利用火炬气联产电力、蒸汽、CH3OH、H2和CO2的多联产系统仿真与经济评价

A. Vatani, M. Jafari, Mohammad Shahab Deljoo
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引用次数: 1

摘要

今天,世界上最具挑战性的问题之一是在石油、天然气和石化工业中适当使用火炬气。燃烧具有高热值的火炬气会造成经济损失和环境污染。使用火炬气体有几种方法;热和发电,生产有价值的燃料,或分离更珍贵的成分是这些方法的例子。在本研究中,设计并模拟了一个多联产系统,用于从South Pars和Assaluyeh气田的火炬气中联合生产电力、蒸汽、甲醇、H2和CO2。多联产系统具有诸如减少温室气体和联合生产和销售能源相关产品等优点。用于将火炬气体转化为能源和各种产品的多联产系统包括酸气去除单元、合成气生产单元、甲醇合成单元、氢净化单元、热电联产单元和CO2捕获单元。本研究的目的是对多电联产系统进行经济评估,并获得该过程的总资金成本、运营利润和投资回收期。仿真结果表明,使用9690 kg/h的火炬气可产生甲醇8133 kg/h、氢气653.7 kg/h、氮气46950 kg/h、二氧化碳9103 kg/h、中压蒸汽109850 kg/h,功率3.7 MW。经济评价结果表明,在多电联产系统中,原材料总成本和公用事业总消耗成本分别为193.8美元和1859.5美元/小时,产品总销售额和公用事业总销售额分别为12941.8美元和2243.5美元/小时;营业利润是每小时13132美元。设备成本、安装成本、总资本成本和总运营成本分别为2970万美元/年、3920万美元/年、7100万美元/年和2790万美元/年;最后,投资回收期为1.5年。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Simulation and Economic Evaluation of Polygeneration System for Coproduction of Power, Steam, CH3OH, H2, and CO2 from Flare Gas
Today, one of the challenging issues all over the world is the appropriate use of flare gases in oil, gas, and petrochemical industries. Burning flare gases having high heating value results in economic losses and the pollution of the environment. There are several methods to use flare gases; the heat and power generation, the production of valuable fuels, or the separation of more precious components are examples of these methods. In this study, a polygeneration system is designed and simulated for the coproduction of power, steam, methanol, H2, and CO2 from the flare gases in South Pars and Assaluyeh gas fields. The polygeneration system has advantages such as reducing greenhouse gases and the coproduction and sales of energy-related products. The polygeneration system for converting flare gases to energy and various products includes an acid gas removal unit, a synthesis gas production unit, a methanol synthesis unit, a hydrogen purification unit, a combined heat and power generation unit, and a CO2 capture unit. The purpose of this study is to conduct an economic evaluation of the polygeneration system and obtain the total capital cost, the operating profit, and the payback period of this process. The simulation results show that using 9690 kg/h of flare gases produces 8133 kg/h methanol, 653.7 kg/h hydrogen, 46950 kg/h nitrogen, 9103 kg/h CO2, 109850 kg/h medium-pressure steam, and 3.7 MW power. The economic evaluation results show that in the polygeneration system, the total raw material cost and the total utilities consumption cost are $193.8 and $1859.5 per hour respectively, and the total product sales and the total utility sales are $12941.8 and $2243.5 per hour respectively; also, the operating profit is $13132 per hour. Also, the equipment cost, the installation cost, the total capital cost, and the total operating cost are $29.7 million per year, $39.2 million per year, $71 million per year, and $27.9 million per year respectively; finally, the payback period is 1.5 years.
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