Abstract
Research and optimization were conducted on heat and mass transfer symmetry of metal hydride thermal compressor (MHTC) between absorption/desorption during the operation of MHTC. On the basis of the local thermal equilibrium model, numerical simulation was performed on a domain with 2D annulus in multi-tube MHTC reactors, and the parameters of the simulation process and structure were also optimized. The results show that for the 4-layer multi-tube reactor, it expends 350 s for the reaction fraction to increase from 0.10 to 0.90 during absorption and 360 s to drop from 0.90 to 0.10 during desorption when the hydrogen pressure, temperature, and heat transfer coefficient are 2/0.05 MPa (absorption/desorption), 293/393 K, 1000 W·m-2·K-1, respectively. The largest temperature differences are 40 K and 43 K, respectively, showing a clear asymmetry between absorption/desorption. The equilibrium pressure inside the multi-tube reactor changes significantly and more than 50% of its total variation occurs in the first 20 s during desorption.
| Original language | English |
|---|---|
| Pages (from-to) | 119-125 |
| Number of pages | 7 |
| Journal | Hsi-An Chiao Tung Ta Hsueh/Journal of Xi'an Jiaotong University |
| Volume | 47 |
| Issue number | 9 |
| DOIs | |
| State | Published - Sep 2013 |
Keywords
- Heat and mass transfer
- Hydride
- Reactor
- Thermal compressor
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