Executive SummaryWashington River Protection Solutions (WRPS), as the Hanford Site tank farms contractor, will be responsible for transferring waste from a double-shell tank (DST) to the Waste Treatment and Immobilization Plant (WTP) when the WTP begins operations. The WRPS approach for predicting mixing and transfer performance (MTP) for a DST involves three primary steps:1. Conduct tests consisting of variations in several parameters in two scaled tanks in the Small Scale Mixing Demonstration (SSMD) platform to generate data on MTP.2. Develop scaling relationships for MTP as a function of the test parameters using the test data from Step 1.
Use the scaling relationships fromStep 2 that are valid for the two test scales, as well as other knowledge and methods for mixing and transfer, to develop scaling relationships applicable to full-scale DST performance.Step 1 has been completed by WRPS, which involved generating data for 26 test combinations performed in both of the two scaled tanks of the SSMD platform (for a total of 52 tests). The two tanks had diameters of 43.2 (referred to as 43 subsequently) and 120 inches, which are 1:21 and 1:8 relative to a full-scale DST, respectively. Other parameters that were varied in testing included mixer-jet nozzle velocity (U), base simulant (BS), supernatant viscosity (SV), (a) and transfer-line capture velocity (CV). The first 22 of the 26 test combinations conducted in both size tanks were selected using a statistical experimental design approach. An additional 4 test combinations performed at both scales used parameter combinations that are most relevant to expected operating conditions, and had not been tested previously. For each of the 52 tests, samples were collected pre-transfer and for each of five batch transfers. The samples were prepared and analyzed, with the results being the concentrations (lb/gal slurry) of the four solids components (gibbsite, stainless steel, sand, and ZrO 2 ) in the base simulant.Step 2 consists of building mathematical models for each of the two scale tanks that describe the MTP as a function of the test parameters. These models can then be used to calculate mixer-jet nozzle velocities where performance is equal between tank scales. These points of equal performance can be used to derive scaling relationships, which will allow estimating performance for full-scale DSTs. This report documents the statistical analyses associated with Step 2, which were performed by Pacific Northwest National Laboratory (PNNL) on data from the 52 tests conducted. Preliminary efforts focused on trying to model MTP metrics consisting of differences or ratios of BS-component concentrations for the five batch transfers relative to pre-transfer. However, depending on the solids component, there was little difference in component concentrations in batch transfers compared to pre-transfer for many to most of the tests. Hence, such differences and ratios of component concentrations were not useful MTP metrics because the effects of the test parameters "canceled ...