Worked Example: Class 5 to Class 3 Estimate
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This page walks through a complete estimating sequence — from the first phone call through a GMP proposal — using a single realistic project. Every number is shown, every decision is explained, and every place where senior judgment is required is flagged.
Read this alongside Phase-by-Phase Workflow, which covers the process steps. This page covers the numbers.
The Project
Section titled “The Project”Project: Midwest Beverage Co. — Production Line Addition Owner: Regional still beverage manufacturer (juices, teas, functional drinks) Location: Chicago, IL metropolitan area Scope: 20,000 SF addition to existing 80,000 SF beverage processing facility + installation of one new 600 BPM still beverage filling line Delivery: Design-Build (GC as design-builder; A/E and process engineer engaged by GC) Schedule: GMP in 10 weeks; construction 14 months Pricing date: Q1 2026
What the owner told you (Day 1, phone call):
- “We need to add a filling line. Probably around 600 bottles per minute for 20 oz still beverages.”
- “We’ll need a new building addition — maybe 20,000 SF.”
- “We want to keep running during construction.”
- “We’d like a number by Friday.”
Phase 1: Class 5 ROM (Day 1–2)
Section titled “Phase 1: Class 5 ROM (Day 1–2)”What You Have
Section titled “What You Have”- Project narrative (phone call)
- Satellite photo of the facility from Google Maps
- Owner’s previous project costs (“we built a similar addition 4 years ago for about $9M but that was before inflation”)
- No drawings. No equipment quotes. No geotech.
Method: $/SF Parametric + Equipment ROM
Section titled “Method: $/SF Parametric + Equipment ROM”Step 1: Classify the project and select the benchmark.
This is a brownfield F&B beverage filling line addition. From Food and Beverage:
- “Expansion line addition (existing facility): $150–$350/SF (TIC)”
- This range includes building + process utilities but NOT the major filling line equipment, which is priced separately.
Chicago is a union market. Apply a market premium to the mid-range: use $200/SF for the building and utility scope.
Step 2: Price the building and utilities.
| Item | Calculation | Amount |
|---|---|---|
| Building + process utilities (parametric) | 20,000 SF × $200/SF | $4,000,000 |
Step 3: Price the equipment.
Owner says 600 BPM still beverage filling line. Based on experience and market knowledge:
- Complete filling line (filler, capper, labeler, inspector, case packer, palletizer, stretch wrapper, accumulation conveyors) at 600 BPM: $1.5M–$2.2M FOB for this type and rate.
- Use $1.8M FOB as the mid-point.
- Installation factor: 1.5× FOB for a complete filling line (mechanical hookups, electrical, integration): $2.7M TIC for equipment.
Wait — the $200/SF parametric for the building already includes typical process utilities for this project type. It does NOT include the specific filling line equipment. Use the equipment separately.
Step 4: Add soft costs.
Soft costs (design/engineering + permits + insurance + testing): typically 10–14% for a brownfield F&B project. Use 12%.
| Item | Calculation | Amount |
|---|---|---|
| Building + utilities | 20,000 SF × $200/SF | $4,000,000 |
| Filling line (FOB) | ROM | $1,800,000 |
| Filling line installation | 0.5 × FOB | $900,000 |
| Subtotal before soft costs | $6,700,000 | |
| Soft costs (12%) | $6,700,000 × 0.12 | $804,000 |
| Subtotal before contingency | $7,504,000 |
Step 5: Apply Class 5 contingency.
AACE Class 5 accuracy: -50% / +100%. For a brownfield project with unknown conditions, use the higher end of contingency: 35%.
| Item | Amount |
|---|---|
| Subtotal before contingency | $7,504,000 |
| Class 5 contingency (35%) | $2,626,000 |
| CLASS 5 ROM | $10,130,000 |
How to present this:
“ROM estimate: approximately $10M, with a Class 5 accuracy range of $7M–$15M. This is based on parametric benchmarks and a rough equipment estimate. Accuracy improves significantly once we have a floor plan and equipment vendor quotes.”
