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Oxygen Plant-200 Nm3/hr-VSA
Stock Number: 600225
Capacity: 200 Nm3/hr (100 Nm3/hr minimum)
Year Built: 1989
Status: Available
Documentation: Controls, Complete Documents Available
Products Produced:
90% purity Oxygen
Brief Overview:
  • Capacity: The VSA Oxygen Plant normal capacity is 200 Nm3/hr.  The plant has a turn down of 50% so the plant can produce up to 100 Nm3/hr.
  • Manufactured:  Mahler, Germany
  • Purity:  Oxygen purity is 90%.
  • Model #: VSA-200/90
  • Year Built:  1989
Process Description:

VSA Process

In any oxy-generation process, air is passed through a bed of zeolite sieve beads, an adsorbent material derived from naturally occurring crystalline inorganic materials, similar to ordinary clays.  Each bead is approximately 2 mm in diameter. This sieve is specifically designed to separate oxygen from nitrogen and other gases in air, by adsorbing the nitrogen molecules, while allowing the oxygen molecules to pass through to a collection vessel.  When the bed of zeolite sieve is full of nitrogen molecules, it must be regenerated to allow the process to continue.  The collected oxygen at 90% purity is the product, while the impure nitrogen combined with any water and carbon dioxide is vented.  A VSA Process produces oxygen at lower pressure (1.5 barg) and totally regenerates the sieve in a mild vacuum (0.5 barg).  A VSA generator does not require an air compressor.

Air enters the generator via an inlet vent, passes through the four way valve (V-1), through a single stage, dry rotary lobe blower, an air cooler and then into the adsorber bed, again via valve V-1. On entering the adsorber vessel water vapor, carbon dioxide and hydrocarbons are removed in a desiccant layer.  Thus only oxygen and nitrogen molecules flow over the sieve bed, where the nitrogen is adsorbed and the oxygen passes out of the vessel and through the open valve CV-2 to fill the O2 buffer tank.

The bed quickly becomes saturated with nitrogen molecules. These now have to be removed in a vacuum step to regenerate the bed.  Valves CV-1 and CV-2 are closed, and the four way valve V-1 rotates such that the blower now acts in reverse and “extracts” nitrogen molecules off the sieve bed, in addition to removing water vapor, carbon dioxide and hydrocarbons off the desiccant layer.  All these exhaust gases are vented out of the system through the same blower (now acting as a vacuum blower) that the air originally entered.

In the purge step valve CV-2 opens to allow oxygen molecules to flow back into the adsorber vessel to help remove any last traces of nitrogen in the system.
Finally, in the re-pressurization step, the whole system is brought back up to atmospheric pressure by valve V-1 rotating into a position such that air can rush back into the inlet.  At the same time oxygen is allowed into the top of the bed, thus ensuring that there is no movement of the sieve bed (sometimes a problem in PSA systems).  The product valve PIC-1 remains open throughout the whole of the above cycle so that a continuous flow of oxygen product is maintained.


Click Here to View Process Flow Diagram  


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