Energy Balance of basic
HVAC processes
Let’s assume a simple steady state air system where moisture air
flows in one direction, and an enveloping duct is perfectly insulated.
And Let’s say 1 refers to inlet status, 2 outlet status, \(\dot{Q}\) heat added (or extracted if
negative), \(\dot{m}_{da}\) dry air
mass rate, \(\dot{m}_{w}\) mass rate of
water added (extracted if negative), W humidity ratio, h moisture air
enthalpy in the state specified by a subscript, \(h_{f}\) liquid water enthalpy. Then the
following laws of conservation of mass and energy apply:
- Mass balance of dry air
\(\dot{m}_{da,1} = \dot{m}_{da,2}\)
- Mass balance of water vapor
\(\dot{m}_{da,1}W_{1} + \dot{m}_{w} =
\dot{m}_{da,2}W_{2}\)
- Heat balance of moist air
\(\dot{m}_{da,1} + \dot{m}_{w}h_{w} + \dot{Q} =
\dot{m}_{da,2}\)
These laws of conservation are the basis of all HVAC process
applications that follow. The same symbols hold true unless noted
otherwise.
1. Sensible heating and
cooling
- energy balance
\(\dot{m}_{da,1}h_{1} + \dot{Q} =
\dot{m}_{da,2}h_{2}\)
2. Adiabatic mixing
- mass balance of dry air
\(\dot{m}_{da,1} + \dot{m}_{da,2} =
\dot{m}_{da,3}\)
- mass balance of water
\(\dot{m}_{da,1}W_{1} + \dot{m}_{da,2}W_{2} =
\dot{m}_{da,3}W_{3}\)
- energy balance
\(\dot{m}_{da,1}h_{1} + \dot{m}_{da,2}h_{2} =
\dot{m}_{da,3}h_{3}\)
where 1 inlet 1 state, 2 inlet 2
state, 3 outlet state
3. Cooling and
dehumidification
- application: cooling coil
- Dehumidification occurs only when the cooling coil surface
temperature is lower than the dew point of incoming air.
- The condition of air leaving the cooling coil is not on the
saturation curve because a portion of air bypasses or is not in intimate
contact with the cooling coil.
- lower bypass rate is not necessarily good because it increases
pressure drop
- mass balance of water and condensation rate
\(\dot{m}_{da}W_{1} = \dot{m}_{w} +
\dot{m}_{da}W_{2}\)
\(\dot{m}_{w} = \dot{m}_{da}(W_{1} - W_{2})\)
- energy balance and cooling coil load
\(\dot{m}_{da}h_{1} = q_{cc} + \dot{m}_{da}h_{2} +
\dot{m}_{w}h_{f}\)
\(\dot{q}_{cc} = \dot{m}_{da}(h_{1} - h_{2}) -
\dot{m}_{w}h_{f} \approx \dot{m}_{a}(h_{1} - h_{2})\)
where \(h_{f}\) liquid water enthalpy
at the cooling coil leaving temperature condition, \(q_{cc}\) cooling coil load.
\(\dot{m}_{w}h_{f}\) is usually negligible
compared to \(\dot{m}_{da}(h_{1} -
h_{2})\)
4. Heating and humidification
- application: space sensible and latent cooling load, heater and
water spray
- mass balance of water and evaporation rate
\(\dot{m}_{da}W_{1} + \dot{m}_{w} =
\dot{m}_{da}W_{2}\)
\(\dot{m}_{w} = \dot{m}_{da}(W_{2} - W_{1})\)
- energy balance
\(\dot{m}_{da}h_{1}
+ q_{heat} + \dot{m}_{w}h_{f} = \dot{m}_{da}h_{2}\)
- cooling sensible and latent load
\(\dot{q}_{sen} + \dot{q}_{lat} = \dot{m}_{da}(h_{2}
- h_{1})\)
- heating and humidification
\(\dot{q}_{hc} + \dot{m}_{w}h_{f} =
\dot{m}_{da}(h_{2} - h_{1})\)
where \(\dot{q}_{hc}\) is heating coil load
5. Evaporative cooling
- application: humidifier water spray, cooling tower
- when unsaturated moist air passes through water, a certain amount of
water evaporate into the air. The latent heat is drawn from the air.
This results in temperature drop and humidity ratio rise of the
air.
- Although the process occurs along a constant wet-bulb temperature
line, it is not strictly isenthalpic because of a latent heat term.
- mass balance of water
\(\dot{m}_{da}W_{1} + \dot{m}_{w} =
\dot{m}_{da}W_{2}\)
\(\dot{m}_{w} = \dot{m}_{da}(W_{2} - W_{1})\)
- energy balance
\(\dot{m}_{da}h_{1}
+ \dot{m}_{w}h_{w} = \dot{m}_{da}h_{2}\)
- overall energy balance on a cooling tower
\(\dot{m}_{da}(h_{air,out} - h_{air,in}) =
\dot{m}_{w}(h_{water,in} - h_{water,out}) + \dot{m}_{da}(W_{out} -
W_{in})h_{f}\)
The evaporative cooling term, \(\dot{m}_{da}(W_{out} - W_{in})h_{f}\), is
smaller compared to the other two major terms.
References
- T.A. Reddy, et al (2016) Heating and cooling of buildings.
Principles and practice of energy efficiency deisgn. 3rd edition
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