Practical ATEX filling advice for your product, packs and production target

Automatic hazardous-area filler

Automatic ATEX Filling Machine

Increase throughput with a conveyor-fed filling platform configured around your flammable liquid, container format, required output and declared hazardous area.

Lancing explosion-protected six-head automatic filling machine

Machine overview

What this automatic configuration can do for your line.

This platform can be configured with pneumatic actuation, protected controls, grounding and bonding provisions, diving nozzles and a dosing module selected around the product. Typical routes include piston, gear-pump, mass-flow or magnetic-flow dosing where technically suitable.

The machine is planned with the surrounding line. Bottle infeed, product supply, extraction, capping, labelling and operator access can all affect the final hazardous-area design.

Hazardous-area suitability is project-specific.

The final machine category, marking, electrical and non-electrical equipment, controls, documentation and installation requirements must match the competent site assessment and agreed specification.

Guarded automatic ATEX filling machine with multi-head liquid filling station

Key features

Tailored to your product and production needs.

1

Explosion-protected design

Enclosures, cabling, operator devices and non-electrical ignition risks are reviewed against the required classification.

2

Pneumatic actuation

Air-driven cylinders can reduce electrical equipment at the point of fill, subject to the complete design assessment.

3

Grounding and bonding

Static-control provisions can be incorporated for compatible containers, product transfer and line components.

4

Diving nozzles

Bottom-up filling can help control splash, foam and vapour release for suitable products and containers.

5

Modular dosing

Piston, pump or flow-meter routes can be compared against viscosity, compatibility and required tolerance.

6

Line integration

Capping, labelling, conveying and bottle handling can be engineered into a coordinated cell or line.

Technical data

Key capabilities to confirm for your project.

Reference dose range50 ml to 5000 ml, pump and configuration dependent
Filling heads1–6 heads, selected around output and fill time
ActuationPrimarily pneumatic with project-specific interlocks
ControlsProtected panel, emergency-stop and operator devices to agreed specification
Static managementGrounding, bonding and dissipative components where required
Frame and contact materialsStainless-steel frame with sealed / compatible product-contact components
Air supplyApproximately 0.4–0.6 MPa reference
Electrical supply110/220 V, 50–60 Hz reference; final supply project-specific
OptionsWeigh cells, mass flow, magnetic flow, nitrogen blanketing, extraction interfaces and guarding

Indicative platform data only. Final performance, conformity, utilities and dimensions are confirmed against the product, container, hazardous-area classification and approved project specification.

Applications

Typical applications.

S

Solvents and chemicals

Acetone, ethanol blends, thinners and compatible reagents after SDS and material review.

A

Alcohol personal care

Perfume bases, body-mist products and alcohol-rich formulations in suitable packs.

S

Speciality liquids

Laboratory and industrial products requiring controlled filling in a classified area.

Typical supply scope

Support from specification to start-up.

  • Machine frame and conveyor arrangement
  • Configured dosing module and filling nozzles
  • Protected controls, pneumatic actuators and safety interlocks
  • Operation, maintenance and agreed conformity documentation
  • Optional line integration, commissioning and training

Quote brief

Send these details for a faster, more accurate recommendation.

  • Product SDS and full formulation / concentration information
  • Zone, gas group and temperature class or site assessment status
  • Fill volumes, container dimensions and neck opening
  • Required sustained output and changeover pattern
  • Available air, power, extraction and product-feed arrangements
  • Capping, labelling, coding and conveyor requirements

Questions

Questions about automatic ATEX filling.

Can the automatic ATEX filler handle different products?

Potentially, but every product must be checked for flammability, compatibility, viscosity, cleaning, seals, hoses and the agreed hazardous-area classification. Changeover procedures also need to be defined.

Can the head count be increased?

The platform can be configured with different head counts, but output is governed by fill volume, product flow, nozzle behaviour, container indexing and downstream line capacity.

Does the machine include extraction?

Extraction and ventilation are site- and process-dependent. Interfaces or containment can be included in the project scope, but the facility design and DSEAR controls remain part of the wider site assessment.

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Engineering brief

Define the dosing, product supply and hazardous-area interfaces as one system.

An automatic filler can only sustain output when the product reaches each nozzle consistently, containers are presented reliably and the downstream line accepts every filled pack. The selection therefore starts with more than the nominal dose range and number of heads.

Product and dosing route

Record viscosity and density at the real operating temperature, together with foam, vapour, particles, shear sensitivity and the required cleaning method. Piston, pump and flow-meter routes respond differently to those variables. The product supply tank, transfer pump, hose length, head pressure and recirculation arrangement can be as important as the filler itself.

For several products, list each formulation and concentration. Compatibility should cover seals, hoses, valves, nozzles and any wetted instrument—not only the main tank or frame material. The proposed recipe and changeover procedure should state what is drained, flushed, dismantled or replaced.

