University of Missouri--Rolla
Modelling of fluid flow and kinetics in counter-current reactors for pyrometallurgical refining
Abstract
dc:description.abstract<p>“Results of physical modelling and kinetic (mass transfer) simulation of a counter-current reaction launder (CCRL) for metals refining are presented. Physical modelling was conducted in a 200 cm long (L) by 20 cm wide (W) channel, using tetrachlorethylene to model 'metal' and water to model 'slag'. A thermal tracer technique was used to measure the eddy thermal diffusivity ( α<sub>e</sub>) and the interphase heat transfer coefficient (h<sub>ov</sub>). The heat and mass transfer analogy was then applied to determine the extent of longitudinal mixing (D<sub>e</sub>/uL) and to estimate the rate of interphase mass transport (k<sub>ov</sub>). Liquid 'metal' height (H<sub>1</sub>) was kept constant at 20 cm, while the liquid 'slag' height (H<sub>u</sub>) was varied between 5 and 18 cm. Nitrogen was bottom injected at a rate per unit area of 7.5 cm/min, through up to 16 central bubblers placed along the length of the CCRL. Low extents of longitudinal mixing in the 'metal' of D<sub>e</sub>/uL less than 0.1 were measured. Interphase mass transfer coefficients of the order of 0.004 cm/s were estimated from the measured interphase heat transfer coefficient (h<sub>ov</sub> = 1.3 to 2.0 kW/mK). Interphase heat transport was found to be a strong function of the gas stirring energy input (∈), according to h<sub>ov</sub> ∞∈ <sup>0.63</sup>, provided H<sub>1</sub>/W and H<sub>1</sub>/H<sub>u</sub> met, or exceeded unity.</p> <p>Kinetic simulation was applied to prediction of the performance of a novel CCRL process for production of low carbon ferromanganese (LC FeMn). A dimensionless (N<sub>CCRL</sub>)<sub>s</sub> = (kAp/m)<sub>s</sub> of 1.8 in the slag was predicted to yield highly refined LC FeMn (0.70 % Si), at a 97 % silicon utilization efficiency, and with a 89 % recovery of manganese to the alloy. A transitory reaction, tanks-in-series kinetic model was used to investigate nitrogen absorption and desorption. Substitution of argon for nitrogen was predicted to reduce the liquid LC FeMn nitrogen content from 0.98 to 0.025 % N, but at an estimated additional operating cost of about $10 /t LC FeMn”--Abstract, page iv.</p>
Degree
thesis:*- Name thesis:degree_name
- Ph. D. in Metallurgical Engineering
- Grantor
- University of Missouri--Rolla
- Year dc:date.available
- 2016
Author and committee
dc:creator, dc:contributor.*- Author dc:creator
-
- Nelson, Lloyd R.
Subjects
dc:subject × 1Identifiers
dc:identifier.*- Repository record dc:identifier
- https://scholarsmine.mst.edu/doctoral_dissertations/1078
- OAI identifier oai:identifier
- oai:scholarsmine.mst.edu:doctoral_dissertations-2080