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HP1.3 · Integrated retrofit, economics and verification

A heater that works in isolation may not deliver a production retrofit. This lesson connects process and electrical interfaces, operating priorities and measured evidence, then separates a period energy comparison from a complete investment case.

Learning objectives

  • Identify heat-exchanger, source, grid and legacy-backup dependencies.
  • Separate energy cost, lifecycle cash flow and verified emissions boundaries.
  • Design an evidence-based acceptance and monitoring plan.

Allow 30–45 minutes including derivations and exercises. All numerical values are teaching assumptions.

1. Map the retrofit around production

List the process users, operating modes, heat-source streams, distribution, electrical supply and existing boilers or chillers. Identify who controls each interface and which production condition is protected. Heat recovery can depend on another process whose schedule, contamination or shutdown may change independently of heat demand.

A retrofit may operate in hybrid mode with legacy equipment during transition or for contingency supply. State how the legacy path starts, its available capacity and fuel/utilities, and the permitted interruption. Retained equipment is a design input with maintenance and operating costs, not automatically a free or immediately available backup. [H1]

2. Coordinate electrical and thermal priorities

The EMS may see a price or network signal, while production requires heat at a minimum state. Define the protected heat inventory, electrical headroom and valid charging/discharging envelope before scheduling flexibility. The controls should have agreed rejection and fallback behaviour if a requested electrical action would breach the process limit.

Separate energy-management scheduling from equipment protection, pressure/temperature control and electrical protection. This course provides a functional boundary, not executable control or safety procedures. Responsible process and electrical specialists must establish interlocks, protection, commissioning methods and permitted operation for the actual installation.

Alternative electrical and thermal service paths

Site electricityMW_e / MWh_eElectric chargingDeclared conversion lossThermal storageUsable window and holdingRecoverable source heatTemperature, flow and timingHeat pumpCOP at source / sink stateUseful process heatMW_th / MWh_th
Functional learning diagram, not an installation single-line, protection or control drawing. Solid arrows show the selected service/evidence path; storage control paths are dashed.

3. Build one useful-service economic baseline

Compare alternatives for the same useful temperature, quantity, timing and reliability. The baseline may include fuel, boiler losses, electricity auxiliaries and maintenance. The new case may include electricity, demand charges, water/source handling, heat exchangers, storage losses, backup and production-change costs. Missing categories should remain visible rather than being silently set to zero.

The initial tool deliberately compares duty energy costs under stated prices. It does not infer annual savings, payback, financing or a discounted lifecycle result. A full business case needs representative time series, annual operation, installed quotations, replacements and consistent discount/tax assumptions, followed by sensitivity testing of the parameters that matter.

4. Measure claims with compatible meters and factors

To calculate an observed heating COP, measure useful heat and all included electrical energy over the same period and boundary. Identify whether pumps, fans, source preparation, defrost, standby or backup are included. A nameplate COP measured at one point should not be presented as a seasonal whole-system COP.

An emissions comparison also requires declared electricity and fuel factors appropriate to the location, time and accounting method. Electrification alone is not numerical evidence of a particular reduction. Keep energy and emissions results separate, disclose factor sources and avoid crediting both purchased certificates and the same physical saving twice.

5. Accept the integrated service and maintain it

Acceptance should test the useful process condition, the complete electrical/thermal boundary and agreed operating transitions, with suitable instrumentation and responsible specialists. Preserve initial conditions, installed configuration, time alignment, source conditions and deviations. Test results should map to the claim they actually support.

Monitoring then tracks useful delivery, temperatures, electricity/fuel inputs, source availability, storage state and maintenance. A changed production schedule, new electricity constraint or degraded exchanger can invalidate an earlier result. Assign owners and review triggers, including what evidence is needed before a revised flexibility service is allowed.

Case and independent exercises

Fictional six-hour test: a process receives 12 MWh_th; the heat-pump compressor uses 4.0 MWh_e, included pumps use 0.5 MWh_e and backup electric heat uses 0.3 MWh_e. A supplier advertises compressor-only COP 3.0. The owner wants to report whole-system COP, annual financial savings and a carbon-reduction percentage from this test alone.

  1. Calculate the compressor-only and declared whole-system COP.
  2. Identify which annual financial and emissions claims remain unsupported.
  3. Specify the next evidence pack and an operational review trigger.

Worked answers and reasoning

Attempt the exercises before opening each answer.

Answer 1 · Include the declared boundary

Compressor-only COP is 12/4=3.0. On the declared whole-system boundary electricity is 4+0.5+0.3=4.8 MWh_e and COP is 12/4.8=2.5. The labels must state the included auxiliaries/backup and common six-hour period. Neither result alone proves annual performance.

Answer 2 · Do not extrapolate beyond the evidence

Annual savings need representative operation, a measured useful-service baseline, complete tariffs and project cash flows. A carbon percentage additionally needs compatible electricity/fuel factors and accounting boundaries. The test supports the observed six-hour energy balance only under its recorded operating conditions.

Answer 3 · Prepare a maintainable claim

Collect synchronised useful-heat and electrical/fuel measurements, source/sink conditions, production modes, tariff/quotation sources and the configuration/acceptance record. A change in source temperature or production schedule should trigger reassessment of COP, useful delivery and flexible charging windows before the service commitment is updated.

Decision method to take away

An industrial heat project is an integrated production service with evidence, costs and operating limits that must remain consistent after commissioning.

Sources and review date

Reviewed 26 October 2026. Text, diagrams and exercises are original. All numerical cases use stated teaching assumptions, rather than site measurements or manufacturer commitments. These primary sources support the technical background; verify their applicability to each project.

[H1] ARENA / HILT CRC · TES for Industrial Process Heat: A Practical Guide (2026) ↗
Integrated assessment of process heat and thermal storage.

[H2] IEA · How a Heat Pump Works ↗
Heat-source, useful-output and COP concepts.

[H3] IEA · Heat Pump Monitor 2026: Key Findings ↗
Industrial integration, temperature and economic context.

[H4] DOE · Industrial Heat Pumps for Steam and Fuel Savings ↗
Foundational engineering explanation; not a current local approval rule.