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Weapons of Mass Destruction (WMD)


Kota
25 10' N 75 50' 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 plants at Manuguru and Kota, which are based on indigenously developed water-hydrogen sulphide exchange process, as well as the other ammonia based plants, have shown very good performance and safety records.

More than 90% of the cumulative world production of heavy water (D20) is by the Hydrogen-sulphide (H2S) water (H20) exchange process, known as the GS process, with the major contribution being from the Canadian plants. Heavy Water Plant at Kota is a solely indigenous effort and is based on the Bithermal H20-H2S exchange process. The plant is located at a distance of 65 KM from Kota Railway Station, adjacent to Rajasthan Atomic Power Plant (RAPP). The Heavy Water Plant is integrated with RAPP for its supply of power and steam. An oil fired Steam Generation Plant is also added to ensure uninterrupted supply of steam during the shut down periods of RAPP.

Water from the nearby Rana Pratap Sagar lake, purified of suspended and dissolved impurities forms the process feed with the D20 coolant of in the feed is enriched 150 ppm (0.015%) enriched to 15% D20 by chemical exchange with H2S and later by vacuum distillation to produce 99.8% D20. The exchange unit is arranged in a 3 stage cascade .The first stage handling large quantities of process water and H2S gas, consists of three pairs of cold and hot towers operating at 30 deg. C. and 130 deg. C. respectively. The second and third stage each consist of one pair of cold and hot towers. The purified water enters the top of first stage cold tower and travels down while hydrogen sulphide gas entering the bottom of the tower meets the water in counter current way on tower internals and the exchange of deuterium takes place. In cold tower the water gets enriched with respect to deuterium while gas gets depleted in deuterium concentration. In hot tower the reverse reaction takes place i.e. the gas gets enriched instead of liquid. By proper liquid and gas flow rates with gas in closed circuit in a pair of towers, a small quantity of enriched liquid can be withdrawn from the bottom of the cold tower as a net product. This is further enriched in a similar way in 2nd and 3rd stages. The hot tower bottoms liquid coming from the first stage is divided into two parts. One part is recycled to the top of humidification section located at the bottom of hot tower for heat recovery while the other part constitutes the waste. Before discarding the waste to the environment it is necessary to recover the H2S dissolved in the waste. For this purpose a waste stripper is provided to strip H2S by direct steam stripping and the evolved gas and steam are put back to first stage hot towers. The enriched water from the 3rd stage is stripped off its H2S in a product stripper and fed to the distillation unit for further enrichment upto nuclear grade.




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