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Q: heat content air ( Answered 5 out of 5 stars,   0 Comments )
Question  
Subject: heat content air
Category: Science > Physics
Asked by: 3rrotec-ga
List Price: $20.00
Posted: 01 Jun 2004 05:12 PDT
Expires: 01 Jul 2004 05:12 PDT
Question ID: 354675
I am interested in formulas and charts to figure the available
recoverable heat of air and water vapor at various temperatures and
humidities. Use pressure of 29.94 in hg. I am familiar with the
formula: w=(1.325*barometer)/temp(absolute) to find the density of dry
air, but how do I figure the vapor part? Thanks! 3rrotec Robert
Williams

Request for Question Clarification by hedgie-ga on 02 Jun 2004 10:59 PDT
Hello 3rrotec
The phrase 'recoverable heat' is not  clear. Perhpas you
mean 'What is the density w of mixture of air and vapor, as function of
T p and c (Temperature, pressure, and composition).

Do you want that answer?

hedgie

Clarification of Question by 3rrotec-ga on 02 Jun 2004 16:51 PDT
Hi hedgie! I think you have helped me in the past. Yes I need to be
able to figure the density of the mixture. I found a chart in a
Schaum's outline - "Heat Transfer" that tells me the density of dry
air at various temperatures.(This chart follows the formula perfectly
if you use 29.94 in hg). The chart also tells me the Cp value
(Btu/LBm-degree F). The chart runs from -280 degrees F to +4160. At
350 degrees F (177 degrees C - 810 degrees R) the density is .0489
Lbs/cu. ft. The Cp value is .2438. If I am reading this correctly, it
is telling me if I reduce the temperature of 1 pound of the dry air to
349 degrees F, I have removed .2438 Btu's. Is this correct? We
manufacture sludge dehydrators. Most sales go to city waste water
treatment plants. Some plants have a surplus of hot air available. The
quality of the air streams vary (percent humidity). I have the chore
to decide if it is worth trying to reclaim this heat from the air
stream and apply it in our drying process. Our web site is
www.sludgedryers.com if you would like to look at our product. I would
like to fax this chart to you if I can. I'm honest and will not try to
screw Google around. If I am reading this chart correctly we are off
and running. If not, get me straightened out first on the chart and I
will post a new question for you! Thanks Robert Williams 3rrotec
Answer  
Subject: Re: heat content air
Answered By: hedgie-ga on 03 Jun 2004 18:32 PDT
Rated:5 out of 5 stars
 
Hi robert

Indeed. We worked together before, more then once.

Let's do this in two installments. In this one I am posting
links to the general theory.
 These pages contain informationon the density of moist air, so I
guess we do not a chart describing  dry air only. It should contain
the chart you have
as a special case.

In second, we can look at specific application to  the heat recovery,
 But please let's use SI (metric) units for any actual calculations
  Btu's give me headache :-).
  
So,
Today's topic, (and search term) is Equation of State,
defined e.g. in wikipedia as folows:

  In physics, equations of state  describes the relationship between
temperature, pressure, and volume for given substance or mixture of
substances.

http://en.wikipedia.org/wiki/Equation_of_state

In our case Dalton's law is of interest:
 In physics, Dalton's law (also called Dalton's law of partial
pressure) is a law that states the total pressure exerted by a gaseous
mixture is equal to the sum of the pressures that would be exerted by
the gases if they alone were present and occupied the total volume.
 
So, treating the water and air as a mixture of ideal gases, we can obtain the
 density w  at any T and p. All we  need to are molecular weights of
all the components
 (O2, N2, H2O ..). Ideal gas in as aproximation, which is well
applicable near room
 temperature and normal atmospheric pressure.
 
 Since water/air is an important mixture, there is a number of sites
where the numbers are
 already derived. Here is powerpoint presentation:
 http://snowball.millersville.edu/~amuller/esci385/equation%20of%20state.ppt
 
 and here a simple pages from NASA which reviews composition of air and units.
 http://www.grc.nasa.gov/WWW/K-12/airplane/airprop.html

 and here are the equations worked out in bothe sets of units 
 http://www.engineeringtoolbox.com/8_677.html
 
 Both sites have related pages
 
This page describes amount of water vapor in the air,  often expressed
as a vapor pressure, given the symbol e.
 http://snobear.colorado.edu/Markw/SnowHydro/Phases/phases.html
 
 
 For practical use, it would be useful to have a spreatsheet or program.
 
