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KEMPROCAST MOULD POWDERS
  • LING: Lubricating powders for slabs, billets, rounds, thin slab

Introduction
Chemical composition of mould powders
Functions of mould powders
Physical properties of fluxes
        Melting rate
        Viscosity
        Break Solidification and Melting Temperatures
Mould powders characteristics
How to read a mould powder technical data sheet

Introduction

The primary functions of the mould flux are:

  1. to form a liquid slag pool which protects the surface of the steel from oxidation
  2. to provide thermal insulation which prevents the surface of the steel from freezing
  3. to lubricate the newly-formed shell
  4. to control the horizontal heat transfer between shell and mould
  5. to absorb inclusions from the steel

The most important of the five functions of the mould flux are providing lubrication and the right level of heat transfer. However the continuous casting process is a very complicated process and “everything counts”.
The casting powder must be ‘tailored’ to perform satisfactorily for the casting conditions.
The casting powder cannot act on its own and satisfactory operation requires that other casting variables should be carefully adjusted, for example:

  • good steelmaking practice (minimise Al2O3 formation, inclusion engineering)
  • good mould level control
  • careful design and positioning of the SEN to ensure good temperature and steel flow pattern at meniscus
  • mould oscillation characteristics.

Modern synthetic powders usually contain:

  1. raw materials with similar melting points (eg lithium feldspar, sodium feldspar, wollastonite) to provide more uniform melting
  2. a minimum number of raw materials to achieve the desired composition so as to keep the recipe simple and simplify quality assurance.

Spray dried powders were introduced to provide better quality control and minimise health hazard.
Pulverised powders do have the following disadvantages:

  • fine dusts present health problems to plant operations
  • some inhomogeneity of supplies can arise because fine particles tend to gravitate towards the bottom of bag.

For the production of Spray dried spherical powders, the various powdered raw materials are weighed and mixed with water for > 5 hours to form a ‘slurry’ or suspension. It is then sieved and pumped into a stirrer (to prevent segregation) and is then fed to an atomiser in a spray tower. Fine spherical droplets are formed. Hot air is introduced and the evaporation of water in droplets is very rapid since the drops have a high ratio surface area/ volume.
The result is dry spherical hollow particles, which are then sieved, cooled, sieved and packaged.

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Chemical composition of mould powders

Continuous casting powders are made up of several components as shown in the following:

Glass formers SiO2 17 - 56% Basic Oxides CaO 22 - 45%
Al2O3 0 - 13% MgO 0 - 10%
B2O3 0 - 19% BaO 0 - 10%
Fe2O3 0 - 6% SrO 0 - 5%
Alkali Na2O 0 - 25% Fluidiser F 2 - 15%
Li2O 0 - 5% MnO 0 - 5%
K2O 0 - 2% Melting rate control C 2 - 20%

The effects of these various components on the viscosity, melting point and solidification temperature are summarised in the following table

Increase Viscosity Solidification Point Melting Point
CaO Decrease Increase Increase
SiO2 Increase Decrease Decrease
CaO / SiO2 Decrease Increase Increase
Al2O3 Increase Decrease Increase
Na2O Decrease Decrease Decrease
F Decrease Increase Decrease
Fe2O3 Decrease Decrease Decrease
MnO Decrease Decrease Decrease
MgO Decrease Decrease Decrease
B2O3 Decrease Decrease Decrease
BaO Decrease Decrease Decrease
Li2O Decrease Decrease Decrease
TiO2 No Change Increase Increase
K2O Decrease Decrease Decrease

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Functions of mould powders

Powders are added continuously to the mould and form 4 layers over the steel surface:

  1. raw powder layer
  2. sintered layer
  3. mushy layer (mixture of slag globules and carbon particles)
  4. a pool of liquid slag

Chemical protection
The presence of a liquid slag pool above the meniscus and carbon particles in the sintered and powder layers prevent oxidation of the steel surface

Thermal insulation
The principal factors affecting thermal insulation is the bulk density.

Lubrication of the steel
Liquid slag infiltrates into the gap between the solid slag film formed against the water-cooled mould and provides lubrication for the solidified steel shell. It is desirable that this layer of slag should remain molten through the whole length of the mould.

Uniform heat transfer between steel and mould
Longitudinal cracking is known to be related to both the excessive magnitude and variability of the heat flux. The heat flux is controlled by the slag film formed between the steel and mould.
The principal factors affecting the heat transfer between steel and mould are

  • thickness of the slag layer, this increases with increasing solidification or break temperature and viscosity of the flux
  • the crystallisation tendency of the slag film that acts as a good shield to the radiant heat
  • interfacial resistance caused by the air gap formed resulting from the steel shrinkage.

Absorption of inclusions
The principal non-metallic inclusions formed in the continuous casting process are Al2O3 and TiO2, in Ti-containing grades. Alumina is formed principally by oxidation of the steel particularly in Al-killed grades; consequently the powder has to maintain its properties after alumina absorption.

