Automatic Feeding, Grouping, and Shrink Wrapping Machine for Small Cylindrical Products

Executive Summary

An automatic feeding, grouping, and shrinking machine indexes small individual products from a continuous single-file line, collates them into predetermined matrix patterns, encloses the bundle in polyolefin (POF) film, and heat-shrinks the multipack in a recirculation air tunnel. This turns loose-piece packaging into uniform, transport-ready multipacks with reduced manual labor and exact piece counts. Engineered to accommodate specific product geometries, stability ratios, and line throughputs, this technical guide explains the operational stages, pack collation matrices, film sizing formulas, operating tolerances, and procurement integration checklists.


Infeed mechanics channel individual containers along precision guide rails into an automated collation station. High-speed pneumatic sweep cylinders or servo-actuated pushers index the products into multi-lane rows (such as a 2 × 6 matrix) directly onto the transfer platform. The grouped collation transfers smoothly via synchronized friction belts through an integrated film-forming section, where continuous mechanical sealing creates a fully enclosed sleeve. The bundle then indexes across a variable-speed metal mesh belt through an insulated convection shrink tunnel, utilizing dual-zone temperature controls and silicone air-baffle curtains to achieve uniform, tamper-evident package tensioning.

Table of Contents

Why Group and Shrink Small Products

Manual collation and casing of small rolls, cosmetic tubes, aerosol cans, and vials introduces labor bottlenecks, high piece-count errors, and scuffing from loose transit contact. Automated collation and shrink-bundling provides three primary operational advantages:

  • Structural Integrity: Tightly contracted cross-linked film holds unstable cylindrical products in fixed structural geometry without secondary carton partitions or corrugated trays.
  • Visual Inspection and Barcode Readability: Transparent shrink film allows direct lot verification, primary brand visibility, and optical barcode scanning through the wrap.
  • Line Balance and Exact Count Verification: Integrated optical gate sensors verify batch quantity prior to wrapping, preventing under-count or over-count errors downstream.

The Three Stages of Automated Collation

  1. Precision Infeed Feeding: Single-track feeding conveyors receive containers upright from upstream filling, labeling, or capping lines. Side guides and dynamic acceleration belts singulate and pitch the items while maintaining vertical stability.
  2. Pneumatic or Servo Collation: Once a lane reaches the target part counter, a multi-stage pusher mechanism sweeps the batch laterally into the collation matrix (e.g., 2 × 6 or 3 × 4). Pneumatic cylinder air lines run at regulated pressures (0.6–0.8 MPa) with cushions to prevent toppling during transfer.
  3. Enclosing, Sealing, and Shrinking: The grouped block moves synchronously through an adjustable film former. Mechanical sealing jaws separate and seal the pouch, which immediately enters the hot-air convection tunnel (regulated between 140 °C and 180 °C). High-velocity circulating airflow shrinks the film uniformly, and the pack exits onto a cooling runout conveyor.

Grouping Patterns and Matrix Layouts

Pattern (Rows × Columns) Pieces per Pack Typical Applications Mechanical Infeed Configuration
1 × 6 6 Slim tubes, pharmaceutical vials, lip balms Single-row linear push, direct belt inline feed
2 × 6 12 Miniature beverage cans, tape rolls, small jars Dual-stroke side-pusher with mechanical stops
2 × 8 16 Condiment bottles, compact cylindrical bearings High-stroke indexing pusher, lane dividing gates
3 × 4 12 Standard beverage cans, squat jars, wide rolls Multi-lane diverging guides, servo cross-transfer

Note: Transitioning between matrix configurations requires adjusting lane guide spacing, photo-eye positioning, pusher stroke length, and film former dimensions. Standard mechanical changeover requires 15–30 minutes.