 SEARCH TERM 'moist air' produces:
 http://www.mathtools.net/Excel/Chemometrics/
 page, promising:
 
  MoistAirTab - Following our success with the SteamTab products,
ChemicaLogic is proud to introduce MoistAirTab?, a unique new
spreadsheet add-in. MoistAirTab? gives you access to a comprehensive
set of air, water, steam and ice properties - allowing you to easily
do complex simulations involving moist air.
  
  similar tools are promised at this university site:
  
  Welcome to TEST - a visual environment to solve thermo problems,
pursue what-if scenarios, perform numerical experiments, and continue
a life-long learning experience to challenge Sommerfield! Browse a few
slides from Slide Show (10 min) followed by a hands-on Tutorial (30
min) to put TEST to full use without much of a learning curve.
 
  http://kahuna.sdsu.edu/testcenter/testhome/index.html
  
  These tools would have to be tested. I have not done that (so far).
  
  Hedgie

Request for Answer Clarification by 3rrotec-ga on 04 Jun 2004 12:12 PDT
Thanks Hedgie! I will digest this this weekend and get back to you
Monday. I will send you some sample calculations to make sure I
understand. Have a good weekend! Thanks again 3rrotec Robert Williams

Clarification of Answer by hedgie-ga on 05 Jun 2004 23:01 PDT
OK, I will look for it.

1) It seems that what you are looking is not just 
 mixture density w(T,p,c) but mostly for 

Maximum moisture holding capacity of air at selected air temperatures
as shown e.g. here

http://www.bae.umn.edu/extens/aeu/aeu14.html


is that right?


2) Are you considering (a smaller scale perhaps) of a Biosolids drying plant
like this one from spain?

 Thermal Drying Plant at the South Madrid Waste Water Recycling
Station, which went into operation in the first quarter of 2001....

http://www.infopower.es/infopower58/58reportbutarquepag15eng.htm

Request for Answer Clarification by 3rrotec-ga on 06 Jun 2004 14:49 PDT
Hi Hedgie! I've already declined the recovery of heat for the proposed
site. Not economically feasible to build the heat exchanger. I still
want to proceed with you. I want a mathematical understanding of heat
in air, moist and dry, and the ability to readily figure different
psychrometric events. This will entail study from me and patience from
you. Good luck working with a 57 year old machinist, engineer, and
redneck! You will find I'm full of questions and will not proceed to
step two until I understand step one. On to clarification number one.
I am working on "Humid Air and the Ideal Gas Law" (Engineering tool
box- I sure like this format!). I can't get the mass equation to come
out in SI units. I'm willing to work in SI units as long as I can
transpose them correctly. I think in English units. I can't think in
metric yet but I'm trying. Our customers also use the english system
(Ft/sec, Btu's, Lbs/cu. ft., etc).
 I took the equation PV=MRT.  I assumed the following:
   Volume= 1 cubic ft
   Temp= 492 R
   Gas constant= 1716
   Pressure= 29.94 inches mercury=2117.5 lbs/sq ft
   Gravity constant 32.16 ft/sec*sec
Solving for M,  M=.0025 Lbs  since I assumed 1 cu ft, answer is .0025 lbs/cu ft
Next I took the equation W=1.3125*Barometer/Temp R
   W=.080 lbs/cu ft
I suppose the mass equation is in outer space, but I'm on Earth, so I
multiplied it by the gravity constant
   .0025*32.16=.080
The answers equal so I assume I'm correct. This also agrees with the
charts (I don't trust charts unless I can mathematically prove them.
That way I know I understand)
Next I tried the SI units as follows:
   Volume=1 cu meter
   Pressure= 29.94 in hg= 101389 newtons/sq meter
   Gas constant=286.9
   Temp=273 Kg
Solving for M,  M=.772 Kg   Since I assumed 1 cu meter answer is
   .772Kg /cu.meter
converting to Lbs/cu ft
   .772*.0624=.048 Lbs/cu ft
.048 does not equal .0025. Where did I screw up and what is the metric
gravity constant? As soon as we clear this up I will close this
question and post a new one. Thanks Robert

