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Archive | 2008

Pulse Jet Mixer Overblow Testing for Assessment of Loadings During Multiple Overblows

David M. Pfund; Jagannadha R. Bontha; Thomas E. Michener; Franz Nigl; Satoru T. Yokuda; Richard J. Leigh; Elizabeth C. Golovich; Aaron W. Baumann; Dean E. Kurath; Mark Hoza; William H. Combs; James A. Fort; Ofelia P. Bredt

The U.S. Department of Energy (DOE) Office of River Protection’s Waste Treatment Plant (WTP) is being designed and built to pretreat and then vitrify a large portion of the wastes in Hanford’s 177 underground waste storage tanks. The WTP consists of three primary facilities: pretreatment, low-activity waste (LAW) vitrification, and high-level waste (HLW) vitrification. The pretreatment facility will receive waste feed from the Hanford tank farms and separate it into 1) a high-volume, low-activity liquid stream stripped of most solids and radionuclides and 2) a much smaller volume of HLW slurry containing most of the solids and most of the radioactivity. Many of the vessels in the pretreatment facility will contain pulse jet mixers (PJMs) that will provide some or all of the mixing in the vessels. This technology was selected for use in so-called “black cell” regions of the WTP, where maintenance capability will not be available for the operating life of the WTP. PJM technology was selected for use in these regions because it has no moving mechanical parts that require maintenance. The vessels with the most concentrated slurries will also be mixed with air spargers and/or steady jets in addition to the mixing provided by the PJMs. This report contains the results of single and multiple PJM overblow tests conducted in a large, ~13 ft-diameter × 15-ft-tall tank located in the high bay of the Pacific Northwest National Laboratory (PNNL) 336 Building test facility. These single and multiple PJM overblow tests were conducted using water and a clay simulant to bound the lower and upper rheological properties of the waste streams anticipated to be processed in the WTP. Hydrodynamic pressures were measured at a number of locations in the test vessel using an array of nine pressure sensors and four hydrophones. These measurements were made under normal and limiting vessel operating conditions (i.e., maximum PJM fluid emptying velocity, maximum and minimum vessel contents for PJM operation, and maximum and minimum rheological properties). Test data collected from the PJM overblow tests were provided to Bechtel National, Inc. (BNI) for assessing hydrostatic, dynamic, and acoustic pressure loadings on in-tank structures during 1) single overblows; 2) multiple overlapping overblows of two to four PJMs; 3) simultaneous overblows of pairs of PJMs.


ASME 2007 International Mechanical Engineering Congress and Exposition | 2007

Evaluating Pulse Jet Mixing With Non-Newtonian Slurries

Judith A. Bamberger; Perry A. Meyer; Jagan R. Bontha; James A. Fort; Franz Nigl; James M. Bates; Carl W. Enderlin; Sato T. Yokuda; Dean E. Kurath; Adam P. Poloski; Harry D. Smith; Gary L. Smith; Mark A. Gerber

Pulse jet mixer technology has been selected for implementation in the Hanford Waste Treatment Plant. However, processing non-Newtonian fluids using this technology is not mature. Experiments were conducted at several scales to develop an understanding of the scaling mechanisms that govern this type of mixer performance.Copyright


Archive | 1996

Microcomponent chemical process sheet architecture

Robert S. Wegeng; M. Kevin Drost; Charles J. Call; Joseph G. Birmingham; Carolyn Evans Mcdonald; Dean E. Kurath; Michele Friedrich


Archive | 1999

Microcomponent assembly for efficient contacting of fluid

Monte Kevin Drost; Robert S. Wegeng; Michele Friedrich; William T. Hanna; Charles J. Call; Dean E. Kurath


Archive | 2006

Scaling Laws for Reduced-Scale Tests of Pulse Jet Mixing Systems in Non-Newtonian Slurries: Gas Retention and Release Behavior

Charles W. Stewart; Perry A. Meyer; Dean E. Kurath; Steven M. Barnes


Journal of the American Ceramic Society | 1998

Ceramic Membranes for Separation of Sodium

Glenn W. Hollenberg; Dean E. Kurath; Kriston P. Brooks


Archive | 1996

Plattenarchitektur für chemischen Prozess auf Basis von Mikrokomponenten

Robert S. Wegeng; Kevin M. Drost; Charles J. Call; Carolyn Evans Mcdonald; Dean E. Kurath; Michelle Friedrich; Joseph G. Birmingham


Archive | 2006

Scaling Laws for Reduced-Scale Tests of Pulse Jet Mixing Systems in Non-Newtonian Slurries: Mixing Cavern Behavior

Perry A. Meyer; Dean E. Kurath; Judith Ann Bamberger; Steven M. Barnes; Arthur W. Etchells


Archive | 2006

Overview of Pulse Jet Mixer/Hybrid Mixing System Development to Support the Hanford Waste Treatment Plant

Dean E. Kurath; Perry A. Meyer; Charles W. Stewart; Steven M. Barnes


Archive | 1999

Assemblage de microcomposants pour la mise en contact efficace de fluide

Monte Kevin Drost; Robert S. Wegeng; Michele Friedrich; William T. Hanna; Charles J. Call; Dean E. Kurath

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Charles J. Call

Battelle Memorial Institute

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Robert S. Wegeng

Battelle Memorial Institute

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Perry A. Meyer

Pacific Northwest National Laboratory

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M. Kevin Drost

Pacific Northwest National Laboratory

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Michele Friedrich

Battelle Memorial Institute

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Franz Nigl

Battelle Memorial Institute

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James A. Fort

Battelle Memorial Institute

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Monte Kevin Drost

Battelle Memorial Institute

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