Release and ignition controls

The competent site assessment should identify where vapour or mist can be released and which parts of the line sit inside the classified area. The machinery review then considers protected electrical equipment, non-electrical ignition risks, hot surfaces, friction, impact, static, earthing and bonding, operator devices and maintenance access.

Extraction may be a facility service, a hood or enclosure interface, or part of a combined scope. The quotation should identify who designs the airflow, who proves its performance, what interlock is required and what the machine must do if extraction is unavailable.

Output should be stated as a sustained operating case.

Specify the product, fill quantity, container, number of heads, indexing pattern, fill profile and downstream stages. A short dry-cycle rate is not the same as sustained filled-container output with real cut-off, cap handling, rejects and operator interventions.

Changeover and acceptance

Plan cleaning, change parts and FAT evidence before manufacture.

C

Cleaning method

Define drain points, flush media, dismantling, retained product, waste handling and how the cleaned state is checked. Flammable cleaning media may create a separate operating case that belongs in the risk review.

Δ

Format change

List bottle dimensions, neck openings, closure families and label formats. Agree which rails, guides, nozzles, timing screws or recipes change and how the correct set-up is verified.

F

Factory acceptance

Agree the test product or representative medium, sample quantity, run length, output basis, fill-measurement method, alarm and interlock tests, reject conditions and the records supplied after FAT.

Site acceptance should separately verify installation interfaces, utilities, earthing, extraction, guarding, line controls and the operating conditions that cannot be reproduced at the factory. See the sample-trial and FAT guide for a practical evidence list.

What samples are needed for an automatic filling trial?

Provide the real product where transport and safety arrangements permit, together with every relevant container and closure, current SDS information and the intended operating temperature. The sample quantity should support start-up, adjustment, a representative run and cleaning checks rather than a single demonstration fill.

Can an existing capper or labeller be connected to the ATEX filler?

Potentially. Its location, ignition risks, controls, line height, transfer, performance and documentation must be reviewed against the classified area and the complete-line risk and conformity plan. Existing equipment should not be assumed suitable solely because it operates downstream of the nozzle.

What should be recorded during FAT?

Record the declared product or test medium, containers, recipe, target quantities, measurement method, achieved results, test duration, output basis, alarms, interlocks, rejects, changeover observations and any open actions. The record should make clear which site-dependent checks remain for SAT.

Where no hazardous-area requirement applies, broader automatic liquid-filler technology is covered by liquidfillers.co.uk and volumetric selection by volumetricfillers.co.uk.

Automatic fill-cycle evidence

Specify the complete flammable-liquid filling cycle under real product-feed and line conditions.

An automatic ATEX filling machine is not defined only by the number of heads. The fill result and sustained output depend on the product arriving consistently, each container being located correctly, the nozzle closing cleanly and the downstream equipment accepting the pack without forcing an unsafe accumulation or restart.

Cycle stageVariables to defineEvidence to capture during trial or FAT
Product supplySource vessel, batch level, pump or pressure, hose route, filtration, recirculation, temperature and permissible retained product.Stable supply across the run, response to low product, isolation, drainage and safe stop behaviour.
Container detection and indexingPack dimensions, transparency, neck location, conveyor guides, gaps, fallen-pack response and permitted accumulation.No-container/no-fill performance, repeatable position, recovery from a misfeed and restart without uncontrolled discharge.
Coarse and fine fillingDosing method, fill profile, nozzle position, foam or splash control, cut-off and any material still moving after the stop command.Results against the agreed measurement method, drips, tails, visible splash, fill time and repeatability at the minimum and maximum dose.
Open-pack transferDistance and time to closure, extraction coverage, container cleaning, reject path and line stops between filling and capping.Condition of the filled container, residual drips, exposure during accumulation and the action taken when the capper is unavailable.
Cleaning and changeoverDrain points, flush medium, dismantling, recipe control, change parts, waste or recovery and verification of the clean state.Access, hold-up, cross-contamination controls, safe handling of the cleaning medium and correct restart after changeover.

When an automatic filler may not be the best first route

A lower-output or operator-assisted system may be preferable where batches are small, containers vary widely, the product needs frequent manual observation or the classified-area and facility work needed for a full conveyor line is disproportionate. Larger packs controlled by mass may point towards an ATEX weigh filler instead.

The decision should compare total operating effort, including product change, cleaning, cap replenishment, rejects and operator interventions—not only the shortest theoretical fill time.

Static and extraction are line interfaces

Earthing and bonding should cover the real conductive path and should not be reduced to adding a clamp without assessing the container, product and transfer system. The static-control guide sets out the information needed for that review.

Extraction should have a named design basis, owner, verification method and machine response when it is unavailable. Those site-dependent matters should be identified separately from the functions demonstrated at FAT.

The six-second machine video is process evidence, not an ATEX conformity claim.

The demonstration shows multiple nozzles filling indexed containers. It can help buyers discuss container movement, nozzle alignment and simultaneous filling, but the final hazardous-area suitability, product compatibility, protection concepts and documentation remain project-specific. Use the trial and FAT guide to define the evidence needed for the actual application.

