Hot Water Heating System  Design Procedure
Hot water heating system design procedure with heat loss, boiler rating, heater units and more.
The design of a hot water heating system may follow the procedure as indicated below:
 Calculate the heat loss from the rooms
 Calculate the boiler output
 Select heater units
 Select type, size and duty of circulation pump
 Make pipe scheme and calculate pipe sizes
 Calculate expansion tank
 Calculate safetyvalves
1. Calculating Heat loss
Calculate transmission heat losses through walls, windows, doors, ceilings, floors etc. In addition heat loss caused by ventilation and infiltration of outdoor air must be calculated.
2. Boiler Rating
Boiler rating can be expressed as
B = H (1 + x) (1)
where
B = boiler rating (kW)
H = total heat loss (kW)
x = margin for heating up  it is common to use values in range 0.1 to 0.2
The correct boiler must be selected from manufacturing documentation.
3. Selecting Room heaters
Radiators and room heaters rating can be calculated as
R = H (1 + x) (2)
where
R = rating of heaters in room (W)
H = heat loss from the room (W)
x = margin for heating up the room  common values in the range 0.1 to 0.2
Heaters with correct ratings must be selected from manufacturing documentation.
4. Sizing Pumps
Capacity of circulation pumps can be calculated as
Q = H / (h_{1}  h_{2}) ρ (3)
where
Q = volume of water (m^{3} /s)
H = total heat loss (kW)
h_{1} = enthalpy flow water (kJ/kg) (4.204 kJ/kg. ^{o}C at 5 ^{o}C, 4.219 kJ/kg. ^{o}C at 100 ^{o}C )
h_{2}= enthalpy of return water (kJ/kg)
ρ = density of water at pump (kg/m^{3} ) (1000 kg/m^{3} at 5 ^{o}C, 958 kg/m^{3} at 100 ^{o}C)
For low pressure pumped circulation systems  LPHW (3) can be approximated to
Q = H / 4.185 (t_{1} t_{2}) (3b)
where
t_{1} = flow temperature (^{o}C)
t_{2}= return temperature (^{o}C)
For low pressure pumped circulation systems  LPHW a head 10 to 60 kN/m^{2} and major pipe friction resistance of 80 to 250 N/m^{2} per meter pipe is common.
For high pressure pumped circulation systems  HPHW a head 60 to 250 kN/m^{2} and major pipe friction resistance of 100 to 300 N/m^{2} per m pipe is common.
The circulating force in a gravity system can be calculated as
p = h g (ρ_{1}  ρ_{2}) (4)
where
p = circulating pressure available (N/m^{2})
h = height between center of boiler and center of radiator (m)
g = acceleration of gravity = 9.81 (m/s^{2})
ρ_{1} = density of water at flow temperature (kg/m^{3} )
ρ_{2}= density of water at return temperature (kg/m^{3} )
5. Sizing Pipes
The total pressure loss in a hot water piping system can bed expressed as
p_{t } = p_{1} + p_{2}(5)
where
p_{t } = total pressure loss in the system (N/m^{2})
p_{1} = major pressure loss due to friction ( N/m^{2})
p_{2}= minor pressure loss due to fittings ( N/m^{2})
The major pressure loss due to friction may alternatively be expressed as
p_{1} = i l (6)
where
i = major pipe friction resistance per length of pipe (N/m^{2}per meter pipe)
l = length of pipe (m)
Friction resistance values for the actual pipes and volume flows may be obtained from the special charts made for the pipes or tubes.
Minor pressure loss due to fittings as bends, elbows, valves and similar may be calculated as:
p_{2}= ξ 1/2 ρ v^{2}(7)
or as expressed as "head"
h_{loss } = ξ v^{2}/ 2 g (7b)
where
ξ = minor loss coefficient
p_{loss } = pressure loss (Pa (N/m^{2}), psi (lb/ft^{2}))
ρ = density (kg/m^{3}, slugs/ft^{3} )
v = flow velocity (m/s, ft/s)
h_{loss } = head loss (m, ft)
g = acceleration of gravity (9.81 m/s^{2}, 32.17 ft/s^{2})
6. The Expansion Tank
When a fluid heats up it expands. The expansion of water heated from 7 ^{o}C to 100 ^{o}C is approximately 4% . To avoid the expansion building up a pressure in the system exceeding the design pressure, it is common to led the expanding fluid to a tank  open or or closed.
Open expansion tank
An open expansion tank is only relevant for Low Pressured Hot Water  LPHW  systems. The pressure is limited by the highest location of the tank.
The volume of an open expansion tank should be the double of the estimated expansion volume in the system. The formula below can be used for a hot water system heated from 7 ^{o}C to 100 ^{o}C (4%):
V_{t } = 2 0.04 V_{w } (8)
where
V_{t } = volume of expansion tank (m^{3} )
V_{w } = volume of water in the system (m^{3} )
Closed expansion tank
In an closed expansion tank the pressure in the system is maintained partly by compressed air. The expansion tank volume can be expressed as:
V_{t } = V_{e } p_{w } / (p_{w }  p_{i } ) (8b)
where
V_{t } = volume of expansion tank (m^{3} )
V_{e } = volume by which water contents expands (m^{3} )
p_{w } = absolute pressure of tank at working temperature  operating system (kN/m^{2})
p_{i } = absolute pressure of cold tank at filling  non operating system (kN/m^{2})
The expanding volume may be expressed as:
V_{e } = V_{w } (ρ_{i }  ρ_{w } ) / ρ_{w } (8c)
where
V_{w } = volume of water in the system (m^{3} )
ρ_{i } = density of cold water at filling temperature (kg/m^{3} )
ρ_{w } = density of water at working temperature (kg/m^{3} )
The working pressure of the system  p _{ w }  should be so that the working pressure at highest point of the system corresponds to the boiling point 10 ^{o}C above the working temperature.
p_{w } = working pressure at highest point
+ static pressure difference between highest point and tank
+/ pump pressure (+/ according the position of the pump)
7. Selecting Safety Valves
Safety valves for forced circulation (pump) systems
Safety valve settings = pressure on outlet side of pump + 70 kN/m^{2}
Safety valves for gravity circulation systems
Safety valve settings = pressure in system + 15 kN/m^{2}
To prevent leakage due to shocks in the system, it is common that the setting is no less than 240 kN/m^{2}.
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