Reference Technical Specifications

Typical engineering specifications for the continuous collation and shrink wrapping system:

Parameter Operational Range / Specification
Multipack Footprint (L × W × H) Length: 100–450 mm Width: 40–190 mm Height: 35–75 mm
Operating Throughput 30–150 packs/min (dependent on pack volume and pitch)
Film Compatibility Center-folded or flat POF (Polyolefin), 15–25 µm, max web width 590 mm
Pneumatic Supply Requirement 0.6–0.8 MPa dry compressed air, ~150 NL/min
Sealer Electrical Load 220 V / 50 Hz (or 60 Hz customized), Single-Phase, 3.6 kW
Shrink Tunnel Electrical Load 380 V / 50 Hz (or 460 V / 60 Hz 3-Phase), 16.5 kW continuous heating
Sealing Unit Dimensions & Weight 4,930 mm (L) × 1,130 mm (W) × 1,500 mm (H) ~1,000 kg
Tunnel Dimensions & Weight 2,400 mm (L) × 600 mm (W) × 1,550 mm (H) ~600 kg

Sizing Film Width and Output Calculations

Accurate film width selection prevents material waste and sealing failure. The total roll web width must account for the cross-sectional perimeter of the compiled product pack plus a lateral sealing overlap allowance.

Film Width Calculation: W_film = 2 × (W_pack + H_pack) + C_seal (where C_seal is typically 30–40 mm to account for film tracking and trim margin)

Throughput Calculation: Packs/min = Infeed Inflow Rate (items/min) ÷ Items per Multipack

Worked Engineering Example (2 × 6 Grouping of Ø40 mm × 60 mm Cylinders):

Engineering Check Governing Equation / Values Calculation Result
Pack Dimensions Length: 6 × 40 mm, Width: 2 × 40 mm, Height: 60 mm 240 mm (L) × 80 mm (W) × 60 mm (H)
Required Film Width 2 × (80 + 60) + 30 mm 310 mm flat web width
Film Cut Length / Pitch Pack Length (240 mm) + Pack Height Allowance (60 mm) ~300 mm web advance per stroke
Line Rate (at 360 items/min) 360 items/min ÷ 12 items/pack 30 multipacks/min
Thermal Energy Demand 16.5 kW tunnel rated output ÷ (30 packs/min × 60 min/h) ~0.009 kWh/pack (baseline full load)

System notes: Running at 30 packs/min represents the lower speed threshold of this chassis; intermediate buffering tables or intermittent cycling logic should be implemented if upstream inflow drops below 300 items/min. Steady-state shrink tunnel power draw drops by 30%–45% once thermal equilibrium is reached.

Common Operating Problems and Root Causes

  • Product Instability / Toppling in Infeed Lanes: Typically caused by excessive lateral clearance in guide tracks, high infeed conveyor vibration, or unfavorable Height-to-Diameter (H/D) ratios exceeding 2.5:1.
    • Corrective Action: Adjust guide rails to container diameter with a +1.0 mm clearance; use low-friction UHMW wear strips; smooth out acceleration profiles on the indexing belts.
  • Piece-Count Discrepancies: Occurs when infeed speed overwhelms the optical register or when photoelectric eye thresholds fail on reflective or transparent containers.
    • Corrective Action: Recalibrate fiber-optic sensors; integrate polarising filters for glossy cans/bottles; establish electronic handshake interlocking between grouping pushers and upstream line stops.
  • Loose Film, Ballooning, or Surface Burn Marks: Unbalanced thermal profiles, mismatched conveyor travel speeds, or missing film micro-perforations.
    • Corrective Action: Adjust tunnel airflow velocity and internal air dampers; verify that needle-wheel perforators are opening venting holes to allow hot air escape during shrinkage; optimize conveyor velocity to set dwell time between 3 and 6 seconds.
  • Protruding Corner Triangles (“Dog Ears”): Excessive film bag length around the leading and trailing pack faces.
    • Corrective Action: Lower the vertical cross-seal jaw travel stroke; reduce bag pitch cutoff length closer to the true physical bundle envelope; balance tunnel bottom-air damper flow.