Automation handover

Confirm that the full line can sustain the same approved operating case.

Adding heads or increasing conveyor speed does not create usable output if product supply, bottle indexing, capping, extraction or downstream transfer becomes the limiting stage. The final line balance should be demonstrated with the agreed product and containers.

Compare operator-assisted filling first

Where campaigns are short, formats change frequently or an operator can manage the pack safely, a semi-automatic ATEX filling machine may be the stronger commercial route. The comparison should include repetitive handling, open-container time, closure placement and future growth.

The automation comparison guide provides a like-for-like decision matrix.

Write the line cause-and-effect

Define how the filler responds to container absence, lost extraction, missing earthing permissive, product-supply faults, open guards and downstream blockage. State the safe state and recovery route for each condition.

Use the controls and interlocks guide to prepare the functional description and FAT script.

Include site readiness in the order programme.

The installation and site-preparation guide covers layout, utilities, extraction, earthing, drainage, delivery and SAT interfaces that can otherwise delay a completed machine.

Automatic filling questions

Questions buyers ask about automatic ATEX filling cycles.

Automatic operation should be evaluated as a complete sequence, including container detection, permissives, product flow, downstream capacity and recovery from interruptions.

What limits the sustained output of an automatic ATEX filling line?

Sustained output is limited by the slowest repeatable part of the complete accepted-pack cycle, not by the filler’s fastest isolated movement. Product supply, fill time, settling, nozzle withdrawal, conveyor indexing, container spacing, capping, rejects, downstream accumulation and safe recovery can each become the governing step.

Define output as accepted filled and closed containers over an agreed measured run, using representative product and packs. The ATEX line output guide explains how to distinguish a component cycle rate from production capacity.

How are empty-container detection and no-container-no-fill controls used?

Container detection is used to confirm that the intended pack is correctly positioned before product is released. A no-container-no-fill function can inhibit a new dose, but the specification should also address misaligned containers, wrong-height packs, a container removed mid-cycle, sensor contamination and the disposition of any partial fill.

The sensor and response must suit the real container material, colour, geometry and line speed. FAT should test normal detection, credible misplacement and recovery rather than only demonstrating one successful cycle.

What should happen if extraction or earthing permissives are lost?

The approved cause-and-effect schedule should define whether loss of a relied-upon extraction or earthing condition prevents a new fill, stops product flow, completes a controlled step or requires immediate isolation. The correct response depends on the risk assessment, process state, stored energy and the way the condition is monitored.

Specify the signal source, expected state, response, alarm, reset and restart checks. Do not rely on a generic “machine stops” statement, because a stop that traps product, leaves a valve open or permits an uncontrolled restart may not be the required safe state.

Can an automatic ATEX filler run short campaigns without excessive changeover?

An automatic ATEX filler can run short campaigns when format parts, product-contact components, recipes, cleaning and verification are designed around the real change pattern. Automation does not automatically make changeover fast; additional heads, hoses, valves, conveyors and sensors can increase the number of items to clean, adjust and prove.

List the smallest campaign, change frequency, product sequence, allowed residues, pack range and required release checks. A representative changeover trial can show whether the automatic route remains practical or whether a simpler station offers better campaign flexibility.

Test the cycle that production will actually run.

Combine the sustained-output method, the flammable-liquid nozzle questions and the existing trial and FAT framework before fixing the acceptance test.

Architecture and permissives

Separate automation level from the hazardous-area protection strategy.

An automatic ATEX filling machine can use electrical and pneumatic functions when the complete design matches the intended duty. Conversely, a machine described as pneumatic is not automatically suitable for a Zone. Review the pneumatic-filler safety question and define any ventilation or gas-detection permissives in the cause-and-effect schedule.

Information to add to the automatic-line URS

  • Drive, valve, sensor and control-panel architecture.
  • Location of every item relative to the approved Zone boundary.
  • Extraction, gas detection and product-supply healthy signals.
  • Safe state following loss of air, power, ventilation or detector availability.
  • Restart authority and FAT/SAT test method.

Product delivery and nozzle strategy

Match the pump response and fill profile to the real flammable liquid.

Automatic output depends on more than the nominal number of heads. The product-feed pump, coarse/fine control, nozzle movement, pressure, air entrainment, valve closure and residual product all affect accepted fills and safe fault response.

Multi-head verification

Record each filling head before accepting a line average.

An overall batch average can conceal a head that consistently gives a different result. Identify the nozzle position against the checked packs during the agreed trial, then compare normal operation, pause/restart and end-of-batch behaviour. Record rejects and the conditions of the reference check rather than selecting only clean, correctly filled containers.

A multi-head specification should state which quantity is controlled, how an individual head is adjusted, who authorises changes and how the line confirms the result afterwards. These are functions to agree for the project, not a statement that every control feature is standard.

Use fill-accuracy and checkweighing guidance for acceptance evidence. For coloured or reactive formulations, see the different handling tasks for finished solvent inks and separate resin and hardener packs.

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