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The MEG (Mono Ethylene) Injection Gas Dehydration Process Evaluation for the Margarita Field Development

机译:玛格丽塔油田开发的MEG(单乙烯)注入气体脱水工艺评估

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The objective of the study is to select the gas dehydration process system within the Margarita Field Development Project based on “MEG (MONO ETHYLENE) Injection with Mechanical Refrigeration” and compare it with the “Glycol Dehydration Process System”, from the technological and economical point of view. The dehydration process based on TEG is the most common process for natural gas dehydration; it is an efficient technology and its operation is very well known. In order to reduce the CAPEX and OPEX of the Project, the operator has studied potential process options. One way to optimize the gas dehydration process is by simplifying and combining it with other processes, which is the case when considering the combined MEG injection with mechanical refrigeration, a common practice in the Industry. The scope of this report covers: o Estimate of the downstream and utility equipments as required (glycol loss, glycol rate recirculation, electrical requirements, etc) o Cost Estimate (OPEX / CAPEX). O Explanation of uncertainties and risks that may be associated in applying the dehydration process on this particular application, and steps (if required) to eliminate those uncertainties. O To take experience of similar plants with similar requirement. The MEG Injection together with a Dew Point Plant is able to dehydrate the natural gas, because the chiller unit operates at low temperatures and it permits the water content of the gas to be condensed and removed in "cold separation", but this process requires inhibitor injection in order to avoid hydration formation, being glycol the usual inhibitor. Removing the Contactor Tower and changing TEG by MEG has little impact in the Dew Point Plant design. The additional power required in the propane compressor is compensated in the glycol pump which is lower power consumption because the MEG injection rate is lower than the TEG one. The different aspects evaluated between MEG Injection and Contactor Tower with TEG, are favorable toward the MEG Injection as: o CAPEX: FOB Cost. O MEG Injection saves MEG regeneration unit which is smaller and lighter. O Elimination of TEG contactors will simplify the plant, reduce installation cost and avoid large heavy vessels with transportation constraints. O MEG injection is easier to regenerate than TEG and alleviates environmental issues with BTEX emission. After taking in consideration all the points in favor of the MEG Injection, it is recommended to install it in the Gas Treatment Plant.
机译:该研究的目的是在玛格丽塔油田开发项目中,以“ MEG(单乙烯)机械制冷注入”为基础,选择气体脱水工艺系统,并从技术和经济角度将其与“乙二醇脱水工艺系统”进行比较。观点。基于TEG的脱水过程是天然气脱水中最常见的过程。它是一种高效的技术,其操作众所周知。为了减少项目的资本支出和运营支出,运营商已经研究了潜在的工艺选择。优化气体脱水过程的一种方法是将其简化并与其他过程结合,这是考虑将MEG注入与机械制冷相结合的一种情况,这是工业界的一种普遍做法。该报告的范围包括:o根据需要估算下游设备和公用设备(乙二醇损失,乙二醇速率再循环,电力需求等)o成本估算(OPEX / CAPEX)。 O说明在此特定应用程序上应用脱水过程可能涉及的不确定性和风险,以及消除这些不确定性的步骤(如果需要)。 O吸收具有类似要求的类似工厂的经验。 MEG注入设备与露点设备一起能够使天然气脱水,因为冷却器单元在低温下运行,并且可以在“冷分离”过程中冷凝并除去气体中的水分,但是此过程需要抑制剂为了避免水合形成注射剂,通常是乙二醇的抑制剂。除去接触器塔并通过MEG更换TEG对露点设备设计几乎没有影响。丙烷压缩机所需的额外功率在乙二醇泵中得到补偿,这是较低的能耗,因为MEG的注入速率低于TEG的注入速率。 MEG注入和带有TEG的接触器塔之间评估的不同方面有利于MEG注入,因为:CAPEX:FOB成本。 O MEG喷射节省了更小,更轻的MEG再生装置。 O取消TEG接触器将简化工厂,降低安装成本,并避免运输受限的大型重型船舶。 O MEG注入比TEG更易于再生,并减轻了BTEX排放的环境问题。考虑到所有支持MEG注入的因素后,建议将其安装在气体处理厂中。

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