Centrifugal pumps are one of the world’s most commonly used machines. Every day, test labs evaluate their performance. Most of these pumps have been designed to transport fluids or create pressure in an industrial process. Therefore, the most important measurements include pump pressure (head), flow and power, and maintenance and environmental factors—such as vibration, sound levels and operating temperature.
What should the test engineer consider when the main purpose of a pump is not the movement of fluids—but the transport of rocks, sand, gravel and mud? A centrifugal pump is usually not considered for such purposes, but that is exactly what slurry pumps do in the mining and dredging industries.
Although water (or some other fluid) is always present with the solids in slurry pump operations, it is usually only a carrier. While it may be recycled, the power expended to move and pressurize it is lost energy. In some cases, the presence of water adds disadvantages to the process—such as in dredging operations focused on land building for ports and harbors, or in mining operations in which large amounts of rock remaining after the ore has been removed must be returned to the landscape in an environmentally responsible and geologically stable manner.
Reducing water use to the bare minimum can be important in these cases to ensure stability and to conserve scarce water resources. A large portion of the water that transports these solids remains in the ground and must be replaced—even a bucket of wet dirt is 35 percent water.
Pump wear and tear is another consideration. While transportation at high solids concentration is the most efficient strategy for conservation of electrical power and water resources, these dense slurry mixtures (sometimes more than 40 percent solids by volume) take a tremendous toll on the wetted parts of the slurry pump. An impeller or casing liner often becomes completely worn, losing as much as half its original weight within a few months. Considering that a typical slurry pump is moving between 500 to 5,000 cubic meters per hour (m3/hr) of high-density slurry, with some large operations in the range of 10,000 to 20,000 m3/hr (44,000 to 88,000 gallons per minute—gpm), the size and expense of replacement parts becomes a factor. In fact, it can approach 40 percent of the total cost of ownership, including power costs. Downtime must also be considered because a large mine can lose as much as $100,000 USD per hour in revenue when a critical slurry pump unexpectedly goes offline.
While a slurry pump hydraulic lab carries out conventional pump performance tests on clear water (useful as a design baseline), the slurry testing provides the most interesting results. Given the range of effects and considerations, the tests themselves vary widely. This article discusses two examples to help illustrate this.
In some applications, such as dredging a new channel or in the “hydrotransport” of phosphate matrix and oil sands, the largest solids can exceed 100 millimeters (mm), or 4 inches, in diameter. At this size, impact wear at the impeller inlet and casing cutwater will often limit service life. While several tests exist for quantifying slurry wear resistance, they invariably use sand-sized particles, so little is known about the impact resistance of typical slurry pump materials under more extreme loads. Because many such materials are relatively hard and brittle, this issue cannot be overlooked. Key questions include:
- Do the relative rankings of materials change as the impact becomes more severe?
- Is there a limit of strength or toughness that must be maintained?
- Does the third power relationship between impact velocity and wear still hold true?
To answer these questions, the hydraulic lab constructed a “wear test” rig consisting of a 28-inch (710 mm) suction pump operating in a 20-inch (508 mm) pipeline at velocities of up to 33 feet per second (ft/s), or 10 meters per second (m/s). The test solids consisted of granite “rip-rap,”passed through a screen to obtain a top size of 6 inches (150 mm) and average diameter of 3 inches (75 mm). The wear samples consisted of 2-inch (50 mm) bars placed vertically into the pipeline against the full impact force of the solids as they moved along the bottom of the pipe. Different materials were tested—including several grades of white iron, tungsten carbide and welded coatings. An alloy steel bar was also included as a control sample. Tests were performed at different velocities and in each case, fresh rock was added to the system every 15 minutes over the course of four hours, eventually reaching a concentration of approximately 6 percent by volume. Attrition of the solids was severe, with few particles remaining larger than 3 inches.