Fruit and Particulate Fillings
Define fruit form, pieces, solids / concentration, hydration and the required integrity after agitation, heating, pumping and filling. The accepted customer baked or chilled result is a separate trial condition.
Scope fruit, cream or savory filling preparation, texture, heat / transfer duty and bulk packaging against the customer’s accepted bakery application.
Discuss Your Project

Define fruit form, pieces, solids / concentration, hydration and the required integrity after agitation, heating, pumping and filling. The accepted customer baked or chilled result is a separate trial condition.
Ingredient functionality, starch / hydrocolloid hydration, fat / protein systems and thermal / cooling history can affect final texture. Specify qualified package / storage and cleaning requirements.
Meat / vegetable pieces, sauce binding, raw / cooked status and preservation require product-specific qualified scope. Do not transfer a fruit-filling equipment setting to a savory product by nominal batch volume.
Define the ingredient / process envelope and required application performance before comparing cooker or mixer prices.
Measure the complete batch and quality through actual viscosity and particle changes.
Map flavor / allergen changes, high-soil circuits, manual tasks and bulk / customer packaging.
Review each system by its operating duty and the interfaces to be agreed before procurement.
Only the agreed filling cook / mix duty.
Approved ingredient or filling holding duty.
Defined filling-soil / allergen circuits.
Specialist shear / thermal / transfer / package equipment.
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| System | Operating duty | Relevant DPS guide | Confirm before purchase |
|---|---|---|---|
| Configured cookers | Only the agreed filling cook / mix duty. | DPS kettles & cookers ↗ | Ingredient hydration, particles, heat / cold and discharge. |
| Configured tanks / vessels | Approved ingredient or filling holding duty. | DPS tanks & vessels ↗ | Texture, permitted residence and cleaning. |
| CIP equipment and circuit interfaces | Defined filling-soil / allergen circuits. | DPS CIP systems ↗ | Qualified verification and manual tasks. |
| Specialist equipment interfaces | Specialist shear / thermal / transfer / package equipment. | Installation & integration ↗ | Customer application and final accepted quality. |
Ask suppliers to define accepted filling at discharge, after packing and in the agreed customer application. Keep fruit, cream and savory duties distinct where ingredients or preservation differ. Compare all installed and customer-trial scope; nominal mixer / kettle size alone cannot establish suitable bakery-filling production.
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| Buying question | Evidence to prepare | Engineering decision |
|---|---|---|
| Does the filling survive customer use? | Qualified application, package / storage and texture tests. | Assign product / customer acceptance responsibility. |
| Which particle quality is accepted? | Samples after agitation, pump and fill. | Trial the complete route. |
| What does the project include? | Cook / cool, transfer, utilities, cleaning and customer trials. | Compare matched installed scope. |
Start with the business outcome
A bakery filling maker must meet accepted texture, particle integrity and performance in the customer’s product, not only complete a hot batch. DPS can assess applicable agreed cooker / mixing, vessel, utility, controls, cleaning and integration interfaces. The investment case needs product-qualified output, actual purchased costs and the complete package / customer-trial boundary before equipment is selected.
Confirm the exact bakery filling product, preservation route and project suitability with DPS before assigning a delivery scope. Confirm recipe, bake / freeze stability, customer application, preservation, specialist mixing / thermal and filling responsibilities with qualified teams. This guide is a scope-assessment framework; it does not claim DPS proprietary filling formulation, universal bake stability or a demonstrated filling customer ROI.
Define fruit pieces or savory ingredients, concentration, cream or starch behavior and the accepted baked or chilled customer result.
Check representative recipes through agitation, heating, cooling, pumps and filling, including texture and piece integrity after the complete train.
Verify accepted batch mass, ingredient retention, qualified allergen or flavor changes and the agreed customer-use evaluation.

Review the scope, cost assumptions and operating case for your project. The examples and calculators below support early planning and are not DPS quotations.
Start with accepted texture, pieces, application results and complete-cycle losses. Review the retained equipment and downstream package before selecting more volume or shear.
Define customer / recipe / package envelope, specialist trials, cooking / cooling, sanitation, utilities and demand.
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| Observed condition | Measure before design | DPS / team decision | Economic basis |
|---|---|---|---|
| Off-texture / damaged pieces | Quality after the complete process and customer application. | Trial agitation / shear / transfer with specialists. | Verified actual reject / input costs. |
| Long cook / cooling cycle | Full cycle and accepted mass per batch. | Target the measured heating, cooling or discharge step. | Usable accepted filling, not cooker gallons. |
| Costly ingredient residuals | Actual purchases and unchanged good-output balance. | Review qualified recovery / routing changes. | Avoided input cost once. |
| Allergen / flavor changeover | Qualified cleaning, setup, release and resource timeline. | Coordinate circuits, records and package access. | Useful time and independent baseline resources. |
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| Decision | Targeted Work | Broader Scope |
|---|---|---|
| Texture and Pieces | Trial agitation, shear and transfer using demanding recipes. | Change process packages where retained handling cannot meet customer acceptance. |
| Batch Cycle | Correct the limiting heating, cooling or discharge stage. | Add capacity using accepted mass per complete cycle. |
| Product Changes | Improve qualified cleaning, records and package access. | Add capability for incompatible fruit, cream or savory requirements. |
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 | $60,000 |
| Capital contingency (15%) | $69,000 |
| Separate one-time startup / shutdown cost | $40,000 |
| Incremental working capital | $25,000 |
| Total initial cash | $594,000 |
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 × 950 good kg/h × 55% realization gives 65,312.5 incremental sold kg/year after the 100,000 kg demand ceiling. Net price $5.1/kg less incremental variable cost $3.35/kg gives $1.75/kg contribution. The baseline inputs assume $16,000 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: $134,296.87 steady net benefit; initial cash $594,000 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 $134,297; year-one net cash $73,378; cash payback 4.88 years; five-year NPV at 10% is −$140,290. 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: 65,313 kg/year at $1.75/kg contribution. The base case does not recover the required discounted return within five years. Year-one net cash: $73,378.
Realization needed for the target operating payback
53.3%
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 | −$594,000 | −$594,000 | −$594,000 |
| Year 1 | $73,378 | −$520,622 | $66,707 |
| Year 2 | $134,297 | −$386,325 | $110,989 |
| Year 3 | $134,297 | −$252,028 | $100,899 |
| Year 4 | $134,297 | −$117,731 | $91,727 |
| Year 5 | $134,297 | $16,566 | $83,388 |
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| Case | Annual benefit | NPV | Cash payback |
|---|---|---|---|
| Downside | $88,578 | −$402,775 | Beyond 5 years |
| Base | $134,297 | −$140,290 | 4.88 years |
| Upside | $164,586 | −$36,486 | 4.05 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 $16,000/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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