Cost per Part: Resin Dripping Economics Full Model

Cost per Part: Resin Dripping Economics Full Model

For a junior technician in a plating or surface-treatment factory, resin cost is not simply the price of one drum divided by the number of drops. The useful number is the total cost of producing one accepted part. Incorrect mixing, oversized batches, bubbles, overflow, delayed inspection, and damaged plated hardware can outweigh a small saving on resin.

This guide covers two-component epoxy dispensing into decorative recesses on rigid zinc-alloy bag hardware. Silicone, PVC plastisol, polyurethane, and UV-curable systems need separate recipes. Your responsibility is to measure consumption, follow the released work instruction, identify drift early, and give the supervisor reliable records.

1. Know Which Numbers Are Evidence

No authenticated QLQ resin-dripping batch report was available in the local knowledge base. The comparison below therefore separates published supplier data from an unperformed factory trial. It does not claim measured salt-spray performance for your plated hardware. All later prices, production counts, and control limits are explicitly illustrative planning assumptions, not quotations or universal processing specifications.

The local equipment catalogue, QLQ knowledge base: 03-Equipment Technology / Company Catalogue / Machine Catalogue / Page 25, identifies silicone mixing, vacuum, and dispensing equipment separately from PVC equipment. It provides no epoxy process capability. Never infer epoxy compatibility from a machine name.

2. Working Data: Published Tests and Batch Comparison

Reference or trialMix ratio by massHardness / exposure resultThicknessTest conditionUse in costing
Feroca ClearWater rigid doming epoxy; supplier reference100 A : 30 BPublished Shore D 80Not reportedSupplier lists 24-hour cure and 48–72 hours for full mechanical cure; hardness specimen geometry and method not disclosedReference only; qualify on the actual finish
Fong Yong E-126 / H-100; supplier reference3 A : 1 BPublished Shore D 80; appearance unchanged after salt solution exposureNot reportedHardness at 25°C after seven-day room-temperature cure or 80°C for two hours; salt exposure: 5% NaCl, 24 hours, immersion, not salt sprayReference for cure scheduling; not evidence of corrosion life
Factory control batch A: approved plated hardwareReleased recipePending measurement; record adhesion and defectsPending; measure cured cross-sectionProposed: 30 parts, existing cure schedule, matched witness specimens; record temperature, batch mass, cure ageMeasure resin input and accepted count
Factory trial batch B: smaller mix sizeSame released recipePending measurement; same inspection criteria as APending; same measurement positionsProposed: 30 matched parts; change mix size only; retain identical substrate, application, and cure conditionsCompare cup residue, labor time, and yield

Sources: Feroca product instructions and Fong Yong published technical data. These are external resin references, not QLQ formulations. They use different hardeners and must not share a recipe.

For a customer requiring salt spray, obtain an agreed method, duration, edge treatment, and acceptance criterion before testing the complete plated assembly. Do not translate salt immersion into salt-spray hours. A thin dome on metal also cannot automatically provide a valid bulk Shore hardness reading; use a suitable witness specimen and the agreed test method.

3. Complete Application Formulation: Keep the Chemistry Fixed

The following clear application recipe uses the published Feroca 100:30 mass ratio. It is a complete two-component application mix, not a disclosure of proprietary raw ingredients. The supplier does not publish an allowable ratio tolerance: the nominal value is mandatory. For 130 g mixed material, weigh 100 g A and 30 g B. Approve adhesion to the actual plating or lacquer before release.

ComponentRangeTypicalFunctionReplenishment
Matched epoxy resin AFixed at 100 mass parts; tolerance requires supplier confirmation100 gForms the decorative resin matrixPrepare a fresh weighed batch; keep container closed
Matched hardener BFixed at 30 mass parts per 100 A; tolerance requires confirmation30 gCures the matched resinAdd only before initial mixing; never correct aging mixed resin
Compatible pigment0 for this clear recipe; any colored version requires separate approval0 gColor when separately qualifiedNo addition to this released clear mix
Solvent / water / extra defoamer / filler0 added0 gNo approved role in this application recipeDo not add; use the matched supplied components

Replenishment here means making another fresh batch, not maintaining a reusable plating bath. Unused cured material, wash solvent, and rejected mixed resin belong in separate waste records. Follow the product safety data sheet, suitable gloves and eye protection, and the factory ventilation and waste procedure. Never use an open flame for bubble removal beside chemicals.

4. Build the Cost Model From Weighed Material

Choose one order, one part design, and one accounting period. Record dry cup tare, resin and hardener input, retained mixed residue, usable output, rejects, and rework. Do not estimate shot weight by counting drops: nozzle size, viscosity, and dispensing time change the mass. Weigh ten consecutive shots into a tared cup and divide by ten.

