低温蒸馏提高纳土纳D α资源利用率的方案:概念设计与敏感性研究

Wijoyo Niti Daton, Ezra Revolin, Siptian Nugrahawan, P. A. Aziz, T. Ariadji, S. Chandra, J. Nainggolan
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摘要

从相应储层开采的天然气需要经过处理,以满足销售用气的规格要求。二氧化碳是需要从天然气中分离出来的成分之一。天然气中的CO2浓度从小于20mol %到大于80mol %不等。当CO2含量非常高时就会出现问题,因此有必要通过修改设备或改变操作条件来修改CO2水平降低,以满足所需的CO2纯度。本文以天然气成分为71% CO2和29%甲烷的东纳土纳气田为研究对象,根据现有设备的能力和容量对其进行了压力调整。从现场条件和特点出发,选择了低温精馏从天然气中分离CO2的方法。本文对影响天然气中CO2低温精馏分离方法的技术参数进行了分析和敏感性研究。灵敏度是通过改变压力参数和非常高的进料气流量来实现的。此外,利用计算公式对精馏塔的直径和高度进行了计算,并利用商业工艺流程软件对计算结果进行了模拟。本研究采用深冷精馏分离CO2工艺,甲烷的期望产品规格为99%。采用两个精馏塔进行模拟设计,第一精馏塔的操作压力为45 bar,温度为19.19 of,第二精馏塔的操作压力为35 bar。结果表明,在流量为8000 MMSCFD的情况下,获得了直径7.4 m、高17.66 m的第一柱数量为16个,直径8 m、高22.38 m的第二柱数量为4个。由于海上条件的限制,本文的研究结果仍不太适合东纳土纳气田的实际情况,因此在设计和现场应用时需要进一步研究其他方法。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
A Solution to Increase Natuna D Alpha’s Resource Utilization by Cryogenic Distillation: Conceptual Design & Sensitivity Study
Natural gas extracted from its respective reservoir needs to be processed to meet the specifications of sales gas. CO2 is one of the components that needs to be separated from natural gas. The CO2 concentration of natural gas varies from a content of less than 20 mole % to more than 80 mole%. There is a problem when the content of CO2 is very high so it is necessary to modify the CO2 level reduction by modifying the equipment or changing the operating conditions to meet the desired CO2 purity. In this study, field conditions and characteristics reviewed is East Natuna Gas Field which has a gas composition of 71% CO2 and 29% methane with modified pressure based on the capability and capacity of available equipment. From the conditions and characteristics of the field, the CO2 method of separation from natural gas using cryogenic distillation was chosen.This research presents analysis and sensitivity of technical parameters that influence the method of CO2 separation from natural gas using cryogenic distillation. The sensitivity is done by changing parameters of pressure and very high feed gas flow rate into the column. In addition, the calculation of the diameter and height of the distillation column using the calculation of the formula and the results of the simulation using commercial process flow software. This study applies a CO2 separation process with cryogenic distillation and the desired product specification of CH 4 is 99%. The design of the equipment was simulated using two distillation columns with operating pressure at the first distillation column of 45 bar and the temperature of 19.19 oF, and for the second distillation column the operating pressure was reduced to 35 bar. The results are for the 8000 MMSCFD flow rate case obtained the first number of columns as many as 16 with the size of 7.4 meters diameter and 17.66 meters high, while the number of second column of 4 with the size of 8 meters diameter and 22.38 meters high. The results presented are still less suitable with the conditions in the East Natuna Gas Field because offshore constrains so need to be studied further for design and other methods in application in the field.
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