The FOAMCARP process: foaming of aluminium MMCs by the chalk-aluminium reaction in precursors

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Abstract

A brief outline is presented of the factors involved in the search for gas-generating agents offering superior performance for foaming of liquid aluminium alloys. These include kinetic and thermodynamic characteristics of decomposition reactions, the ease of dispersion of the powdered foaming agent in the melt, the nature and likely effect of decomposition products on melt flow, potential reactions between the foaming gas and the melt and the availability, cost and ease of handling of the powder concerned. There is one very promising candidate material, calcium carbonate, which offers advantages compared to currently-employed hydride powders in virtually all aspects of their performance. It is shown that foams can be produced having appreciably finer cells (<1 mm diameter) and more uniform cell structures than currently-available melt route foams, a potentially lower ceramic content in the cell walls and dramatically reduced raw material costs. The presence of an oxidising foaming gas in the cells leads to reaction with the liquid cell surface, forming a continuous oxide film. The presence of this film has a significant effect on foam stabilisation, slowing down cell coalescence and melt drainage.

Introduction

Interest in closed cell aluminium foams for structural and energy absorption applications is currently high [1], [2]. There is a strong incentive to develop economically attractive processing routes [3] for such foams, creating material having a fine, uniform cell structure (preferably without coarse, embrittling constituents [4]). Routes based on the handling of a melt [5], [6] are potentially cheaper and more tolerant of impurities than those based on a powder compact [7], [8]. They can also be used as a ‘recycling’ procedure for certain type of scrap metal matrix composites (MMCs) by converting them into MMC-based foams [9]. By far the most commonly employed foaming agent for aluminium alloys is titanium hydride (TiH2), owing mainly to its high specific hydrogen content, a reasonably good correspondence between its decomposition temperature and typical alloy melting temperatures and the rapid kinetics of the decomposition reaction.

The recently-developed FORMGRIP process [10], in which a protective oxide coating is created on the surface of TiH2 powder particles, eliminates the problem of premature gas release during the hydride dispersion in the melt, facilitating production of a foamable precursor via a melt route. This is subsequently baked in order to produce the foam component. However, while this procedure works well, there is a need for a gas-generating agent with superior cell face stabilisation characteristics. There is also a strong commercial incentive to find an agent which is cheaper and easier to handle than hydrides such as TiH2. A highly promising alternative foaming agent suitable for the melt-route production, calcium carbonate (CaCO3), was reported in a preliminary study by the present authors [11]. A coating procedure facilitating easy dispersion of CaCO3 in aluminium melts has been proposed [12] by researchers in Japan. Although this compound was listed as one of the potentially suitable foaming agents in several early patents [13], [14], its suitability for production of Al-based foams via a melt-route has not yet been systematically assessed. In the current paper, the performance of calcium carbonate as a foaming agent is studied in detail and the associated Al-melt foaming behaviour is discussed.

Section snippets

Materials and foam production

A DURALCAN type metal matrix composite was used in the preparation of all the foams. The metal matrix (Al–9wt.%Si–0.5wt.%Mg, with a max. of 0.2 wt.% of Cu, Mg and Ti) contains 10 vol.% of SiC particulate, with a mean particle size of about 13 μm. Two types of calcium carbonate materials were employed as gas-generating agents: 99.5% pure powder synthesised by precipitation (Alfa Aesar, Johnson Matthey, GmbH, Karlsruhe, Germany) and 99.3% pure limestone granules (Omya UK, Ltd, Dorking, Surrey).

Gas-evolution kinetics and reaction thermodynamics

TGA curves for the calcium carbonate powders are plotted in Fig. 3. The behaviour of as-received and pre-oxidised TiH2 powder is also included, for comparison purposes. It has been previously established [10] that use of the TiH2 foaming agent requires a thermal oxidation pre-treatment to prevent premature gas-release during preparation of foamable precursors via a melt route. The results of the analysis show that the onset temperature of CO2 evolution from both calcium carbonate powders is

Conclusions

The following conclusions can be drawn from this work.

  • (i)

    The decomposition characteristics of CaCO3 are such that it is well-suited to foaming of aluminium melts. It has been shown that foams with high porosity levels and fine cell sizes can readily be produced.

  • (ii)

    TGA studies of the CaCO3 powders indicate that they undergo thermal decomposition above about 650 °C and this becomes rapid at about 750 °C. This is consistent with the observed effect of higher foaming temperatures leading to somewhat

Acknowledgements

Financial support for the work described here has been provided by EPSRC, QinetiQ Ltd, and Cymat Corporation. Useful discussions have been held with several people including Steve Flitcroft and Brian Borradaile (QinetiQ), Scott Nichol (Cymat) and Richard Jones (DSTL). The XPS work was carried out at the Surface Analysis Laboratory, University of Surrey, and the assistance of John Watts and Steve Greaves is gratefully acknowledged.

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    2022, Materials Science and Engineering: B
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    Foaming Mg alloys (Mg-Al-Zn-Ca or Mg-Ca) by directly adding blowing agents such as CaCO3, TiH2 and MgCO3 in liquid metal was reported [5–8,19–21]. Magnesium alloy foaming follows similar steps of aluminium foaming processes such as ALPORAS® (thickening the liquid metal using Ca) and FOAMCARP (using SiC particles for stabilization) or ALCOA process (using CaCO3 as blowing agent) [22–24]. However, the structure obtained till now have fine rounded and interconnected pores with poor distribution and solidification defects and therefore their structure is inferior to Al foams.

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