NATE Gas Heating Service study materials
NATE Gas Heating Service study resources

NATE Gas Heating Service cheat sheet

NATE Gas Heating Service · Keep the key ideas within reach.

Quick reference

Combustion Theory and Gas Fundamentals

  • Complete combustion of methane: CH4 + 2O2 → CO2 + 2H2O; each volume of methane needs 2 volumes of oxygen (about 9.5 volumes of air).

  • Stoichiometric (perfect) air for natural gas is roughly 10 ft³ air per ft³ gas; typical setup targets 25–50% excess air for safety margin.

  • The three elements of the combustion triangle are fuel, oxygen, and an ignition source; removing any one stops combustion.

  • Flame color diagnosis: stable blue cone = good combustion; lazy yellow tip = insufficient primary air; lifting flame = excessive primary air or high gas pressure.

  • Heating value: natural gas about 1,000–1,050 Btu/ft³ HHV; propane about 2,500 Btu/ft³; LP is heavier than air (about 1.5–2.0 specific gravity) and pools at low points.

  • CO is produced by incomplete combustion: insufficient air, overfiring, blocked flue, dirty burners, or flame impingement on a cool surface.

  • Lower flammability limit for natural gas is about 4–5% gas in air; upper limit about 15%; within this band an ignition source causes ignition.

  • Gas-specific gravity vs air: natural gas about 0.60 (rises and vents high), propane about 1.5 (sinks); leak detection and ventilation strategy follow this difference.

  • Draft is created by temperature difference (stack effect) and by the vent connector height; a Category I appliance needs a negative pressure in the flue at all times.

Quick reference

Venting and Combustion Air

  • Category I: non-condensing, negative flue pressure, must vent vertically or with approved slope; Category IV: condensing, positive pressure, uses PVC/CPVC and must be pitched back to the appliance.

  • Category III is positive pressure, non-condensing (usually stainless); Category II is negative pressure, condensing - rarely encountered.

  • A single-wall metal vent connector needs 6 in. clearance to combustibles; a Type B double-wall vent needs 1 in. to combustibles in most listings.

  • Vent connector slope: at least 1/4 in. per foot rise toward the chimney for natural draft appliances; horizontal runs should be as short as possible.

  • Standard (fan-assisted) category I appliances commonly use double-wall Type B vent; a listed vent cap or termination is required at the outlet.

  • Combustion air by the standard method: 50 ft³ per 1,000 Btu/hr input for an unconfined space; a confined space needs two permanent openings (high and low).

  • Two-opening rule: each opening sized at 1 in² free area per 1,000 Btu/hr of total input when communicating directly with outdoors, or 1 in² per 2,000 Btu/hr through vertical ducts.

  • A blocked flue or reversed draft spills combustion products into the space; a draft hood spill test (match flame at the relief opening) confirms proper draft.

  • Condensing appliance venting: PVC flue gas is acidic (condensate pH about 3–5); condensate must drain to an approved neutralizer or drain, and vent slope is back to the appliance.

Quick reference

Gas Piping, Valves, and Burner Components

  • Gas piping sizing uses longest-length method or branch-length method with tables based on Btu/hr load, specific gravity, and pressure drop; undersizing causes pressure drop and underfiring.

  • Sediment trap (drip leg) is required at the appliance connection: a tee with a capped nipple below, installed so debris falls out before reaching the gas valve.

  • A manual shutoff valve must be installed in the supply line within 6 ft of the appliance and be readily accessible; a union allows service removal.

  • Leak test: pressurize the new piping with air or inert gas (commonly 10–15 psig for a short duration or per local code); never use a flame, and isolate the appliance gas valve.

  • Manifold gas pressure for natural gas is typically 3.5 in. w.c.; propane typically 10–11 in. w.c.; supply pressure is higher and is reduced by the appliance regulator.

  • Combination gas valve functions: manual shutoff, pressure regulation, safety shutoff (automatic), and manifold pressure adjustment; some include a redundant operator.

  • Burner components: orifice (meters gas by size), mixer/venturi (entrains primary air), manifold, burner ports, and flame spreader; a dirty orifice changes input rate.

  • Orifice sizing: input Btu/hr = orifice capacity factor × manifold pressure correction; drilling out or swapping orifices changes firing rate and must follow the rating plate.

