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Hanford underground storage tank waste filtration process evaluation
Author(s) -
B.W. Walker,
D.J. McCabe
Publication year - 1997
Publication title -
osti oai (u.s. department of energy office of scientific and technical information)
Language(s) - English
Resource type - Reports
DOI - 10.2172/568424
Subject(s) - decantation , filtration (mathematics) , shearing (physics) , cross flow filtration , filter (signal processing) , filter press , waste management , volumetric flow rate , leaching (pedology) , materials science , filter cake , hanford site , environmental science , chromatography , chemistry , environmental engineering , membrane , radioactive waste , engineering , composite material , mechanics , mathematics , biochemistry , soil science , soil water , statistics , physics , electrical engineering
The purpose of this filter study was to evaluate cross-flow filtration as effective solid-liquid separation technology for treating Hanford wastes, outline operating conditions for equipment, examine the expected filter flow rates, and determine proper cleaning. Two Hanford waste processing applications have been identified as candidates for the use of cross-flow filtration. The first of the Hanford applications involves filtration of the decanted supernate from sludge leaching and washing operations. This process involves the concentration and removal of dilute (0.05 wt percent) fines from the bulk of the supernate. The second application involves filtration to wash and concentrate the sludge during out-of-tank processing. This process employs a relatively concentrated (8 wt percent) solids feed stream. Filter studies were conducted with simulants to evaluate whether 0.5 micron cross-flow sintered metal Mott filters and 0.1 micron cross-flow Graver filters can perform solid-liquid separation of the solid/liquid waste streams effectively. In cross-flow filtration the fluid to be filtered flows in parallel to the membrane surface and generates shearing forces and/or turbulence across the filter medium. This shearing influences formation of filter cake stabilizing the filtrate flow rate

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