Efficiency of aluminium refining on a foundry degassing unit depending on the rotor geometry and the degree of its wear

. 2025 Jul 22 ; 15 (1) : 26628. [epub] 20250722

Status PubMed-not-MEDLINE Jazyk angličtina Země Anglie, Velká Británie Médium electronic

Typ dokumentu časopisecké články

Perzistentní odkaz   https://www.medvik.cz/link/pmid40696101

Grantová podpora
TH04010449 Technology Agency of the Czech Republic
07SVV2325 Ministry of Education, Youth and Sports
11/020/RGJ24/0128 Silesian University of Technology
11/020/BK_25/0143 Silesian University of Technology
11/020/BK_25/0143 Silesian University of Technology

Odkazy

PubMed 40696101
PubMed Central PMC12283922
DOI 10.1038/s41598-025-12447-z
PII: 10.1038/s41598-025-12447-z
Knihovny.cz E-zdroje

The article studies the issues involved in refining aluminium alloys when introducing small gas bubbles. A good level of dispersion throughout the entire volume of the degassing unit is achieved by using appropriate rotor geometry and selecting optimal process parameters. This study uses physical modelling employing a water model of a foundry degassing unit. Three pump-type rotors of different designs were tested. Variants A and C with a circular cross-section and cylindrical shape differ in the design and arrangement of the gas flow control blades, while variant B with the shape of a truncated cone is a kind of monolith with control blades placed in the lower part of the rotor. These rotors with were studied, with gas flows ranging from 13 to 21 l/min and rotor speeds ranging from 275 to 425 rpm. Tests included visualisation of the gas injection process and measurement of oxygen removal from water as an analogy of hydrogen removal from liquid metal. Then a mathematical model for the quantitative interpretation of research results was developed, in which the dimensionless parameter of degassing efficiency a was determined, which allows for a simple comparison of its value for all rotors, both new and used. The highest values of parameter a are observed for rotor C, only slightly worse values occur for rotor A, and the most significant differences are visible for rotor B. The research results were validated under industrial conditions - the Dichte Index was calculated for all rotors for selected process parameters and illustrated with porosity samples.

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