Results after the installation
An ammonia plant with 168 catalyst tubes compared tube metal temperatures for 2.5 months before and 3.5 months after its tunnels were replaced with StaBlox. The study was published in World Fertilizer in 2020.
| Measured value |
Before |
After |
| Standard deviation of tube metal temperature |
42 °F |
21 °F |
| Spread from coolest to hottest tube |
222 °F |
116 °F |
| Methane slip |
9.94% |
6.94% |
| Production |
|
+3.3% |
With the hottest tubes closer to the average, the plant could raise the reformer outlet temperature, which lowered methane slip and raised production.
Material and expansion
The blocks are cast from mullite bonded high alumina. In published tests it keeps a hot modulus of rupture of 1,700 psi, where super duty brick stays under 600 psi, and it deflects 1.11% under creep load at 1,649 °C, against 7.86% for super duty brick at 1,427 °C.
The lid is where most brick tunnels fail first. A finite element analysis of a lid at 1,900 °F shows only about 10 psi from its own weight, but 1,500 psi from a top to bottom temperature difference of just 10 °F. That is why the StaBlox lid is hollow and the joints are designed to move.
Running with a damaged tunnel
Many plants keep running with a damaged or missing tunnel. A published CFD study of a theoretical reformer with eight tunnels found up to 9.7% less hydrogen next to a missing outer tunnel and 0.95% less across the furnace. For a 2,000 t/d ammonia plant limited by its primary reformer, the authors estimated a loss of about 19 t/d. A single collapsed tunnel can be rebuilt with StaBlox on its own, without waiting for a full revamp.