Bubbles and loss of prime
Leaking suction joints, low vessel level or aggressive transfer can introduce air. This can change measured quantity, visible level, foam and pump behaviour.
Line engineering guide
A bottle filler can only dose consistently when it receives product under controlled conditions. Tank level, transfer pump, pipework, temperature, aeration, recirculation and cleaning should be designed with the filler rather than treated as separate utilities.

Direct answer
A bottle filling machine needs a repeatable supply of suitable product at the expected temperature, pressure and level, without avoidable air, foam or contamination. The supply arrangement must refill fast enough for production while remaining cleanable, drainable and compatible with the product.
Supply routes
The best route is the simplest arrangement that gives the filler a stable product condition and can be cleaned and operated safely.
| Supply arrangement | Where it can fit | Questions to resolve |
|---|---|---|
| Header tank above the filler | Readily flowing products using gravity or controlled head. | Level variation, refill rate, foam, overflow, access, cleaning and support structure. |
| Machine hopper | Viscous or paste products supplied locally to a piston or positive-displacement filler. | Settling, agitation, heating, usable volume, operator refill and product recovery. |
| Suction from a floor vessel | Suitable self-priming pump systems with a defined suction path. | Suction lift, hose length, priming, air leaks, empty-vessel detection and cleaning. |
| Transfer pump to day tank | Central product source feeding a smaller controlled vessel near the filler. | Pump control, high/low level, overfill protection, refill surges and return route. |
| Pressurised or recirculating loop | Applications needing maintained flow, temperature or suspension. | Pressure stability, shear, heat, bypass, balance across heads and safe isolation. |
Failure modes
Variation at the filler inlet can be mistaken for a dosing fault. Record supply conditions whenever fill results drift.
Leaking suction joints, low vessel level or aggressive transfer can introduce air. This can change measured quantity, visible level, foam and pump behaviour.
An oversized transfer pump, unstable regulator or changing static head can alter nozzle flow and channel balance.
Cooling, heating, settling or phase separation can change viscosity and density between the first and last bottle in a batch.
The filler may starve when the transfer route cannot replace product at the average and peak demand of the selected fill cycle.
Unplanned low points, long hoses and inaccessible valves can retain product and extend changeover time.
Refilling during a critical dose can disturb head or pressure. Level logic and pump timing should be tested with the full cycle.
Sizing sequence
Do not choose the transfer pump from a catalogue flow rate alone. Work from the product, line demand, pressure losses and cleaning route.
Record viscosity, density, temperature, particles, foam, shear sensitivity, settling, corrosivity and SDS requirements.
Use dose × filling heads × actual cycle rate, then include refill strategy and realistic peak demand without assuming every pump delivers its nominal rating in the process.
State vessel location, height, pipe or hose length, bends, valves, filters, connectors, elevation and the filler inlet.
Define high/low level, dry-run protection, overfill protection, pressure monitoring, alarms, isolation and safe fault response.
Review access, low points, product recovery, rinse capture, dismantling and acceptance between products.
Quotation checklist
Buyer questions
No. Some fillers can draw from a vessel or use a local hopper or gravity head. A transfer pump is needed when the source location, product behaviour or production demand requires controlled movement to the filler.
Size the pump from the real liquid, required average and peak flow, suction conditions, pipe losses, pressure, temperature and control method. Catalogue flow measured on water should not be assumed for another product or installation.
Changing level can alter static head, suction conditions or refill events. The effect depends on the dosing method, so level control and refill timing should be tested across a representative batch.
Yes. Excessive speed, splashing returns, suction air leaks or unsuitable pump action can aerate a surfactant product. The supply route should be tested for air entrainment before the fill profile is blamed.
Recirculation may help maintain temperature, suspension or a ready supply, but it can also add shear, heat or air. The return point, flow, bypass and stop conditions must suit the product.
Short, accessible routes with drainable low points, suitable connections, removable or cleanable valves and an agreed product-recovery method usually reduce retained product and changeover effort.
Send the product, source-vessel arrangement, pipe route, fill range and output so Lancing can review the complete feed and filling system.