Broth / Savory Bases
Specify dissolved and suspended ingredients, fat behavior, target concentration and intended customer dilution. Accepted consistency and flavor distribution must survive hold, transfer and filling.
Foodservice Base & Concentrate Processing
Define concentration, reconstitution / customer performance, cooking / transfer duty and bulk packaging before scoping a foodservice ingredient line.
Discuss Your Project
Foodservice Base & Concentrate Production Requirements and Product Variants.
Concentrated Sauces / Pastes
Viscosity can change as solids hydrate and temperature changes. Define heat transfer, mixing, discharge and package duty across the process, including worst-case end-of-batch handling.
Dessert / Beverage Concentrates
Different ingredient, emulsion, allergen and qualified preservation requirements may apply. Group only compatible families rather than assuming every “concentrate” shares one line.
Connect the Production Process
Distinguish evaporation / reduction from blending concentrated purchased ingredients.
- Define raw inputBase, powder or dilute material.
- Specify accepted concentrateComposition and customer-use basis.
- Assign specialist processReduction / blending / treatment.
- Trial customer applicationQualified reconstitution or use.
Resolve before procurementA blending-system estimate does not include an unspecified evaporation plant.
Measure complete batch, quality and discharge duty across representative concentrates.
- Record recipe stagesCharging, heating, mixing and cool.
- Check viscosity / solidsActual process history.
- Review discharge / packagePassages, holding and access.
- Verify accepted productConcentrate and customer-use criteria.
Resolve before procurementThe financial kg basis is good concentrate, not an inflated reconstituted quantity.
Map high-solids / fat / particulate soils, customer identities and qualified transitions.
- Classify productsIngredients, allergens and packages.
- Map installed circuitsCIP, returns and manual tasks.
- Coordinate recipes / lotsCustomer identity and release.
- Measure next good outputUseful time and actual resource cost.
Resolve before procurementDo not shorten qualified cleaning to force an attractive concentrate-line payback.
Equipment & Integration Scope
Review each system by its operating duty and the interfaces to be agreed before procurement.
Configured Cookers
Agreed batch cooking / mixing duty.
Configured Tanks / Vessels
Product-approved staging / holding / blend duty.
CIP Equipment and Circuit Interfaces
Defined concentrate-soil and customer transition circuits.
Specialist Equipment Interfaces
Specialist concentration / shear / preservation / filling.
System Duties & Engineering Questions
Equipment Duties, Utilities and Supplier Responsibilities.
Swipe horizontally to compare all columns ↔
| System | Operating duty | Relevant DPS guide | Confirm before purchase |
|---|---|---|---|
| Configured cookers | Agreed batch cooking / mixing duty. | DPS kettles & cookers ↗ | Viscosity history, thermal transfer and discharge. |
| Configured tanks / vessels | Product-approved staging / holding / blend duty. | DPS tanks & vessels ↗ | Concentration, suspension and cleaning. |
| CIP equipment and circuit interfaces | Defined concentrate-soil and customer transition circuits. | DPS CIP systems ↗ | Return conditions and qualified verification. |
| Specialist equipment interfaces | Specialist concentration / shear / preservation / filling. | Installation & integration ↗ | Actual customer product and acceptance boundary. |
Foodservice Base & Concentrate Equipment Selection: Resolve the Operating Duty First.
Compare proposals against accepted concentrate and customer-use requirements. State whether raw feed is already concentrated, what specialist reduction / treatment is included, and whether the quote covers discharge, bulk containers and qualified cleaning. Final customer dilution volume is not the same as the concentrate manufacturer’s saleable kg.
Swipe horizontally to compare all columns ↔
| Buying question | Evidence to prepare | Engineering decision |
|---|---|---|
| Blend or reduce / evaporate? | Actual input composition and desired concentrate. | Assign the complete process boundary. |
| Which quantity earns revenue? | Good concentrate and actual customer / fee agreement. | Avoid multiplying sales by downstream dilution. |
| What does customer acceptance require? | Qualified concentrate, package and application trials. | Include trial and release ownership before capital. |
Engineering the Whole Line
Start with the business outcome
A foodservice-base producer must meet customer performance after reconstitution or further cooking, not only make a concentrated batch. DPS can assess agreed cooker / vessel, utility, controls, transfer, cleaning and installation interfaces. Equipment suitability and the ROI case depend on the actual product, accepted concentration / texture, package, customer qualification and commercial demand.
