Dual-stage vacuum pressure swing adsorption for green hydrogen recovery from natural gas grids

被引:0
|
作者
Zafanelli, Lucas F. A. S. [1 ,2 ,3 ]
Aly, Ezzeldin [1 ]
Henrique, Adriano [1 ]
Rodrigues, Alirio E. [2 ,3 ]
Silva, Jose A. C. [1 ]
机构
[1] Inst Politecn Braganca, CIMO, LA SusTEC, Campus Santa Apolonia, P-5300253 Braganca, Portugal
[2] Univ Porto, Fac Engn, LSRE, LCM, Rua Dr Roberto Frias, P-4200465 Porto, Portugal
[3] Univ Porto, Fac Engn, ALiCE Associate Lab Chem Engn, Rua Dr Roberto Frias, P-4200465 Porto, Portugal
关键词
Dual-stage vacuum pressure swing adsorption; Green hydrogen; Hydrogen separation; Hydrogen recovery; Natural gas pipelines; Fuel cell grade hydrogen; Aspen adsorption; EFFICIENT EXTRACTION; CO-STREAM; SEPARATION; FUEL; PSA; SIMULATION; MIXTURES; H-2;
D O I
10.1016/j.seppur.2024.130869
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Purification of green hydrogen (GH) from natural gas grids (NGG) can be expensive and challenging through a single-step Pressure Swing Adsorption (PSA) process due to the low H-2 concentration in the grid (<20 % v/v). Herein, we report for the first time the design of a dual-stage vacuum pressure swing adsorption process (DS-VPSA) to purify H-2 blended in NGG with a synergy action of two types of adsorbents: a Carbon Molecular Sieve 3K-172 (CMS) in stage 1 and zeolite 13X in stage 2. In Stage 1, the CMS kinetically separates H-2 from CH4, pre-concentrating H-2 from 20 % to over 50-60 % (v/v), followed by Stage 2, where a thermodynamic separation with zeolite 13X achieves a final product with a high H-2 purity content (>99 % v/v). A mathematical model is developed in Aspen adsorption, where numerical simulations are performed to establish the best operating conditions of the global DS-VPSA. A parametric study is also conducted to optimize performance parameters such as recovery, purity, productivity, and specific energy. The results indicate that it is possible to achieve a final H-2 product with a purity of 99.97 % (fuel cell grade), a recovery of 67 %, and productivity of 1.60x10(-2) kg(H2)/kg(ads)/hr, and a total specific energy consumption of 10.06 MJ/kg(H2), which is a significant achievement reported so far.
引用
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页数:10
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