{"title":"关于控制和减少胺基溶剂中泡沫形成的全面综述","authors":"Reza Shahouni , Mohsen Abbasi , Mohammad Akrami","doi":"10.1016/j.ceja.2024.100618","DOIUrl":null,"url":null,"abstract":"<div><p>Amine solvent processes are often confronted with the problem of foaming, which can lead to reduced amine efficiency in H2S and CO2 absorption. To this end, it is crucial to investigate the causes of foaming in amine systems and develop a procedure to effectively combat this problem. According to this research, the main causes of foaming in amine solutions are hydrocarbon condensate, suspended solids, amine degradation products, corrosion inhibitors and operating parameters. To prevent foaming in the scrubber, it is important to use filter coalescers, activated carbon, and precoat filters that can remove solid particles and hydrocarbon mists from the feed gas and amine solution. It is also recommended to maintain the amine inlet temperature at 5–10 °C above the dew point of the feed gas to prevent the hydrocarbons from condensing in the scrubber. Foaming can be significantly influenced by unsaturated fatty acids even in small amounts of 10 ppm in the amine solution. Acetic acid and octanoic acid are also notable amine degradation byproducts that can reduce foam volume by 25% and 23%, respectively. On the other hand, piperazine and bicine are other amine byproducts that can significantly impact the foam breaking time by 467% and 344%, respectively. To prevent amine degradation, it is recommended to maintain the temperature of the amine at 125–130 °C in the stripper and at 40–45 °C in the scrubber. To effectively manage and control foaming in amine solutions, a comprehensive procedure is advised to control and mitigate this issue. Lastly, future areas of research have been identified to address the problem of foam in amine systems.</p></div>","PeriodicalId":9749,"journal":{"name":"Chemical Engineering Journal Advances","volume":"19 ","pages":"Article 100618"},"PeriodicalIF":5.5000,"publicationDate":"2024-05-22","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://www.sciencedirect.com/science/article/pii/S266682112400036X/pdfft?md5=02d5f828cfb50f3808297bfe2af0b43c&pid=1-s2.0-S266682112400036X-main.pdf","citationCount":"0","resultStr":"{\"title\":\"A comprehensive review on control and mitigating the foam formation in amine-based solvents\",\"authors\":\"Reza Shahouni , Mohsen Abbasi , Mohammad Akrami\",\"doi\":\"10.1016/j.ceja.2024.100618\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>Amine solvent processes are often confronted with the problem of foaming, which can lead to reduced amine efficiency in H2S and CO2 absorption. To this end, it is crucial to investigate the causes of foaming in amine systems and develop a procedure to effectively combat this problem. According to this research, the main causes of foaming in amine solutions are hydrocarbon condensate, suspended solids, amine degradation products, corrosion inhibitors and operating parameters. To prevent foaming in the scrubber, it is important to use filter coalescers, activated carbon, and precoat filters that can remove solid particles and hydrocarbon mists from the feed gas and amine solution. It is also recommended to maintain the amine inlet temperature at 5–10 °C above the dew point of the feed gas to prevent the hydrocarbons from condensing in the scrubber. Foaming can be significantly influenced by unsaturated fatty acids even in small amounts of 10 ppm in the amine solution. Acetic acid and octanoic acid are also notable amine degradation byproducts that can reduce foam volume by 25% and 23%, respectively. On the other hand, piperazine and bicine are other amine byproducts that can significantly impact the foam breaking time by 467% and 344%, respectively. To prevent amine degradation, it is recommended to maintain the temperature of the amine at 125–130 °C in the stripper and at 40–45 °C in the scrubber. To effectively manage and control foaming in amine solutions, a comprehensive procedure is advised to control and mitigate this issue. 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引用次数: 0
摘要
胺溶剂工艺经常会遇到起泡问题,这可能会降低胺吸收 H2S 和 CO2 的效率。为此,研究胺系统起泡的原因并开发有效解决这一问题的程序至关重要。根据这项研究,胺溶液起泡的主要原因包括碳氢化合物冷凝物、悬浮固体、胺降解产物、腐蚀抑制剂和操作参数。为防止洗涤器中产生泡沫,必须使用过滤器凝聚器、活性炭和预涂层过滤器,以去除原料气和胺溶液中的固体颗粒和碳氢化合物雾气。此外,还建议将胺液入口温度保持在高于原料气露点 5-10 °C 的水平,以防止碳氢化合物在洗涤器中凝结。即使胺溶液中的不饱和脂肪酸含量仅为 10 ppm,也会对起泡产生重大影响。乙酸和辛酸也是胺降解的显著副产物,可使泡沫体积分别减少 25% 和 23%。另一方面,哌嗪和联苯胺也是其他胺类副产物,可显著影响泡沫破裂时间,影响程度分别为 467% 和 344%。为防止胺降解,建议在汽提塔中将胺的温度保持在 125-130 ℃,在洗涤塔中保持在 40-45 ℃。为有效管理和控制胺溶液中的泡沫,建议采用综合程序来控制和缓解这一问题。最后,还确定了未来的研究领域,以解决胺系统中的泡沫问题。
A comprehensive review on control and mitigating the foam formation in amine-based solvents
Amine solvent processes are often confronted with the problem of foaming, which can lead to reduced amine efficiency in H2S and CO2 absorption. To this end, it is crucial to investigate the causes of foaming in amine systems and develop a procedure to effectively combat this problem. According to this research, the main causes of foaming in amine solutions are hydrocarbon condensate, suspended solids, amine degradation products, corrosion inhibitors and operating parameters. To prevent foaming in the scrubber, it is important to use filter coalescers, activated carbon, and precoat filters that can remove solid particles and hydrocarbon mists from the feed gas and amine solution. It is also recommended to maintain the amine inlet temperature at 5–10 °C above the dew point of the feed gas to prevent the hydrocarbons from condensing in the scrubber. Foaming can be significantly influenced by unsaturated fatty acids even in small amounts of 10 ppm in the amine solution. Acetic acid and octanoic acid are also notable amine degradation byproducts that can reduce foam volume by 25% and 23%, respectively. On the other hand, piperazine and bicine are other amine byproducts that can significantly impact the foam breaking time by 467% and 344%, respectively. To prevent amine degradation, it is recommended to maintain the temperature of the amine at 125–130 °C in the stripper and at 40–45 °C in the scrubber. To effectively manage and control foaming in amine solutions, a comprehensive procedure is advised to control and mitigate this issue. Lastly, future areas of research have been identified to address the problem of foam in amine systems.