利用上游作业数据分析解决天然气脱水系统中乙二醇损失的问题

M. Soliman, Mohammed Abdo Alwani, Abdullah Younis Aiderous
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引用次数: 1

摘要

本文的目的是展示成功和创新的故障排除数据分析技术,以减少乙二醇的损失,并满足上游气油分离装置(GOSP)的一个气体脱水系统的产品规格。三甘醇(TEG)气体脱水系统是上游生产中应用最广泛、最可靠的气体脱水系统。这些经过验证的数据分析技术用于解决与气体脱水系统操作相关的主要和长期问题,这些问题导致乙二醇损失过多、乙二醇降解和产品不合规格。乙二醇损失是气体脱水系统中最重要的操作问题,也是操作人员关注的问题。根据TEG接触器的工作温度,大多数脱水装置的设计目标是每百万标准立方英尺处理的天然气损失低于1磅乙二醇。在本文中,将对加剧不期望的乙二醇损失降解和不规范产品的潜在根本原因进行全面的数据分析,并提出最小化预期影响的解决方案。例如,在高温下操作吸收容器(接触器)或蒸馏塔会增加乙二醇蒸发损失。此外,乙二醇再生段的乙二醇损失通常是由再沸器温度过高引起的,这会导致乙二醇(TEG)蒸发或热分解。此外,过高的最高温度在蒸馏塔允许蒸发的乙二醇与水蒸气从蒸馏塔逸出。接触器工作温度过高可能是乙二醇冷却器故障或TEG流量过高的结果。本文将重点介绍一个在油气分离厂运行的TEG系统的详细案例研究。
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Troubleshooting Glycol Loss in Gas Dehydration Systems Using Data Analysis at Upstream Operation
The objective of this paper is to showcase the successful and innovative troubleshooting data analysis techniques to reduce glycol loss and to meet the product specifications in one of the gas dehydration systems in an upstream gas oil separation plant (GOSP). The gas dehydration system using Triethylene Glycol (TEG) is the most widely used and reliable gas dehydration system in upstream operation. These proven data analysis techniques were used to tackle major and chronic issues associated with gas dehydration system operation that lead to excessive glycol losses, glycol degradation, and off-specification products. Glycol loss is the most important operating problem in the gas dehydration system and it represents a concern to the operation personnel. Most dehydration units are designed for a loss of less than 1 pound of glycol per million standard cubic feet of natural gas treated, depending on the TEG contactor operating temperature. In this paper, comprehensive data analysis of the potential root causes that aggravate undesired glycol losses degradation and off-specification products will be discussed along with solutions to minimize the expected impact. For example, operating the absorption vessel (contactor) or still column at high temperature will increase the glycol loss by vaporization. Also, the glycol losses occurring in the glycol regenerator section are usually caused by excessive reboiler temperature, which causes vaporization or thermal decomposition of glycol (TEG). In addition, excessive top temperature in the still column allows vaporized glycol to escape from the still column with the water vapor. Excessive contactor operating temperature could be the result of malfunction glycol cooler or high TEG flow rate. This paper will focus on a detailed case study in one of the running TEG systems at a gas-oil separation plant.
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