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PRESSURE SWING ADSORPTION (PSA) NITROGEN GAS GENERATOR / PLANT: | |||||||||||||||||||||||||||||||
What is PSA Process? | |||||||||||||||||||||||||||||||
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“PSA” stands for Pressure Swing Adsorption. This is the separation technology which separates Nitrogen and Oxygen Molecules from rich compressed air. Commercial nitrogen production process usually employ Carbon Molecular Sieves as adsorbents. These process depends on kinetic separation accomplished by a faster diffusion of oxygen molecules through the pore structure of the adsorbent. The Oxygen is adsorbed to its equilibrium value much faster than Nitrogen. This is because Oxygen which is smaller in size (kinetic diameter 3.46 A.o) diffuses much faster in Carbon Molecular Sieves than Nitrogen (kinetic diameter 3.64 A.o). |
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How Does it Works ? | |||||||||||||||||||||||||||||||
This equipment comprises 2 beds filled with Carbon Molecular Sieves and 08-Nos. control valves interconnecting both the beds. The compressed air at 7.0 Kg/Cm2G is passed through the bottom of the bed-1 and Nitrogen is recovered at the top at 5.5 Kg/Cm2G pressure while the other bed is simultaneously regenerated by depressurization to atmospheric pressure. | |||||||||||||||||||||||||||||||
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| MODEL ATLP
AND ATHP : |
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| APPLICATION : |
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Ø Blanketing in Process Plant, Chemical & Petro-Chemical Industries.Ø
Storage
against Oxygen and Moisture. Ø
Pressure
transfer of sensitive
Chemicals. Ø
Packing
against Oxidation Contamination in Food, Dairy,
Pharmaceutical. Ø
Fire Control
in Coal Mines. Ø
POY / PFY
process. |
| FLOW SCHEME DIAGRAM : |
| MODEL ATUHP
: |
In addition to the basic simplest model yielding 99.0 % Nitrogen, Hydrogen (from Ammonia Cracker or from Hydrogen Bottle) is mixed and is passed through a Palladium based Deoxo unit where the below specified reaction takes place : |
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O2
+ 2H2 |
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After above
reaction the product Gas would be with higher temperature which is cooled
down in a Heat Exchanger and simultaneously its moisture is removed by the
Gas Dryer.The Gas
Composition of this model comprises 1 to 3 PPM of Oxygen content and 0.5
to 5.0 % Hydrogen which is
desirable as reducing agent in most of the Heat Treatment
Application. Atmosphere of
desired composition and character is made by selective addition of
Hydrogen / Hydro-Carbon, Methanol to Nitrogen as appropriate to specific
heat treatment process and metals to be treated. |
| APPLICATION: |
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Ø
Heat Treatment
Application to avoid Oxidation in Metallurgical Industries. Ø Nitrogen Based
Control Furnace whose atmospheres in heat treatment process like
Annealing, Normalizing, Carburizing, Hardening etc. of metals. Ø
All type of Chemical, Food, Dairy, Petro-Chemical,
Pigments, Paints, Packing Industries etc. |
| FLOW SCHEME DIAGRAM : |
| MODEL
ATSUHP : |
This model is suitable for Oxygen free Nitrogen. The product Gas comprises 1 PPM Oxygen and Zero Hydrogen (or adjustable as desired). This Composition is achieved by adding a module called Copper-Deoxo consisting of Cupric Oxide. The following would be the chemical reaction : |
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02 + 2Cu --------------> 2CuO |
| After above reaction the product Gas would be with
higher temperature which is cooled down in a Heat Exchanger and
simultaneously its moisture is removed by the Gas Dryer. |
| APPLICATION: |
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Ø
Semi-Conductor
application Ø
Electronics
etc. |
| FLOW SCHEME DIAGRAM : |
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