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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.
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页数:10
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