Extraction versus blending
Clarify whether the operation extracts from raw material, receives an extract / concentrate or blends prepared ingredients. These create different equipment, solids, waste and cleaning interfaces.
Separate extraction or blending requirements, ingredient / flavor behavior, qualified preservation, package interfaces and launch demand before adapting a beverage line.

Start with the business outcome
A coffee or tea product launch is a product / package feasibility project before it is an equipment purchase. DPS’s process engineering, utilities, controls and integration services can be evaluated against the actual project interfaces. Confirm product-specific experience, extraction / treatment equipment and qualified responsibilities rather than assuming every coffee, tea or cold-brew product shares one processing route.
Qualified formulation, extraction / brewing, preservation and packaging specialists establish product conditions, shelf life and release. No universal cold-brew safety process, extraction setting, DPS specialty-equipment manufacturing claim or published launch return is supplied.

Clarify whether the operation extracts from raw material, receives an extract / concentrate or blends prepared ingredients. These create different equipment, solids, waste and cleaning interfaces.
Define coffee / tea solids, milk or plant ingredients, sweeteners, acidity, flavor and intended distribution. Recipe appearance or the word cold brew does not establish a preservation route.
Specify container, closure, qualified process, campaigns, trial / customer acceptance and demand. Product launch volume should not be confused with the retained line’s theoretical unused hours.
Resolve ingredient and preservation / package responsibilities before layout or capex.
Compare actual mixing, thermal / cold, transfer, filler and cleaning duties.
Coordinate plant trials, launch inventory, customer acceptance and real demand ramp.
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| System | Operating duty | Relevant DPS guide | Confirm before purchase |
|---|---|---|---|
| Process engineering | Turn measured requirements into an interface and duty specification. | Process engineering ↗ | Actual product envelope, baseline data, qualified trials and responsibilities. |
| Configured process vessels | Provide the specified working volume, mixing / holding and connections. | Tanks and vessels ↗ | Working duty, material, agitation, residence, cleaning and access. |
| Utility supply and return | Meet the duty where the process actually uses it. | Utility infrastructure ↗ | Peak overlap, recovery, quality, point-of-use conditions and isolation. |
| OEM and field interfaces | Connect the selected equipment to the existing operating train. | Installation & integration ↗ | Mechanical, electrical, software, site access and integrated acceptance. |
Project suitability and a qualified product / package route must be established for each alternative before comparing cost.
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| Decision | What to compare | Acceptance evidence |
|---|---|---|
| In-house extraction | Raw material, specialist equipment, solids / waste and cleaning | Qualified product route and complete operating boundary. |
| Concentrate / ingredient blending | Supplier material, mixing, preservation / package and inventory | Accepted product and correct purchased-material / working-capital cost. |
| External production alternative | Qualified product, package, supplier capacity and commercial terms | Matched landed contribution, launch risk and owner cash need. |
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| Observed condition | Measure before design | DPS / team decision | Economic basis |
|---|---|---|---|
| Undefined extraction / blending | Clarify material and specialist process duty. | Select qualified trials before equipment. | Avoid an invalid or incomplete capital boundary. |
| Retained-line mismatch | Observe full-route product and package response. | Compare adaptation or specialist packages. | Accepted launch product at real demand. |
| Launch underutilization | Use qualified customer and campaign forecast. | Phase commercial and capital gates. | Contribution after added fixed and variable cost. |
| Running-line interruption | Cost uncovered retained-production exposure. | Plan controlled tie-ins and trials. | One-time outage separate from new-product ramp. |
Clarify in-house extraction versus purchased extract / concentrate, then test the qualified product / package against retained mixing, treatment, transfer, filling and cleaning. Define only supported equipment and interface changes.
Compare a dedicated extraction / process train or an appropriately qualified external producer where retained equipment, specialist treatment, transitions or commercial scale does not fit. Confirm each actual process and package route.
