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Cascade refrigeration systems in integrated cryogenic natural gas process (natural gas liquids (NGL), liquefied natural gas (LNG) and nitrogen rejection unit (NRU))

机译:集成低温天然气工艺中的级联制冷系统(天然气液体(NGL),液化天然气(LNG)和除氮装置(NRU))

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Heavy components in the natural gas itself can feed downstream units and also due to the low temperature process may be formed solid. Therefore heavy components separation is a necessity and can produce useful products. Virtually all natural gases are containing nitrogen that would lower the heating value of natural gas. This study investigates design and optimization of integrated process recovery of natural gas liquids, natural gas liquefaction, and nitrogen remove unit. In this integrated process, design of low temperature processes is started from the core process and continued by heat exchangers network design and cooling system based on MFC. Design and integration processes of units at the same time reduces the number of required equipment and energy consumption. The results show that the new integrated process has specific power around 0.343-0.33 (kW-h/kg-LNG) and its thermal efficiency equal to 62.82%, compared to other integrated systems have the lowest and highest values. Exergy analysis shows that towers has the highest Exergy destruction among other equipment. Sensitivity analysis shows that the structure of the integrated process capable of removing nitrogen from natural gas at a concentration of between 5% and 15%. By analyzing the operating parameters shows reduction in the Total specific power from 19.5% to 24% and the Specific power from 2.57% to 11%, yet surging in the Ethane recovery from 2.5% to 17%. Sensitivity analysis is the method to identification of the Decision variables, finally Genetic Algorithm used to identify optimum of objective function (minimization of Specific Power) and reduction of it to 6%. (C) 2016 Elsevier Ltd. All rights reserved.
机译:天然气本身中的重组分可以供给下游单元,并且由于低温过程也可能形成固体。因此,重组分分离是必要的,并且可以生产有用的产品。几乎所有的天然气都含有氮,这会降低天然气的热值。本研究研究了天然气液体,天然气液化和脱氮装置的集成工艺回收的设计和优化。在此集成过程中,低温过程的设计从核心过程开始,并继续进行基于MFC的热交换器网络设计和冷却系统。单元的设计和集成过程可以同时减少所需设备的数量和能耗。结果表明,与其他集成系统的最低和最高值相比,新集成工艺的比功率约为0.343-0.33(kW-h / kg-LNG),其热效率等于62.82%。火用分析表明,塔架在其他设备中的火用破坏最高。敏感性分析表明,该集成过程的结构能够以5%至15%的浓度从天然气中去除氮。通过分析运行参数可以看出,总比功率从19.5%降低到24%,比功率从2.57%降低到11%,而乙烷回收率却从2.5%激增到17%。灵敏度分析是确定决策变量的方法,最后是遗传算法,用于确定目标函数的最佳值(比功率的最小值)并将其降低到6%。 (C)2016 Elsevier Ltd.保留所有权利。

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