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Subtitle: feed slurry: 10 to 40 vol.-% solid volume fraction, in-situ and in a VDI pressure nutsch built filter cakes

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Additional titleSubtitle: feed slurry: 10 to 40 vol.-% solid volume fraction, in-situ and in a VDI pressure nutsch built filter cakes
Alternative existing references for this datasetCF_010_055200_021
Alternative existing references for this datasetCF_015_055200_020
Alternative existing references for this datasetCF_020_055200_016
Alternative existing references for this datasetCF_025_055200_019
Alternative existing references for this datasetCF_030_055200_017
Alternative existing references for this datasetCF_035_055200_015
Alternative existing references for this datasetCF_040_055200_018
Alternative existing references for this datasetVDI_025_055200_003
Alternative existing references for this datasetVDI_025_055200_007
Alternative existing references for this datasetVDI_025_055200_008
Alternative existing references for this datasetVDI_025_055200_009
Other contributing persons, institutions or organisationsLeißner, Thomas - Technical University Bergakademie Freiberg - Institute of Mechanical Process Engineering and Mineral Processing - Supervisor
Other contributing persons, institutions or organisationsPeuker, Urs Alexander - Technical University Bergakademie Freiberg - Institute of Mechanical Process Engineering and Mineral Processing - Supervisor
Other contributing persons, institutions or organisationsGerman Research Foundation - Sponsor
Person(s) who is (are) responsible for the content of the research dataLöwer, Erik - Technical University Bergakademie Freiberg - Institute of Mechanical Process Engineering and Mineral Processing (ORCID: 0000-0002-6956-8054)
Description of further data processingautomatic centre shift, beam hardening correction (0.05), gauss smoothing filter (kernel 0.7)
Type of data acquisitionExperiment: cake filtration (in-situ experiment, 5 mm flow cell)
Type of data acquisitionExperiment: cake filtration (sampled filter cakes, 50 mm diameter of pressure nutsch)
Used research instruments or devicesX-ray microscope (ZEISS X-radia Versa 510)
Research objectsSubstance: potassium iodide (manufacturer Carl Roth, > 99 %, 25 mmol/l)
Research objectsSubstance: glycerol (manufacturer Carl Roth, > 99,8 %, 24 m.-%)
Research objectsSubstance: water (demineralized)
Research objectsSubstance: gamma-Al2O3 (manufacturer Almatis, solid powder, 55 µm < x < 200 µm)
AbstractX-ray tomography measurements (Zeiss X-radia Versa 510) of in-situ and in a VDI pressure nutsch built filter cakes (Al2O3 crushed particles in 25 mmol/l KI brine with 24 m.-% glycerol). The filter cakes are measured completely saturated. The initial slurry contains Al2O3 particles by variation of the solid content from 10 to 40 vol.-%.
Applied methods and techniquescake filtration according VDI 2762-1, VDI 2762-2, VDI 2762-3
Additional descriptive information to understand the datasee notes in parameter.png for each measurement (measurement and reconstruction parameters)
Series informationVariation in solid volume fraction and comparison of in-situ built filter cakes ('CF') and in a conventional pressure nutsch ('VDI'), both scanned by X-ray tomography (Zeiss X-radia Versa 510). The initial slurry contains Al2O3 particles suspended in a potassium iodide-glycerol solution. These were separated by cake-forming filtration.
Table of contentsCF_010_055200_021 (feed slurry: 10 vol.-% solid volume fraction, in-situ cake filtration), CF_015_055200_020 (feed slurry: 15 vol.-% solid volume fraction, in-situ cake filtration), CF_020_055200_016 (feed slurry: 20 vol.-% solid volume fraction, in-situ cake filtration), CF_025_055200_019 (feed slurry: 25 vol.-% solid volume fraction, in-situ cake filtration), CF_030_055200_017 (feed slurry: 30 vol.-% solid volume fraction, in-situ cake filtration), CF_035_055200_015 (feed slurry: 35 vol.-% solid volume fraction, in-situ cake filtration), CF_040_055200_018 (feed slurry: 40 vol.-% solid volume fraction, in-situ cake filtration), VDI_025_055200_003a (feed slurry: 25 vol.-% solid volume fraction, sampled cake, built according VDI 2762, above filte cloth, centre of cake), VDI_025_055200_003b (feed slurry: 25 vol.-% solid volume fraction, sampled cake, built according VDI 2762, beneath surface, centre of cake), VDI_025_055200_007a (feed slurry: 25 vol.-% solid volume fraction, sampled cake, built according VDI 2762, above filte cloth, next nutsch wall), VDI_025_055200_007b (feed slurry: 25 vol.-% solid volume fraction, sampled cake, built according VDI 2762, beneath surface, next nutsch wall), VDI_025_055200_008 (feed slurry: 25 vol.-% solid volume fraction, sampled cake, built according VDI 2762, total cake height, centre of cake), VDI_025_055200_009 (feed slurry: 25 vol.-% solid volume fraction, sampled cake, built according VDI 2762, total cake height, next nutsch wall)
Additional keywordscake filtration, X-ray tomography, in-situ, VDI 2762
Languageeng
Year or period of data production2017-2018
Publication year2021
PublisherTechnical University Bergakademie Freiberg - Institute of Mechanical Process Engineering and Mineral Processing
References on related materialsIsSourceOf: 10.1016/j.powtec.2019.12.054 (DOI)
Content of the research dataDataset: X-ray tomography scans of filter cakes (.tiff stacks)
Holder of usage rightsTechnical University Bergakademie Freiberg - Institute of Mechanical Process Engineering and Mineral Processing
Usage rights of the dataCC-BY-4.0
SoftwareResource Production: Xradia XMReconstructor 10.7
Additional precise description of disciplineMechanical Process Engineering - Solid-Liquid-Separation - Cake Filtration
Discipline(s)Engineeringde
Title of the datasetX-ray tomography scans of filter cakes (feed slurry: variation in solid volume fraction)


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  • Publication A: Study on the influence of solids volume fraction on filter cake structures using micro tomography [1]Open Access Icon
    Prediction of micro processes, filter cake build-up and porous media flow is a key challenge to describe macroscopic parameters like filter cake resistance. This is based on a precise description, not only of the disperse solid fraction, but the distributed properties of the voids between the particles. Lab-experiments are carried outwith alumina and limestone,which differ in particle size distribution (PSD) and resulting filter cake structure. Filter cakes of bothmaterials are characterized by standardized lab tests and additionally, alumina cakes aremeasured with X-ray microscopy (XRM). Focusing on distributed process key parameters, the data gives a deeper understanding of the laboratory experiments. The solid volume fraction inside the feed strongly influences the particle sedimentation and leads typically to a top layer formation of fine particles in the final filter cake,which has a negative influence on subsequent process steps. The top layers seal the filter cake for washing liquid and increase the capillary entry pressure for gas differential pressure de-watering. The influence on cake structure can be seen in a change of porosity, particle size and shape distribution over the height of the filter cake. In all measurements, homogenous filter cake structures could only be achieved by increasing the solid volume fraction inside the suspension above a certain percentage, at which particle size related sedimentation effects could be neglected and only zone sedimentation occurred. XRM offers the chance to quantify these effects, which previously could only be described qualitatively.

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