Do NOT: Give a single number without the range. Do NOT say “the project costs $10M.” Say “the ROM is $10M with a ±range.”
Senior judgment applied here:
- Choice of $200/SF (mid-to-upper range) vs. $175/SF (mid-range). Chicago union market, brownfield premium, and beverage utility complexity all push toward the upper end.
- Equipment FOB of $1.8M. A junior estimator will look up “beverage filling line cost” and find wide variance. A 600 BPM still beverage line for 20 oz PET bottles is a commodity machine — this is reasonable.
- Contingency of 35% vs. 25%. With no geotech, no drawings, and a brownfield site, 35% is appropriate.
Phase 2: Class 4 Feasibility (Weeks 3–4)
Section titled “Phase 2: Class 4 Feasibility (Weeks 3–4)”What You Have Now
Section titled “What You Have Now”- Preliminary floor plan (30% sketch — enough to verify 20,000 SF and room layout)
- Owner’s equipment list: 1 filling line, 600 BPM still beverage, 20 oz PET; owner has sent an RFQ to KHS and Krones
- Preliminary process utility sizing from the process engineer: steam (2,000 lb/hr), CAS (200 SCFM), chilled water (120 tons)
- Budget quotes from the mechanical sub and electrical sub (30-day verbal estimates)
- Filling line vendor budget quote received from KHS: $1,620,000 FOB
Method: Equipment-Factored + Building Assembly + Utility Packages
Section titled “Method: Equipment-Factored + Building Assembly + Utility Packages”Now you price each major system separately, using actual vendor data where you have it.
Equipment:
| Item | Source | Amount |
|---|---|---|
| Filling line FOB (KHS budget quote) | Vendor | $1,620,000 |
| Installation (0.5 × FOB) | Factor | $810,000 |
| Equipment subtotal | $2,430,000 |
Building — assembly level from preliminary floor plan:
| Item | Quantity | Rate | Amount |
|---|---|---|---|
| Metal building structure | 20,000 SF | $20/SF | $400,000 |
| Foundation / slab on grade | 20,000 SF | $5/SF | $100,000 |
| Building envelope (walls + roof) | 20,000 SF | $23/SF | $460,000 |
| Doors, hardware, accessories | LS | — | $45,000 |
| Building subtotal | $1,005,000 |
Process utilities — preliminary sizing:
| Item | Basis | Amount |
|---|---|---|
| Steam system (tie-in from existing boiler, 20,000 SF distribution) | $8/SF | $160,000 |
| Compressed air (header extension + dryer upgrade, 200 SCFM) | $10,000/SCFM × 200 | $200,000 |
| Chilled water (tie-in + distribution, 120 tons) | $600/ton | $72,000 |
| CIP skid (1 CIP skid for filling line) | Budget | $175,000 |
| Process drains + sanitary floors | 20,000 SF × $12/SF | $240,000 |
| Utilities subtotal | $847,000 |
Mechanical and electrical subs:
| Item | Source | Amount |
|---|---|---|
| HVAC (budget quote from mechanical sub) | Sub 30-day verbal | $265,000 |
| Plumbing (process drains) | Sub 30-day verbal | $185,000 |
| Electrical — MCC, feeders, lighting (budget quote from electrical sub) | Sub 30-day verbal | $385,000 |
| MEP subtotal | $835,000 |
Site/civil (minimal — brownfield, existing pavement adequate):
| Item | Amount |
|---|---|
| Minor site grading + tie-in to existing pavement | $75,000 |
General Conditions: 5% of direct cost
| Item | Basis | Amount |
|---|---|---|
| General conditions | 5% × $5,192,000 | $260,000 |
Direct cost subtotal:
| Category | Amount |
|---|---|
| Equipment | $2,430,000 |
| Building | $1,005,000 |
| Process utilities | $847,000 |
| MEP | $835,000 |
| Site/civil | $75,000 |
| General conditions | $260,000 |
| Direct cost subtotal | $5,452,000 |
Soft costs:
| Item | Amount |
|---|---|
| Design/engineering (8% of direct) | $436,000 |
| Permits + insurance + testing | $65,000 |
| Contractor fee (5% of direct) | $273,000 |
| Soft cost subtotal | $774,000 |
Subtotal before contingency: $6,226,000
Class 4 contingency (20%): $1,245,000
CLASS 4 ESTIMATE: $7,471,000
Presented as: $7.5M, accuracy range $6M–$9.5M (AACE Class 4)
Why did the estimate drop from $10M to $7.5M?
