Home > Outotec discuss the structural difference between open and closed thickener feedwells

Outotec discuss the structural difference between open and closed thickener feedwells

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article image A feedwell in a high rate thickener

According to Ian Arbuthnot, Director-Special Projects, Outotec , one need not think that only by the next generation technology the processing of orebodies can be optimised. Arbuthnot outlines the importance of open feedwells and closed feedwells and also how closed feedwells can be a better choice in the thickening process.

In thickening, for example, open versus closed feedwells is still a debating point. The closed feedwells have been adopted on a wide range of mineral processing duties and have proven effective in giving better performance and lower reagent costs. To have a clear understanding, Ian Arbuthnot discuss about the structural difference between open and closed feedwells based on the design basics.

When the world’s first SUPAFLO high-rate thickener was built in 1986, the closed bottom feedwell design redefined thickening and clarifying methods. The feedwell design in high rate thickeners formed a distinctly separate chamber from the surrounding thickener volume, and the material within the feedwell does not have a direct exit path, but passed out through the annular gap defined by the feedwell outlet flange and the deflector plate.

The traditional ‘open’ feedwell is a cylindrical well, with the bottom outlet to the thickener volume being of the same diameter as the rest of the feedwell. There is a significant difference between the performance of the two feedwell types. The open type of feedwell was suitable for conventional thickeners, and without the use of flocculants, a more sophisticated feedwell design was required.

A thickener feedwell has six basic functions to fulfil - dissipate the energy of the incoming feed, introduce dilution water to achieve the optimal density in the feedwell for flocculation of the solids, deaerate the incoming feed, mix the flocculant into the incoming feed, retain feed in the feedwell whilst dilution and flocculation occur, and distribute the flocculated material evenly over the thickener diameter.

Optimising these tasks in a single chamber is at times difficult. Energy dissipation creates high shear zones in the feedwell, which can result in aggregate breakage. However, energy dissipation within the feedwell also provides the driving force required to provide sufficient mixing of the feed and dilution water streams and to prevent feed short-circuiting. Optimising these factors is critical to feedwell performance.

In an open feedwell, energy dissipation is minimal. Dilution occurs, but is largely an uncontrolled upflow of dilution liquid through the bottom of the feedwell, which results in accelerated bypassing of the higher density feed. Deaeration is minimal. The most serious drawbacks of the open configuration, however, are the lack of mixing and inability to retain solids for the important dilution and flocculation steps.

It is generally understood that 30 to 45 seconds is the optimum time for dilution, mixing and flocculation of thickener feed. The closed feedwell provides the necessary volume for this to occur, as opposed to dropping the feed straight through, as in the open feedwell. Efficient mixing allows smaller and larger particles to agglomerate, prevent short circuiting and ensuring less fines are left unflocculated. It also ensures lower operational costs, as fewer reagents is required when the feed is properly mixed.

As explained above, demand for closed feedwells has been driven by the desire for higher performance and the need to exploit larger, difficult-to-process orebodies. However, conventional or open feedwells do still have limited use in the industry. Conventional thickeners are useful where no or low reagent is required. With a fast-settling, uncomplicated orebody, such as some iron ores for example, the heavier particles can pass straight through the open feedwell and settle at the bottom of the thickener with relatively less mixing and reagent required.

As the feedwell gets bigger for larger tonnage applications both types of feedwell need to increase in diameter, with less increase in depth. This creates a “flat” aspect ratio for large feedwells, which inherently creates difficulties in the distribution and mixing of feed with dilution liquor and flocculant. The introduction of annular shelves and other types of baffle have been used to improve distribution in large feedwells.

Outotec has carried out extensive CFD studies on large feedwells, mostly in collaboration with CSIRO, utilising their knowledge gained from the AMIRA P266 “Improving Thickener Technology” programme. The resulting designs retain Outotec’s basic “closed” SUPAFLO configuration, enhanced by the addition of a suitably designed shelf, a set of angled vanes, and tangential addition of the dilution flow.

This arrangement has been installed and tested in two operating thickeners, and found to be a significant improvement on the original feedwells. Essentially, the additional shelf and vanes are used to allow the feedwell to be divided into two compartments, the upper section being for mixing and dilution, and the lower section for energy dissipation, prior to the flocculated material being distributed evenly into the thickeners through the annular deflector cone gap.

The myth of aggregate breakage on exit from a closed bottom feedwell has also been dismissed by the CSIRO studies. It should be understood that the open feedwell arrangement does not readily lend itself to such design innovations. Though open feedwells do have their uses in limited applications, in the context of today’s requirement for high performance in minerals processing, open cylindrical feedwells are fundamentally outdated, a “dinosaur” of a previous age.

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