Catalysts and industrial sorbents activity measurement:
|
| |
|
Measurement conditions |
| No |
Process |
Temperature [°C] |
Pressure [MPa] |
Reactor Type |
| 1 |
Methane reforming |
450-800 |
0,1-3 |
A, F |
| 2 |
HTS |
300-450 |
0,1-2,5 |
A, E |
| 3 |
LTS |
180-240 |
0,1-2,5 |
A, E |
| 4 |
CO and CO2 methanisation |
180-350 |
0,1-2,5 |
A |
| 5 |
Ammonia synthesis |
350-520 |
10-30 |
B, C |
| 6 |
Methanol synthesis |
180-260 |
5-10 |
B |
| 7 |
Benzene hydrogenation |
100-300 |
0,1-1 |
A, D |
| 8 |
Acetylene hydrogenation |
30-150 |
0,1-2,5 |
A |
| 9 |
Sulphur compounds hydrogenation |
200-400 |
0,1-2,5 |
A |
| 10 |
Gas desulphurization on zinc sorbent |
20-400 |
0,1-2,5 |
A, D |
- A. Gradientless CSTR
- B. Gradientless
- C. 6-channel differential reactor with preliminary contacting
- D. Tiomkin reactor
- E. 4-channel Tiomkin reactor
- F. 4-channel differential reactor
|
