Black Coffee and Tea RTD
Define extraction from raw material versus use of purchased extract, solids / filtration, quality targets and storage objective. These choices change the equipment and site cost fundamentally.
Define extraction or blending, product treatment, storage and packaging before scoping an RTD coffee, tea or botanical beverage line.
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Define extraction from raw material versus use of purchased extract, solids / filtration, quality targets and storage objective. These choices change the equipment and site cost fundamentally.
The added base changes hydration, emulsion / stability, heat behavior, allergens and cleaning. Trial the actual formula through the selected preservation and package route.
Plant particles, oils, flavor carryover and ingredient sensitivity may require different filtration, mixing and transfer duties. Confirm product identity and qualified acceptance with specialists.
Compare the processing boundary rather than pricing a blend tank as if it included extraction.
Coordinate recipe, ingredients, qualified preservation, cooling and package interfaces.
Record recipe setup, transfer residue, qualified cleaning, release and package change time.
Review each system by its operating duty and the interfaces to be agreed before procurement.
Purchased-extract / ingredient blending duty.
Defined flavor / base transition circuits.
Heating / cooling and return interfaces.
Extraction, filtration, treatment and packaging OEMs.
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| System | Operating duty | Relevant DPS guide | Confirm before purchase |
|---|---|---|---|
| Configured tanks / vessels | Purchased-extract / ingredient blending duty. | DPS tanks & vessels ↗ | Actual formula, viscosity and approved holding. |
| CIP equipment and circuit interfaces | Defined flavor / base transition circuits. | DPS CIP systems ↗ | Soil, manual tasks and qualified verification. |
| Process utilities and distribution | Heating / cooling and return interfaces. | Utility infrastructure planning ↗ | Actual qualified duty and simultaneous use. |
| Specialist equipment interfaces | Extraction, filtration, treatment and packaging OEMs. | Installation & integration ↗ | Explicit responsibilities and full product / package trials. |
Before requesting equipment prices, state whether the plant processes raw beans / leaves or receives an ingredient extract. Then define product quality, ingredient sensitivity, preservation, package and cleaning. This prevents a low blend-room estimate from being compared with a supplier’s much broader extraction and packaging project.
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| Buying question | Evidence to prepare | Engineering decision |
|---|---|---|
| Extract in-house or buy concentrate? | Ingredient supply, quality, demand and complete cost boundary. | Compare raw handling / extraction / waste with ingredient purchase. |
| Can retained thermal and filler packages be used? | Representative full-process and package evaluation. | Qualified OEM / product team confirms suitability. |
| Does a botanical recipe share the same duty? | Particles, oils, sensitivity and transition requirements. | Define compatible routes and added trial / equipment scope. |
Start with the business outcome
A coffee or tea brand may need an equipment project when extraction, ingredient addition, cooling, treatment or package changeovers limit production. Start by defining which of those duties actually belongs in the plant. DPS can discuss process / utility / controls and installation interfaces for an agreed scope; qualified product and specialist suppliers must establish extraction, formulation and preservation requirements.
Confirm the exact coffee & tea beverage product, preservation route and project suitability with DPS before assigning a delivery scope. Confirm extraction, concentration, aroma management, dairy or plant-base blending, thermal / aseptic packages, filling and shelf-life responsibilities before claiming suitability. A coffee / tea project is assessed on its actual recipe and package; this guide does not establish DPS manufacture of extraction or aseptic technology.
Agree whether raw-material extraction or purchased-extract blending is included, together with solids, filtration, quality and storage requirements.
Check milk or plant-base additions, botanical particles, heat behavior and package compatibility with the relevant ingredient and equipment specialists.
Confirm product identity, qualified cleaning, ready-product availability and accepted packaged output across the agreed beverage families.

Review the scope, cost assumptions and operating case for your project. The examples and calculators below support early planning and are not DPS quotations.
Check whether the retained operation already has the required ingredient and preservation boundary. Measure actual batch / release / package constraints before selecting a targeted adaptation.
Choose extraction or bought-extract scope, formula families, qualified preservation / package route, demand, utilities and waste basis first.