  • A gas valve that fails to open, a stuck redundant operator, or a bad thermocouple/pilot generator all present as no heat with the inducer running.

Quick reference

Ignition, Safety Controls, and Electrical Interface

  • Standing pilot: thermocouple generates about 25–30 mV open circuit; the gas valve needs roughly 10–15 mV under load to hold the pilot operator open.

  • Intermittent pilot (IP) ignition: spark ignites pilot, flame rectification proves it, then main valve opens; a dirty flame sensor causes lockout after a short trial.

  • Direct spark ignition (DSI) and hot surface ignition (HSI) prove flame by flame rectification (microamp signal, typically 1–5 µA); a weak signal causes nuisance lockout.

  • Flame rectification requires the flame to touch the sensor and the burner ground to be intact; reversed polarity or a poor ground prevents proving.

  • Sequence of operation: call for heat → inducer proves (pressure switch) → ignition source energizes → gas valve opens → flame proved → blower on delay → heat rise → blower off delay.

  • Pressure switch proves inducer airflow; a blocked port, water in the tubing, or a weak inducer prevents the switch from closing and the sequence stops before ignition.

  • Limit switch (high limit) opens on excess temperature and breaks the thermostat circuit; rollout switch is a manual-reset device that trips on flame rollout.

  • Control board lockout: after a set number of failed trials the board locks out; reset by cycling power or thermostat, and the LED fault code identifies the failed step.

  • 24 V control circuit: thermostat R–W call energizes the gas valve and safeties in series; a blown low-voltage fuse or open safety anywhere in the string stops the call.

Quick reference

Airflow, Heat Exchangers, and Temperature Rise

  • Temperature rise = supply air temperature minus return air temperature; compare to the rating plate range (commonly 35–65°F for residential furnaces).

  • CFM ≈ output Btu/hr ÷ (1.08 × temperature rise); 1.08 is the sensible heat constant for standard air at sea level.

  • High temperature rise: low airflow, dirty filter, restricted evaporator coil, dirty blower wheel, or wrong blower speed - check static pressure and filter first.

  • Low temperature rise: overfiring, oversized blower speed, or duct leakage; verify manifold pressure and gas input before changing blower speed.

  • External static pressure: measure with a manometer across the furnace; typical residential design is 0.5 in. w.c. total; excessive static means duct restriction.

  • Heat exchanger inspection: look for cracks at the cell seams, discoloration, water stains, and flame distortion; a cracked heat exchanger can allow CO into supply air.

  • Blower motor types: PSC (permanent split capacitor) speed set by taps; ECM/X13 (constant torque) and variable-speed ECM maintain airflow against static changes.

  • Combustion air and dilution air must not be blocked by a dirty filter or a closed louver; verify the inducer wheel and flue are clear before diagnosing airflow.

  • A heat exchanger with a restricted secondary passage shows high rise, high flue temperature, and a yellow flame - a combustion analysis confirms before replacement.

Quick reference

Startup, Combustion Analysis, and Troubleshooting

  • Combustion analyzer readings for natural gas: O2 about 4–9%, CO2 about 8–9.5%, CO under 100 ppm air-free (target under 50 ppm), stack temperature per rating.

  • Air-free CO = measured CO × (20.9 ÷ (20.9 − measured O2)); air-free CO corrects for dilution and is the number compared to limits.

  • Excess air % = (20.9 ÷ (20.9 − O2)) − 1, then ×100; 25–50% excess air is typical for a properly set natural gas appliance.

  • Draft check: measure draft in the flue with a manometer or draft gauge; a Category I appliance should show negative draft (about −0.02 to −0.04 in. w.c. at the relief opening).

  • Startup checklist: verify gas supply pressure at the valve inlet, manifold pressure, flame appearance, temperature rise, static pressure, and combustion readings.

  • Flame signal (microamps) below the manufacturer's minimum (often 1–2 µA) causes intermittent lockout; clean the sensor and verify ground before replacing the board.

  • Troubleshooting order: confirm thermostat call, check 24 V at the board, confirm inducer and pressure switch, confirm ignition, then confirm gas valve and flame proof.

  • Gas leak at the manifold or valve shows as a pressure drop with the appliance off; test with a manometer or leak detector solution, never an open flame.

  • Short cycling causes: high limit trip (low airflow), thermostat location, oversized unit, or a failing flame sensor dropping the call - verify rise and static first.