 Home ● Fuel Costs ● Installation ● Library ● Fireplace Doctor ● Tables, Data and Formulas ● More ≡

Tables, Data and Formulas
for solid fuel heating engineers.

APPLIANCE PERFORMANCE - SIEGERT'S FORMULA
For estimating appliance efficiency from CO2 concentration in flue gas Where:
E is Efficiency as a percentage
Ta is the temperature of the exiting flue gas, in ºC
Tr is the ambient (room) temperature, in ºC
CO2 is the percentage CO2 in the exiting flue gas
A1 is a fuel factor: Anthracite=0.683, Coke=0.290, Bituminous Coal=0.672, Lignite=1.0, Peat Briquettes=0.7, Dry Wood=0.650

The total heat output in kW is then estimated from: Where:
P is the total heat output in kW
E is the Efficiency as a percentage
F is the fuel used, in kg
T is the burn time in hours
CV is the potential heat of the fuel in kW per kg, using data on the fuel properties page

Boiler output is then calculated from: Where:
Pw is the boiler output in kW
Cp is the specific heat of water = 4.18
Mw is the water flow rate in kg / hr
N is the water temperature rise in Celsius degrees
The room heating output of this boiler appliance is then estimated by subtracting the boiler output Pw from the previously calculated total output, P.

'NET' AND 'GROSS' EFFICIENCY
The 'net' (higher) efficiency figure applied to solid fuel appliances tested to EN Standards doesn't account for the heat wasted in boiling off the water in the fuel. It is a bit difficult to calculate, but the more accurate 'gross' (lower) efficiency is usually about 0.91 of the the net efficiency for wood fuels and about 0.98 for mineral fuels, so a European wood-burning appliance claiming to be 80% (net) efficient is probably closer to 73% (gross).
See: The UK Government’s Standard Assessment Procedure (SAP) for assessing the energy performance of dwellings: http://www.bre.co.uk/filelibrary/SAP/2009/SAP-2009_9-90.pdf

CHIMNEY PERFORMANCE (ROUGH)
(Hughes' Formula) Chimney pressure:
ΔP = 0.02 x (Tc - Ta) x h

Where:
ΔP = The pressure difference (draught) in Pascals
Tc = Average chimney flue internal temperature, °C
Ta = Ambient (outside) temperature, °C
h = The chimney height in metres.

OR...

Flue draught = Assuming that the molecular mass (i.e., molecular weight) of the flue gas and the external air are equal and that the frictional pressure and heat losses are negligible:
where:
Q = chimney draught/draft flow rate, m³/s
A = cross-sectional area of chimney, m² (assuming it has a constant cross-section)
C = discharge coefficient (usually taken to be from 0.65 to 0.70)
g = gravitational acceleration, 9.807 m/s²
H = height of chimney, m
Ti = average temperature inside the chimney, K
Te = external air temperature, K.

OPEN FIRES
Openings for open fireplaces 'The Method of Metres'

The maximum area of an open fireplace opening is (Hughes' Formula)
A = H x F

Where:
A = Fireplace opening area
H = Height of chimney in metres
F = Flue cross-section area

APPLIANCE PERFORMANCE (ROUGH)
Appliance output (kW) (rough guess) = volume of firebed (m³) x 400

GAS CONCENTRATION
To (approximately) convert between mass per unit volume and ppm (parts per million) OR Where:
mg/m3 is milligrams of pollutant per cubic meter of gas
ppmv is pollutant concentration, in parts per million by volume
T is ambient temperature in Kelvin (temp in °C + 273)
0.08205 is the universal gas constant
M is the molecular mass (or molecular weight, in g/mol) of the substance, CO = 28, CO2 = 44, NO2 = 46, CH4 = 16

ENERGY STORAGE IN WATER
Water can store about 4181 Joules of heat energy per kg (or litre) of water for every degree (°C) of temperature difference between the water and whatever (usually the room air) it is going to be transferred to.
So, given a thermal store of 400 litres capacity at 70°C when the house around it is at 15°C, how many hours heat can it store?
The temperature difference is 70-15 = 55°K, multiplied by the capacity of 400, multiplied by 4181 = 91982000 Joules stored.
A Joule is a Watt per second and a kW is a thousand watts (per hour), so divide by 3 600 000, and a 400 litre store can hold about 26kW.
If the home has a heat requirement of, say, 6 kWh, then the store can provide about 4 hours heat.
Note that if the stored temperature was raised to 80°C, the store could hold 30kW, about 5 hours heat.
Roughly, it takes 1.16 Watts to heat 1 litre of water by 1 °C, and, typically every 100 litres can hold about 6kWh.

