to liquid sulfur's extreme rheological behavior. Upon melting at 115°C, sulfur's viscosity remains low until reaching 160°C, the λ-transition region, where the viscosity increases to a maximum of 93,000 × 10−3 Pa s at 187°C. Within this study, our previous viscosity measurements for pure liquid elemental sulfur have been discussed along with new measurements on sulfur containing physically and chemically dissolved hydrogen sulfide (H2S). H2S is always incorporated into industrial sulfur which has been recovered through the modified Claus process in gas plants and oil refineries. Using the experimental data from this study, a semi-empirical correlation model was reported based on the reptation model of Cates to estimate the impact of H2S on liquid sulfur's viscosity as a function of temperature. The equation can be applied to commercial sources of sulfur with 0–500 ppm of total dissolved H2S. 相似文献
107.
为使克劳斯硫回收装置的硫回收率达到100%,讨论并比较了碱洗涤与生产硫酸这2种尾气处理技术。这2种技术都可用于满足最苛刻的排放要求,生产硫酸的成本略低。但除了成本之外,还应考虑炼油厂的总体布置、原油类型及硫和氮含量、产品酸的市场需求、所需公用工程的供应等因素。 相似文献
108.
S. ASADI M. PAKIZEH M. POURAFSHARI CHENAR 《Frontiers of Chemical Science and Engineering》2011,5(3):362
In a modern day sulfur recovery unit (SRU), hydrogen sulfide (H2S) is converted to elemental sulfur using a modified Claus unit. A process simulator called TSWEET has been used to consider the Claus process. The effect of the H2S concentration, the H2S/CO2 ratio, the input air flow rate, the acid gas flow of the acid gas (AG) splitter and the temperature of the acid gas feed at three different oxygen concentrations (in the air input) on the main burner temperature have been studied. Also the effects of the tail gas ratio and the catalytic bed type on the sulfur recovery were studied. The bed temperatures were optimized in order to enhance the sulfur recovery for a given acid gas feed and air input. Initially when the fraction of AG splitter flow to the main burner was increased, the temperature of the main burner increased to a maximum but then decreased sharply when the flow fraction was further increased; this was true for all three concentrations of oxygen. However, if three other parameters (the concentration of H2S, the ratio H2S/CO2 and the flow rate of air) were increased, the temperature of the main burner increased monotonically. This increase had different slopes depending on the oxygen concentration in the input air. But, by increasing the temperature of the acid gas feed, the temperature of the main burner decreased. In general, the concentration of oxygen in the input air into the Claus unit had little effect on the temperature of the main burner (This is true for all parameters). The optimal catalytic bed temperature, tail gas ratio and type of catalytic bed were also determined and these conditions are a minimum temperature of 300°C, a ratio of 2.0 and a hydrolysing Claus bed. 相似文献
109.
110.
采用自行研制的4条气路、双高灵敏热导检测器、五柱管专用气相色谱仪,对川西北净化厂引进的三级转化MCRC硫回收装置进行考核分析。用这台仪器检出该工艺过程涉及的15个组分的控制分析,由分析数据所得的考核值与工艺模拟电算程序的结果吻合。本文介绍的分析技术快速、可靠,适用于天然气净化厂硫磺回收及尾气处理工艺装置的控制分析和考核分析。 相似文献