The 5 MUSTS for Choosing the Best Slurry Pump

The design of a slurry pump is critical to making sure that the abrasive and often corrosive aspects of the slurry does not destroy the impeller. Additionally, slurry and sludge may contain large unforeseen solids that will inevitably clog many types of pumps. Since most centrifugal pumps have an impeller with a close tolerance to the volute, the abrasive and sometimes corrosive nature of the slurry will quickly wear the volute and ruin the tolerance. This, in turn, causes the pump to lose its suction capability. This causes massive downtime with slurry pumps along with costly maintenance and spare parts.

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For this reason, the EDDY Pump is ideal for slurry pumping applications. The EDDY Pump does not have an impeller, but instead a rotor that does not have any critical tolerances. This allows it to pump slurry at rates of 30% and solids up to 12 inches. This is far more than what centrifugal pumps can handle without any failure or need to change wear parts.

Choosing the proper material for a slurry pump is another critical process for determining the correct pump to handle your slurry. If the slurry is highly abrasive with a neutral pH then the best construction material is a Hi-Chrome. This metallurgy has the highest Brinell hardness that can withstand the abrasive nature of the slurry. On the other hand, if the slurry is not only abrasive but also has a low pH, it is best to go with a duplex stainless steel construction. This material is the best for a slurry pump to withstand caustic material such as acid, while still having a high Brinell level.

Adding lime with water, as a slurry, allows the solution to be pumped considerable distances, making transporting the material easier than mechanically loading into trucks. As you can imagine, the lime slurry is not only corrosive but abrasive as well, which can pose challenges for all types of pumps. Due to these challenges, pump manufacturers are constantly coming up with new designs for reducing the detrimental effects that lime slurry can have on their equipment and production rates. Some of these design ideas are featured on multiple types of pumps including slurry pumps, centrifugal pumps, and peristaltic pumps. Typically, the answer to effectively pumping lime is to keep the fluid moving constantly to maintain the chemical in suspension. With lime slurry, it is important to constantly be reaching a critical line velocity in which there is enough flow and turbulence to prevent sediment from building up in dead spots or crevices found throughout the system. It goes without saying that cleaning limescale in pipes can be very labor intensive, expensive, and particularly in metal pipes. Ideally, the pipeline should be as smooth as possible with an open flow path, making sure the flow rate is directly proportional to maintaining momentum. This is why the EDDY Pump's turbulent flow design is perfect for keeping the slurry agitated enough to not accumulate on the sides of the pipelines.

Determining the proper slurry pump size and power requirements for your application is crucial. Based on the abrasive nature of slurries, it is important to choose a pump size that will allow for the pump to run at a slow enough speed in order to lengthen the duration of the slurry pump's life. An ideal RPM to run a slurry pump at is between 900- RPM. Once you begin to exceed this speed, the life of the pump significantly decreases because the wear points in the slurry pump essentially get sandblasted.

As you can see in the 4' EDDY Pump shown above, the tolerance between the rotor and the volute easily allows the passage of a man's arm, while the tolerance in a centrifugal pump is significantly less.

This means you can pump MORE solids with LESS clogging.

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As a minimum, it is normally required to have both the flow and head of the duty. This will allow for a very basic selection using the available pump curves. It is worth keeping in mind that published curves from manufacturers are based on clean water. This is due to the many various slurries that are available, which would require manufacturers to supply thousands of curves and would not be feasible. This is where manufacturer pump sizing tools come in handy, such as the Metso Outotec PumpDim' tool, which takes the supplied slurry data and system information to provide an adjusted 'slurry curve'. This results in the tool providing an optimal pump recommendation for the operation.

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However, no matter how good a calculation tool is, the result is dependent on the data that is provided. The saying, 'Rubbish in means rubbish out,' is very relevant here. Depending on the abrasiveness of the application, pumps have a sweet spot in which they like to work.

This is called the preferred operating range, which is a percentage of the best efficiency point (BEP). The more abrasive the application, the smaller this sweet spot becomes. To simplify things, these ranges are organized into service classes as determined by the Hydraulics Institute and uses the average particle size (d50) and the slurry specific gravity. Starting at Service Class 1, which is essentially a water duty, and making its way up to the very highly abrasive Service Class 4, which would be like a Mill Discharge application. Using these service classes, we can determine the correct pump to be used along with ensuring the speed of the pump is also correct.

The duty/service class is also used to provide recommended limits for other calculations such as stage pumping and impeller tip speeds.

The importance of data

The importance of data can easily be overlooked especially with a pump that is already installed and has been running on its calculated duty point for some time. As sites develop, it is normal for duty points to change as manufacturing fluctuates to the market demand. An increase in flow may not be considered a major factor on some equipment, but when it comes to a pump it can push its operation from the most efficient point toward a critical range. There are other factors that can have detrimental impacts such as changes in the feed material and installation alterations to pipework like lengths, dimensions, and others. This can result in an increase in friction losses in the system.

The reason pumps like to work at its most efficient point is because this reduces the amount of wear seen, ultimately extending the service life. It is well known in the industry that slurry pumps will not be able to run forever due to the nature of its work. But every mine aims to extend this life as much as possible, which happens by being as close to BEP as possible.

Small adjustments in flow or head can move the duty point on the curve considerably has and have implications on wear life. Moving further to the left of BEP, usually due to a reduction of flow or head, creating recirculation in the pump meaning the material travels around the casing excessively before it is moved down the line. This creates additional wear due to the extra circulation of particles.

Alternatively, the duty point can be pushed to the right of BEP by increasing the flow. This can cause issues with inlet velocity meaning the flow into the pump is greater than the installed size that the pump can manage. And resulting in increased wear rate around the discharge area of the casing and on the eye of the impeller, which is the first obstruction the flow finds when entering the pump.

In some of these cases a pump can be adjusted on speed to help deal with the changes of duty, but in other cases it would be recommended to change the pump size to best fit the altered application. Without taking these changes into consideration, a previously well performing pump can turn into a maintenance headache.

Another factor to keep in mind is that as a pump wears and moves away from its optimum point it has a reflective effect on the power consumption. An increase in power consumption turns into an increase in costs and carbon footprint.

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