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Bolling, Stacey D.

Publications and source records attributed to Bolling, Stacey D..

Tank 241-AN-107 Study for Semi-Volatile Organics in 2017 Grab Samples and Carbonation of Composite for Solids Precipitation and Caustic Demand

Tank 241-AN-107 waste is known to contain high concentrations of complexing organics, and caustic sodium hydroxide has been added due to depleted free hydroxide in the waste. Eight grab samples were taken in August 2017 for routine chemical analyses. Investigations of the tank’s organic contents and solids precipitation at lower pH levels by CO 2 gas, as well as the performance of caustic demand testing at lower pH ranges were examined. Sub-micron particles were visible, suspended in the supernate, using scanning electron microscopy. Trace amounts of precipitation floating on the surface of the supernate were observed and were collected with the surface liquid samples for investigation.

37 INORGANIC, ORGANIC, PHYSICAL, AND ANALYTICAL CH↗

Peroxide Decomposer Module Catalyst Testing to Support Preparations for Increased Demand - 19052

The Hanford Site Effluent Treatment Facility's (ETF) mission is to receive, treat, and dispose of liquid effluents from on-site programs and projects. Its roles in the management and mitigation of tank waste volume is integral to the overall Hanford tank farms mission, as tank space is limited. ETF's role will become even more essential as the Direct-Feed Low Activity Waste process comes online at the Waste Treatment and Immobilization Plant (WTP). In order to accommodate the additional liquid effluent streams, the ETF will undergo a number of facility and equipment upgrades. Included in this is the reinstatement of the Peroxide Decomposer Module (PDM) into the ETF's main treatment train. The PDM is used to remove any residual hydrogen peroxide not fully consumed in the preceding ultraviolet/oxidation (UV/OX) treatment stage for organic destruction. Future waste stream estimates have been shown to contain organic content requiring excess hydrogen peroxide addition. Restoration of the PDM will ensure the ETF can accommodate the higher anticipated levels of organic content in these new influent streams. Due to low organic content levels in the current influents and some operability issues with the PDM, it has not been in operation since 1998. One aspect of the repair and upgrade of the PDM is the usability of manganese dioxide on alumina catalyst, Sud-Chemie T-2525, which was purchased in 2008 but has remained in storage since. The manufacturer of the catalyst states there is no known shelf life for the product and no current data to indicate the catalyst's performance after long-term storage. To determine the usability of the stored catalyst, a laboratory test was developed. The testing of this stored catalyst was based on testing methods and information collected from initial catalyst product testing performed in 2008. This test involved spiking the catalyst with 200 ppm hydrogen peroxide and then testing the resulting solution to determine the extent of peroxide destruction. Initial testing results of the Sud-Chemie T-2525 catalyst indicated reduced performance, so additional catalyst materials were selected for inclusion in the testing. These materials included Carulite{sup R} 200 catalyst, LayneOx{sup R}, natural manganese ore - pyrolusite (Pro-Ox{sup R}), and EnviCat{sup R} 2531 SPH 4-6. With the expansion of the test scope, fines generation testing was added to provide additional data for product selection, as excessive fines cause plugging in the PDM. The resulting test data are compared to the 2008 catalyst product testing data in order to evaluate performance of each product to determine whether the Sud-Chemie T-2525 is still viable and to determine the best candidate for its replacement. This testing provides essential information to the engineering and operations organizations managing the facility and equipment upgrades for the ETF. (authors)

12 MANAGEMENT OF RADIOACTIVE AND NON-RADIOACTIVE W↗

Investigation of Tank 241-AW-104 Composite Floating Layer

Seven grab samples and one field blank were taken June 2, 2017. A visible layer with brown solids was observed floating on the top of two surface tank waste samples (4AW-17-02 and 4AW 17 02DUP). The floating layers were collected, composited, and submitted for chemical analyses and solid phase characterization in order to understand the composition of the floating layer. Tributyl phosphate and tridecane were higher in the floating layer than in the aqueous phase. Density in the floating layer was slightly lower than the mean density of all grab samples. Sodium nitrate and sodium carbonate were major components with a trace of gibbsite and very small size agglomerates were present in the solids of the floating layer. The supernate consisted of organics, soluble salt, and particulates. These agglomerates include uranium extruded from the supernate by the floating organics.

12 MANAGEMENT OF RADIOACTIVE AND NON-RADIOACTIVE W↗

Effluent Treatment Facility Catalyst Testing

ETF needs to bring its peroxide decomposer module back on-line in order to support the Waste Treatment and Immobilization Plant. This report discusses testing of five catalyst materials: Sud-Chemie T-2525, Carulite 200, EnviCat VOC-2531, LayneOx and a natural manganese ore. This testing looked at the amount of fines produced as well as the peroxide destruction abilities of each material. The Sud-Chemie T-2525 material had the least amount of fines and reduced the peroxide to ≤10 ppm within 30 min. The Carulite 200 and EnviCat VOC 2531 catalysts contained more fines than the T-2525 material, but also reduced the peroxide concentration to ≤10 ppm within 30 min. The Pro Ox and LayneOx materials contained the greatest amount of fines and did not reduce as much peroxide when compared to the other catalysts tested.

12 MANAGEMENT OF RADIOACTIVE AND NON-RADIOACTIVE W↗