首页> 外文会议>52nd Laurance Reid Gas Conditioning Conference, Feb 24-27, 2002, Norman Oklahoma >Degradation of amine solvents and the relation with operational problems
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Degradation of amine solvents and the relation with operational problems

机译:胺类溶剂的降解及其与操作问题的关系

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Amine solvent formulations are used for the removal of acidic components such as CO_2 and/or H_2S from natural gas to comply with sales gas specifications or to make the gas suitable for liquefaction. During operation of an amine unit degradation of the solvent occurs due to reaction with contaminants (oxygen, sulphur, CO_2) in the feed gas. As a result of these degradation reactions, amine degradation products are formed including: oxazolidone; other amines; acids and higher molecular weight products (amine dimers and oligomers). These degradation products lead to a number of operational problems in the units if allowed to build up in concentration. Build up over time is related to solvent age, use and handling and will occur in every amine solvent. Operational problems include: 1. Increased corrosion rates, particularly at the lean side of the amine unit. 2. Fouling in those parts of the unit where solvent flow velocities are low and the solvent loading of H_2S or CO_2 is high i.e. trays and bottom of the contactor and the lean/-rich heat exchanger. In "CO_2-only" systems fouling tends to occur more often in the regenerator overhead. Fouling of the heat exchanger leads to a reduction in heat transfer and an increased steam use for regeneration. Ultimately plugging of the heat exchanger may occur, restricting solvent circulation and treating capacity. 3. Decreased treating capacity of the unit due to lower free amine strength and a lower availability. Part of the amine is degraded and part is "tied up" by the acids formed (heat stable salts). 4. Increased foaming tendency of the solvent by the presence of a higher amount of suspended solids (also requiring a high rate of filter change outs). 5. A high flash gas production due to a high carry-under of gas with solvent in the main absorber. Increased corrosion rates can be explained in terms of a high acid content of the solvent decreasing the pH and in terms of high molecular weight degradation products that increase the ability of the solvent to keep iron in solution (high complexing power). The overall result is a high activity of the "iron pump" mechanism leading to high corrosion rates and associated fouling problems. Careful monitoring of the operation of the unit in combination with measuring solvent composition and solvent properties, together with good solvent maintenance practices will ensure reliable operation.
机译:胺溶剂配方用于从天然气中去除酸性成分,例如CO_2和/或H_2S,以符合销售气体规范或使该气体适合液化。在胺单元操作期间,由于溶剂与进料气体中的污染物(氧气,硫磺,CO_2)反应而发生溶剂降解。这些降解反应的结果是,形成了胺降解产物,包括:恶唑烷酮;其他胺酸和更高分子量的产品(胺二聚体和低聚物)。如果允许其集中,这些降解产物会导致单元中的许多操作问题。随着时间的推移,积聚与溶剂的使用期限,使用和处理有关,并且会在每种胺溶剂中发生。操作上的问题包括:1.腐蚀速率增加,尤其是在胺装置的贫油侧。 2.装置中那些溶剂流速低并且H_2S或CO_2的溶剂负荷高的部分,即接触器的塔板和底部以及稀薄/浓热换热器的结垢。在“仅CO_2”系统中,结垢往往发生在再生塔的顶部。热交换器的结垢导致传热的减少和用于再生的蒸汽的增加。最终可能会发生热交换器堵塞,从而限制溶剂循环和处理能力。 3.由于较低的游离胺强度和较低的利用率,导致单元的处理能力下降。一部分胺被降解,一部分被形成的酸(热稳定盐)“束缚”。 4.由于存在大量的悬浮固体(也需要很高的滤芯更换率),溶剂的发泡趋势会增加。 5.由于主吸收塔中带有溶剂的大量气体带入,因此产生了大量的闪蒸气。可以根据溶剂的高酸含量降低pH值以及高分子量降解产物来提高腐蚀速率,这些高分子量降解产物会增加溶剂将铁保持在溶液中的能力(高络合力)。总的结果是“铁泵”机制的高活动性,导致高腐蚀速率和相关的结垢问题。仔细监控设备的运行,结合测量溶剂的组成和溶剂性能,以及良好的溶剂维护做法,将确保可靠的运行。

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