Cavitation of slurry pump and its causes

Cavitation in pumps and its causes. July 22, 2011. Cavitation is a phenomenon that occurs when a liquid, under certain temperature conditions, experiences a drop in pressure below its vapor pressure at that temperature, leading to the formation of vapor bubbles. This process is known as cavitation. When these bubbles move into regions of higher pressure, they collapse rapidly due to the increased surrounding pressure, which can cause significant damage to the pump components. This collapse of vapor bubbles is referred to as cavitation collapse. The main causes of cavitation typically involve a reduction in the absolute pressure of the liquid within the pump, especially in areas such as the inlet of the impeller. When the pressure drops below the vapor pressure of the liquid, vaporization begins, resulting in the formation of numerous bubbles. As these bubbles are carried through the pump and reach high-pressure zones, they suddenly shrink and burst. The rapid collapse of these bubbles creates intense water hammer effects, with impact forces reaching hundreds or even thousands of atmospheres. These impacts occur at very high frequencies—up to tens of thousands per second—and can severely erode metal surfaces, leading to mechanical failure over time. In addition to damaging internal components, cavitation also leads to noise, vibration, and a decline in pump performance. In severe cases, it can cause the pump to lose prime and stop functioning altogether. Understanding and preventing cavitation is crucial for maintaining the efficiency and longevity of pumping systems. What is the characteristic curve of a pump? It is a graphical representation showing the relationship between key performance parameters of a centrifugal pump, such as flow rate (Q), head (H), power (N), and efficiency (η). These curves are derived from actual measurements and provide essential information about how the pump operates under different conditions. The characteristic curves typically include Q-H (flow vs. head), Q-N (flow vs. power), Q-η (flow vs. efficiency), and Q-(NPSH)r (flow vs. net positive suction head required). By referring to these curves, engineers can determine the operating point of the pump, which includes its head, power, efficiency, and NPSH value at a given flow rate. This set of parameters is known as the operating condition or working point. The most efficient operating point is called the best efficiency point (BEP), which is usually close to the design point of the pump. Most centrifugal pumps are rated based on this optimal condition, ensuring both energy efficiency and reliable operation. Understanding these curves is essential for proper pump selection and system design.

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