|
| MOQ: | 1 set |
| Price: | Negotiable |
| Standard Packaging: | conventional |
| Delivery Period: | Customized |
| Payment Method: | L/C, T/T |
| Supply Capacity: | Negotiable |
1500Nm3/H Hydrogen Production From Methanol Hydrogen Recovery Unit
2000Nm3/H Hydrogen Recovery And 1500Nm3/H Hydrogen Production From Methanol
Technology Application:
Using methanol as raw material, crude hydrogen (mainly CO2, H2, and trace CO, CH4) is produced by steam cracking process, and then purified by pressure swing adsorption technology to obtain hydrogen with purity meeting the requirements of users.
The raw methanol and raw desalted water are premixed at a certain ratio, pressurized by metering pump, preheated, gasified and superheated, and then enter the reactor. Under the action of catalyst, the reaction is carried out to generate crude hydrogen. After heat exchange, the heat is recovered, cooled, and then enter the pressure swing adsorption device for final purification.
General equipment and material
| S/N | Item No. | Equipment Name | Unit | Qty. | Material |
| 1 | F0101 | Reformer | Set | 1 | 15CrMoR |
| 2 | E0101 | Superheater | Set | 1 | 0Cr18Ni10Ti/321 |
| 3 | V0101 | Desalt water tank | Set | 1 | 304 |
| 4 | V0102 | Methanol tank | Set | 1 | Q235 |
| 5 | T0101 | Washer/Separator | Set | 1 | 304 |
| 6 | E0102 | Heat exchanger | Set | 1 | SS316 |
Technical indexes:
purity: 99%~99.999%
Capacity: 25~100000Nm3/h
Yield :≥90%
Reference
|
|
| MOQ: | 1 set |
| Price: | Negotiable |
| Standard Packaging: | conventional |
| Delivery Period: | Customized |
| Payment Method: | L/C, T/T |
| Supply Capacity: | Negotiable |
1500Nm3/H Hydrogen Production From Methanol Hydrogen Recovery Unit
2000Nm3/H Hydrogen Recovery And 1500Nm3/H Hydrogen Production From Methanol
Technology Application:
Using methanol as raw material, crude hydrogen (mainly CO2, H2, and trace CO, CH4) is produced by steam cracking process, and then purified by pressure swing adsorption technology to obtain hydrogen with purity meeting the requirements of users.
The raw methanol and raw desalted water are premixed at a certain ratio, pressurized by metering pump, preheated, gasified and superheated, and then enter the reactor. Under the action of catalyst, the reaction is carried out to generate crude hydrogen. After heat exchange, the heat is recovered, cooled, and then enter the pressure swing adsorption device for final purification.
General equipment and material
| S/N | Item No. | Equipment Name | Unit | Qty. | Material |
| 1 | F0101 | Reformer | Set | 1 | 15CrMoR |
| 2 | E0101 | Superheater | Set | 1 | 0Cr18Ni10Ti/321 |
| 3 | V0101 | Desalt water tank | Set | 1 | 304 |
| 4 | V0102 | Methanol tank | Set | 1 | Q235 |
| 5 | T0101 | Washer/Separator | Set | 1 | 304 |
| 6 | E0102 | Heat exchanger | Set | 1 | SS316 |
Technical indexes:
purity: 99%~99.999%
Capacity: 25~100000Nm3/h
Yield :≥90%
Reference
