Define the reason for movement
Use product evidence: settling time, temperature drift, solids distribution or batch-quality method.
Product homogeneity
Recirculation or agitation is useful when the product must remain homogeneous, temperature must be controlled, solids settle or a stable feed condition is otherwise lost during the batch. It can be harmful when it entrains air, creates foam, raises temperature, increases shear or sends an uncontrolled return stream into the source vessel.
Direct answer
Agitation acts within a vessel; recirculation moves product through a loop. Either can maintain homogeneity, but they create different shear, heat, air and cleaning duties. The filler should not be used to correct a mixing problem that has not been defined.
State what must remain uniform—concentration, temperature, suspended solids, colour or another property—and how the site currently verifies it. Then decide whether movement is continuous, intermittent, stopped during filling or controlled by level, temperature or batch time.

Approve the machine or process against the actual product, pack, operating range and site interfaces. Record assumptions and what must be confirmed by trial.
Decision table
| Method | Potential benefit | Potential problem |
|---|---|---|
| No active movement | Lowest shear, air and cleaning complexity | Settling, layering or temperature drift may develop during the batch |
| Vessel agitation | Maintains bulk mixing without a long external loop | Vortex, surface aeration, local shear or poor low-level mixing |
| External recirculation | Conditions the transfer path and can support temperature control | Air leaks, foam, pump heat, retained volume and more complex cleaning |
| Intermittent movement | Reduces continuous shear or foam while restoring uniformity | Requires defined timing, low-level behaviour and restart evidence |
Decision sequence
Use product evidence: settling time, temperature drift, solids distribution or batch-quality method.
Record vessel level, flow or agitator speed, temperature, batch time and when movement stops.
Review suction connections, vortex, free-falling returns and the return entry below or above the liquid surface.
Approve pump, hose, seals, valves, return connection, retained volume and drain-down.
Challenge low level, stop and restart, source change, long hold and first packs after circulation resumes.
Avoidable errors
Buyer questions
Yes. Air can enter through a vortex, suction leak or free-falling return, and pump or valve shear can increase aeration. Observe the entire loop at high and low vessel levels and test the product at the temperature and batch age used in production.
The return arrangement should maintain the required mixing without unnecessary air entrainment, splash or static. Its position, direction, submergence and velocity depend on the vessel and product. The design should also be accessible for inspection, cleaning and safe isolation.
Agitation may be better when bulk homogeneity can be maintained inside the vessel without adding an external product path, pump heat or retained volume. Recirculation may be better when the transfer line also needs conditioning or temperature control. Trials should compare product quality and foam, not just motion.
Movement may need to slow or stop if it changes scale readings, nozzle flow, foam or product level at the pickup. Any pause must not allow rapid settling or temperature drift. Define the sequence and prove it at the smallest and largest source levels.
Speak to Lancing
Send settling or homogeneity information, vessel and transfer layout, batch duration, temperature range, source-level range, foam behaviour and the proposed cleaning method.