Clarification of Answer by hedgie-ga on 07 Jun 2004 12:19 PDT
hello Rob

   I fully support the principle of understanding formulas before using them,
   particularly when using them for some real decisions. I once had a job
   in which I had to  convert all my results to imperial units for use in 
   engineering designs, so I am confident that we can reconcile the units.
   However, it is not just the units. We need to have clarity about what
   system we are talking  about.
   
    When you say  P * V = M * R * T we mean by M mass of what?
   
   So let's first agree on this: We take  Ma  kilograms of air
                                          Mw  kilograms of water
					  
 let  both equilibrate at Temperature T (measured in Kelvins K), high
enough so that all components are in gas state and let's keep them in
a vessel at pressure P (Pascals)
 
 Question  is:  what will be the volume of that mixture?
 
  We can imagine that we have it in a cylinder with a piston on the top.
  As an example, consider area of piston is 2 m *m  and  weight on top
of it is provided by the mass of  M kg.
  
  Then the pressure under the piston is  M * 9.81 /2   Pascals.  OK ?? 
   (please do ask if this is not clear)!!  g=9.81 m/s .s is gravity.
   
  That same thing  can done  in IU (imperial or customary units),
  and checked  e.g. by using this handy calculator:
  http://www.allmeasures.com/conversion.asp?Submit=Converter
  
  E.g.  if mass was 20kg, , P is  98.1 Pa which, using above URL is 
  
  0.0142282020 psi (I had to check the box pressure at the bottom,
which took me to the  page
  http://www.allmeasures.com/conversion.asp?pressure=on&Submit=Converter
  
  BTW this webpages can be downloaded and still work locally.
  
 I suspect that this   W=1.3125*Barometer/Temp R  is the same formula as the 
  Equation of state  P * V = M * R * T
 as density w= V/M  and P is the "barometer" , right? , so I am not
surprised at agrees.
 
 BUT - equation of state of what? air, water, mix 50:50 ?? or what? 
The constant R changes according to the mass ratio  Ma:Mw - and  Mr.
Dalton figured how. That was really your question  and so I want to
finish answering that .
 
 Answer is here:
   http://www.engineeringtoolbox.com/8_680.html
   
   namely:
   
   Based on specific volume of moist air the density can be expressed as: 

 

? = 1 / v = (p / Ra T) (1 + x) / (1 + x Rw / Ra)    (3)

 

where 

 

v = specific volume of moist air per mass unit of dry air and water vapor (m3/kg)

 

Ra = 286.9 - the individual gas constant air (J/kg.K) 

 

Rw = 455 - the individual gas constant water vapor (J/kg.K) 

 

x = specific humidity or humidity ratio (kg/kg)

 

p = pressure in the humid air (Pa)
 
 
 When x, mass ratio, is 0 (no water) this is reduced to your formula
for da="dry air" namely
 
 ?.da = p / Ra T   (4)
 
 
 You cannot use it when x>0.  
 
 Now - problem with conversion: Often, people using lb to denote
 pound of force  and pound of mass get confused, when going to SI,
 since SI is different. The NASA site above is uisng Customary Units,
 but measures mass in slugs and force in pounds. That has same logic as
 SI, which measures mass in kg and force in N. Once you mesure mass in
 either slugs or kg, you do not need g (gravity)
 (except as above, when we are using weight to create the pressure).
 Gravity does not enter the problem any other way, no matter where you are.
  
 So. I expect the conversion to SI problem to diappear if we would  do that
 (if we would not confuse mass and force by measuring them by same unit).
 Please let me know if it does.
 
 hedgie
3rrotec-ga rated this answer:5 out of 5 stars
Thanks Hedgie, on to step two!

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