4.7 Article

A new energy efficient process for hydrogen purification using ZIF-8/glycol-water slurry: Experimental study and process modeling

期刊

INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
卷 46, 期 63, 页码 32081-32098

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijhydene.2021.06.210

关键词

Absorption; Adsorption; ZIF-8; Gas separation; H-2 recovery

资金

  1. National Natural Science Foundation of China [21776301, 21636009, 21878328]
  2. Science Foundation of China University of Petroleum, Beijing [2462018BJC004]
  3. Beijing Municipal Science Technology Project [Z181100005118010]
  4. National Key Research and Development Program of China [2017YFC0307302]

向作者/读者索取更多资源

This paper introduces a new energy efficient process for hydrogen purification from CH4/H-2 mixture in refinery off-gas and coke oven gas. Through experimental and simulation studies, operating conditions and energy consumption were determined, demonstrating the promising application prospects of this process.
Effective recovery of hydrogen from refinery off-gas and coke oven gas, in which hydrogen and methane are key components, is increasingly important for the development of hydrogen energy. In this paper, we introduced a new energy efficient process for hydrogen purification from CH4/H-2 mixture. Firstly, we conducted a phase equilibrium experimental study for CH4/H-2 in zeolitic imidazolate framework-8 (ZIF-8)/glycol-water slurry. The simple absorption and desorption configuration is adopted for the continuous separation of CH4/H-2 using ZIF-8/glycol-water slurry. The multi-stage pseudo-absorption modeling approach was introduced for the modeling and simulation of the absorption-adsorption and desorption columns via using multiple flash modules in Aspen Plus. The binary interaction parameters in the thermodynamic model were fitted by experimental data within an acceptable error (4.93%). The operating conditions (i.e., the number of theoretical stages, feed stage, flash pressure, and desorption pressure) were determined to increase H-2 concentration in product and H-2 recovery ratio. The energy performance of the process was also evaluated. Given the feed gas contains 50 mol% H-2, the gas-slurry volume ratio of 43.27 is required to produce 95 mol% H-2 with a high recovery of 97.94%. The total energy consumption per unit volume of product is 0.06254 kW.h/Nm(3). Results indicate that the hybrid absorption-adsorption process is a promising energy efficient technique to separate CH4/H-2 in the future. (C) 2021 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.

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