| 1.Adsorption Downstream |
| The desiccant is compact with no disturbance and low dust amount. Absorption efficiency can be increased by 15% or more. |
| 2. Procedures of adsorption and regeneration in reverse direction |
| To ensure, in the heating process, there was no repeated adsorption and heating was not a waste of power. |
| 3.Procedures of heating and cooling in the same direction |
| To ensure there was no moisture contamination and no adsorption in advance during cooling procedure. |
| 4.The preheating device by heat exchange |
| Via Heat Exchanger, we could preheat the air stream which saved the heating energy consumption for 50% or more. |
| 5. Patent device for energy saving by reuse of internal waste heat |
| To reuse the waste heat in the desiccant and vessel during the cooling procedure and saved the heating energy consumption for 20% or more. |
| 6.Independent operation, more convenient arrangement of facilities |
| When the air compressor was breakdown, owing to the Heater power was over standard designed, the heating temperature could still reach more than 200℃.Thus, it would not be affected by the failure of the air compressor, and it could be operated independently. |
| 7.Really cooling, and no dew point spike |
| Using the CDA for cooling, the desiccant could be completely cooled, and didn't be worried about water vapor contamination because of low temperature. During switchover stage, there was no temperature impact phenomenon which means no dew point spike occurred. |