Under the Accelerated Basin De-inventory (ABD) program H-Canyon will be dissolving aluminum spent nuclear fuel (ASNF) and then neutralizing that solution without performing head-end strike or uranium recovery operations. After dissolution in H-Canyon the material will be neutralized to a free hydroxide concentration of either 0.6 M or 1.2 M to meet the waste acceptance criteria for transfer to the SRS Concentration, Storage and Transfer Facility (CSTF). In order to ensure the material could be successfully neutralized and transferred, SRNL completed experiments with simulated H-Canyon dissolver solutions. Two bounding simulants were developed based on the expected compositions of ASNF to be dissolved, one containing only Gd as the neutron poison and one containing Fe as an additional poison.The first simulant represented a batch of dissolver solution from dissolution of HFIR fuel after isotopic adjustment to 3 wt% 235 U and poisoning with Gd at a ratio of 0.625:1 Gd: 235 U. The second simulant also represented a batch of dissolved HFIR fuel, adjusted to 3 wt% 235 U enrichment, with Gd added at a ratio of 0.625:1, but also included the addition of Fe as a neutron poison at a ratio of 160:1 Fe: 239 Pu equivalent. Analysis of samples taken throughout the neutralization indicated the lowest Gd: 235 U ratio was observed at about the mid-point of the neutralization where the ratio was 0.549 in the solids. This ratio is still well within the safety limits based on the Nuclear Criticality Safety Evaluation (NCSE) performed to calculate the minimum critically safe Gd: 235 U ratio in an infinite system. The evaluation found this ratio to be 0.025 Gd: 235 U for all credible hydrogen to fissile atom ratios. Similar results were obtained for the simulant also containing Fe, where the minimum Gd: 235 U ratio observed was 0.552 in the solids.Physical and rheological properties of the resulting neutralized simulants were also studied to provide the necessary data for performing flow calculations examining the transfer of neutralized slurry from H-Canyon to the CSTF. All endpoints had a final density above the 1.35 g/mL limit and therefore require further dilution at the end of the neutralization. For Simulant #1, the slurry can be successfully transferred after dilution to a density between 1.27 and 1.35 g/mL for both the 0.6 M and 1.2 M OHendpoints. To minimize water addition for Simulant #1, it is recommended to process at 1.35 g/mL. For Simulant #2, it was determined that flow will backup into the header if the pipe roughness is greater than 0.00015 ft for densities above 1.33 g/mL for the 0.6 M slurry. For Simulant #2 it is recommended to target final densities of 1.33 g/mL for the 0.6 M OHendpoint or 1.35 g/mL for the 1.2 M OHcase if the transfer is non-Newtonian. If simulant #2 is transferred as a Newtonian fluid, target 1.25 g/mL for either the 0.6 M or 1.2 M OHendpoints, given densities higher than 1.25 g/mL should be treated as non-Newtonian. At 1.21 g/mL for Simulant #2, the critical velocity needed to maintain the Na ...