首页> 外文会议>Abu Dhabi International Petroleum Exhibition and Conference >Meeting Ultra-Low Sulphur Dioxide Emissions for Projects Based on Sour and Contaminated Gas Reserves
【24h】

Meeting Ultra-Low Sulphur Dioxide Emissions for Projects Based on Sour and Contaminated Gas Reserves

机译:基于酸和受污染的天然气储备的项目满足超低二氧化硫排放

获取原文

摘要

Designing gas treating line-ups for liquefied natural gas (LNG) and natural gas liquids (NGL) extraction facilities with low hydrogen sulphide (H2S) to carbon dioxide (CO2) ratios in the feed is challenging. The complexity increases by an order of magnitude as the emission requirements become very stringent. Sulphur dioxide (SO2) emission requirements vary from a more typical 150 to 50 ppmv. The acid gas from the acid gas removal units (AGRU) in these facilities i£ typically very lean, whereas Claus sulphur recovery units (SRU) prefer rich acid gas feeds. The presence of benzene, toluene, ethylbenzene, and xylenes (BTEX) and mercaptans in the original feedstock add an additional layer of challenges. It is necessary to maintain a sufficiently high temperature in the Claus furnace for the efficient destruction of these components. This may not be easily attainable with lean acid gases. In this scenario, it may be necessary to add an acid gas enrichment unit (AGEU) to the processing line-up. However, including an AGEU in the line-up would introduce AGEU off-gas containing H2S and mercaptans, which would be routed directly to the incinerator. This increases the SO2 that is emitted to atmosphere, therefore making it very challenging to meet stringent SO2 emission (<50 ppmv) limits. The conventional gas processing line ups are inadequate when dealing with difficult natural gas reserves in low SO2 emission regimes. This is especially true in the presence of organic sulphur (mercaptans and carbonyl sulphide (COS)) and BTEX. While bulk COS removal can be achieved with secondary amines, removal of mercaptans will require hybrid solvents like Sulfinol. The integration of gas treating process units and new breakthrough technologies are necessary to achieve optimal designs. Shell's novel gas processing line-ups address these challenges head-on. This paper focuses on one such innovative integrated line-up and compares it with conventional line-ups for compliance with SO2 emission requirements. The chosen line-up involves the Shell CANSOLV* TGT+ (tail gas treating plus) system, which is an integrated sour gas treating solution that can ensure ultra-low SO2 emissions (less than 10 ppmv), even for natural gas reserves containing unfavourable H2S/CO2 feed ratios and significant BTEX and mercap-tan contamination. It also minimises the complexity of the process line-up. In addition, the Shell CANSOLV TGT+ line-up can improve operational flexibility and the gas processing operating window at comparable capital cost.
机译:将气体处理液化天然气(LNG)和天然气液体(NGL)提取设施的气体处理饲料中的低硫化氢(H2S)(CO 2)比率(CO 2)比例挑战。随着排放要求变得非常严格,复杂性增加了一个数量级。二氧化硫(SO2)排放要求因更典型的150至50ppmV而变化。这些设施中的酸性气体去除装置(Agru)的酸性天然气通常非常瘦,而Claus硫磺恢复单元(SRU)更喜欢富酸性气体供给。原料中存在苯,甲苯,乙苯和二甲苯(BTEX)和硫醇的硫醇添加额外的挑战。有必要在克劳斯炉中保持足够高的温度,以便有效地破坏这些组分。这可能不容易达到瘦酸气体。在这种情况下,可能需要将酸性气体浓缩单元(咏型)添加到处理阵容中。然而,包括阵容的古老古老将引入含有H2S和硫醇的古老气体,这将被直接路由到焚化炉。这增加了发射到大气的SO2,因此使其非常具有挑战性,以满足严格的SO2发射(<50 ppmv)限制。当在低SO2排放制度中处理困难的天然气储量时,传统的气体处理线路上升不足。在有机硫(硫醇和羰基硫化物(COS))和BTEX存在下,这尤其如此。虽然可以通过仲胺实现散装COS去除,但除去硫醇的除去将需要亚磺酰醇的杂种溶剂。储气处理单位和新的突破技术的整合是实现最佳设计所必需的。 Shell的新型天然气处理阵容解决了这些挑战。本文重点介绍了一种这种创新的集成阵容,并将其与传统的阵容进行比较,以遵守SO2排放要求。所选的阵容涉及壳牌CACSOLV * TGT +(尾气处理加)系统,这是一种集成的酸气体处理溶液,即使对于含有不利H2S的天然气储备,也可以保证超低SO2排放(小于10 ppmv) / CO2饲料比率和显着的BTEX和MELAP-TAN污染。它还可以最大限度地减少过程阵容的复杂性。此外,壳牌CACSOLV TGT +阵容可以以可比的资本成本提高运行灵活性和气体加工操作窗口。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号