Confirm the exact foodservice base & concentrate product, preservation route and project suitability with DPS before assigning a delivery scope. Confirm formulation, reduction / evaporation, specialist heat / shear, preservation, package and customer-use requirements with qualified teams. This guide is a product-specific assessment, not a claim of proprietary DPS concentration technology or a guarantee of a customer’s final application result.
Commissioning Tests and Performance Acceptance.
Define Concentrate and Customer Use
Agree ingredient distribution, concentration, viscosity, particles and the intended dilution or reconstitution performance for each product family.
Test Cooking Through Bulk Packaging
Check heat transfer, hydration, cooling where required, end-of-batch discharge and transfer using demanding representative recipes.
Verify Consistency Across Campaigns
Confirm accepted concentrate and customer-use results, product identity, qualified cleaning and good bulk-packaged output after customer changes.
Plan Your Project
Review the scope, cost assumptions and operating case for your project. The examples and calculators below support early planning and are not DPS quotations.
Compare Operating Corrections, Retrofit and Replacement.
Define raw and customer-use boundaries first, then measure complete cycles, quality, utilities, residual product and package constraints.
Investment boundaryThe capacity example assumes accepted concentrate and an established compatible process; no evaporation yield or customer dilution multiplier is monetized.
Confirm product / customer specification, concentration route, package, preservation, ingredient handling, utilities, waste and demand.
Investment boundaryInclude every specialist process, site / utility interface, fixed operating cost, customer trials and working capital.
Long Cook / Discharge, Customer Rejects / Variation and Operating Value.
Swipe horizontally to compare all columns ↔
| Observed condition | Measure before design | DPS / team decision | Economic basis |
|---|---|---|---|
| Long cook / discharge | Complete-cycle and accepted concentration evidence. | Target heat, mixing, transfer or package limitation. | Useful accepted concentrate at customer demand. |
| Customer rejects / variation | Qualified concentrate and reconstitution tests. | Resolve formulation / process / package boundary. | Actual baseline input / rework costs. |
| Resource-intensive concentration | Metered duty, raw boundary and specialist trials. | Compare process and utility alternatives. | Verified bills and added service cost. |
| Frequent customer product changes | Identity, qualified cleaning and first-good-output timeline. | Coordinate recipes, routing and records. | Independent useful time / resource benefits. |
Compare Foodservice-Base Production Scopes
Swipe horizontally to compare all columns ↔
| Decision | Targeted Work | Broader Scope |
|---|---|---|
| Concentration Duty | Correct measured heating, mixing or discharge limitations. | Include additional specialist concentration and utility scope where required. |
| Customer Performance | Trial the complete process and intended reconstitution. | Reconfigure the process when retained equipment cannot meet accepted product use. |
| Product Families | Coordinate compatible recipes, routing and cleaning. | Add separate capability for materially different ingredient or preservation duties. |
Foodservice Base & Concentrate Equipment Price vs Full Installed Project Cost.
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 | $48,000 |
| Defined configured / OEM component allowance | $168,000 |
| Mechanical / electrical field installation | $92,000 |
| Instrumentation and control integration | $48,000 |
| Commissioning and acceptance support | $28,000 |
| Training, documentation and closeout | $16,000 |
| Defined project scope | $400,000 |
| Separate site / facility additions | $65,000 |
| Capital contingency (15%) | $69,750 |
| Separate one-time startup / shutdown cost | $40,000 |
| Incremental working capital | $30,000 |
| Total initial cash | $604,750 |
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.
