MFG-COMP18-04 · Lesson 4 · 12 clock hours · lab
Resin Feed Network Design and Infusion Front Control
Objective. Students will design a resin-feed and vacuum-line layout for a given panel geometry that produces an even infusion front, execute the infusion, and demonstrate front progression from feed to vacuum line without dry spots or race-tracking.
⚠ Pending professional review
This lesson, its worked examples and its practice questions has not yet been verified by a licensed engineer or certified journey-level tradesperson or by a certification or approval body. It is a study draft and may contain errors. Do not use it as instructions for work on a job site or on live equipment. Always follow your instructor, your supervising professional, and current official references and regulations.
VoTechWorks program approval and accreditation are still in progress. Credentials are issued only by the certifying bodies named in each program, after their own exams.
Why Feed-Network Design Matters
Vacuum infusion pulls catalyzed resin through a dry fiber stack by creating a pressure differential between a resin feed line and a vacuum line. The goal is a single, even resin front that advances from the feed side to the vacuum side without leaving dry spots or channeling along unintended paths. Poor network design is the leading cause of infusion defects. Understanding how resin flows through reinforcement lets you arrange your feed and vacuum lines before a drop of resin is committed.
Darcy's Law and Flow-Front Basics
Resin movement through a fiber preform follows Darcy's Law: flow rate is proportional to permeability and pressure gradient, and inversely proportional to resin viscosity. You do not need to solve the equation by hand, but the concept tells you three practical things:
1. Higher permeability = faster flow. Flow media (a coarse mesh layer) has very high in-plane permeability and acts as a distribution highway. Biaxial glass fabric has much lower permeability and controls through-thickness fill.
2. Lower viscosity = faster flow. Infusion-grade vinyl ester is formulated for low viscosity. Mixing temperature, pot temperature, and the time elapsed after catalyzing all affect viscosity. Work within the resin supplier's recommended pot-life window.
3. Pressure gradient drives everything. The vacuum line is your low-pressure sink. Resin enters at atmospheric pressure at the feed port and travels toward vacuum. The front shape reflects the path of least resistance.
Common Feed-Line Patterns
Center-line feed / perimeter vacuum: One feed line runs along the centerline of a rectangular panel; vacuum lines run along both long edges. The front splits left and right symmetrically and travels roughly half the panel width to each vacuum line. Useful for wide, flat panels.
Perimeter feed / center vacuum: Feed line surrounds the part; vacuum line runs down the center. The front converges inward. Good for narrow panels or when a central stiffener is present.
Edge feed / opposite-edge vacuum: The simplest layout for a rectangle. Resin enters one short or long edge and exits the opposite edge. Race-tracking risk is highest at corners because resin reaches the bag edge first and can channel along it before filling the field.
Tapered panels and hull sections: As width changes, so does the distance from feed to vacuum. A single straight feed line on a tapered hull section will deliver resin faster to the wide end. Solutions include angling the feed line to follow the taper, using branch feeds of varying spacing, or segmenting the vacuum line to equalize arrival time.
Joggled steps: A thickness change interrupts permeability. Plan a secondary feed leg that crosses the step, or position a short flow-media patch over the step to bridge the gap.
Race-Tracking and How to Prevent It
Race-tracking occurs when resin finds a low-resistance channel — typically along a bag edge, a wrinkle, or an unsealed spiral-wrap end — and sprints ahead of the main front. The fast channel then blocks vacuum from reaching adjacent dry fiber. Prevention measures:
- Seal spiral-wrap ends with tacky tape so resin exits only at intended ports.
- Keep bag bridges tight against the part edge; bridge folds create channels.
- Extend peel ply to — but not past — the part boundary so no open fiber sits against the bag edge.
- For tapered geometries, stagger feed-line branches to slow resin advance at the wide end.
Vacuum-Line Placement Rules
- The vacuum line is always the last thing resin should reach. Place it at the point geometrically farthest from the feed, accounting for the actual flow path through the reinforcement.
- Use a resin trap (catch pot) between the part and the pump. Without a trap, resin entering the pump causes immediate pump failure and a safety hazard.
- Maintain vacuum at or above the level recommended by the resin supplier — typically 25 in Hg or higher for infusion-grade systems. Test the bag for leaks for a minimum of 15–30 minutes before introducing resin.
Monitoring Front Progression
Once resin enters the preform, watch the translucent wet front advance. Marks on the mold at measured intervals let you confirm the front is on schedule and symmetrical. If one side leads the other by more than your design tolerance, clamp the feed line serving the fast side partially to slow that branch. When resin first appears at the vacuum-line spiral wrap, close the resin feed valve to stop additional resin intake, then maintain vacuum through gelation to compact the laminate.
