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Project | One effect evaporator | Condenser |
/Material name | Alcohol solution | --- |
/PH value | / | --- |
Discharge method | First effect output | --- |
Total feed | 300kg/h | |
Rated evaporation | 200kg/h | |
Raw steam consumption | 200kg/h(Saturated Vapor) | |
Steam consumption ratio | Each ton of water evaporated requires ≤1100kg steam | |
Raw steam temperature (℃) | 105±2 vapor phase | --- |
Secondary steam temperature of each effect (℃) | 70±2 vapor phase | 70±2 vapor phase |
Temperature of each effect material liquid (℃) | 75±2vapor phase | 45±2vapor phase |
Vacuum degree of each effect (-MPa) | ~0.05 | ~0.090 |
The boiling point of each effect material liquid increases (℃) | ~5 | --- |
Temperature loss of each effect (℃) | 2 | --- |
Heat loss of each effect (%) | 0.08 | --- |
Effective heat transfer temperature difference of each effect (℃) | 30 | --- |
Circulation type of each effect evaporator | Falling film circulation | --- |





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