ENERGY EQUIVALENTS
1 TOE (ton oil equivalent) = 11 630 kilowatt hour
1 TCE (ton coal equivalent) = 8 141 kilowatt hour
1 gigajoule = 278 kilowatt hour
1 megajoule = 0.278 kilowatt hour
1 gigawatt hour = 1 000 000 kilowatt hour
1 therm = 29.3 kilowatt hour
1 terajoule = 277 777.777 78 kilowatt hour
1 barrel of oil = 1628 kWh
1 ton wood = 5140 kWh

SMOKE MASS CONVERSIONS
Smoke (particulates) quantity can be expressed in several different ways, none of which is readily converted to the other. The following are approximations based on the stove matrix
Where...
1 mg smoke per m³ flue gas =
3.1 mg smoke per kW heat output =
15.7 mg smoke per kg fuel wood =
0.86 mg of smoke per GigaJoule (GJ) heat output
0.0009 mg of smoke per MegaJoule(MJ) heat output

AIR FLOW THROUGH ORIFICES
Flow of gas through an orifice is given from Where:
Q = gas flow rate in m³ per second
Cd = the 'discharge coefficient', about 0.61 for a hole in a flat plate
A = opening area in m²
ΔP = pressure difference, in Pascals
T = turbulence factor. About 0.5 for a hole in a plate
ρ = density of the gas. Air = about 1.2

TYPICAL FLUE AND AIR REQUIREMENTS
Open fire fresh air opening to room = c½ minimum flue cross-section
Maximum open fire 'face' area = c7 x minimum flue cross-section
or, the 'method of metres' - the ratio of room face opening to flue cross-section = the chimney height in metres
Closed fire air opening to to room = c550 sq mm per kW
Closed fire air opening to firebox = c130 sq mm per kW
Low flue draught = c6 Pa = 0Ģ025 ins water
Normal flue draught = c12 Pa = 0Ģ05 ins water
High flue draught = c17 Pa = 0Ģ07 ins water

PROPERTIES OF MATERIALS
 . Density kg/m³ Specific Heat J/g/°K Air (20°C) N=78%, O2 =21%, CO2=0Ģ04% 1Ģ26 1Ģ1 Water (25°C) 1000 4Ģ18 Water vapor (100°C) 0Ģ60 2Ģ08 Water vapor (200°C) 0Ģ47 1Ģ98 Water vapor (300°C) 0Ģ38 2Ģ01 Iron (25°C) 7870 0Ģ45 Copper (25°C) 8960 0Ģ39 Aluminium (25°C) 2700 0Ģ90 Brick (typical) 2400 0Ģ84

FLOW
1 pound/hour = 0Ģ453 592 kilogram/hour
1 kilogram/minute = 60 kilogram/hour
1 (UK) gallon/minute = 0Ģ075 768 litre/second

ENERGY
1 calorie [IT] = 4Ģ186 joule
1 calorie [thermochemical] = 0Ģ000 001 162 kilowatt
1 Btu = 0Ģ000 293 071 kilowatt = 1 055 Joule
1 kilowatt = 3 412Ģ14 Btu/hour
1 therm = 100,000 Btu = 29Ģ30 kilowatt hour
1 joule = 1 Watt per second
1 kW/hr = 3,600,000 Joules
1 Watt/hr = 3,600 Joules

PRESSURE
1 bar = 100 000 pascal = 100 kPa
1 inch of water [4°C] = 249 pascal
1 millimetre of water [4°C] = 9Ģ81 pascal
1 metre of water [4°C] = 9806 pascal = 9Ģ81 kPa
1 newton/square metre = 1 pascal
1 pound/square inch = 6 894 pascal
Standard Atmosphere = 1Ģ013 250 bar

THERMAL TRANSMITTANCE
Btu/hr,ft²,°F x 5Ģ675 = W/m²,°C
R value (thermal resistance) = 1/U-value

LENGTH
1 metre = 3Ģ281 feet (ft) = 39Ģ37 inches (in)
1 inch = 25.4 millimetre

AREA
1 square foot = 0Ģ09289 m2
1 square yard = 0Ģ09289 m²

VOLUME
1 cubic metre (m3) = 1000 litres
1 US gallon = 3Ģ785 litres, 1 Imperial gallon = 4Ģ546 litres

MASS
1 kilogram (kg) = 2Ģ205 pounds (lb), 1 pound (lb) = 453Ģ6 grams (g)

TEMPERATURE
Temperature Celsius (°C) = 0Ģ714 x (°F- 32)
Temperature Fahrenheit (°F) = (1Ģ8 x °C) + 32
Kelvin or absolute (°K) = degrees Celsius (°C) + 273Ģ15
1 degree interval (°K or °C) = 1Ģ8 °F interval

 MORE FROM Soliftec... Home ● Fuel Costs ● Installation ● Library ● About ● Air Supply ● Blogspot ● Building Rules ● Carbon Monoxide ● CE Marking ● Dictionary ● Efficiency ● Electricity - CHP ● Embodied Energy ● Fascinating Facts ● Fireplace Doctor ● Fuel Properties ● Heat Need ● Heroes ● Legislation ● Manufacturers ● Open Fires ● Ringelmann scale ● Rocket Stoves ● Smoke ● Solid Fuels ● Standards ● Statistics ● Stove History ● Tables, Data and Formulas ● Test Laboratories ● Thatched Roofs ● The Carbon Cycle ● The Chimney Effect ● Wood Fuel ● Email: COPYRIGHT and ALL RIGHTS RESERVED: © , Thursday 23 January 2020 BUILT WITH WHIMBERRY matrixstats