2020
DOI: 10.1016/j.seppur.2020.117215
|View full text |Cite
|
Sign up to set email alerts
|

Insight into filter cake structures using micro tomography: The dewatering equilibrium

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

0
4
0
2

Year Published

2021
2021
2024
2024

Publication Types

Select...
7

Relationship

0
7

Authors

Journals

citations
Cited by 11 publications
(6 citation statements)
references
References 62 publications
0
4
0
2
Order By: Relevance
“…Die Permeabilita ¨t eines poro ¨sen Systems ist ein wichtiger Strukturparameter [25]. Spezifischer Filterkuchenwiderstand des ebenen Referenzfilterkuchens und Filtermediumwiderstand betragen r c = 6 Á 10 12 m -2 und R m = 2 Á 10 10 m -1 .…”
Section: Globale Strukturparameterunclassified
See 1 more Smart Citation
“…Die Permeabilita ¨t eines poro ¨sen Systems ist ein wichtiger Strukturparameter [25]. Spezifischer Filterkuchenwiderstand des ebenen Referenzfilterkuchens und Filtermediumwiderstand betragen r c = 6 Á 10 12 m -2 und R m = 2 Á 10 10 m -1 .…”
Section: Globale Strukturparameterunclassified
“…Die Anwendung eines berührungslosen Messverfahrens bietet Ansatzpunkte für zukünftige Untersuchungen, wie z. B. eine zerstörungsfreie Strukturmessung mittels Mikro‐Computertomographie 10, 25.…”
Section: Ergebnisseunclassified
“…Data stitching of several individual scans covering certain areas of the filter cakes should be avoided in order to keep scanning time to a minimum, which in effect reduces drying and shrinking of the cake structures [21]. With an appropriate FOV, the individual particles, whose sizes are usually in the µm range, cannot be resolved unless the size of the test apparatus itself is adjusted under certain assumptions [22]. In this case, however, it must be ensured that the experiment can be transferred to a smaller scale without the loss of information.…”
Section: Introductionmentioning
confidence: 99%
“…While the properties required for the filter medium and the operating parameters for the filter apparatus are sufficiently well known, the transition from a laboratory scale to larger industrially relevant scales has not been achieved, even at the present time [5][6][7]. In gas differential pressure deliquoring, the liquid present in the pore system of the filter cake is removed after overcoming the inlet capillary pressure, but for fine-grained cohesive particle systems, emptied pores and cracks in the filter cake occur and lead to an undesired gas throughput [8][9][10]. Figure 1 schematically shows the difference between filter cake deliquoring with gas throughput using fabric as a filter medium (Figure 1a) and filter cake deliquoring without gas throughput using emptied pores and cracks in the filter cake occur and lead to an undesired gas throughput [8][9][10].…”
Section: Introductionmentioning
confidence: 99%