Calculate the recoverable heat and the corrosion risk together

| Requirement | What it means in the design |
|---|---|
| Recovery and corrosion must be calculated together | Chasing recovery efficiency without checking dew point corrosion can scrap the unit within one or two years. |
| Dust causes fouling | Dust bridges the fin passages, reducing heat transfer and raising pressure drop. |
| Retrofit space is limited | Adding a unit to an existing system is constrained by site space and flue gas pressure drop. |
| Recovered heat must be used | The hot water or hot air must have a stable use, otherwise the payback does not exist. |
We first calculate flue gas flow, inlet and outlet temperature and recoverable heat, then set the output parameters of the recovery medium. Next we check the cold-end wall temperature against the acid dew point and set fin spacing and cleaning method against dust loading. A payback estimate is provided for the project decision.
Recovery schemes are selected after the heat balance, corrosion check and site constraints are confirmed. We support both new projects and retrofits of existing systems.
| Heat source | Flue gas characteristics | Recommended recovery |
|---|---|---|
| Industrial boiler | Contains sulphur; condensation possible | Flue gas to water; check cold-end wall temperature |
| Industrial kiln | High temperature and dust | Flue gas to air; wide fin spacing or H-fin |
| Drying furnace | Medium temperature and high moisture | Flue gas to air for drying reuse |
| Metallurgy and building materials | High temperature and heavy dust | Cool with a flue gas cooler, then recover |
Send the medium, working conditions and installation envelope for an assessment.