Furnace combustion systems · Recuperative and regenerative air preheat, fuel savings by exhaust temperature, burner start-up sequence and safety times
An industrial furnace combustion system is the set of burners, combustion-air fan, air preheater (recuperator or regenerator), fuel train and burner controller that heats a furnace, kiln or radiant-tube line. Ask three things first: how much fuel the air preheat saves at your exhaust temperature, which burner type suits the furnace (open flame, radiant tube, self-recuperative or regenerative), and what start-up sequence, purge and safety times the burner control enforces.
Combustion systems for fuel-fired industrial furnaces, kilns and heaters: open-flame, radiant-tube, self-recuperative and regenerative burners, combustion-air fans and preheaters, fuel trains and burner controllers, specified as a system. Individual burner selection by air-fuel ratio and NOx is covered on the Industrial burner page, and complete boiler plants on the Industrial steam generation system for process heating page. Gas turbine combustors, flares and thermal oxidisers are outside this page.
Start with your task
01
DOE's Process Heating Tip Sheet #1 (2007) tabulates percent fuel savings from preheated combustion air for natural gas at 10% excess air, quoting the IHEA Combustion Technology Manual. It describes recuperators as gas-to-gas exchangers on the stack and regenerators as paired heat-storage beds that alternate between flue gas and air, needing at least two regenerators and their burners for uninterrupted firing. [1]
The tip sheet treats processes above 1,600 °F as good candidates for preheat and those below 1,000 °F as hard to justify, while noting that justification rests on energy saved, not temperature, and that dirty or corrosive exhaust needs an exchanger chosen for it. [1]
Editorial calculation: a furnace burning 10 MMBtu/h with a 1,600 °F exhaust and 800 °F preheated air saves 22%, or 2.2 MMBtu/h; over 6,000 operating hours that is 13,200 MMBtu a year. Firing rate and hours are assumed examples. [1]
| Furnace exhaust | Air at 600 °F | Air at 800 °F | Air at 1,000 °F | Air at 1,200 °F | Air at 1,600 °F |
|---|---|---|---|---|---|
| 1,200 °F | 14% | 19% | 23% | — | — [1] |
| 1,600 °F | 17% | 22% | 26% | 30% | — [1] |
| 2,000 °F | 20% | 26% | 31% | 35% | 43% [1] |
| 2,400 °F | 26% | 32% | 38% | 43% | 51% [1] |
Give the supplier the furnace type and temperature, heated zones and their firing rates, fuel and its supply pressure, exhaust temperature and cleanliness, required turndown, emission limits, available space for preheaters and fans, and the control interface (PLC or fieldbus).
02
NPA's combustion-system page lists recuperative burners for W- and U-shaped radiant tubes that preheat air to over 650 °C, with a stated energy saving of 20–30% and NOx below 150 mg/Nm³; self-preheating burners with turndown up to 1:15 and flame speed of 60–150 m/s; open-flame burners from 15 to 5,000 kW with ionisation or UV flame detection; and regenerative burners of 400–1,500 kW for application temperatures up to 1,350 °C, with a stated thermal efficiency above 90%. [2]
The same page describes a burner controller with PROFIBUS communication, integrated ignition transformer and flame detector, pulse-fired or flow-regulated combustion, lockout alarm on flame failure, remote and local ignition and reset, and over-temperature and pressure interlocks intended to extend radiant-tube life. [2]
Editorial calculation: the 20–30% saving NPA states for its recuperative burners sits inside the 17–30% DOE tabulates for 600–1,200 °F preheated air on a 1,600 °F exhaust; 650 °C is about 1,200 °F. [2] [1]
03
Siemens' data sheet for its LMO39 burner controls (type-tested to DIN EN 298) defines the start-up timings: waiting time, prepurge time t1, preignition time, safety time at start-up TSA, interval to the second fuel valve and postpurge. Listed versions carry a TSA requirement of 5 s maximum and prepurge requirements of 20 or 30 s minimum; because parameterised times carry ±3% tolerance, maximum times must be set at least 3% lower and minimum times at least 3% higher. [3]
Siemens' worked example sets a 5 s safety time by parameterising no more than 4.85 s (the next lower step is 4.704 s). The controls also supervise the air pressure switch with a function check during start-up and limit restarts after loss of flame. [3]
US Coast Guard rules for automatic auxiliary boilers in 46 CFR part 63 require a low-fire interlock for low-fire start and forbid automatic increase of air flow after an emergency safety trip (§ 63.20-1), and for small units of 400,000 Btu/h (117 kW) or less require a prepurge of at least four air changes of the combustion chamber and stack and not less than 15 seconds (§ 63.25-1). [4] Editorial calculation: if a furnace and flue hold 40 m³ and the purge fan delivers 8,000 m³/h, four air changes take 160 m³ ÷ 8,000 m³/h = 72 s, so the volume rule, not the 15 s floor, sets the purge. Volume and fan rate are assumed examples. [4]
04
The listing reviewed covers recuperative, self-preheating, open-flame and regenerative burners, high-temperature heat exchangers and burner controllers for metallurgical furnaces.
