Optimization of Flow Rate TEG (Triethylene Glycol) in Absorbing Water Levels in Glycol Contactor (V-5400) With ASPEN HYSYS Simulation

M. Ihsan
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Abstract

The purpose of this research is to determine the amount of TEG flow rate required to get dry gas with a moisture content consistent with industry requirements and to determine how much water content is absorbed in dry gas after TEG flow rate optimization. The glycol contactor (V-5400) is the primary piece of equipment for this activity, and the materials are dry gas and TEG solution in the dehydration unit. The research method employed is descriptive quantitative simulation via the use of the Aspen HYSYS V8.8 application tool. According to the simulation findings on the glycol contactor (V-5400) using Aspen HYSYS, in order to get dry gas with a moisture content of 4-7 lb/MMscf, a TEG solution with a flow rate of 2.4 ft3/min and a water content of 2.4 ft3/min is required. absorbed following flow rate optimization TEG is used to convert 7.6026 lb/MMscf water content to 6.7881 lb/MMscf water content with a percentage difference of 0.8145, but real data converts 7.4702 lb/MMscf water content to 6.6984 lb/MMscf water content with a percentage difference of 0.7718.
用ASPEN HYSYS模拟优化乙二醇接触器(V-5400)吸水量
本研究的目的是确定获得含水率符合行业要求的干气所需的TEG流量,并确定TEG流量优化后干气中吸收了多少水分。乙二醇接触器(V-5400)是该工艺的主要设备,物料为脱水装置中的干气和TEG溶液。研究方法为描述性定量模拟,采用Aspen HYSYS V8.8应用工具。根据使用Aspen HYSYS对乙二醇接触器(V-5400)的模拟结果,为了获得水分含量为4-7 lb/MMscf的干气,需要流速为2.4 ft3/min,含水量为2.4 ft3/min的TEG溶液。TEG可以将7.6026 lb/MMscf的含水率转化为6.7881 lb/MMscf的含水率,差异为0.8145,但实际数据将7.4702 lb/MMscf的含水率转化为6.6984 lb/MMscf的含水率,差异为0.7718。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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