Time-aligned operating evidence
Record the complete product, cleaning and package schedule with upstream / downstream states. A stopped machine may be a symptom of another constrained step rather than the asset that needs investment.
The plant has enough nominal machine capacity but loses useful production between short campaigns, including cleaning, setup, release and restart rejects.

Start with the business outcome
The plant has enough nominal machine capacity but loses useful production between short campaigns, including cleaning, setup, release and restart rejects. Separate end-product drain, approved cleaning, manual checks, recipe settings, package setup and first-good-product time. Target a measured delay without removing required quality or cleaning tasks. 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’s process, controls, cleaning and installation scope supports a measured bottleneck project. No generic OEE uplift, throughput percentage or customer ROI is assumed. Qualified cleaning, product release and specialist OEM changes require explicit scope.

Record the complete product, cleaning and package schedule with upstream / downstream states. A stopped machine may be a symptom of another constrained step rather than the asset that needs investment.
Use complete batches or verified useful production time at the real constrained good-output rate. Keep first-good-product and site release in the schedule; do not value unapproved shortened cleaning.
Cap extra sales by demand, staffing and downstream capacity. Baseline resources and paid hours must be independent of the variable production costs already deducted from incremental sales.
Log state, cycle, product, utilities and accepted output in the same time base.
Compare sequence, transfer, utility, control and targeted mechanical changes.
Re-run representative schedules and reconcile useful output with orders.
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| System | Operating duty | Relevant DPS guide | Confirm before purchase |
|---|---|---|---|
| Constraint engineering | Map product / process duty and complete-cycle evidence. | Process engineering ↗ | Actual good output and qualified operating envelope. |
| Sequence / instruments | Improve agreed states, recipe / setup and observed causes. | Automation & controls ↗ | Operating exceptions and package handshakes. |
| CIP interfaces | Coordinate the installed cleaning circuits and resources. | CIP systems ↗ | Qualified sequence and verification ownership. |
| Installation | Integrate the chosen correction within live production. | Installation & integration ↗ | Scope, outage, tests and useful line performance. |
Record the full transition matrix by product / allergen / package. Value useful recovered time at the constrained good-output rate and the share actually sold, while separately reconciling baseline resources and real paid cost.
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| Decision area | Operating / site evidence | Acceptance or responsibility |
|---|---|---|
| Full transition clock | Last good product to first accepted product. | Include release and downstream setup. |
| Qualified cleaning | Circuits, manual tasks and product transition basis. | No assumed reduction in required duty. |
| Recipe / package setup | Settings, version checks, tools and OEM steps. | Define safe overlaps and verified sequence changes. |
| Financial realization | Demand, constrained rate and paid cost. | Count each recovered hour once. |
The main example’s 18-minute qualified improvement per transition is decomposed below. Required cleaning remains 45 minutes in both assumptions; changes are in recoverable drain / transfer, recipe setup and verified first-good-product preparation. Two transitions/day release 36 minutes/day, exactly the financial preset’s 0.6 hour/day. At 1,000 accepted kg/h, 250 days and 65% realization, 97,500 kg/year can be sold only if the proposed transitions and downstream availability are actually demonstrated.
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| Transition element | Current | Proposed |
|---|---|---|
| Drain / transfer | 20 | 15 |
| Required qualified cleaning | 45 | 45 |
| Recipe / setup checks | 15 | 8 |
| Release / first-good preparation | 20 | 14 |
| Total per transition | 100 | 82 |
| Two transitions per day | 200 | 164 |
| Useful time difference | 36 minutes/day | 0.6 productive hour/day; do not shorten required quality checks. |
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| Observed condition | Measure before design | DPS / team decision | Economic basis |
|---|---|---|---|
| Full transition clock | Last good product to first accepted product. | Include release and downstream setup. | Use the matched product / site baseline and the agreed counterfactual. |
| Qualified cleaning | Circuits, manual tasks and product transition basis. | No assumed reduction in required duty. | Include complete capital and one-time transition cash. |
| Recipe / package setup | Settings, version checks, tools and OEM steps. | Define safe overlaps and verified sequence changes. | Count only independent cash costs actually avoided or useful sold output. |
| Financial realization | Demand, constrained rate and paid cost. | Count each recovered hour once. | Separate recurring operating benefit from one-time project exposure. |
Separate end-product drain, approved cleaning, manual checks, recipe settings, package setup and first-good-product time. Target a measured delay without removing required quality or cleaning tasks.
Record the full transition matrix by product / allergen / package. Value useful recovered time at the constrained good-output rate and the share actually sold, while separately reconciling baseline resources and real paid 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 |
|---|---|
| Survey, measured baseline and engineering | $35,000 |
| Defined equipment / interface components | $80,000 |
| Field mechanical / electrical installation | $62,500 |
| Controls and instrument interfaces | $35,000 |
| Commissioning / qualified test support | $25,000 |
| Training, records and closeout | $12,500 |
| Defined project scope | $250,000 |
| Separate site / facility additions | $25,000 |
| Capital contingency (15%) | $41,250 |
| Separate one-time startup / shutdown cost | $30,000 |
| Incremental working capital | $25,000 |
| Total initial cash | $371,250 |
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 production capacity lost to SKU and package changeovers: 250 days × 0.6 useful hour/day × 1,000 accepted kg/h × 65% realization gives 97,500 kg potential extra sales; the 100,000 kg demand ceiling yields 97,500 sold kg/year. Net price $3.80 less $2.45 incremental variable cost gives $1.35/kg contribution. Separately verified baseline energy / cleaning / maintenance assumptions are $20,800/year; actual paid-hour avoidance is $0/year. Added fixed operating cost is $12,000/year, and year-one gross benefit realizes at 65%. These values are original owner-planning assumptions, not supplier prices or a customer result.
Calculated from these assumptions: steady annual net benefit $140,425; year-one net cash $87,076; cash payback 3.02 years; five-year NPV at 10% is $112,572. 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: 97,500 kg/year at $1.35/kg contribution. The base case has a nonnegative five-year NPV at the selected discount rate. Year-one net cash: $87,076.
Realization needed for the target operating payback
46.5%
Minimum capacity realization for a 4-year operating cash payback; terminal recovery excluded. Demand and unit margin must also hold.
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 | −$371,250 | −$371,250 | −$371,250 |
| Year 1 | $87,076 | −$284,174 | $79,160 |
| Year 2 | $140,425 | −$143,749 | $116,054 |
| Year 3 | $140,425 | −$3,324 | $105,503 |
| Year 4 | $140,425 | $137,101 | $95,912 |
| Year 5 | $140,425 | $277,526 | $87,193 |
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| Case | Annual benefit | NPV | Cash payback |
|---|---|---|---|
| Downside | $87,775 | −$133,510 | Beyond 5 years |
| Base | $140,425 | $112,572 | 3.02 years |
| Upside | $157,300 | $171,173 | 2.74 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.
A hypothetical verified 18-minute reduction across two daily transitions gives 0.6 hour/day. The worksheet returns gross capacity; the main model then applies 65% realization and the 100,000 kg demand ceiling. Required cleaning and release tasks remain included.
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.
Checklist and model data stay in this browser until you choose to share them.
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.

Compare another shift, shorter changeovers and a new line using the actual bottleneck, saleable output, added operating cost and incremental investment.

Plan food processing and packaging as one path. Compare rates, batch presentation, buffers, interfaces and staged capacity before selecting equipment.

Compare utility peak capacity, sequencing and buffers using a timed load model, DPS CIP interfaces and a reported retrofit case with staged tie-ins.