Porous adsorbent for trapping radioactive iodine gas and method of manufacturing the same

Abstract

Provided are an adsorbent for trapping a radioactive iodine gas generated in a process of oxidizing a nuclear fuel at a high temperature after use and a method of preparing the same, and more particularly, a radioactive iodine gas adsorbent which is formed of bismuth as a main component, thereby exhibiting an excellent radioactive iodine gas trapping capability and an excellent thermal stability after trapping, and a method of preparing the same. An adsorbent for trapping a radioactive iodine gas prepared by a method of preparing an adsorbent for trapping a radioactive iodine gas according to the present disclosure may effectively trap a radioactive iodine off-gas generated in a nuclear fuel pre-treated oxidizing process after use. Particularly, the adsorbent may trap iodine in a larger amount, which is twice or more, than a silver-containing zeolite widely used to trap a radioactive iodine gas, and the trapped iodine forms a stable compound, which is more advantageous for long-term storage. In addition, since an iodine gas is trapped using inexpensive bismuth, instead of expensive silver, in consideration of trapping a large amount of a radioactive iodine gas, the adsorbent has very excellent economic feasibility.

1 .- 9 . (canceled) 
     
     
         10 . A porous adsorbent for trapping radioactive iodine gas: comprising Bi and Bi 2 O 3 . 
     
     
         11 . The porous adsorbent according to  claim 10 , wherein the porous adsorbent manufactured by the manufacturing method comprising the following steps of:
 (a) preparing a mixed solution by mixing a solution including 10 to 20 wt % of bismuth nitrate and a solution including 10 to 20 wt % of polyvinylalcohol;   (b) preparing a mixture by drying the mixed solution to remove moisture;   (c) preparing an oxide by heat-treating the mixture in an air atmospheric ambience to remove the polyvinylalcohol; and   (d) reducing the oxide to an element bismuth state by heat-treating the oxide in a hydrogen-containing ambience.   
     
     
         12 . The porous adsorbent according to  claim 11 , wherein, in the step (a), the solution including 10 to 20 wt % of bismuth nitrate includes 10 to 50 ml of nitric acid per 100 ml of distilled water. 
     
     
         13 . The porous adsorbent according to  claim 11 , wherein the drying in the step (b) is performed at 40 to 70° C. for 1 to 4 days. 
     
     
         14 . The porous adsorbent according to  claim 11 , wherein the heat-treatment in the step (c) is performed in an air atmospheric ambience at 400 to 500° C. for 2 to 3 hours. 
     
     
         15 . The porous adsorbent according to  claim 11 , wherein the reduction in the step (d) is performed in a 4% hydrogen-containing ambience at 300 to 350° C. for 6 to 12 hours.