Safety Requirements for This Lab
PPE is mandatory throughout: nitrile gloves (double-glove for extended resin contact), safety glasses or chemical splash goggles, and an air-purifying respirator with organic-vapor cartridges rated for styrene/vinyl ester vapors. A disposable Tyvek suit protects skin and clothing.
Ventilation: Infusion-grade vinyl ester releases styrene vapor. Work only in the designated ventilated infusion area. Confirm exhaust ventilation is operating before opening any resin container.
MEKP handling: Methyl ethyl ketone peroxide is a strong oxidizer and can cause serious eye and skin injury. Measure it into a separate container before adding to resin — never add resin to the MEKP container. Store MEKP away from heat, open flame, and incompatible materials. Know the location of the eyewash station.
Spill response: Have absorbent material and a labeled waste container at the workstation. Catalyzed resin waste must be spread thin to dissipate exotherm before disposal per your facility's hazardous-waste procedure.
Electrical: The vacuum pump is a running motor. Keep resin and solvent away from the motor housing. If a resin trap overflows, shut off the pump before clearing it — this is a lockout/tagout situation if the pump requires service.
Key terms10
Darcy's LawA principle stating that fluid flow rate through a porous medium is proportional to permeability and pressure gradient, and inversely proportional to fluid viscosity; the theoretical basis for predicting resin flow in vacuum infusion.
PermeabilityA measure of how easily a fluid passes through a porous material such as a fiber reinforcement or flow media; higher permeability means faster resin travel.
Flow mediaA coarse, open-weave mesh placed in the layup to create a high-permeability distribution layer that rapidly delivers resin across large areas before it infiltrates the reinforcement below.
Race-trackingA defect in which resin finds a low-resistance path — such as a bag edge, wrinkle, or unsealed spiral-wrap end — and advances far ahead of the main flow front, leaving adjacent fiber dry and unreachable.
Resin trap (catch pot)A sealed container installed in the vacuum line between the infusion bag and the vacuum pump; it collects any resin that reaches the line, preventing pump damage and a potential safety hazard.
Infusion frontThe visible boundary between wetted and dry reinforcement as resin advances through the preform during vacuum infusion; even, symmetrical front progression is the goal of proper feed-network design.
Spiral wrapFlexible, corrugated plastic tubing used to carry resin from the pot to the feed port or to carry vacuum to the vacuum line; its open structure provides a high-permeability channel along its length.
Peel plyA tightly woven release fabric placed directly on the reinforcement; it infuses with resin, cures bonded to the laminate surface, and is peeled off after cure to leave a clean, bondable texture.
Pot lifeThe working time after catalyst is added to resin during which viscosity remains low enough for successful infusion; exceeding pot life causes resin to gel before the front reaches the vacuum line.
MEKP (methyl ethyl ketone peroxide)The organic peroxide catalyst used to initiate cure of polyester and vinyl ester resins; a strong oxidizer that requires careful measurement, segregated storage, and appropriate PPE during handling.
Worked examples4
1. A rectangular panel is 24 in wide and 36 in long. A single edge feed line is placed along one 24-in edge and a vacuum line along the opposite 24-in edge. The resin front advances at an average rate of 1.5 in per minute across the full width. How many minutes should it take the front to travel from the feed line to the vacuum line, and what is the total infusion window needed if the resin supplier requires closure of the feed line at least 5 minutes before the resin's 45-minute pot life expires?
- Step 1 — Calculate travel distance: feed to vacuum = 36 in (the length of the panel).
- Step 2 — Calculate travel time: 36 in ÷ 1.5 in/min = 24 minutes for the front to reach the vacuum line.
- Step 3 — Add the required 5-minute buffer before pot life expires: latest acceptable front-arrival time = 45 min − 5 min = 40 min.
- Step 4 — Compare: front arrives at 24 min, pot life deadline is 40 min. The 16-minute margin confirms the design is acceptable at the given flow rate.
- Step 5 — State the answer clearly: estimated infusion time is 24 minutes; the operator must close the feed line by minute 40 at the latest.
Answer: The front reaches the vacuum line in approximately 24 minutes, leaving a 16-minute safety margin before the 40-minute feed-closure deadline.
2. A tapered hull section is 12 in wide at one end and 30 in wide at the other, with a centerline length of 48 in. A straight centerline feed line runs along the 48-in axis, and vacuum lines run along both long (slanted) edges. Estimate the flow distance from the centerline to the vacuum line at the narrow end and at the wide end.
- Step 1 — The centerline feed is equidistant from both side edges at any given cross-section.
- Step 2 — At the narrow end, total width = 12 in, so each half = 12 ÷ 2 = 6 in. Flow distance from centerline to vacuum line = 6 in.