- The parametric $/SF in Class 5 used the upper-middle of a wide range; it included headroom for a more complex utility scope.
- The KHS equipment quote came in at the lower end of the FOB range ($1.62M vs. $1.8M estimated).
- The process engineer’s utility sizing confirmed this is a relatively low-complexity beverage operation — steam load is modest, no ammonia refrigeration, no CIP cleaning of complex circuits.
- The $10M ROM was not wrong. A Class 5 estimate for this project type with no information SHOULD carry a large range. $7.5M is within the -50%/+100% accuracy of $10M.
Phase 3: Class 3 GMP Candidate (Weeks 8–10)
Section titled “Phase 3: Class 3 GMP Candidate (Weeks 8–10)”What You Have Now
Section titled “What You Have Now”- 35% design drawings: preliminary floor plan, grading plan, structural framing concept, electrical one-line, mechanical HVAC concept
- P&ID: 60% complete; equipment and major piping confirmed; some instrument tags still TBD
- Sub quotes: formal packages sent at Week 5; quotes received from 2–3 subs per trade
- Equipment: KHS filling line quote firmed at $1,625,000 FOB; payment terms 30%/30%/30%/10%
- Geotech report received: soil bearing capacity confirmed at 2,500 PSF (adequate for this project)
- No hazmat found (Phase I ESA complete; Phase II not needed)
- Key discovery: existing electrical switchgear at 70% capacity; new 2,000A MCC required at $402,000 (confirmed by sub)
Method: Bottom-Up by CSI Division with Sub Quotes
Section titled “Method: Bottom-Up by CSI Division with Sub Quotes”Detailed estimate:
| Division | Description | Amount |
|---|---|---|
| 01 | General Conditions — 14 month superintendent + PM + facilities | $372,000 |
| 02/31 | Site work — minor; tie-in to existing pavement, new curb | $62,000 |
| 03 | Concrete — 20,000 SF SOG sanitary spec ($8.50/SF) + 6 equipment pads | $197,000 |
| 05 | Structural steel — metal building frame, 20,000 SF @ $19/SF | $380,000 |
| 06/07 | Building envelope — metal wall panels + TPO roof | $460,000 |
| 08 | Doors, windows, hardware | $62,000 |
| 09a | FRP wall panels — wet process area, 4,000 SF @ $14/SF | $56,000 |
| 09b | Epoxy floor — wet areas, 6,000 SF @ $10/SF | $60,000 |
| 09c | Standard floor — dry areas, 14,000 SF @ $3.50/SF | $49,000 |
| 22a | Process drains + floor drain system | $185,000 |
| 22b | Domestic plumbing | $38,000 |
| 23 | HVAC — food zone AHUs + exhaust (sub quote, low bid) | $278,000 |
| 26 | Electrical — 2,000A MCC + feeders + lighting (sub quote, low bid) | $402,000 |
| 40a | Process interconnecting piping — stainless, beverage grade | $192,000 |
| 40b | Tie-in allowance — 8% of Div 22+23+26+40 process mechanical scope | $86,000 |
| 43a | Steam system extension | $138,000 |
| 43b | Compressed air extension + dryer upgrade | $115,000 |
| 43c | CIP skid + piping (1 circuit) | $195,000 |
| 43d | Chilled water tie-in | $78,000 |
| 41 | Filling line installation — vendor-supervised; GC mechanical hookups + rigging | $248,000 |
| Equipment | Filling line FOB — KHS firm quote | $1,625,000 |
| DIRECT COST TOTAL | $5,278,000 |
Soft costs:
| Item | Basis | Amount |
|---|---|---|
| Design/engineering | 8% of direct | $422,000 |
| Permits + testing + special inspections | — | $52,000 |
| Contractor fee | 5% of direct | $264,000 |
| Soft cost subtotal | $738,000 |
Pre-contingency total: $6,016,000
Contingency — risk-based breakdown:
| Risk Category | Basis | Amount |
|---|---|---|
| Design development | 35% design; instrumentation not complete; some architectural details TBD | $175,000 |
| Execution risk | Brownfield tie-in work; existing building conditions could differ from drawings | $210,000 |
