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Hydrogen Production through CO_2 Absorption Enhanced Diesel Steam Reforming for PEMFC Systems

机译:通过CO_2吸收的氢气产生增强PEMFC系统的柴油蒸汽重整

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CO_2 absorption enhanced diesel steam reforming was investigated for hydrogen production in this paper. The utilization of CO_2 absorbent in the reforming reactor sharply decreases the CO_2 level in the reacting gas and shifts the equilibrium towards hydrogen formation. This increases the diesel conversion and reforming rate of hydrocarbon at relatively low temperature. At the temperature of 600°C, reforming rate of hydrocarbon reached 95%, and that is 30 percent higher than that in traditional steam reforming reaction without absorbent. In an optimal temperature range of 545-625°C, diesel conversion could reach near 100%. Hydrogen concentration reached 95% when using CO_2 absorbent, correspondingly concentrations of CO, CH_4, and CO_2 decreased obviously, while hydrogen concentration was about 70% in conventional diesel steam reforming process. Further, a novel PEMFC system for hydrogen production was proposed by combining CO_2 absorption enhanced diesel steam reforming (AEDSR) with chemical-looping combustion (CLC) process, which could continuously produce hydrogen and regenerate absorbent at the same time, heat balance of steam reforming and CO_2 absorption reaction could also be obtained by adjusting the amount of reforming catalyst and CaO.
机译:研究了CO_2吸收增强的柴油蒸汽重整,用于本文的氢气生产。在重整反应器中的CO_2吸收剂的利用急剧地降低了反应气体中的CO_2水平,并将朝向氢形成的平衡转移。这使得柴油转换和烃的含量在较低温度下的重整速率增加。在600℃的温度下,烃的重整速率达到95%,比传统蒸汽重整反应高30%,没有吸收剂。在545-625°C的最佳温度范围内,柴油转换可能达到100%。当使用CO_2吸收剂时,氢浓度达到95%,相应浓度的CO,CH_4和CO_2明显下降,而常规柴油蒸汽重整过程中的氢浓度为约70%。此外,通过将CO_2吸收增强型柴油蒸汽重整(AEDSR)与化学循环燃烧(CLC)工艺组合,提出了一种用于氢生产的新型PEMFC系统,该方法可以同时连续地生产氢和再生吸收剂,蒸汽重整的热平衡通过调节重整催化剂和CaO的量,也可以获得CO_2吸收反应。

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