Retained mechanical duty
Review actual product quality, working load, materials, cleanability and asset condition. A software migration cannot correct every physical mixing, thermal, transfer or packaging limitation.
The owner needs to migrate unsupported controls while preserving approved recipes, equipment states, OEM interfaces and the ability to recover production.

Start with the business outcome
The owner needs to migrate unsupported controls while preserving approved recipes, equipment states, OEM interfaces and the ability to recover production. Compare phased migration with a defined full cutover. Inventory software, I/O, networks, drives, instruments, safety-related interfaces and package handshakes, then agree backups, testing and a realistic recovery path. DPS can connect the process basis, capital alternatives, field / supplier interfaces, controls and project execution so the owner can make a reviewable investment decision.
DPS publishes equipment retrofit, controls and integration scope. Product requirements, safety-related system design, specialist packages and qualified acceptance remain explicit owner / supplier boundaries. Lower support risk is not assigned a fictitious annual cash value.

Review actual product quality, working load, materials, cleanability and asset condition. A software migration cannot correct every physical mixing, thermal, transfer or packaging limitation.
Inventory software, recipes, networks, drives, instruments and package dependencies. Define the required behavior, records and support strategy before selecting a new platform.
Plan readiness, isolation, tests, training and recovery for live production. Reconcile actual maintenance / energy / payroll reduction after stabilization; no extra sales are assumed unless useful capacity is demonstrated.
Use actual failure, support and operating evidence across representative products.
Compare retained condition, interfaces, supported life and the qualified future duty.
Verify backup, test readiness, owner / OEM interfaces and the operating recovery plan.
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| System | Operating duty | Relevant DPS guide | Confirm before purchase |
|---|---|---|---|
| Retrofit design | Translate the measured equipment gap into a duty. | Process engineering ↗ | Retained-asset limits and qualified trials. |
| Controls renewal | Specify states, recipes, alarms, backups and interfaces. | Automation & controls ↗ | I/O, test plan, migration and training. |
| Configured components | Supply suitable process equipment within confirmed scope. | Equipment manufacturing & supply ↗ | Do not assume specialist OEM packages are DPS-manufactured. |
| Field execution | Coordinate changes and production restart. | Installation & integration ↗ | Live areas, access, temporary services and handover. |
Record actual downtime / support costs, controller dependencies, operator steps and version ownership. Released troubleshooting time becomes cash only when payroll or maintenance spend is genuinely avoided.
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| Decision area | Operating / site evidence | Acceptance or responsibility |
|---|---|---|
| Baseline / backups | Versions, programs, recipes, tags and controller inventory. | Verified recoverable owner-controlled records. |
| Functional mapping | States, permissives, alarms, sequences and OEM handshakes. | Agreed functional specification and test cases. |
| Cutover readiness | FAT / simulation, wiring, spares and isolation. | No-go points and qualified rollback / recovery plan. |
| Operator handover | Access rights, exception handling, records and training. | Demonstrated use and supported ownership. |
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| Observed condition | Measure before design | DPS / team decision | Economic basis |
|---|---|---|---|
| Baseline / backups | Versions, programs, recipes, tags and controller inventory. | Verified recoverable owner-controlled records. | Use the matched product / site baseline and the agreed counterfactual. |
| Functional mapping | States, permissives, alarms, sequences and OEM handshakes. | Agreed functional specification and test cases. | Include complete capital and one-time transition cash. |
| Cutover readiness | FAT / simulation, wiring, spares and isolation. | No-go points and qualified rollback / recovery plan. | Count only independent cash costs actually avoided or useful sold output. |
| Operator handover | Access rights, exception handling, records and training. | Demonstrated use and supported ownership. | Separate recurring operating benefit from one-time project exposure. |
Compare phased migration with a defined full cutover. Inventory software, I/O, networks, drives, instruments, safety-related interfaces and package handshakes, then agree backups, testing and a realistic recovery path.
Record actual downtime / support costs, controller dependencies, operator steps and version ownership. Released troubleshooting time becomes cash only when payroll or maintenance spend is genuinely avoided.
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 |
|---|---|
| Survey, measured baseline and engineering | $39,200 |
| Defined equipment / interface components | $89,600 |
| Field mechanical / electrical installation | $70,000 |
| Controls and instrument interfaces | $39,200 |
| Commissioning / qualified test support | $28,000 |
| Training, records and closeout | $14,000 |
| Defined project scope | $280,000 |
| Separate site / facility additions | $25,000 |
| Capital contingency (15%) | $45,750 |
| Separate one-time startup / shutdown cost | $35,000 |
| Incremental working capital | $10,000 |
| Total initial cash | $395,750 |
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 case for legacy food plant PLC SCADA replacement and cutover: 250 days × 0 useful hour/day × 0 accepted kg/h × 0% realization gives 0 kg potential extra sales; the 0 kg demand ceiling yields 0 sold kg/year. Net price $0.00 less $0.00 incremental variable cost gives $0.00/kg contribution. Separately verified baseline energy / cleaning / maintenance assumptions are $35,000/year; actual paid-hour avoidance is $20,000/year. Added fixed operating cost is $12,000/year, and year-one gross benefit realizes at 80%. These values are original owner-planning assumptions, not supplier prices or a customer result.
Calculated from these assumptions: steady annual net benefit $43,000; year-one net cash $32,000; cash payback Beyond 5 years; five-year NPV at 10% is −$242,746. 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: 0 kg/year at $0.00/kg contribution. The base case does not recover the required discounted return within five years. Year-one net cash: $32,000.
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 | −$395,750 | −$395,750 | −$395,750 |
| Year 1 | $32,000 | −$363,750 | $29,091 |
| Year 2 | $43,000 | −$320,750 | $35,537 |
| Year 3 | $43,000 | −$277,750 | $32,307 |
| Year 4 | $43,000 | −$234,750 | $29,370 |
| Year 5 | $43,000 | −$191,750 | $26,700 |
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| Case | Annual benefit | NPV | Cash payback |
|---|---|---|---|
| Downside | $43,000 | −$312,896 | Beyond 5 years |
| Base | $43,000 | −$242,746 | Beyond 5 years |
| Upside | $43,000 | −$242,746 | 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.
This independent energy-only teaching example is not the main controls case, which assumes $5,000 gross energy saving. Its net result must not be combined with that main case.
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
DPS publishes food / beverage project, process, utility, installation and controls context. Those materials establish relevant delivery disciplines. None of the amounts, recovered time, energy reductions, schedules or payback in this original screening example is attributed to a customer case.
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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 manufacturing-scenarios overview and linked service descriptions support engineering / integration context. The site-specific findings, illustrative financial assumptions and decision register on this page require project assessment; they are not published DPS customer results.
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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