Abstract
The performance of a solar chemical heat pipe was studied using CO2 reforming of methane as the endothermic reaction. A directly heated vertical reactor, packed with a rhodium catalyst was used. The solar tests were carried out in the Schaeffer solar furnace of the Weizmann Institute of Science. The power absorbed was up to 6.3 KW, the maximal flow rates of the gases reached 11,000 1/h, and the methane conversions reached 85%. A computer model was developed to simulate the process. Agreement of the calculations with the experimental results was quite satisfactory.
Original language | English |
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Pages (from-to) | 395-402 |
Number of pages | 8 |
Journal | Solar Energy |
Volume | 48 |
Issue number | 6 |
DOIs | |
State | Published - 1992 |
Externally published | Yes |