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https://hdl.handle.net/10216/138590| Author(s): | Yáñez, M. Relvas, F. Ortiz, A. Gorri, D. Adélio Mendes Ortiz, I. |
| Title: | PSA purification of waste hydrogen from ammonia plants to fuel cell grade |
| Issue Date: | 2020-06-01 |
| Abstract: | Industrial hydrogen-rich waste streams hold promises in their upgrading to feed fuel cell stacks. As in the ammonia synthesis process, a stream of up to 180-240 Nm(3) per ton of ammonia is purged to keep the inert gases concentration below a threshold value; this stream contains large hydrogen quantities, which could be recovered. In the current work, a four-column PSA unit has been used to produce a high-purity hydrogen stream for fuel cell applications from a synthetic mixture with a molar composition of 58% H-2, 25% N-2, 15% CH4 and 2% Ar, based on ammonia purge gas. Firstly, a comparative performance of four commercially adsorbents was accomplished to obtain the adsorption isotherms of H-2, N-2, CH4, and Ar, leading to the selection of 5A zeolite adsorbent. Then, the dynamic behavior of a packed bed was studied by single and multicomponent breakthrough experiments and simulated using Aspen Adsorption (R). The results, simulations and experimental, indicate that after H-2 the first impurity to break thought the column is Ar, followed by N-2 and finally by CH4. Then, a design-of-experiments (DoE) methodology was used to select the best operating conditions of the experimental cyclic PSA unit to reach different target hydrogen product concentrations; the overall PSA performance was evaluated in terms of purity and recovery of H-2 product. According to the results, the four-column PSA unit running at 9 bar produced a stream with hydrogen concentration of 99.25% and 99.97% of H-2, with a recovery of 75.3% and 55.5%, respectively, where the impurities were mostly Ar and N-2. In addition to the technical performance, the economic assessment concluded that the cost to compress, transport and purify waste hydrogen to a concentration of 99.97% using a small-scale PSA unit from ammonia plants has been estimated in the range of 1.17-1.39 (sic) kg H-2(-1), depending on the dispensing pressure of 350 or 700 bar, respectively. These assessments offer a cost-effective solution to produce high-purity H-2 as low cost transportation, allowing hydrogen penetration into the mass markets. |
| Subject: | Engenharia química Chemical engineering |
| Scientific areas: | Ciências da engenharia e tecnologias::Engenharia química Engineering and technology::Chemical engineering |
| DOI: | 10.1016/j.seppur.2019.116334 |
| URI: | https://hdl.handle.net/10216/138590 |
| Document Type: | Artigo em Revista Científica Internacional |
| Rights: | restrictedAccess |
| Appears in Collections: | FEUP - Artigo em Revista Científica Internacional |
Files in This Item:
| File | Description | Size | Format | |
|---|---|---|---|---|
| 452180.pdf Restricted Access | 2.66 MB | Adobe PDF | View/Open |
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