Compare proposals with the same product duty, supplier boundaries and acceptance basis. The amount below is a transparent planning example, not a market price range, supplier estimate or DPS quotation.
| Cost bucket | Assumed amount |
|---|---|
| Product / process gap and supplier engineering | $60,000 |
| Defined blending / transfer / specialist interface components | $200,000 |
| Mechanical / electrical installation | $110,000 |
| Recipe and package-interface controls | $70,000 |
| Commissioning and agreed product-trial support | $45,000 |
| Training and documentation | $15,000 |
| Defined project scope | $500,000 |
| Separate site / facility additions | $85,000 |
| Capital contingency (15%) | $87,750 |
| Separate one-time startup / shutdown cost | $65,000 |
| Incremental working capital | $100,000 |
| Total initial cash | $837,750 |
The defined scope assumes applicable freight, procurement charges and taxes are included in the owner’s estimate. Add missing civil, land / shell, OEM, environmental, validation and permitting costs explicitly. Site and field conditions, duty, production access and quoted supplier scope determine actual price. Financing is excluded.
Hypothetical screening case: 250 days × 0.5 equivalent useful hour/day × 1,500 accepted kg/h × 60% realization, capped at 100,000 kg incremental demand, gives 100,000 additional sold kg/year. Net price $4.2/kg less incremental variable cost $2.6/kg gives $1.6/kg contribution. Verified baseline purchase savings are $0, realized payroll savings $0, energy $0, cleaning resources $0 and maintenance $0 per year. Deduct $85,000 additional annual fixed cost. This new-SKU example does not claim historical savings from the new coffee / tea product. The $85,000 added annual fixed cost includes assumed fixed launch staffing, support and overhead beyond variable production cost. The $65,000 startup boundary includes $57,600 retained-product outage exposure plus $7,400 independent launch expense; new-product operating ramp is separate. Annual capacity counterfactual: this illustrative default assumes a schedule study has verified 0.5 usable idle or recovered hour/day after required cleaning, holds and existing orders; the new SKU does not displace any current contribution-generating order. Confirm that spare window, downstream availability and incremental demand before using the result. If new-product volume replaces an existing profitable SKU, subtract the foregone baseline contribution as an explicit opportunity cost or rebuild the model around the net contribution difference. Do not count the new product’s gross contribution unadjusted; set unsupported incremental hours or demand to zero.
Calculated from these assumptions: steady annual net benefit $75,000; year-one net cash −$13,000; cash payback Beyond 5 years; five-year NPV at 10% is −$633,441. Change the assumptions below to test a different case.
Replace the illustrative inputs with your own measured or quoted values. The five-year pre-tax model uses good kilograms, demand-capped contribution and separately verified baseline savings; it is not a project quotation.
All defaults are illustrative. The default case is an operating-plant improvement, not a greenfield quote. For a new operation, set baseline savings to zero and enter every additional operating and capital cost.
Includes contingency, startup and working capital
Incremental operating cash before tax
Includes year-one ramp assumption
At 10% annual discount
Net annual benefit ÷ initial cash
Net cumulative gain ÷ initial cash
Modeled incremental sales: 100,000 kg/year at $1.60/kg contribution. The demand ceiling limits sales. The base case does not recover the required discounted return within five years. Year-one net cash: −$13,000.
Realization needed for the target operating payback
Not feasible
Demand, time, contribution or other cash benefits cannot meet the 4-year target under these assumptions.
CSV export is local. No inputs are submitted.
Swipe the chart to compare all five years ↔
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| Year | Net cash | Cumulative cash | Discounted cash |
|---|---|---|---|
| Initial | −$837,750 | −$837,750 | −$837,750 |
| Year 1 | −$13,000 | −$850,750 | −$11,818 |
| Year 2 | $75,000 | −$775,750 | $61,983 |
| Year 3 | $75,000 | −$700,750 | $56,349 |
| Year 4 | $75,000 | −$625,750 | $51,226 |
| Year 5 | $75,000 | −$550,750 | $46,569 |
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| Case | Annual benefit | NPV | Cash payback |
|---|---|---|---|
| Downside | $23,000 | −$939,112 | Beyond 5 years |
| Base | $75,000 | −$633,441 | Beyond 5 years |
| Upside | $91,000 | −$580,788 | Beyond 5 years |
Downside: installed and site costs +20%, realization ×0.75 and unit contribution reduced by 20% of its absolute value. Upside: realization ×1.15, capped at 100%, and unit contribution improved by 10% of its absolute value. The demand ceiling still applies.
