SUMMARYDissolution kinetics of alumina type non-radioactive calcine was investigated as part of ongoing research that addresses permanent disposal of Idaho High Level Waste (HLW). Calcine waste was produced from the processing of nuclear fuel at the Idaho Nuclear Technology and Engineering Center (INTEC). Acidic radioactive raffinates were solidified at ~500ºC in a fluidized bed reactor to form the dry granular calcine material. Several Waste Management alternatives for the calcine are presented in the Idaho High Level Waste Draft EIS. The Separations Alternative addresses the processing of the calcine so that the HLW is ready for removal to a national geological repository by the year 2035. Calcine dissolution is the key front-end unit operation for the separations alternative.Because aluminum and zirconium-type fuels were predominately reprocessed at the INTEC, alumina and zirconia-type calcines were produced and stored. Dissolution kinetics testing with non-radioactive pilot plant zirconia calcine has been previously investigated. Similar to that work, the scope of this present alumina calcine dissolution work included: 1) chemical and physical analyses of the calcine material, 2) baseline dissolution testing to determine: order of reaction, activation energy (Arrhenius analysis), and dissolution rate controlling mechanism (chemical reaction or mass transfer limited). Testing was also performed to determine if complete dissolution is equilibrium/solubility inhibited.Chemical and physical analyses were performed on the RSH-1 alumina type pilot plant calcine bed material. Elemental fusion analysis results agree well with microprobe analysis results. An average value of the calcine acid consumption coefficient, b, was determined for RSH-1 bed product material; b = 19.8 grams RSH-1 dissolved per mol of acid consumed. The order of reaction testing revealed that, just as in the case for the Run74 zirconia pilot plant calcine testing, the homogeneous rate form fit the rate data better than the heterogeneous rate form. A characteristic dissolution fractal dimension, D R , was determined for alumina and zirconia pilot plant calcine milled material and bed particles. The result from this fractal treatment of the dissolution data further supports the indication that calcine dissolution is more dependent upon its physical characteristics, rather than its chemical characteristics. Arrhenius testing yielded an apparent activation energy (E A ) of 26.9 kcal/mol for RSH-1 alumina pilot plant calcine under conditions of constant 6 M acid concentration. The dissolution rate controlling mechanism testing results were inconclusive. Nevertheless, it was noted that, just as with all previous calcine dissolution testing, this testing with RSH-1 showed the familiar initial rapid dissolution then the leveling-out of the rate, and the non-attainment of 100% dissolution after long dissolution times-it too had the characteristics of internal mass diffusion controlled dissolution. The equilibrium/solubility inhibition testing results ind...