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Sulphur Degassing - Technical Improvements and Best Practices

机译:脱硫-技术改进和最佳实践

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Un-degassed liquid sulphur produced from a Claus sulphur recovery unit typically contains 200 to 350 ppmw H_2S. The dissolved gas is partly present in the form of polysulfides (H_2S_x). If liquid sulphur is not degassed, then H_2S will be released during storage, handling, loading, and transport. Un-degassed sulphur can create an explosive mixture of H_2S in air, and poses a toxicity hazard as well as a noxious odor problem when H_2S is released from the un-degassed liquid or solid sulphur. Further, with regulations on SO_2 emissions continuing to tighten and as sulphur recovery efficiencies are routinely mandated higher, other sources of emissions in the sulphur recovery complex such as pit sweep air and storage tank vents are receiving increased scrutiny in North America and around the globe. Degassing of the liquid sulphur produced in a Claus plant can address the potential threats posed by un-degassed sulphur. Further, this can also mitigate emissions from the sulphur pit and storage tanks. This paper will briefly cover the main commercially available in-pit and out-of-pit sulphur degassing technologies and then focus on the D'GAASS technology which operates,at elevated pressures outside of the sulphur pit. The D'GASS technology permits recycle of the degassing air back to the SRU reaction furnace without the necessity of recycle gas blowers or ejectors and thereby totally eliminates emissions from the degassing operations. Such emissions can be significant for in pit degassing processes. While sulphur degassing to 10 ppmw H_2S is the common industry standard, the D'GAASS process can guarantee 5 ppmw thus providing additional safety and environmental benefits, which is of increasing interest to operators. To bring further relevance to the topic, several mechanical design, instrumentation and controls' lessons learned as the D'GAASS process was refined through the years will be shared to highlight best practice. In particular, the paper will demonstrate how the application of these lessons through process design improvements has increased the reliability and robustness of the process. This has led to over 90 units and 60,000 LTPD of licensed capacity globally with installations ranging in size from 10 MTPD to as large as 2,600 MTPD.
机译:由克劳斯硫磺回收装置生产的未脱气的液态硫通常包含200至350 ppmw H_2S。溶解的气体部分以多硫化物(H_2S_x)的形式存在。如果不对液态硫进行脱气,则在存储,处理,装载和运输过程中会释放出H_2S。未脱气的硫会在空气中形成H_2S的爆炸性混合物,当从未脱气的液态或固态硫中释放H_2S时,会产生毒性危害以及有害的气味问题。此外,随着关于SO_2排放的法规不断收紧,并且通常要求提高硫回收效率,因此在北美和全球范围内,越来越多的对硫回收综合体的其他排放源(如矿井清扫空气和储罐通风口)进行了审查。对克劳斯工厂生产的液态硫进行脱气可以解决未脱气硫的潜在威胁。此外,这还可以减轻来自硫坑和储罐的排放。本文将简要介绍市售的主要矿井内和矿井外硫磺脱气技术,然后重点介绍在硫磺井外高压下运行的D'GAASS技术。 D'GASS技术允许将脱气空气循环回SRU反应炉,而无需使用循环鼓风机或喷射器,从而完全消除了脱气操作的排放。这样的排放对于矿井脱气过程可能非常重要。虽然将硫脱气至10 ppmw H_2S是常见的工业标准,但D'GAASS工艺可以保证5 ppmw,从而提供了额外的安全性和环境效益,这对操作员越来越感兴趣。为了与该主题进一步相关,将分享多年来通过D'GAASS流程改进而汲取的一些机械设计,仪表和控制方面的经验教训,以突出最佳实践。特别是,本文将演示通过改进流程设计来应用这些课程如何提高流程的可靠性和健壮性。这在全球范围内已导致90多个单位和60,000 LTPD的许可容量,安装大小从10 MTPD到最大2,600 MTPD不等。

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