Initial cash = (defined project scope + site additions) × (1 + contingency) + separate startup / shutdown cost + working capital. Contingency is conservatively treated as spent initially.
Sold incremental kg = min(days × recovered hours/day × constrained good kg/hour × realization, incremental demand). Contribution = sold incremental kg × (net price − incremental variable cost). New-volume labor, energy and packaging belong in that variable cost.
Baseline material benefit uses the verified percentage of actual purchases avoided at unchanged accepted baseline output. It is not a direct subtraction of two loss rates. Count a recovered kilogram once, either as its applicable cash saving or as incremental contribution.
Net annual benefit = contribution + independently realized baseline cash savings − added fixed operating cost. Year one scales gross benefits by the ramp factor while paying the full added fixed operating cost. Do not also count the same launch loss in the one-time startup amount.
Cash ROI = net annual benefit / initial cash. Five-year net ROI = (five-year cash inflows − initial cash) / initial cash. NPV = −initial cash + Σ cash flow(t)/(1 + discount rate)^t. Payback uses annual cash with linear interpolation within the recovery year. The threshold solver excludes terminal working-capital recovery.
This is a five-year screening horizon, not an asset’s entire life. No tax, debt, depreciation, grants, escalation, asset resale or additional replacement capital is modeled. Include recurring service costs in operating expense and use a detailed monthly budget for formal capital approval.
The selected shorter plan exposes 48 baseline hours × $1,200 = $57,600, included in the main startup boundary. A 24-hour reduction is worth $28,800 versus $23,000 extra execution cost including contingency: $5,800 one-time difference, not recurring new-product profit. The annual new-SKU capacity case separately assumes 0.5 verified idle or recovered hour/day without displacing current profitable orders. This worksheet does not prove that spare annual capacity. Any displaced baseline contribution must be deducted or the counterfactual rebuilt; the one-time tie-in exposure remains separate.
Use representative products, measured constraints and a documented utility / cleaning envelope. Assign each supplier and owner interface.
Plan FAT / SAT, instruments, recipes, permissives, quality checks and upstream / downstream handshakes as appropriate to the scope.
After stabilization, compare matched products and operating conditions. Reconcile extra output with sales, and baseline savings with actual purchases, bills and payroll.

Published scope / project context
This is a product-specific feasibility guide using original hypothetical launch economics. It does not represent an established DPS coffee extraction, cold-brew preservation or customer ROI capability.
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| Decision | Targeted intervention | Broader replacement / new operation |
|---|---|---|
| Constraint | A measured gap can be corrected within retained assets. | The verified operating envelope cannot meet product, demand or reliability needs. |
| Cost scope | Include engineering, interfaces, shutdown, commissioning and retained-asset risk. | Include all new systems, site / facility work, OEMs, utilities, ramp and working capital. |
| Benefit | Only incremental contribution and genuinely avoided costs versus the current operation. | Demand-supported contribution less the full additional operating cost versus the agreed alternative. |
| Acceptance | Verify the changed duty and its effect on the complete line. | Verify the integrated new train and the owner’s readiness to operate. |
Prepare the information below, export the assumptions you have modeled, and discuss the unknowns with DPS. An unmeasured input is a question to resolve, not a reason to invent precision.
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The DPS engineering scope provides a basis for defining ingredients, product / package requirements, utilities and equipment interfaces. Coffee / tea-specific experience and specialist process responsibilities require confirmation; no achieved DPS launch case is claimed.
Guide assumptions reviewed on 26 October 2026. Qualified site / product teams establish regulatory and food-safety requirements; this guide does not prescribe a validated process.

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