05
| Part | Role | Fix in the order |
|---|---|---|
| Burners | Release heat; open flame, radiant tube, recuperative or regenerative. [2] | Type, rating, turndown, NOx. |
| Air preheater | Recovers exhaust heat into combustion air. [1] | Recuperator or regenerator; air temperature. |
| Combustion-air fan | Supplies air and purge flow. [4] | Flow, pressure, damper. |
| Fuel train | Shut-off, regulation and proving of fuel. | Valve classes and proving. |
| Burner controller | Sequences purge, ignition and safety time. [3] [2] | Timings, flame detection, interface. |
| Flame detector | Ionisation rod or UV. [2] | Type per burner. |
06
Ask for the basis of each efficiency and NOx figure: the DOE savings table assumes natural gas at 10% excess air, and NPA's NOx value is stated for its recuperative burners. [1] [2]
| Field | What it means and published values | Ask the supplier for |
|---|---|---|
| Thermal Capacity (MW) | NPA open-flame burners 15–5,000 kW; regenerative 400–1,500 kW. [2] | Rating per zone. |
| Thermal Efficiency (%) | NPA states >90% for regenerative systems. [2] | Basis of the figure. |
| Fuel Type | DOE table is for natural gas at 10% excess air. [1] | Fuels and supply pressure. |
| Fuel Consumption (Nm³/h) | Falls with preheat per DOE table. [1] | At rated and minimum fire. |
| Excess Air Ratio | DOE table basis 10% excess air. [1] | Setpoint and trim. |
| NOx Emission (mg/Nm³) | NPA states <150 mg/Nm³ for recuperative burners. [2] | Guarantee and O₂ reference. |
| CO Emission (mg/Nm³) | Combustion completeness. | Guarantee. |
| Operating Pressure (MPa) | Fuel and air supply pressures. | Pressures at burner. |
| Operating Temperature (°C) | Regenerative to 1,350 °C (NPA). [2] | Furnace and air temperatures. |
| Control Voltage (V DC) | Controller supply. | Voltage. |
| Power Consumption (kW) | Fans and controls. | Absorbed power. |
| Material Grade | Heat-resistant alloys for tubes and exchangers. [2] | Grades and tests. |
| Weight (kg) | Burners, fans, exchangers. | Weights. |
| Dimensions (L×W×H) (mm) | Burner and preheater envelope. | Drawing. |
07
Paste it into your enquiry below or into an email to a maker, then replace every bracket.
Furnace: [type; temperature; zones; firing per zone] Fuel: [type; supply pressure] Exhaust: [temperature; cleanliness] Burners: [type; turndown; NOx limit] Preheat: [recuperator or regenerator; air temperature] Control: [purge; safety time; detection; interface]
1 company lists this product among what they make. Company figures are quoted from each company's own website; every card states where the relationship came from.
Lists recuperative, self-preheating, open-flame and regenerative burners, heat exchangers and burner controllers for industrial furnaces.
Product scope checked 2026-10-12
Explore company information and manufacturing capabilities, then discuss the scope of your project with a relevant supplier.
DOE's Process Heating Tip Sheet #1 gives 22% with 800 °F air on a 1,600 °F exhaust and up to 51% with 1,600 °F air on a 2,400 °F exhaust, for natural gas at 10% excess air. [1]
Siemens' LMO39 data sheet lists a start-up safety time (TSA) requirement of 5 s maximum, set at least 3% lower to allow for tolerance. [3]
For small automatic auxiliary boilers (117 kW or less), 46 CFR 63.25-1 requires at least four air changes of the combustion chamber and stack and not less than 15 seconds. [4]
Sources checked 2026-10-12. DOE's tip sheet and the eCFR are US government sources. Siemens' data sheet describes its own burner controls, and NPA's page describes its own combustion products.
Ask for use case, specification boundaries, supplier type, and RFQ preparation information for this product.
Compare manufacturer profiles with relevant product and process capability.