Product Description
| Tank | Volume (m³) | loading mass (ton) | standard and configuration | |
| 1 | Liquid ammonia tank | 10 | 5.2 | Execution standard: GB150 “pressure vessel” and “fixed pressure vessel safety technology and supervision code” design pressure: 21.6 design temperature: 50 ° c filling ratio: 0.52 corrosion allowance: material: 2 mm subject Q345R |
| 2 | 20 | 10.4 | ||
| 3 | Liquid ammonia tank | 25 | 13 | |
| 4 | 32 | 16.64 | ||
| 5 | Liquid ammonia tank | 50 | 26 | |
| 6 | 60 | 32.2 | ||
| 7 | Liquid ammonia tank | 80 | 41.6 | |
| 8 | 100 | 46.8 |
Butane Tank Horizontal Storage 40m3 (Pressure Vessel ) for LPG Gas Propane, Liquid Sulfur Dioxide, Isobutane, Dimethyl Ether
Propane design pressure of 1.77 MPa design temperature 50 ºC corrosion allowance 1 mm density of 0.42 T/M3
Design of liquid ammonia pressure of 2.16 MPa design temperature 50 ºC corrosion allowance 2 mm density of 0.52 T/M3
Propane design pressure of 1.77 MPa design temperature 50 ºC corrosion allowance 1 mm density of 0.42 T/M3
Propane design pressure of 2.16 MPa design temperature 50 ºC corrosion allowance 1 mm density of 0.43 T/M3
Liquid sulfur dioxide design pressure of 0.98 MPa design temperature 50 ºC corrosion allowance 4 mm density of 1.2 T/M3
Gas pressure is 4.1 MPa design temperature 50 ºC corrosion allowance of 1.4 mm
Propane design pressure of 1.77 MPa design temperature 50 ºC corrosion allowance 1 mm density of 0.42 T/M3
Isobutane design pressure of 0.79 MPa design temperature 50 ºC corrosion allowance 1 mm density of 0.49 T/M3
Dimethyl ether design pressure of 1.15 MPa design temperature 50 ºC corrosion allowance 1 mm density of 0.58 T/M3
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