Solutions · Heat Recovery & Steam Generation
This technical page defines the engineering basis, supply boundaries and enquiry data for HRSG-Based Heat Recovery Solutions. Each project is configured around capacity, feed composition, product specification, ambient conditions, available utilities and the owner’s operating requirements rather than a fixed catalogue arrangement.
From project definition to delivery
Engineering of HRSG-Based Heat Recovery Solutions concentrates on gas and steam temperature profiles, pinch and approach temperatures, steam conditions, circulation, gas-side pressure drop, water chemistry, metallurgy, fouling and start-up transients. The selected configuration is verified against normal, minimum, start-up, shutdown and credible upset cases, then checked for operability, maintainability, energy use, process safety and site interfaces before the design is frozen.
Rated capacity, minimum stable load, feed envelope, inlet and outlet conditions, product specification, start-up and shutdown cases, design life and acceptance criteria are agreed before equipment definition is frozen. The review also records utility margins, interfaces, inspection hold points, maintainability constraints and the evidence required for a controlled handover.
Materials, corrosion allowance, sour-service requirements, piping classes, nozzle design, insulation, coating, supports and maintenance access are coordinated with the actual process conditions and project code hierarchy.
Control philosophy, alarms and trips, cause-and-effect logic, interlocks, start-up and shutdown sequences, safe depressurization and operator access are developed consistently from the P&IDs through functional testing.
Battery limits, tie-in points, structural loads, cabling, instrumentation, drains, vents, access routes, lifting envelopes and shipping constraints are controlled through coordinated models and interface drawings.
From project definition to delivery
Proposal quality depends on complete input data and an explicit acceptance basis. The following lists provide a practical starting point and are completed during technical clarification.
Delham Engineering
Send the available process data, battery limits and expected document list for a technical proposal. The engineering team will identify missing information through a structured clarification register.
Technical Datasheet
The values are two distinct published CHP project examples, not one HRSG product range. Total thermal output is stated at plant level and must not be mistaken for HRSG steam duty.
| Parameter | Published value | Reference basis | Applicability / limit |
|---|---|---|---|
| Natural-gas CHP live-steam example | 17.5 bar; 242 °C | Published steam conditions for one CHP project; plant maximum heat output was 40 MWth. | Project example only; the 40 MWth plant value is not an isolated HRSG rating. |
| Biomass CHP live-steam example | 120 bar; 520 °C | Separate published biomass CHP project; plant maximum heat output was 35 MWth. | Do not combine with the natural-gas case to imply a common HRSG envelope; gas turbine/boiler exhaust and steam-cycle design govern. |
| HRSG design basis needed | Gas-turbine exhaust flow, temperature and load cases | Published engineering descriptions identify HRSG output as dependent on the upstream gas turbine and steam cycle. | No universal steam-capacity range is inferred from plant gross output; obtain OEM exhaust curves and define supplemental firing/duct-burner cases. |
