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Thermoeconomic assessment of a novel integrated CHP system incorporating solar energy based biogas-steam reformer with methanol and hydrogen production

机译:新型集成热电联产系统的热经济评估,该系统将基于太阳能的沼气-蒸汽重整器与甲醇和氢气一起生产

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This paper deals with a novel solar-biogas fueled combined heat and power system with methanol and hydrogen production. The proposed energy system consists following subsystems: solar based biogas-steam reformer, gas turbine cycle, Rankine and organic Rankine cycles, pressure swing adsorption, carbon capture and sequestration and methanol synthesis unit. The selected solar system is molten salt tower-based concentrated solar thermal plant that provides required thermal energy for reforming process. The multigeneration system is comprehensive analyzed thermoeconomically and exergoenvironmentally. A parametric study is conducted to find the effects of key parameters on the system performance. The considered key parameters include steam to carbon ratio of reforming process, operating temperature and pressure of reformer. The results show that T-r is the most effective parameters for improving system performance. A 200 K increase in reforming temperature, from 923 K to 1123 K, leads to decreases of 15% and 10% in the energy and exergy efficiencies, respectively. The opposite trend is observed for net power output and mass flow rate of produced methanol when key parameters change. Nevertheless, mass flow rate of produced methanol plays most important role for evaluating energy and exergy efficiencies. Also, gas turbine cycle and reformer have highest exergy destruction rate of 140 MW and 134 MW, respectively when system operates in optimum condition. Moreover, best exergoenvironmental parameters are obtained at higher value of reforming temperature and lower values of reforming pressure and steam to carbon ratio of reforming process.
机译:本文研究了一种新型的以太阳能沼气为燃料的热电联产系统,该系统可以生产甲醇和氢气。拟议的能源系统包括以下子系统:太阳能沼气蒸汽重整器,燃气轮机循环,朗肯循环和有机朗肯循环,变压吸附,碳捕获和封存以及甲醇合成装置。所选的太阳能系统是基于熔融盐塔的集中式太阳能热力发电厂,可为重整过程提供所需的热能。对多代发电系统进行了热经济和能动环境的综合分析。进行了参数研究,以发现关键参数对系统性能的影响。所考虑的关键参数包括重整过程中的蒸汽与碳比,重整炉的工作温度和压力。结果表明,T-r是提高系统性能的最有效参数。重整温度从923 K升高到1123 K 200 K,导致能量效率和火用效率分别降低15%和10%。当关键参数发生变化时,观察到相反的趋势,即净功率输出和生产的甲醇的质量流量。然而,生产的甲醇的质量流量在评估能量和火用效率方面起着最重要的作用。同样,当系统在最佳条件下运行时,燃气轮机循环和重整炉的最高火用破坏率分别为140 MW和134 MW。此外,在较高的重整温度值和较低的重整压力值以及重整过程的水蒸气碳比下,可以获得最佳的能效环境参数。

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