Purchased resin mass, kg = started parts × shot mass, g ÷ [1,000 × material utilization].

Blended price per kg = (100 × A price + 30 × B price) ÷ 130 for the example 100:30 system.

Accepted parts = first-pass accepted parts + successfully recovered rework parts.

Cost per accepted part = (material + labor + energy + consumables + equipment allocation + inspection + incremental rework + irrecoverable hardware loss) ÷ accepted parts.

Material utilization is deposited mass divided by purchased mix consumed, including cup and mixer waste. Yield is accepted pieces divided by started pieces. They are different denominators. If measured purchased consumption already includes waste, do not add another waste percentage. Likewise, rework resin and labor already in measured totals must not be counted twice.

5. A Fully Reconciled Worked Order

This training scenario uses USD solely as an accounting unit. Assume 10,000 started parts, 0.20 g deposited per part, 85% material utilization, and a hypothetical blended resin price of $12/kg. First-pass inspection accepts 9,400 parts. Rework recovers 200 of the remaining 600; 400 plated parts are irrecoverable. Final accepted quantity is 9,600.

Cost categoryCalculation / assumptionOrder cost
Initial resin application10,000 × 0.20 / 1,000 / 0.85 × $12$28.24
Direct labor8 paid operator-hours × $6/hour; hypothetical loaded rate$48.00
Measured energy10 kWh × assumed $0.15/kWh$1.50
ConsumablesCups, wipes, gloves, tips allocated to this order$8.00
Equipment allocationAssumed $2/hour × 4 occupied equipment-hours$8.00
InspectionSeparate inspection labor; excluded from direct labor$6.00
Incremental reworkAdditional resin and labor only; not included above$10.00
Lost plated hardware400 irrecoverable parts × assumed $0.08 incoming value$32.00
Total / accepted part$141.74 / 9,600$0.01476

This is conversion cost plus hardware loss, not the complete selling cost. To include hardware in every accepted part, add its incoming value separately and reconcile any salvage credit. Packaging, freight, administration, and margin are outside this example. Record whether inspection is independent labor or already included in the operator rate.

Equipment allocation should use a consistent productive-hour basis: annual depreciation and maintenance divided by expected productive hours. Electricity is metered energy, not motor nameplate power multiplied blindly by shift duration. Cure occupancy can constrain output even when the dispenser is idle.

6. Trend Bands and Stop Limits

The limits below are proposed internal trial controls for the worked 0.20 g part, not resin-manufacturer guarantees. The engineer must validate and sign them before production. A tighter approved supplier instruction always overrides them. Epoxy mixing is not controlled by the pH bands used for plating baths.

ParameterNormal operating bandDanger / hold thresholdTechnician response
A:B mass ratioNominal 100:30; example internal B check 29.7–30.3 per 100 AOutside the approved tolerance; example outside 29.7–30.3Hold batch; do not assume this internal tolerance is supplier-approved
Room / material temperatureProposed 20–25°COutside approved window; provisional hold below 18°C or above 30°CStabilize unopened materials; escalate cure or flow drift
Mixed batch ageProposed dispensing within 0–10 minutes10–15 minutes: warning; at 15 minutes stop for this reference systemStart timer at first component contact; validate for actual batch mass
Ten-shot meanProposed 0.190–0.210 g/partOutside this released trial band, or any visible overflowHold output since last good check; verify nozzle and settings
Material utilizationPlanning target 85–90%Below 80%: investigation triggerWeigh residue; reduce unnecessary mix size
First-pass yieldPlanning target 94–98%Below 92% in a 100-part sampleHold and separate bubbles, overflow, contamination, and cure defects
Unapproved additions0 g water or solventAny additionQuarantine affected mix and parts

A stable average can hide a single leaking valve. Record individual shot measurements during setup, not only the mean. Consecutive readings moving toward a limit warrant adjustment before rejects accumulate. Pot life must be verified at the actual cup mass and temperature; a supplier reference is not a timer guarantee for a larger batch.

7. Two Practical Troubleshooting Scenarios

Scenario A: Excess resin left in cups

This is a worked scenario, not a claimed customer result. If utilization rises from 85% to 92%, the example order needs 2.174 kg instead of 2.353 kg, saving only about $2.15 at $12/kg. If extra mixing adds half an operator-hour at $6/hour, labor rises $3. Smaller batches then increase total cost despite reducing waste. Trial two batch sizes and record mixing time, residue, accepted count, and bubble defects.

