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Year 1999 No 4

Blacha L., Steindor J.
MÖGLICHKEITEN DER BI - ENTFERNUNG AUS FLÜSSIGEM CU DURCH VERDAMPFEN
Keywords:
No 4 (1999), p. 240-250
  mag01.pdf (112 kB)
mag01_eng.txt (429 B)  

Ballóková B., Hvizdoš P., Lofaj F.
MICROSTRUCTURE AND FRACTURE MECHANICAL PROPERTIES
Keywords:
No 4 (1999), p. 251-256
  mag02.pdf (86 kB)
mag02_eng.txt (2 kB)  

Plešingerová B., Kriššaková S., Števulová N., Trpčevská J.
CHARACTERISATION OF MA-SPINEL OBTAINED BY SOLID-STATE SYNTHESIS FROM POWDERY MG AND AL OXIDES AND HYDROXIDES
Keywords: MA-spinel|solid-state synthesis|conversion to spinel|mechanochemical reaction|
No 4 (1999), p. 257-266
  mag03.pdf (223 kB)
mag03_eng.txt (2 kB)  

Raschman P.
UNCERTAINTY OF KINETIC LEACHING DATA INTRODUCED BY APPLIED EXPERIMENTAL PROCEDURE
Abstract
Reliable kinetic data is important for an engineering, as well as for a scientific analysis of the leaching process. The present paper is focused on the methodology of measuring the kinetic data in reacting suspensions - chemical reactions of granular or powdered solids with liquids play a significant role not only in metallurgy and technical chemistry, but also in materials- and environmental engineering.
Since the overall rate of leaching is always a result of interactions between chemical reactions and transport phenomena, accuracy, validity and adequacy of the measured kinetic data are strongly affected by the factors related to the applied experimental procedure. Contacting of the phases in the reaction mixture and the liquid-phase hydrodynamics are determined by the choice of an appropriate reactor - simple, perfectly mixed reactors are therefore recommended. As far as the reaction conditions are considered, variation of the values of rate-controlling parameters (such as mass or heat transfer coefficients, or leaching agent concentration) should be under control - e.g. the values of kinetic parameters can be calculated much more easily when concentration of the leaching agent does not vary significantly during individual leaching tests. Though it is simple to measure time itself, some difficulties may arise when the actual reaction (leaching) time is to be measured - total time which is necessary to withdraw a sample from the reaction suspension and stop the reaction should be much shorter than the characteristic time of chemical reaction (e.g. half-time of reaction), otherwise it can become a source of a significant systematic error. The rates of intrinsic chemical reactions are very sensitive to temperature - temperature difference 1K, caused by the heat of reaction, may result in a relative error about 10%. The latter fact is also valid for the rates of chemical reactions taking place at the liquid-solid interface and isothermal conditions in the whole leaching system are therefore necessary to obtain accurate and valid kinetic data. The results of individual measurements are commonly presented in terms of conversion-time curves - adequate analytical methods should be therefore used to determine the compositions of liquid and solid phases before, during and after leaching.
Using experiments and mathematical modelling simultaneously is recommended. Adequate model equations can be used to analyse the effects of individual factors on the overall rate of leaching and to design leaching experiments - more accurate values of model parameters can be obtained more easily using this method, if compared with a "traditional" approach based on carrying out the measurements and consequent processing of the data collected.

Keywords: leaching|kinetics|experiment|measurement|sources of inaccuracy|
No 4 (1999), p. 267-274
  mag04.pdf (203 kB)
mag04_eng.txt (3 kB)  

Fedoročková A.
EFFECT OF REACTION CONDITIONS ON DISSOLUTION OF MAGNESIUM, IRON AND CALCIUM DURING LEACHING OF BURNED MAGNESITE IN HYDROCHLORIC ACID
Keywords: leaching|burned magnesite|hydrochloric acid|magnesium|calcium|iron|
No 4 (1999), p. 275-279
  mag05.pdf (189 kB)
mag05_eng.txt (1 kB)  

Mihok Ľ., Fedičová D., Weagová Z., Potocký Ľ., Öveçoglü M.L.
INFLUENCE OF GANGUE CONTENT ON PROPERTIES OF BLAST FURNACE PELLETS
Keywords: blast furnace pellets|gangue content|
No 4 (1999), p. 280-287
  mag06.pdf (147 kB)
mag06_eng.txt (448 B)  

Plešingerová B., Macáková J., Klapáč M.
DETERMINATION OF DIMENSIONS OF THE PATTERN FOR THE MANUFACTURING OF PLASTER MOULDS FROM SHRINKAGE OF CERAMIC BODY
Keywords: dimensions of pattern|shrinkage of ceramic body|casting|
No 4 (1999), p. 288-293
  mag07.pdf (194 kB)
mag07_eng.txt (810 B)  

Cehlár M., Kyseľová K.
FEASIBILITY STUDY AND HER CALCULATIVE EXECUTION
Keywords: investment analysis|ash-flow|internal rate of return|net present value|pay back period|
No 4 (1999), p. 294-309
  mag08.pdf (265 kB)
mag08_eng.txt (2 kB)