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| Observed condition | Measure before design | DPS / team decision | Economic basis |
|---|---|---|---|
| Slow ingredient preparation | Actual extraction / bought-extract and blend cycle records. | Define the process boundary and limiting step. | Useful good output with downstream / demand. |
| Unstable product after treatment | Qualified formula / process / package trials. | Resolve ingredient and specialist duty before scaling. | Verified baseline reject cost, not assumed full selling-price savings. |
| Long flavor changes | Full qualified transition and resource records. | Coordinate routing, recipes and CIP interfaces. | Independent resource and realized capacity effects. |
| Unclear new-line scope | Extract vs raw processing and site interfaces. | Compare matched installed alternatives. | Include missing waste, utilities, OEM and launch costs. |
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| Decision | Targeted Work | Broader Scope |
|---|---|---|
| Ingredient Boundary | Improve blending around a qualified purchased extract. | Include extraction, raw handling and specialist filtration when required. |
| Formula Compatibility | Trial additions through retained treatment and packaging. | Integrate different specialist duties for incompatible product requirements. |
| Flavor Changes | Correct routing, recipes and cleaning interfaces. | Add capability where the approved product families need separate duties. |
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 and interface engineering | $42,000 |
| Defined configured / OEM component allowance | $147,000 |
| Mechanical / electrical field installation | $81,000 |
| Instrumentation and control integration | $42,000 |
| Commissioning and acceptance support | $25,000 |
| Training, documentation and closeout | $13,000 |
| Defined project scope | $350,000 |
| Separate site / facility additions | $50,000 |
| Capital contingency (15%) | $60,000 |
| Separate one-time startup / shutdown cost | $35,000 |
| Incremental working capital | $25,000 |
| Total initial cash | $520,000 |
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 owner-budget case: 250 days × 0.5 useful recovered hour/day × 900 good kg/h × 60% realization gives 67,500 incremental sold kg/year after the 90,000 kg demand ceiling. Net price $4/kg less incremental variable cost $2.6/kg gives $1.4/kg contribution. The baseline inputs assume $14,000 energy, $12,000 water / chemistry and $5,000 maintenance reductions per year. Avoided payroll is 0 hours × $40 × 0% cash realization. Verified baseline purchase reduction contributes $0; its basis is unchanged accepted baseline output. Deduct $16,000 added annual fixed cost. Result: $109,500 steady net benefit; initial cash $520,000 includes the separate site, contingency, startup and working-capital inputs. These are original illustrative assumptions, not a quotation, price benchmark or achieved DPS result.
Calculated from these assumptions: steady annual net benefit $109,500; year-one net cash $59,300; cash payback Beyond 5 years; five-year NPV at 10% is −$150,545. 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: 67,500 kg/year at $1.40/kg contribution. The base case does not recover the required discounted return within five years. Year-one net cash: $59,300.
Realization needed for the target operating payback
63.1%
Minimum capacity realization for a 5-year operating cash payback; terminal recovery excluded. Demand and unit margin must also hold.
CSV export is local. No inputs are submitted.
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| Year | Net cash | Cumulative cash | Discounted cash |
|---|---|---|---|
| Initial | −$520,000 | −$520,000 | −$520,000 |
| Year 1 | $59,300 | −$460,700 | $53,909 |
| Year 2 | $109,500 | −$351,200 | $90,496 |
| Year 3 | $109,500 | −$241,700 | $82,269 |
| Year 4 | $109,500 | −$132,200 | $74,790 |
| Year 5 | $109,500 | −$22,700 | $67,991 |
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| Case | Annual benefit | NPV | Cash payback |
|---|---|---|---|
| Downside | $71,700 | −$372,091 | Beyond 5 years |
| Base | $109,500 | −$150,545 | Beyond 5 years |
| Upside | $134,542 | −$64,721 | 4.31 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.
The default reproduces the main retrofit energy input of $14,000/year before added maintenance. The narrow worksheet is not a product-process calculation and does not automatically transfer values into the ROI model. Additional annual service is included in the main added-fixed-cost allowance; deduct it once.
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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Separate extraction or blending requirements, ingredient / flavor behavior, qualified preservation, package interfaces and launch demand before adapting a beverage line.
Bring your product requirements, operating priorities and site constraints to an initial scope discussion with DPS.