Abstract
At present the ammonium uranyl carbonate (AUC) route is developed at a scale of 10 kg/day of UO{sub 2}. This UO{sub 2} is directly compactible and sinterable to densities of 10.55-10.65 gm/cc. The equipment developed include precipitation tank with filtration and methanol washing and fluidized bed furnaces for thermal treatment of AUC and U{sub 3}O{sub 8}. During the design and development of these furnaces many experiments were conducted to study fluidization of AUC powder. In this paper the findings of these studies are presented. (author). 3 refs., 4 figs., 3 tabs.
Citation Formats
Gupta, U C, Anuradha, M, and Meena, R.
Development of fluidized-bed furnace for thermal treatment of ammonium uranyl carbonate.
India: N. p.,
1994.
Web.
Gupta, U C, Anuradha, M, & Meena, R.
Development of fluidized-bed furnace for thermal treatment of ammonium uranyl carbonate.
India.
Gupta, U C, Anuradha, M, and Meena, R.
1994.
"Development of fluidized-bed furnace for thermal treatment of ammonium uranyl carbonate."
India.
@misc{etde_592012,
title = {Development of fluidized-bed furnace for thermal treatment of ammonium uranyl carbonate}
author = {Gupta, U C, Anuradha, M, and Meena, R}
abstractNote = {At present the ammonium uranyl carbonate (AUC) route is developed at a scale of 10 kg/day of UO{sub 2}. This UO{sub 2} is directly compactible and sinterable to densities of 10.55-10.65 gm/cc. The equipment developed include precipitation tank with filtration and methanol washing and fluidized bed furnaces for thermal treatment of AUC and U{sub 3}O{sub 8}. During the design and development of these furnaces many experiments were conducted to study fluidization of AUC powder. In this paper the findings of these studies are presented. (author). 3 refs., 4 figs., 3 tabs.}
place = {India}
year = {1994}
month = {Jun}
}
title = {Development of fluidized-bed furnace for thermal treatment of ammonium uranyl carbonate}
author = {Gupta, U C, Anuradha, M, and Meena, R}
abstractNote = {At present the ammonium uranyl carbonate (AUC) route is developed at a scale of 10 kg/day of UO{sub 2}. This UO{sub 2} is directly compactible and sinterable to densities of 10.55-10.65 gm/cc. The equipment developed include precipitation tank with filtration and methanol washing and fluidized bed furnaces for thermal treatment of AUC and U{sub 3}O{sub 8}. During the design and development of these furnaces many experiments were conducted to study fluidization of AUC powder. In this paper the findings of these studies are presented. (author). 3 refs., 4 figs., 3 tabs.}
place = {India}
year = {1994}
month = {Jun}
}