Worked Operating Case
Hypothetical owner-budget case: 250 days × 0.5 useful recovered hour/day × 900 good kg/h × 55% realization gives 61,875 incremental sold kg/year after the 90,000 kg demand ceiling. Net price $5.6/kg less incremental variable cost $3.8/kg gives $1.8/kg contribution. The baseline inputs assume $20,000 energy, $14,000 water / chemistry and $8,000 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 $18,000 added annual fixed cost. Result: $135,375 steady net benefit; initial cash $604,750 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 $135,375; year-one net cash $74,025; cash payback 4.92 years; five-year NPV at 10% is −$147,345. Change the assumptions below to test a different case.
Foodservice Base & Concentrate Upgrade ROI, Payback and Cash Flow.
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.
- Initial cash investment
- $604.8k
- Steady annual net benefit
- $135.4k
- Cash payback
- 4.92 years
- 5-year NPV
- −$147.3k
- Steady annual cash ROI
- 22.4%
- 5-year net cash ROI
- 1.8%
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: 61,875 kg/year at $1.80/kg contribution. The base case does not recover the required discounted return within five years. Year-one net cash: $74,025.
Realization needed for the target operating payback
53.8%
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.
Cumulative Project Cash
BaseDownside
Swipe the chart to compare all five years ↔
Inspect Annual Cash Flow and Sensitivity
Swipe horizontally to compare all columns ↔
| Year | Net cash | Cumulative cash | Discounted cash |
|---|---|---|---|
| Initial | −$604,750 | −$604,750 | −$604,750 |
| Year 1 | $74,025 | −$530,725 | $67,295 |
| Year 2 | $135,375 | −$395,350 | $111,880 |
| Year 3 | $135,375 | −$259,975 | $101,709 |
| Year 4 | $135,375 | −$124,600 | $92,463 |
| Year 5 | $135,375 | $10,775 | $84,057 |
Swipe horizontally to compare all columns ↔
| Case | Annual benefit | NPV | Cash payback |
|---|---|---|---|
| Downside | $90,825 | −$406,975 | Beyond 5 years |
| Base | $135,375 | −$147,345 | 4.92 years |
| Upside | $164,889 | −$46,195 | 4.11 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.
Calculation Basis
- Five-year, pre-tax cash flow. Financing, depreciation and asset resale are excluded.
- Initial cash includes contingency, startup costs and working capital; year one reflects ramp-up.
- Output is capped by demand. Count each production gain or verified cash saving once.
Foodservice Base & Concentrate Baseline Energy-Cost Worksheet
The default reproduces the main retrofit energy input of $20,000/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 a Foodservice Base & Concentrate Equipment / Upgrade Brief.
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.
Checklist and model data stay in this browser until you choose to share them.
Foodservice Base & Concentrate Equipment and Plant Upgrade FAQ.
Is all concentrate production an evaporation process?
No. Some products are blended from concentrated ingredients; others need specialist reduction or separation. Define the actual boundary.
Can reconstituted volume be used as our sales capacity?
Use the quantity the manufacturer actually sells or bills, with consistent price / cost. Customer dilution does not create extra shipped concentrate.
What makes a foodservice base equipment quote comparable?
The same ingredient, concentration, accepted customer performance, package, preservation, utilities, installed scope and trial / handover basis.
Are these prices or returns a DPS commitment?
No. The example inputs exist to make the business-case calculation reviewable. Actual scope, prices, schedule, savings and performance need project-specific assessment and agreement.
What should the first DPS conversation include?
Bring the product and package mix, operating baseline, commercial target, retained assets, site constraints, available outage window and the capital options you are considering. Mark unknowns for measurement or supplier trials.
Related Planning Guides
Ready Meal Factory Design: Plan Cooking, Assembly, Cooling and Distribution
Design a ready-meal operation around component cooking, assembly, cooling and distribution, with explicit release gates and equipment interfaces.
Food Processing Plant Layout: Plan Product Flow, People Flow and Future Growth
Plan a food processing plant layout around product, people, packaging and waste flows, then test space, access, storage and future expansion.
Food Processing and Packaging Line Integration: Design the Factory Around the Bottleneck
Plan food processing and packaging as one path. Compare rates, batch presentation, buffers, interfaces and staged capacity before selecting equipment.
Discuss Your Foodservice Bases & Concentrates Project
Bring your product requirements, operating priorities and site constraints to an initial scope discussion with DPS.