炼油厂混合制冷系统露点控制装置的先进分析

M. Afshar, H. rad
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引用次数: 1

摘要

对某炼油厂天然气露点控制装置的新型混合压缩-吸收式制冷系统进行了深入分析。该装置分离天然气中的重烃分子,传统上是通过压缩制冷循环(CRS)中的天然气冷却来进行的。制冷循环压缩机所需的动力输入通常由燃气轮机提供。燃气轮机的低效率和运行CRS压缩机所需的过大功率使得研究不同的方法来降低这种冷却系统的能耗变得至关重要。燃气轮机烟气的余热可以回收利用,作为运行吸收式制冷系统(ARS)的热源,提供部分所需的冷负荷;因此,推出了混合压缩吸收制冷系统(HCARS)。在这项工作中,HCARS的应用扩展到目前使用CRS运行的Fajr-e-Jam天然气精炼厂,并对拟议的ARS进行了先进的火用分析,以进一步改进拟议的系统。研究了不同变量对HCARS性能的影响。所提出的系统和这些分析对于炼油厂露点控制装置来说是新颖的。所有的研究都采用了真实的CRS运行数据,并提出了适当的方法来验证仿真结果。在天然气消耗相同的情况下,与目前的CRS(7670千瓦)相比,拟议的系统使HCARS的冷却能力增加了63%(12550千瓦),总体上节省了约50000 SCMD的天然气。通过对所有设备的火用分析,所提出的ARS的火用效率为0.155。此外,还对燃气轮机烟气出口温度及流量、环境温度、CRS部分负荷运行、吸收溶液流量、浓度等因素对HCARS性能的影响进行了参数化研究。这些研究应提供在不同情况下操作拟议系统所需的资料。
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Advanced Analysis of Dew Point Control Unit of Hybrid Refrigeration Systems in Gas Refineries
In this paper, an advanced analysis of a novel hybrid compression-absorption refrigeration system (HCARS) for natural gas dew point control unit in a gas refinery is presented. This unit separates the heavy hydrocarbon molecules in the natural gas, which is traditionally carried out by natural gas cooling in a compression refrigeration cycle (CRS). The power input required for the refrigeration cycle compressors is usually provided by gas turbines. The low efficiency of gas turbines and the excessive power required for running the CRS compressors have made it crucial to investigate different means to decrease the energy consumption of this cooling system. The waste heat of gas turbines flue gas can be recovered and utilized as the heating source for running an absorption refrigeration system (ARS) to provide part of the needed cooling load; hence, a hybrid compression absorption refrigeration system (HCARS) is launched. In this work, the application of HCARS is extended to the Fajr-e-Jam gas refinery currently operating with a CRS, and an advanced exergetic analysis of the proposed ARS is performed to further improve the proposed system. The effect of different variables on the performance of the proposed HCARS is also inspected. The proposed system and these analyses are novel for the gas refinery dew point control unit. Real CRS operational data are utilized in all the investigations, and proper means are presented for the validation of the simulation results. The proposed system resulted in 63% additional cooling capacity of the HCARS (12550 KW) in comparison to the current CRS (7670 kW) for the equal natural gas consumption, which overall saves about 50000 SCMD of natural gas. Based on the exergy analysis of all the equipment, the exergy efficiency of the proposed ARS is 0.155. In addition, the parametric study of the effects of the gas turbine flue gas exit temperature and flow rate, ambient temperature, partial load operation of CRS, absorption solution flow rate, and concentration on the HCARS performance is carried out. These studies should provide the information needed for operating the proposed system in different situations.
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