Engineering Selection Checklist

Verify the following primary parameters prior to machine specification and layout approval:

  1. Product Dimensional Envelope: Exact base diameter, overall height, weight, surface finish, and center-of-gravity (CG) location.
  2. Matrix Packaging Formats: Required row-and-column arrays (e.g., 1 × 6, 2 × 6, 3 × 4) and total distinct SKU part numbers sharing the system.
  3. Upstream Infeed Capacity: Instantaneous and average line output rates (items/minute), continuous vs. batched supply.
  4. Packaging Film Properties: Film material (cross-linked POF vs. standard LDPE), film thickness (typically 15 µm, 19 µm, or 25 µm), unprinted vs. registered print requirements.
  5. Downstream Integration: Handshake protocol with secondary wrap-around case packers, robotic palletizers, or manual inspection stations.
  6. Facility Utilities: Factory plant voltage/frequency (e.g., 208 V, 380 V, 480 V; 50/60 Hz) and compressed air supply capacity at the point of drop.

Machine Safety and Compliance Standards

This equipment is designed and validated in strict alignment with international packaging machinery safety codes:

  • EN ISO 12100:2010: Safety of machinery — General principles for design — Risk assessment and risk reduction.
  • EN 415-10: Safety of packaging machines — Part 10: General requirements for collating and shrink-wrapping machinery.
  • EN 60204-1: Safety of machinery — Electrical equipment of machines — General requirements.
  • Mechanical Safeguarding: Tunnel thermal chambers are fully insulated and protected by mechanical access barriers; high-speed collation pushers and rotary/guillotine sealing bars are housed behind dual-channel interlocked acrylic safety doors rated to Category 3 / PL d architecture with integrated Lockout/Tagout (LOTO) disconnect points.

Engineering FAQ

Q: What container geometries and container materials can this unit collate? A: The system handles rigid and semi-rigid cylinders including metal aerosol cans, small tin containers, plastic cosmetic tubes, glass bottles, and rolled tape cores. Containers must have flat, stable seating bases with an H/D ratio generally under 3:1 for continuous upright conveyance.

Q: What is the maximum throughput for a 2 × 6 pack configuration? A: With servo-assisted infeed collation and dynamic continuous sealing, output ranges from 30 up to 100 packs per minute (corresponding to 360 to 1,200 individual items per minute fed upstream), constrained primarily by the thermal shrink velocity and container tipping thresholds.

Q: Why is POF film preferred over PE or PVC for small grouping multipacks? A: Polyolefin (POF) provides higher tensile puncture resistance, excellent optical clarity (gloss > 85%), high multi-directional shrink ratios (up to 60%), and yields clean, odor-free seals without emitting hydrochloric acid vapors associated with PVC.

Q: How are different pack patterns accommodated on one physical machine? A: Quick-release tool-less guide rails, digital position counters on lane widths, swappable pusher matrix heads, and programmable recipe selection in the touchscreen HMI allow SKU changeovers in under 20 minutes.

Next Steps and Technical Inquiries

  1. Submit Application Parameters: Send product dimensions (3D CAD or 2D technical drawings), desired multipack layouts, and production line speeds (items/min) to info@fhopepack.com.
  2. Engineering Review & Sizing: Our mechanical team verifies lane kinematics, determines exact sealing jaw clearance, and provides thermal shrink tunnel calculations.
  3. Formal Turnkey Quotation: Receive a comprehensive 2D/3D plant layout drawing, budget breakdown, and 48-hour delivery timeline proposal.

Engineering References

  • FHOPEPACK Engineering Data Sheet: Continuous Flow Wrap & Collation Series LD-059
  • ISO 12100 / EN 415-10 Machinery Safety Guidelines
  • Internal Testing: High-Speed POF Shrink Film Dynamics and Recirculation Tunnel Thermodynamics

Last updated: 2026-10-29