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Heavy Water Plant at Talcher employs the
ammonia-hydrogen exchange process (Bithermal). The plant is located at a distance of 150
Kms. from Bhubaneshwar. The work on this plant in October 1972 and it was commissioned in
March 1985. |
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| containing 140 ppm (0.014%) of deuterium, produced in one of the adjacent ammonia plant for their captive use, is routed through the plant at a rate of 99,600 Nm3/hr. | ||
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The pressure of the synthesis gas is first raised by 10-15 Kg/cm2. to take care of pressure drop in the transfer section. The gas is passed through a purification unit to remove impurities like O2, CO, CO2, Oil and water vapour, and to saturate it with ammonia by washing with liquid ammonia and ammonical solution of potassium amide. The purified saturated gas is then passed through the transfer column operating at -30 deg. C., where deuterium in the gas is transferred to a counter current streams of liquid ammonia obtained from the enrichment section and containing potassium amide catalyst. The depleted synthesis gas from the transfer column is sent back to the fertilizer plant |
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| while enriched liquid ammonia is fed to the enrichment section for further enrichment. | ||
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