Consider temperature, volume and liquid feed control
by Mike Cothern & Daniel Hagnbuchner
January 4, 2018

A spray dryer is a device in which a specific solution or suspension of solids and liquids is fed through spray nozzles into a drying chamber. There, it is mixed with heated air or gas to accomplish evaporation of the carrier liquid so the solids of a particular size and shape remain as the finished product.

typical progressing cavity spray dryer feed pumpFigure 1. Typical progressing cavity pump. (Images and graphics courtesy of FELUWA Pumps)

To obtain the required particle size, shape and dryness of the finished solid product, several factors must be closely controlled. While the temperature and volume of air play important roles in the drying process, they are fairly easy to control. The liquid feed step in this process, however, can be a bit more difficult.

worn rotorFigure 2. Worn rotor

Proper atomization of the solution or suspension is just as vital to the success of the operation and presents many more challenges when dealing with solids containing slurries. Of utmost importance is the selection of the proper spray dryer feed pump. The feed pump type and construction depend on the following variables:

  • capacity
  • pressure
  • viscosity
  • slurry shear sensitivity
  • solids characteristics
    • abrasiveness
    • sticky/agglomerating
    • attrition sensitivity
  • liquid characteristics
    • corrosiveness
    • temperature
    • net positive suction head (NPSH)

The more challenging spray dryer feed pump applications involve a slurry/suspension feed that contains abrasive or agglomerating solids at pressures over 200 pounds per square inch gauge (psig). These applications have presented operational and reliability issues for many pump types that have been used historically.

Because this application requires a metering capability at relatively low flow rates (0.25 gallons per minute [gpm] to 200 gpm) against relatively high discharge pressures (200 psi to 2,500 psi), positive displacement pumps are typically required. Many types of positive displacement pumps have been used or trialed on this application with varying levels of success. This article will discuss the three most common types: progressing cavity pumps, flat diaphragm pumps and hose diaphragm pumps.

Typical flat diaphragm pumpsFigure 3. Typical flat diaphragm pumps.

Progressing Cavity Pumps

Progressing cavity pumps (PCPs), also known as progressive cavity pumps, consist of a single helical metal rotor rotating inside a double helical elastomeric stator, which inherently forms cavities in the portions of the double helix that are not occupied by the rotor. As the rotor turns, the cavity progresses through the stator. The steel rotor seals against the elastomeric stator resulting in a pumping action that is similar to a piston pump, which is always in its forward stroke. This type of pump offers the perceived benefit of no pulsations, no check valves, relatively small installation footprint and low initial cost.

However, in abrasive duties such as spray dryer feeding, there can be a high rate of wear­—first in the elastomeric stator and then in the steel rotor. As the elastomeric stator begins to wear, the seal between rotor and stator is compromised, which results in slip of high pressure slurry back to the lower pressure suction. This slip accelerates the wear and pump performance diminishes until the parts are replaced.

Because this is a rotary motion pump, shaft seals or packing are required to keep the process fluid from leaking out of the rotating input shaft. Additionally, universal joints are required to connect the concentric input shaft to the eccentric motion helical rotor. Since these universal joints operate within the solids-laden process fluid, they can also be problematic. The maintenance costs of PCPs can eclipse the low initial costs very quickly.

Typical check valve componentFigure 4. Typical check valve component.

Flat Diaphragm Pumps

Flat diaphragm pumps use an elastomeric diaphragm typically actuated by a propellant fluid, which is actuated by a piston. Slurry is segregated from the hydraulic fluid via the diaphragm and directed in and out of the pump by means of metal check valves. This style of pump is considered a sealless design. Pulsations generated by this reciprocating pump are controlled to a process acceptable level via a downstream pulsation dampener.

Ruptured/torn diaphragmFigure 5. Ruptured/torn diaphragm

In some less expensive versions of this design, a hydraulic design similar to that of a lifter in an engine is used to propel hydraulic fluid to actuate the flat elastomeric diaphragm. Typically, these lower cost designs use small, stamped steel check valves and operate at relatively high speeds (100–200 strokes per minute). This kind of pump offers the perceived benefit of a small installation footprint and low initial capital investment.

However, experience has shown that these pumps can suffer from low mean time between repairs in abrasive applications such as spray dryer feed. Flat diaphragms have a tendency to fail at their clamping location (perimeter) due to work hardening of the elastomers and build-up of solids at the clamping location.