Weapons of Mass Destruction (WMD)


Tuticorin
08 48' N 78 10' E

Indian heavy-water production supports domestic natural uranium [versus enriched uranium] nuclear power plants. Difficulties in supplying reactor inventories have been mitigated by nuclear power plant construction delays. A total of eight operating heavy-water plants have a total production capacity of more than 650 te/yr, adequate both to support current domestic requirements and export sales [including 100 te to South Korea and 350 te to Romania]. Six of the plants use ammonia exchange processes and are associated with fertilizer production plants, and the other two use the hydrogen sulfide process.

The Heavy Water Plant at Tuticorin is located at a distance of about 14 km from Tuticorin Railway Station. Work on HWP Tuticorin was commenced in September 1971 and the plant was commissioned in July 1978.

The plant employs the ammonia-hydrogen exchange process (monothermal).Synthesis gas (a mixture of three parts of hydrogen and one part of nitrogen) containing deuterium, produced in one of the adjacent Ammonia Plant for their captive use, is routed through the plant at a flow rate of about 48 T/hr. at a pressure of about 191-216 kgs./cm2. The pressure of the gas is first raised by 40 kg/cm2 to take care of pressure drop in the HWP. It is then cooled in a heat exchanger by the outgoing cold gas to Ammonia Plant. The gas is thereafter passed through a purification unit. In this unit the impurities contained in the gas such as water, carbon monoxide, carbon dioxide and oxygen are removed and the gas is saturated with ammonia. The cooled and purified synthesis gas saturated with ammonia is then passed through the first isotopic exchange tower working at minus 25 degree Celsius where deuterium in the gas is transferred to a counter current stream of liquid ammonia fed from the top of the tower in the presence of potassium amide catalyst dissolved in liquid ammonia.The deuterium enriched ammonia from the bottom of the exchange tower, is then fed to the second isotopic exchange tower where it gets further enriched by coming in contact with the cracked gases obtained by cracking of enriched ammonia.

A part of the enriched gas and liquid from the second isotopic exchange tower is then taken to the final enrichment section where the concentration of deuterium in the ammonia can be further increased, as desired, upto 99.8%. However, for reasons of better recovery efficiency the concentration of deuterium in ammonia from the final enrichment section is kept at around 60%. The enriched ammonia so obtained is cracked and a portion of this enriched synthesis gas is burnt with dry air to produce off-grade heavy water and the off-grade heavy water is further distilled in an upgrading plant to produce nuclear grade heavy water.





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