100% saturated liquid hydrogen production: Mixed-refrigerant cascaded process with two-stage ortho-to-para hydrogen conversion. (15th October 2021)

• Record Type: Journal Article
• Authors: Qyyum, Muhammad Abdul; Riaz, Amjad; Naquash, Ahmad; Haider, Junaid; Qadeer, Kinza; Nawaz, Alam; Lee, Hyunhee; Lee, Moonyong
• Is Part Of: Energy conversion and management. Volume 246(2021)
• Publication Date: 2021-10-15
• Subjects: Liquid hydrogen -- Mixed fluid cascade -- Optimization -- Energy consumption -- Composite curves -- Exergy analysis; Direct energy conversion -- Periodicals; Energy storage -- Periodicals; Energy transfer -- Periodicals; Énergie -- Conversion directe -- Périodiques; Direct energy conversion; Periodicals; 621.3105
• DOI: 10.1016/j.enconman.2021.114659
• Languages: English
• ISSNs: 0196-8904

Abstract

Graphical abstract: Highlights: Liquefaction is promising approach for long distance H2 storage and transportation. Commercial H2 liquefaction plants have specific energy consumption of 10–12. kWh / kg LH 2 . Increased number of ortho-to-para converters increases the process complexity. Mixed refrigerant cascaded process with only two catalytic converters is proposed. Hydrogen is liquefied at the expense of 6.45 kWh / kg LH 2 with 47.2% exergy efficiency. Abstract: To reduce CO2 emissions and address climate change concerns, most futuristic studies investigating 100% renewable energy sources and subsequent power-to-gas/fuel/liquid/X technological developments have been based on hydrogen (H2 ). The long-term storage and transportation of H2 over long distances restrict its feasibility as an energy vector, mainly due to its low energy density. Liquefaction is a promising approach for overcoming these issues. However, it requires a large amount of energy, and if H2 itself is used to provide this energy, then 25% to 35% of the initial quantity of H2 is consumed. The existing H2 liquefaction plants have specific energy consumption values in the range of 10–12 kWh / kg LH 2 and exergy efficiencies in the range of 20%–30% with complicated configurations. Therefore, a thermodynamically efficient and compact design is required to facilitate a roadmap to H2 economy. This paper proposes a simple, energy-efficient, and cost-effective process for H2 liquefaction. Three refrigeration cycles with optimal mixed-refrigerant compositions are used, which makes the proposed process energy-efficient. Additionally, two-stage ortho-to-para conversion makes the process compact. The proposed process is unique in terms of its configuration and mixed-refrigerant combination. The modified coordinate descent approach was adopted to identify the optimal design variables for the proposed H2 liquefaction process. The proposed process consumes an energy of 6.45 kWh / kg LH 2, which is 36.5% and 16.1% lower than that consumed by the base design of the proposed process and a published base case, respectively. Additionally, the exergy efficiency of the proposed process is 47.2%. This study will help process engineers achieve a sustainable green economy by improving the competitiveness of H2 storage and transportation over long distances.