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CONTROLLING AMINE DEGRADATION IN A SULFINOL-D GAS SWEETENING FACILITY

机译:控制氨基酚-D燃气加油设施中的胺降解

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A midstream facility in Northeast British Columbia is located within one of Canada's most sour conventional gas fields.The facility processes gas from wells with H2S as high as 40 wt%,containing extremely high amounts of other contaminants including mercaptans,elemental sulphur and CO2.Located at the heart of this field is a multi-towered amine system utilizing Shell's patented Sulfinol-D,which consists of a blend of Diisopropanolamine(DIPA),Sulfolane and water.The solution is used to sweeten a typical inlet gas of 165 mmscfd containing 12% H2S,10% CO2,>200 ppm COS and>150 ppm mercaptans. Over the past 30 years,the Sulfinol-D solution has experienced elevated degradation rates,requiring multiple investigations to help battle the amine degradation.Mitigation steps from these investigations have included [1] the replacement of the reboiler bundle to reduce thermal degradation,[2] the installation of horizontal coalescing filters to reduce inlet contamination and [3] on-site vacuum distillation to reduce heat stable salts and DIPA-Ox.Degradation rates have typically been controlled at 5-6 lbs/mmscf through these initiatives. In 2017,through to 2019,degradation rates began to unexpectantly climb.At their peak,rates in excess of 20-23 lbs/mmscf were observed,well beyond typical Sulfinol-D degradation rates of 2-3 lbs/mmscf.During this time degradation was controlled primarily by bleed and feed; a very expensive solution resulting in the facility replacing roughly 80% of their inventory per year. This paper follows the steps taken to reduce the amine degradation from 23 lb/mmscf to 2 lb/mmscf over a one-year period from November 2019 to October 2020.It will highlight the inlet feed upgrades completed during the 2019 turnaround and will evaluate the overall effectiveness of all other amine degradation control measures put in place.This will include an evaluation of the reduction in the overall amine degradation rate and will specifically break down the amine degradation mechanism(CO2,O2 and sulphur)observed during each stage of the program.
机译:东北不列颠哥伦比亚省甲中游工厂位于加拿大最常规酸气等多个领域设施工艺气体中的一个内从井用H2S高达40重量%,含有极高量的其它污染物,包括硫醇,单质硫和CO2.Located的在这个领域的心脏是利用壳牌公司的专利Sulfinol-d,它由二异丙醇胺(DIPA)的共混物的多耸立胺体系,环丁砜和water.The溶液用于增甜的典型入口气体的165 MMSCFD含有12 %H 2 S,10%CO 2,> 200ppm的COS和> 150ppm的硫醇。在过去的30年中,Sulfinol-d溶液经历升高的降解率,需要多个调查,以帮助从战斗这些调查胺degradation.Mitigation步骤已包括[1]替换再沸器束的,以减少热降解,[2 ]的水平聚结过滤器的安装,以减少污染的入口和[3]在现场真空蒸馏,以减少已典型地在5-6磅/透过这些措施百万标准立方英尺被控制热稳定盐和DIPA-Ox.Degradation率。 2017年,通过对2019年,降解速率开始unexpectantly climb.At高峰,超过了20-23磅率/百万标准立方英尺观察,远远超出了2-3磅典型Sulfinol-d降解率/ mmscf.During此时降解主要是由泄放和进料控制;一个非常昂贵的解决方案,导致工厂更换它们每年库存的80%左右。本文遵循以减少23胺降解所采取的步骤磅/百万标准立方英尺至2磅/百万标准立方英尺超过一年的时间从​​十一月到2019年十月2020.It将突出2019检修期间完成入口进料中的升级和将评估的投入place.This所有其他的胺降解控制措施整体有效性将包括在整体的胺降解速率的降低的评估和将特异性分解过程中该程序的每个阶段中观察到的胺降解机制(CO2,O2和硫) 。

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