EFRT M-12 Issue Resolution: Comparison of Filter Performance at PEP and CUF Scale | |
Daniel, Richard C. ; Billing, Justin M. ; Bontha, Jagannadha R. ; Brown, Christopher F. ; Eslinger, Paul W. ; Hanson, Brady D. ; Huckaby, James L. ; Karri, Naveen K. ; Kimura, Marcia L. ; Kurath, Dean E. ; Minette, Michael J. | |
关键词: AR FACILITIES; RADIOACTIVE WASTE PROCESSING; FILTERS; PERFORMANCE; ULTRAFILTRATION; RADIOACTIVE WASTES; LEACHING; COMPARATIVE EVALUATIONS; | |
DOI : 10.2172/963841 RP-ID : PNNL-18498 PID : OSTI ID: 963841 Others : Other: 830403000 Others : TRN: US0903292 |
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学科分类:核能源与工程 | |
美国|英语 | |
来源: SciTech Connect | |
【 摘 要 】
Pacific Northwest National Laboratory (PNNL) has been tasked by Bechtel National Inc. (BNI) on the River Protection Project-Hanford Tank Waste Treatment and Immobilization Plant (RPP-WTP) project to perform research and development activities to resolve technical issues identified for the Pretreatment Facility (PTF). The Pretreatment Engineering Platform (PEP) was designed and constructed and is to be operated as part of a plan to respond to issue M12, Undemonstrated Leaching Processes. The PEP is a 1/4.5-scale test platform designed to simulate the WTP pretreatment caustic leaching, oxidative leaching, ultrafiltration solids concentration, and slurry washing processes. The PEP replicates the WTP leaching processes using prototypic equipment and control strategies. The PEP also includes non-prototypic ancillary equipment to support the core processing. Two operating scenarios are currently being evaluated for the ultrafiltration process (UFP) and leaching operations. The first scenario has caustic leaching performed in the UFP-2 ultrafiltration feed vessels (i.e., vessel UFP-VSL-T02A in the PEP and vessels UFP-VSL-00002A and B in the WTP PTF). The second scenario has caustic leaching conducted in the UFP-1 ultrafiltration feed-preparation vessels (i.e., vessels UFP-VSL-T01A and B in the PEP; vessels UFP-VSL-00001A and B in the WTP PTF). In both scenarios, 19-M sodium hydroxide solution (NaOH, caustic) is added to the waste slurry in the vessels to leach solid aluminum compounds (e.g., gibbsite, boehmite). Caustic addition is followed by a heating step that uses direct injection of steam to accelerate the leach process. Following the caustic leach, the vessel contents are cooled using vessel cooling jackets and/or external heat exchangers. The main difference between the two scenarios is that for leaching in UFP1, the 19-M NaOH is added to un-concentrated waste slurry (3 to 8 wt% solids), while for leaching in UFP2, the slurry is concentrated to nominally 20 wt% solids using cross-flow ultrafiltration before the addition of caustic. The work described in this report presents filter flux results obtained at two different scales based on tests performed with a Hanford tank waste simulant. The tests were made at the lab-bench scale on a cold (i.e., designated for non-radioactive simulant test materials) Cells Unit Filter [CUF]) and in the Pretreatment Engineering Platform (PEP), which is a 1/4.5-scale mock-up of key PTF process equipment. One set of tests was conducted with the simulant feed (low solids), and one test was conducted at a relatively high solids concentration. The results of these tests are compared to support a scale factor for use in the WTP.
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