- Step 3 — At the wide end, total width = 30 in, so each half = 30 ÷ 2 = 15 in. Flow distance from centerline to vacuum line = 15 in.
- Step 4 — Ratio of distances: 15 in ÷ 6 in = 2.5. At the same permeability and pressure gradient, resin reaches the narrow-end vacuum line 2.5 times sooner than the wide-end vacuum line.
- Step 5 — Identify the design implication: the wide end will be last to fill and is the highest dry-spot risk. Consider staggering feed branches or angling the feed line toward the wide end to equalize arrival time.
Answer: Flow distance is 6 in at the narrow end and 15 in at the wide end; the wide end fills 2.5× slower and requires design compensation.
3. During the dye-flow test, photographs show the leading edge of the flow front on the left side of the panel is 18 in from the feed line while the right side is only 14 in from the feed line at the same 10-minute mark. Calculate the percent asymmetry and determine whether the result passes the 15% symmetry tolerance used in this lab.
- Step 1 — Identify the faster side (right, 14 in) and slower side (left, 18 in). Wait — re-read: left is at 18 in, right is at 14 in. So left has advanced farther and is the faster side.
- Step 2 — Calculate the difference in advance distance: 18 in − 14 in = 4 in.
- Step 3 — Express asymmetry as a percentage of the larger (faster) value: 4 in ÷ 18 in × 100 = 22.2%.
- Step 4 — Compare to the 15% tolerance: 22.2% > 15%, so the result does NOT pass.
- Step 5 — Corrective action: partially clamp the feed branch feeding the left (faster) side to slow resin delivery to that region before proceeding to the production infusion.
Answer: Asymmetry is 22.2%, which exceeds the 15% tolerance; the test fails and the feed-network layout must be adjusted before the production infusion.
4. You are mixing infusion vinyl ester for a 2 ft × 3 ft panel (6 sq ft). The instructor's process sheet calls for 0.065 lb of resin per square foot of biaxial glass at the target fiber-volume fraction for this infusion. The resin supplier specifies 1.5% MEKP by weight for the expected shop temperature. Calculate the weight of resin needed and the weight of MEKP to add.
- Step 1 — Calculate resin weight: 6 sq ft × 0.065 lb/sq ft = 0.39 lb of resin.
- Step 2 — Add a reasonable overage for the feed line and trap (typically the process sheet specifies this; assume the instructor specifies 25% overage): 0.39 lb × 1.25 = 0.4875 lb. Round to 0.49 lb.
- Step 3 — Calculate MEKP weight at 1.5% of total resin weight: 0.49 lb × 0.015 = 0.00735 lb.
- Step 4 — Convert MEKP to grams for practical measuring (1 lb = 453.6 g): 0.00735 lb × 453.6 g/lb ≈ 3.3 g of MEKP.
- Step 5 — Verify on the digital scale, measuring MEKP into a separate cup first before combining with resin.
Answer: Approximately 0.49 lb of resin with approximately 3.3 g (0.007 lb) of MEKP; measure MEKP separately before adding to the resin container.
The math in this lesson2
Learners compute resin quantity at 0.065 lb per square foot and flow-front rates across a panel.
6.RP.3G-MG.1
In class: Design exercise: instructor provides scaled drawings of three panel geometries (rectangle, tapered hull section, joggled step); student teams sketch feed-line patterns and vacuum-line placement on the drawings, then present their rationale to the class for critique using ACMA flow-analysis principles. · Controlled-dye infusion: students infuse a flat panel using water-soluble dye mixed into water (no resin) to visualize flow front on a clear plastic mold backing; photographs are taken at 2-minute intervals and compared to the predicted front. · Production infusion of a 2 ft × 3 ft biaxial glass panel using catalyzed vinyl ester; students monitor front progression, adjust clamps on feed lines as needed, and close the resin pot when the vacuum line shows resin arriving.
Materials: Scaled panel-geometry drawings, clear acrylic mold backing for dye test, water-soluble dye, biaxial fiberglass reinforcement (0/90 and ±45), infusion vinyl ester resin, MEKP catalyst, graduated mixing containers, digital scale, digital timer, vacuum pump, spiral wrap, flow media, peel ply, vacuum bag consumables, personal protective equipment
Check: Dye-test photographs reviewed by instructor; front must be within 15% symmetry tolerance for the panel geometry. Production panel is post-cured and cross-sectioned at one corner; instructor inspects for dry spots, gross voids, or resin-starved areas using a 10× loupe. Pass = no dry spots larger than 6 mm and no race-tracking channels visible. ABYC composite laminate quality standard referenced.
Practice check8
Answer each question, then check it. Nothing is recorded; this is your own practice.
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