CO₂ Gas Dryer are used to removing of Moisture in   Co₂ gas mostly used in food and Braveries Industry. After Installed Co₂ dryer dew point of (-) 60^oC . In this design, the desiccant is regenerated at higher temperature, along with small quantity of dry Co₂ Purge.  Due to purging with dry Co₂ and thermal regeneration, residual moisture loading on desiccant becomes low and this gives very low dew points.

Capacity :

• Gas  Capacity : 20kg/hr to 2000kg/hr
• Dew Point :   Up to ( -40^oC) to (-80^oC)
• Operating Pressure :  5 to 80 Kg/cm2g

Operating Principle :
The Co₂ drying unit has 2 vessels filled with Molecular sieves desiccant. One vessel remains in drying cycle for 4 hours, while other vessel is simultaneously regenerates at atmospheric pressure. Around 2 to 3% flow of dryer capacity is used as purge for regeneration. Electrical heaters are provided in a central finned stainless steel pipe in both drying vessels. Heating cycle is for 2 hours and in this time hot purge air increases desiccant temperature to around 150 degree c. At this temperature regeneration is complete (due to dry Co2 purge). Dew point achieved is around (-60 ~C) If still lower dew point is required, Co2 purging rate is slightly increased to 5% for (-60 ~C) and to 7.5% for (-80 ~C) Dew point requirements.

Filters : A pre-filter provided to remove any physical moisture from Co₂ Plant / Co₂ tanker before entering Co₂ Dryer. A  Micron filter is also provided in dryer outlet to arrest any desiccant dust particles, up to 1 micron size. Thus you get absolutely “Clean & dry compressed air.

Features :

• A fully automatics unit requiring no attention of the operator. Heaters switch ON/Off and all valves operate automatically.
• Pressure is equalized to line pressure before changeover of drying vessels. This prevents pressure and flow surge and desiccant dusting.
• Desiccant life is around 5 year.
• Internal heaters provided maximum heat transfer efficiency resulting in lower power requirements.
• Counter current heated dry purge air provides maximum removal of moisture with minimum gas purge loss.
• Heaters are not in physical contact with the desiccant resulting in long life or desiccant.

CO₂ Gas Dryer are used to removing of Moisture in   Co₂ gas mostly used in food and Braveries Industry. After Installed Co₂ dryer dew point of (-) 60^oC . In this design, the desiccant is regenerated at higher temperature, along with small quantity of dry Co₂ Purge.  Due to purging with dry Co₂ and thermal regeneration, residual moisture loading on desiccant becomes low and this gives very low dew points.

Capacity :

• Gas  Capacity : 20kg/hr to 2000kg/hr
• Dew Point :   Up to ( -40^oC) to (-80^oC)
• Operating Pressure :  5 to 80 Kg/cm2g

Operating Principle :
The Co₂ drying unit has 2 vessels filled with Molecular sieves desiccant. One vessel remains in drying cycle for 4 hours, while other vessel is simultaneously regenerates at atmospheric pressure. Around 2 to 3% flow of dryer capacity is used as purge for regeneration. Electrical heaters are provided in a central finned stainless steel pipe in both drying vessels. Heating cycle is for 2 hours and in this time hot purge air increases desiccant temperature to around 150 degree c. At this temperature regeneration is complete (due to dry Co2 purge). Dew point achieved is around (-60 ~C) If still lower dew point is required, Co2 purging rate is slightly increased to 5% for (-60 ~C) and to 7.5% for (-80 ~C) Dew point requirements.

Filters : A pre-filter provided to remove any physical moisture from Co₂ Plant / Co₂ tanker before entering Co₂ Dryer. A  Micron filter is also provided in dryer outlet to arrest any desiccant dust particles, up to 1 micron size. Thus you get absolutely “Clean & dry compressed air.

Features :

• A fully automatics unit requiring no attention of the operator. Heaters switch ON/Off and all valves operate automatically.
• Pressure is equalized to line pressure before changeover of drying vessels. This prevents pressure and flow surge and desiccant dusting.
• Desiccant life is around 5 year.
• Internal heaters provided maximum heat transfer efficiency resulting in lower power requirements.
• Counter current heated dry purge air provides maximum removal of moisture with minimum gas purge loss.
• Heaters are not in physical contact with the desiccant resulting in long life or desiccant.