| Market / escalation | 9-month construction window; steel and copper exposed; Q1→Q3 2026 escalation | $130,000 |
| Total contingency | $515,000 |
GMP: $6,531,000 (contingency = 8.6% of pre-contingency cost)
Presented as:
GMP Proposal: $6,531,000 AACE Class 3 | Accuracy: -15% / +20% | Pricing Date: Q1 2026 Contingency: $515,000 (8.6%) | Design completion: ~35%
The Estimate Progression — Summary
Section titled “The Estimate Progression — Summary”| Phase | Method | Estimate | Accuracy Range |
|---|---|---|---|
| Class 5 ROM | $/SF parametric + equipment ROM | $10,130,000 | $7M – $15M |
| Class 4 Feasibility | Equipment-factored + assembly | $7,471,000 | $6M – $9.5M |
| Class 3 GMP Candidate | Bottom-up with sub quotes | $6,531,000 | $5.5M – $7.8M |
All three ranges overlap. This is correct — it confirms each estimate was calibrated appropriately and no phase made an inexplicable jump. The downward progression from Class 5 to Class 3 is normal: Class 5 included headroom for conditions that turned out to be favorable (clean site, modest utility scope, vendor quote at the low end).
What Would Have Changed This Estimate
Section titled “What Would Have Changed This Estimate”Higher:
- Geotech showed soft soil requiring deep foundations (+$200K–$600K)
- Hazmat found in the expansion area (+$100K–$400K abatement)
- Filling line vendor quote came in at $2.2M FOB (added $580K to GMP)
- Owner required full ammonia refrigeration instead of chilled water (+$400K)
- Winter construction schedule triggered cold-weather concrete protection (+$80K)
Lower:
- Owner self-performed controls integration (removed ~$60K from electrical scope)
- Existing electrical capacity was adequate (removed the $402K MCC and used existing panels at a $180K scope instead)
- Owner furnished and installed (OFOI) the CIP skid (removed $195K from GMP)
These scenarios are real. On a real project, you document the assumptions that could swing the estimate in each direction, put them in the BOE, and set your contingency accordingly.
Key Lessons From This Example
Section titled “Key Lessons From This Example”-
Class 5 is always wider than it feels. The owner asked for a number on Day 1. The right answer was $10M ± a very wide range, not $10M as a commitment. Never let a Class 5 get treated as a budget.
-
The equipment quote is the most important single piece of new information. Going from ROM to a vendor budget quote reduced the estimate range more than anything else.
-
Brownfield tie-ins need their own line item. The $86,000 tie-in allowance is visible in the GMP. If it were buried in the MEP divisions, it would disappear under scope creep.
-
Contingency should be built from a list, not a %, even at Class 3. The three risk categories (design development, execution, market) are named and sized independently. When contingency is drawn down during construction, you know which bucket it’s coming from.
-
The estimate progression is a communication tool. The owner sees the estimate improve at each phase. The widening uncertainty → tightening accuracy → GMP commitment tells a coherent story about what was known when.
Related Pages
Section titled “Related Pages”- Estimate Classification and BOE — AACE Class 1–5 definitions and BOE structure
- BOE Template — fill-in template for the BOE accompanying this estimate
- Phase-by-Phase Workflow — the project workflow this estimate sequence follows
- Food and Beverage — F&B-specific benchmarks used in the parametric
- Parametric Estimating Models — formal parametric methods behind the Class 5 $/SF approach
- Risk Contingency and Escalation — how to build a risk-based contingency register
- Scope Misses Checklist — what to check before submitting the GMP
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