HVAC Ventilation
HVAC Ventilation
1-31-07
Bill Greco
      The following concerns Pharmaceutical production areas, research areas and other areas where
 annoying or dangerous vapors can be released. Many times vapors are not controlled by special ventilation
 apparatus such as hoods or carbon filtration. Vapors can be caused by laboratory accidents, use of cleaning
 solvents applied outside of the influence of the exhaust system or by special adhoc procedures conjured up
 by jury rigged processes. The primary general HVAC system often becomes the last line of defense to confine and
 dilute these vapors which have escaped into a conditioned space. A primary general HVAC system is
 meant to serve as supply and exhaust of air to control comfort or specifically produce a controlled environment
 within regulated room classification requirements. If vapors are re-circulated and confined within a
 primary general HVAC system, only outside air will dilute the unwanted vapor. Unfortunately opening
 a window in most cases is not a possibility.
    A prime function of many substances especially solvents is to evaporate into the local atmosphere
 leaving behind a physically or chemically transformed material formerly associated with it. Evaporation
 of many substances cause fumes, gases, vapors and / or mists. It is nearly always possible to
 estimate the rate or use of total liquid composition, to determine the rate of evaporation.
 This makes it especially simple, to handle vapor ventilation problems on a quantitative basis with relation to time.
      The following could be used to calculate any concentration of vapor or could be representative of the
 differential of a mixture of some substance being added over a time period in a tank of fluid through which
 fresh fluid is being added and continuously removed. The procedure can be applied to any case where air is
 initially charged with contaminant and it is desired to estimate the conditions in the space in relation to time.
 Assume evaporation of one pound of turpentine C10 H16 which has a molecular weight of 136.23
 that has evaporated over a period of one hour. The total volume of vapor per hour is :
     2.839 cuft/ hour or 0.047 cuft/min or a generation rate (G) of 0.047 cfm
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1-31-07
Bill Greco
                      Vapor Dilution with respect to Outside Air over a period of Time
     An increase in the quantity of vapor in the space during the time interval dt, is equal to the
 rate of vapor being added to the space minus the removal rate of vapor leaving the space.
   The relation between the ratio of concentration of vapor c and time t can be developed
  from the equation:
        where:
           Q = Ventilation Rate, cfm (air exhausted)
           G = Vapor generation rate, cfm
           c = Ratio of substance vapor to air in parts per million expressed as a fraction at time t
           c_initial = Initial ratio of substance vapor parts per million at time t=0
           P = Cubic Displacement of the space
c t
which becomes:
solving for t =
and:
Simplifying:
      Changing signs:
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1-31-07
Bill Greco
                   Vapor Dilution with respect to Outside Air over a period of Time
 :
Multiply by P =
Divide by 0.435Q =
Rearranging =
   Example-1:
   Assume a research lab 30 feets long x 15 feet wide with a 10 foot high ceiling.
 A repetitive procedure is being performed in which a lab technician is using 1 pound of acetone on
 a lab bench for 30 minutes during each process, the procedure must be conducted outside of the
 labs hood area. The primary general HVAC system as shown in Figure-1 supplies conditioned air
 to the space, 170 cfm is being exhausted from the room. The room temperature is controlled
 to 700 F. The procedure is started with 0 parts per million (ppm) in the room.
 How long will the procedure be allowed to continue prior to reaching acetone’s threshold level
 of 1,000 parts per million ?
  If the process is stopped at 1,000 ppm, how long will it take the room air in example-1 to
 dilute and reach 500 ppm ?
 Refernce:
   Hemeon, W.C.L.       Plant and Process Ventilation Second Edition         pp 228-232