Abstract

A new conceptual layout of transforming distributed co-generation plants into quad-generation plants, which combines the generation of hydrogen, cooling, heating, and power, is derived and analyzed. Two chemical looping techniques are developed in this methane-based quad-generation system, namely, calcium looping CO2 absorption and nickel-based chemical looping combustion (CLC). The objective of the present study is to produce hydrogen as the main product with both high purity and high flux through CLC thermally coupled with sorption-enhanced steam methane reforming (CLC–SESMR) and simultaneously to integrate combined cooling, heating, and power production as by-products through the combined cycle. The implementation of CLC integrated with the SESMR system is designed to fulfill the heat requirements of the reformer and calciner and provide straightforward carbon capture at a relatively low energy penalty. The efforts of four prime parameters, including calcium oxide-to-methane ratio, steam-to-methane ratio, reforming pressure, and reforming temperature, seem to exert significant impact on the properties of the regarded process. Therefore, detailed studies related to these variations have been examined. Meanwhile, the thermodynamic performance of this suggested process, including system efficiencies and the fuel energy saving ratio (FESR), is evaluated under design conditions and reaction parameters. In parallel, the exergy destruction analysis of the whole process is also under discussion. As a result, the total energy and exergy efficiencies as well as FESR are calculated to be 83.91%, 74.05%, and 21.27% in summer and 83.17%, 74.42%, and 21.36% in winter, respectively.

Highlights

  • Global energy demand is soaring as a result of the growth of the world’s population, and it is forecasted to exceed 10.9 × 109 by 2100,1 exacerbating the existing primary and secondary energy sources’ depletion

  • (3) A comparative exergy analysis is conducted to prove the thermodynamic feasibility of the chemical looping combustion (CLC)–sorption-enhanced steam methane reforming (SESMR)–CCHP process

  • The results reveal that the exergy efficiency of the suggested scitation.org/journal/adv system is considerably higher than the steam methane reforming (SMR) process with a benefit of about 8.81% points

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Summary

Introduction

Global energy demand is soaring as a result of the growth of the world’s population, and it is forecasted to exceed 10.9 × 109 by 2100,1 exacerbating the existing primary and secondary energy sources’ depletion. Yi and Harrison tested the stability of the SESMR experiment in a laboratory-scale fixed-bed reactor at a lower reaction temperature They reported the capability of CaO adsorbents to capture CO2 and observed the formation of high-purity hydrogen and low-concentration CO in the reformer gas. Tzanetis et al. proposed a CaO-based SESMR process in which the necessary reaction heat from the reformer and calciner is supplied by burning additional methane in air This process has resulted in high energy consumption and costs of capturing CO2 from the combustion flue gases.. For the sake of avoiding the use of the ASU and improving the overall energy efficiency, various alternative schemes have been presented, such as heating by high-temperature combustion gas, indirect heating via the heat transfer surface, as well as utilizing waste heat by coupling solid oxide fuel cells (SOFCs).17 They are uneconomical due to the need for large heat transfer areas or airflows that exist at extremely high temperatures For the sake of avoiding the use of the ASU and improving the overall energy efficiency, various alternative schemes have been presented, such as heating by high-temperature combustion gas, indirect heating via the heat transfer surface, as well as utilizing waste heat by coupling solid oxide fuel cells (SOFCs). they are uneconomical due to the need for large heat transfer areas or airflows that exist at extremely high temperatures

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