Scenario B: Cheaper resin but more damaged hardware

Again, this is a hypothetical decision example. A $2/kg reduction saves about $4.71 on the original resin quantity. If it produces 100 additional irrecoverable plated rejects at $0.08 each, hardware loss rises $8 and accepted output falls by 100. Reject the saving claim until the same substrate, cure conditions, and inspection criteria demonstrate equal performance. Check cleaner residue, wet parts, and lacquer compatibility before blaming resin price.

8. Engineer Notes

  1. Tare each clean cup and check the scale with an approved reference weight before weighing components.
  2. Separate the A and B transfer tools; label containers and record both lot numbers before mixing.
  3. Prepare clean, dry, level parts before combining components; start the batch timer immediately.
  4. Run a ten-shot weighing check after a tip change, stoppage, or recipe setup; retain the readings.
  5. Use approved mixing and degassing instructions; never dilute thickening mixed resin or add hardener to revive it.
  6. Label each cure tray with start time and recipe; prevent touching or stacking before approved handling release.
  7. Weigh waste separately and classify rejects by cause; preserve suspect samples for the engineer instead of discarding evidence.

9. Shift Checks

Shift stageCheck itemFrequencyAcceptance criterionRecord
Before shiftRecipe, component identity, scale, environment, dry hardwareEvery setup and material lot changeReleased recipe; verified scale; approved conditions; no moisture or contaminationSetup sheet, lot IDs, temperature, reference-weight result
During shiftWeighing ratio and batch timerEvery mixApproved ratio and usable time; no unauthorized additionsA/B masses, contact time, operator
During shiftShot weight and visual defectsFirst ten shots; hourly and after interventionReleased weight band; correct fill, no bubbles or overflow under agreed inspectionIndividual weights and defect counts
During shiftCure trays and witness samplesEvery tray; release check for every batchTraceable cure schedule and agreed acceptance testsTray ID, cure times, inspection sign-off
After shiftMaterial and output reconciliationEvery order / shift closeStarted count equals accepted, rejected, and remaining work-in-process; explain material differencesWaste masses, rework, accepted count, cost sheet

Do not count uncured work-in-process as accepted output. Carry its quantity and cost forward. Keep cleaned hardware and mixed resin away from polishing dust, oil mist, and solvent work; layout discipline protects both quality and the accuracy of the cost model.

10. Questions a Technician Might Ask AI

These are example technician prompts, not authenticated customer quotations.

“AI, why is my cost per part rising when the resin price has not changed?”

Compare deposited shot weight, cup waste, paid hours, accepted count, and incoming hardware loss. Check the denominator first: fewer accepted parts spread the same setup and inspection costs over fewer units. Reconcile one complete order before comparing monthly averages with different product sizes.

“AI, can I add less hardener to make the resin last longer?”

No. Keep the matched supplier ratio. Change batch size, staging, or approved temperature control instead. Quarantine incorrectly mixed material. Ask the engineer to verify actual working time at your cup mass; changing hardener quantity is not an authorized cost-saving adjustment.

“AI, is Shore D 80 enough to prove my resin-coated hardware will pass salt spray?”

No. Hardness describes a polymer property, not the corrosion performance of the complete plated assembly. Qualify adhesion, edges, underlying finish, and cure using the customer's agreed tests. Published salt immersion results cannot substitute for your required salt-spray report.

11. What Would You Like to Solve?

Bring the problem down to one traceable order: part geometry, existing plating or lacquer, resin identity, shot weights, waste masses, cure records, and defect photographs. That information lets an engineer distinguish dispensing loss from substrate failure or incomplete cure.

For a process review, email [email protected] with your records and acceptance requirements. See surface-treatment line equipment, chemicals, and process support when upstream cleaning or finishing may be contributing to the issue. The objective is a verified lower cost per accepted part, without weakening the released recipe or quality standard.

Cost per Part: Resin Dripping Economics Full Model A twelve-second schematic follows controlled resin dispensing, curing and inspection. All batch costs, including losses, are divided by accepted parts, not total parts started. Use measured batch costs and accepted output; no prices or process settings are assumed. Resin dripping: cost per good part Track material, time and yield over the same batch. Schematic process — not a curing recipe. 1 / Meter the dose Net dose + purge / waste 2 / Cure the resin Energy + occupied capacity 3 / Inspect output Accepted parts Reject / rework Count only accepted output 4 / Calculate unit cost Total batch cost Accepted parts = Cost per good part Lower yield raises unit cost. Batch cost = resin used + labor + energy + consumables + allocated equipment / overhead Include purge, scrap and rework costs once; do not divide by all parts started. Use actual measured batch data.
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