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Physical properties of fluxes

The physical properties of the casting flux are important to the success of the casting process


Melting rate
Carbon, in the form of either carbon black, graphite or coke dust is added to the mould powder to control its melting rate and to provide insulation to both the steel and the liquid slag.
Carbon particles are non-wetting to molten slag and thus separate the mineral particles and slow down the agglomeration of molten slag globules. Thus the more C, the more time required to agglomerate, the slower the melting rate.
The powder bed above the steel meniscus consists of four layers, powder, sinter, mushy (mixture of slag globules and carbon particles) and molten slag pool.
The melting rate is controlled by several factors

  1. the vertical heat flux density which is affected by various casting parameters such as casting speed, superheat, turbulence, etc.
  2. the free carbon content of the powder
  3. the type of carbon and particle size of carbon
  4. the carbonate content of the mould flux (as the CO2 developed from carbonates decomposition causes turbulence in the mould powder layers so favouring its melting)
  5. the presence of exothermic agents which can raise the melting rate.

Viscosity

The viscosity of the casting powder is a key physical property since it influences:

  • the lubrication of the steel shell
  • slag entrapment (lower with higher viscosity)
  • depth of oscillation marks (lower with higher viscosity)
  • SEN erosion (higher with lower viscosity)

Several investigators have determined the effects of different additions on the viscosities of mould powders:

  • Al2O3 additions cause increase in viscosity since they favour in a prone polymerised slag
  • Li2O, Na2O and CaF2 cause a decrease in viscosity since they result in a more depolymerised melt
  • Additions of TiO2 result in a slight decreases in viscosity up to the solubility limit of about 10% beyond which the viscosity increases because of the solids present.
    Addition of ZrO2 probably have a similar effect.

Measurements of viscosity as a function of temperature are made only when a new powder is designed. Usually values of viscosity are calculated by means of mathematical models.


Break (Tbr) Solidification (Tsol) and Melting (Tmelt) Temperatures

  • The break temperature is the temperature below which there is a marked change in viscosity and represents the point where liquid lubrication starts to break down.
    Break temperatures are obtained from viscosity measurements during the cooling cycle. Break temperatures are dependent upon the cooling rate and are usually quoted for a cooling rate of 10°C/min but cooling rate in the mould could be > 50 times that. Consequently, Tbr values in the mould could be substantially lower than those quoted for 10°C/min.
    It should be noted that high-viscosity fluxes such as those used in the billet-casting have no break temperature since they form super-cooled liquids.
  • The solidification temperature is the temperature where the flux starts solidifying (formation of crystalline phase) and is sometimes called Crystallisation temperature. It is usually measured during cooling cycle in Differential Thermal Analysis (DTA) or Differential Scanning Calorimetry (DSC) measurements.
  • The melting temperature is the temperature where flux becomes totally fluid and is usually measured on the heating cycle in DTA/DSC experiments.

Differential Thermal Analysis are made only when a new powder is designed. Usually, the characteristic temperatures (softening, melting and fluidity) are determined by means of Heating Microscope.

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Mould powders characteristics

As the mould powders performance influences both continuous casting operations and slabs surface quality, mould powders need to have the following fundamental characteristics:

  • melting temperature suitable to guarantee, at a fixed casting temperature, a sufficient slag fluidity for the infiltration into the gap between steel and mould. The casting powders are essentially mixtures of oxides, present as different mineralogical phases, which do not melt simultaneously; for this reason the heating of these powders give rise to a temperature melting range instead of a melting temperature
  • a viscosity suitable for both the infiltration into a very narrow gap and minimisation of the friction between steel and mould
  • a melting rate suitable to guarantee a proper molten slag reserve
  • convenient values of the break and solidification temperatures that are very important for their influence on the slag lubricating ability and heat flux regulation.
    When a slag changes from the molten phase to doughy and then glassy phase, it maintains a certain lubricating ability due to the fact that a glass is an undercooled liquid. When a slag changes from the molten phase to a crystalline one, its lubricating ability is completely lost

Concernings the heat flux regulation it has to be remembered that a glassy slag layer between steel and mould does not shield the radiant heat and it is suitable to cast steels not subjected to longitudinal cracks. A slag with high tendency to the crystallisation forms a good shield to the radiant heat and it is recommended for casting of steels generally subjected to longitudinal cracks.

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How to read a mould powder technical data sheet

Chemical Analysis

  • The basicity index (IB = CaO/SiO2) gives an idea of the slag tendency to crystallisation:
    - IB > 1.0 generally means that the powder has a certain tendency to crystallisation and so it is best suited to cast steels subjected to longitudinal cracks;
    - IB < 1.0 generally means that the powder is prone to form a glassy film between mould and steel, so the powder has good lubricant ability but does not shield the radiant heat.
  • The Free Carbon content indicates the melting rate of the powder: low free C corresponds to high melting rate and consequently high molten pool depth (keeping constant operative parameters and powder viscosity).

Physical Analysis

  • The characteristic temperatures (softening, melting and fluidity), determined by means of Heating Microscope are important, especially the fluidity temperature which determines the thickness of the slag rim. When this temperature is too high it can cause a big slag rim that can inhibit the slag inflow into the channel between mould and steel.
  • Viscosity calculated as a function of temperature. Generally, the viscosity has to be lower for higher casting speed to guarantee a good lubrication.


Free Carbon content and viscosity are the most important parameters in determining the molten slag pool depth.
Free Carbon content controls how much liquid slag is produced; viscosity controls how much liquid slag infiltrates; in practice that means that if you need to reduce the viscosity the free Carbon content has to be reduced too, in order to keep constant the liquid slag pool depth.


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