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Dive into the research topics where K. Hadler is active.

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Featured researches published by K. Hadler.


Langmuir | 2009

Measurements of Interactions between Particles and Charged Microbubbles Using a Combined Micro- and Macroscopic Strategy

Daniel Johnson; Nidal Hilal; Kristian E. Waters; K. Hadler; J.J. Cilliers

We report the use of atomic force microscopy (AFM) to study the interactions between silica glass colloidal probes and charged microbubbles created using one of two different surfactants: anionic sodium dodecyl sulfate (SDS) and cationic dodecyl trimethylammonium bromide (DTAB) in an aqueous environment. On close approach between the glass probe and a SDS microbubble, an appreciable repulsive force was observed prior to contact. This was not observed when using a DTAB microbubble, where only attractive forces were observed prior to contact. zeta-potential analysis showed that silica surfaces are negatively charged across the pH range of 3-10 when surfactant is not present. Addition of SDS did not alter the zeta-potential significantly, indicating that adsorption onto the particle surface did not occur. Conversely, the addition of DTAB decreased the negativity of the zeta-potential, reversing the sign, indicating that adsorption had occurred. This analysis was used in the removal of fine particles from suspension using charged microbubbles. Silica particles were recovered using positively charged microbubbles from DTAB but not when using negatively charged microbubbles generated from SDS. Taken together, the data suggest that repulsive long-range interactions were responsible for the selective attachment of silica particles to microbubbles in a charge-dependent manner.


Advances in Colloid and Interface Science | 2018

Zeta potentials of the rare earth element fluorcarbonate minerals focusing on bastnäsite and parisite

C.L. Owens; G. R. Nash; K. Hadler; R.S. Fitzpatrick; C.G. Anderson; Frances Wall

Rare earth elements (REE) are critical to a wide range of technologies ranging from mobile phones to wind turbines. Processing and extraction of REE minerals from ore bodies is, however, both challenging and relatively poorly understood, as the majority of deposits contain only limited enrichment of REEs. An improved understanding of the surface properties of the minerals is important in informing and optimising their processing, in particular for separation by froth flotation. The measurement of zeta potential can be used to extract information regarding the electrical double layer, and hence surface properties of these minerals. There are over 34 REE fluorcarbonate minerals currently identified, however bastnäsite, synchysite and parisite are of most economic importance. Bastnäsite-(Ce), the most common REE fluorcarbonate, supplies over 50% of the worlds REE. Previous studies of bastnäsite have showed a wide range of surface behaviour, with the iso-electric point (IEP), being measured between pH values of 4.6 and 9.3. In contrast, no values of IEP have been reported for parisite or synchysite. In this work, we review previous studies of the zeta potentials of bastnäsite to investigate the effects of different methodologies and sample preparation. In addition, measurements of zeta potentials of parisite under water, collector and supernatant conditions were conducted, the first to be reported. These results showed an iso-electric point for parisite of 5.6 under water, with a shift to a more negative zeta potential with both collector (hydroxamic and fatty acids) and supernatant conditions. The IEP with collectors and supernatant was <3.5. As zeta potential measurements in the presence of reagents and supernatants are the most rigorous way of determining the efficiency of a flotation reagent, the agreement between parisite zeta potentials obtained here and previous work on bastnäsite suggests that parisite may be processed using similar reagent schemes to bastnäsite. This is important for future processing of REE deposits, comprising of more complex REE mineralogy.


Minerals Engineering | 2005

The froth stability column: linking froth stability and flotation performance

N. Barbian; K. Hadler; Esther Ventura-Medina; J.J. Cilliers


Minerals Engineering | 2009

The relationship between the peak in air recovery and flotation bank performance

K. Hadler; J.J. Cilliers


Minerals Engineering | 2006

The froth stability column : Measuring froth stability at an industrial scale

Nicolas Barbian; K. Hadler; J.J. Cilliers


Minerals Engineering | 2005

The effects of frother and collector distribution on flotation performance

K. Hadler; Zeki Aktas; J.J. Cilliers


Minerals Engineering | 2010

Recovery vs. mass pull: The link to air recovery

K. Hadler; C.D. Smith; J.J. Cilliers


Minerals Engineering | 2012

The effect of froth depth on air recovery and flotation performance

K. Hadler; M. Greyling; N. Plint; J.J. Cilliers


Minerals Engineering | 2010

Flotation bank air addition and distribution for optimal performance

C.D. Smith; K. Hadler; J.J. Cilliers


Chemical Engineering Science | 2013

Determining flotation circuit layout using genetic algorithms with pulp and froth models

W. Hu; K. Hadler; S.J. Neethling; J.J. Cilliers

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B. Shean

Imperial College London

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K.E. Cole

Imperial College London

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A. Morrison

Imperial College London

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