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Multi-Objective Design Optimization of Hydride Hydrogen Storage Reactor structured with helical tubes based on Energetic and Economic analyses

Subcategory (under Clean Energy): Hydrogen
Technology Readiness Level (TRL): TRL 4 - Early prototype
Technology Outline (Process Description)

The study focuses on optimizing the thermal-static performance of helically coiled metal hydride reactors, which employs coupled RSM-Computational modeling-Desirability function methodology to investigate the correlation of structural geometric parameters on responses and identify the best novel helical design. The current study is the first of its kind that combinatorically assessed the gravimetric density (weight ratio), the efficacy of the heat exchanger (thermal power), and H2 absorption time: by using a quadratic regression technique followed by computational modeling and then multi-response desirability optimization. The optimal base case and finned reactor reached complete saturation in 550 s and 460s, respectively, when maintained at 298 K, 10 lpm, and 5 bar supply pressure, with the latter contributing to about 16.36% saving in absorption time despite 5.66% drop in weight ratio. The vivid comparison between the optimized finned helical reactor and those described in the literature proved the superiority of the designed novel reactor and substantiated the use of helical tubes for better weight ratio and shorter absorption time.

Salient Features/Advantages

  • The multi-objective response optimization (weight ratio, absorption time, energy, and economic analysis) will be helpful for all researchers in the metal hydride community to choose the appropriate heat exchanger design from diverse configurations based on equal weightage or decision-maker’s choice of weightage.

Key Outcomes

  • The optimum configuration metrics for the base case and finned reactor are 5 in shell diameter, 125 in pipe diameter, 6.5 mm pitch, 4 coils, CD = 2 coil placement, 0.25 mm fin height, 1.5 mm thickness, and 5 mm spacing.
  • When operated at higher pressures and fluid input temperatures, the finned reactor’s thermal power boost over the ideal base case increased to 26% from 12-14%.
  • The heat exchanger cost significantly   determines the LCOHS. The optimised finned reactor became economical when its price to base case ratio was cut from 1.5 to 1.1.

IP Protection details

  • Patent filed (Title, national/International): Nil
  • Patents Granted: Nil
  • Copyrights obtained /progress on commercialisation /Pl. specify connect with industry: Nil

Contact details (for more information)

  • Nodal Person name: Prof. S. Anbarasu
  • Email ID: anbarasus@nitrkl.ac.in
  • Organisation name (Relevant link/web page): National Institute of Technology, Rourkela, Odisha
Supporting Photographs/Images

Organizations involved in the development (logo/name)

National Institute of Technology, Rourkela, Odisha

DST-IITB Energy Storage Platform on Hydrogen

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