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From: "rmichaelkeller" <rmichaelkeller@em*.ms*.co*>
To: "Christopher Brown" <hokiediver@ya*.co*>, <techdiver@aquanaut.com>
Subject: Re: Helium thermal properties
Date: Wed, 21 Feb 2001 19:59:31 -0500
From: Ray M Keller on 10/07/97 04:07 PM


I wrote this some time ago for the rebreather list and it still holds true
today.  If you want to know the physics behind the thermal properties of
Argon read on....

To:   edb2otid@mh*.ns*.go*.au*, rebreather@nw*.co*
cc:
Subject:  Re: Argon as suit inflation gas...?


This is an effort to explain to Bruce etal.  the physics of why Will's
Willie
stays warmer in Argon vs Air. This is going to be a bumpy road so please
read
through this a couple of times before you raise questions or provide
comment.

Argon has better insulating properties than air.  This is a statement that
we
have all heard hundreds of times.  But, what does it really mean to a man
hanging on a deco line with a chilly willie?  To answer this question we
must
first understand how the following two things relate: 1. The thermal
conductivity of Argon Vs Air and  2. Heat transfer

Part 1  Thermal conductivity of Argon Vs Air
In one ATM at 270 Kelvin,  Argon will conduct 0.1619 millwatt per centimeter
Kelvin (mW cm-1 K-1) of energy whereas Air will conduct 0.2374 millwatt per
centimeter Kelvin (mW cm-1 K-1).
In one ATM at 40 degrees Fahrenheit or 4.4 degrees C,  Argon will conduct
40.09
cal/(sec)(cm2)(C/cm) x 10-6 whereas air will conduct 58.31
cal/(sec)(cm2)(C/cm)
x 10-6.
In one ATM at 40 degrees Fahrenheit or 4.4 degrees C,  Argon will conduct
9698.13 Btu/(hr)(ft2)(F/ft2) x 10-6  whereas air will conduct
140105.71Btu/(hr)(ft2)(F/ft2) x 10-6.

Part 2  Heat Transfer
Heat is transferred by conduction, convection and radiation.  The principle
that
is applicable to this discussion is stagnant gas conduction* in a steady
state
of heat transfer.  This involves two fluids (liquid or gas) at different
temperatures, separated by a solid barrier,  such as a tube or pipe,  or in
this
case the wall of a dry suit.  The rate of heat flow q from the hot fluid to
the
cold equals the product of a proportionality factor commonly referred to as
the
overall heat-transfer rate U, the amount of barrier surface (undergarments
and
dry suit) through which the heat flows A,  and the temperature difference
between the two fluids Dt (water and gas inside the dry suit).

q = U A Dt

The above equation applies for local conditions only,  unless the three
factors
on the right side remain constant with respect to the flow paths of the
fluids.
With changing conditions this equation must be expressed in differential
form.

dq = U Dt dA

These two equations are directly applicable to systems involving conductive
and
convective heat transfer and may be adapted easily for use in systems
involving
radiant heat transfer.

The rate of heat flow q, called duty or heat exchanged, is the rate of
transfer
of energy with respect to time through the heat transfer surface.  The
overall
heat transfer rate U, accounts for the multiple resistances r, to heat flow
that
are present in a system.  Such resistances include the fluids themselves,
fouling deposits that may be present on the hot and cold surfaces of the
barrier
separating the fluids, and the barrier wall resistance itself.  The overall
heat
transfer rate is equal to the inverse sum of all of the resistances in a
series
as expressed in the following equation:

U = 1/(rh + rhf + rw + rcf + rc)

This equation applies directly to heat transfer through barriers with
constant
area normal to the direction of heat flow,  e.g. flat plates or the wall of
a
dry suit (this means no cooling fins).

The inverse of each of these resistances is referred to as conductance, h(h
=
1/r).  The higher the conductance (remember part one from above?) or lower
the
resistance, the greater is the ability of the fluid or material involved to
transmit heat.  In the case of hot and cold fluids, the conductances, hh and
hc,
are generally referred to as film coefficients.  These coefficients depend
on
the mode of heat transfer, i.e. conduction, convection, radiation, or a
combination thereof.  Numerous other factors influence fluid-film
coefficients,
including, but not limited to, system geometry, fluid-flow velocities, fluid
physical properties, difference between bulk fluid and wall temperature,
etc...
The steady-state rate of heat flow, q, is equal through all series
resistances.

*Conduction refers to the molecular transmission of heat through a body from
point to point within the body or from one body to another in direct contact
with it.  Conduction is generally limited to the transfer of heat through a
solid, such as a metal tube wall, or a series of solids in contact with each
other.  Heat transfer by conduction may occur in stagnant liquids or gases
when
no mixing occurs.  The basic theory of heat transfer by conduction was
established over a century ago by Fourier who expressed it as:

q= dQ/d0 = -kA(dt/dx)

It states that the rate of heat flow is equal to the thermal conductivity k
multiplied by the area of heat transfer and the temperature gradient.  A, is
the
surface area normal to the direction of heat flow, and dt/dx is the rate of
change of temperature with distance in the direction of heat flow.

My name is Raymond M. Keller, I am a chemist with a nuclear DOE facility
responsible for the interpretation of  organic and radiochemical
environmental
analytical data.








----- Original Message -----
From: Christopher Brown <hokiediver@ya*.co*>
To: <techdiver@aquanaut.com>
Sent: Wednesday, February 21, 2001 7:47 AM
Subject: Re: Helium thermal properties


> Brad is correct.  There are two types of specific
> heat, constant volume (Cv) and constant pressure(Cp).
> I think the one we are concerned with in dry suits or
> your lungs is the constant pressure, since the volume
> of the dry suit (or lung) is not fixed.  In your tank,
> it would be a different story, since the volume is
> fixed and the pressure is slowly varying, but who
> cares how chilly your tank is?  There is not much
> difference the magnitude of Cv and Cp.
>
> Argon Cp=1.14 kJ/(kg*C)
> Helium Cp=22.8 kJ/(kg*C)
> Nitrogen Cp=2.06 kJ/(kg*C)
>
> As you can see, the Helium Cp differs by a bunch.
> Roughly speaking, at the same mass (kg) and initial
> temp (C), Helium would carry away 22 times the energy
> (aka heat) (kJ) as Argon.  The Nitrogen is included as
> a reference, since that's about what air would be...
>
> To do Brad's second reccomendation (amount of body eat
> "lost" when filling with Air vs. Argon), we would have
> to use the first law of thermodynamics, but that is
> another bullet in another foot.
>
> Chris Brown
> Suffolk, Virginia
>
> --- Brad Beskin <bradb@ex*.ne*> wrote:
> > Helium is lighter (less dense)than air, and
> > therefore it conducts heat much more quickly.  This
> > is the reason you do not inflate your drysuit with
> > backgas.  Use an independent inflation system with
> > argon or air (argon is very dense and therfore
> > insulates well).
> >
> > To answer your physics question:
> > c = the specific heat of a gas (the amount of heat
> > necessary to change 1 kg of the substance 1 degree
> > celcius)
> > This would be helpful (in that shoot yourself in the
> > foot kind of way) to calculate the joules of body
> > heat you're gonna lose if you fill your drysuit with
> > He instead of Ar or Air.
> > -CB
> >   From: moorea(uol)
> >   To: techdiver@aquanaut.com
> >   Sent: Tuesday, February 20, 2001 8:05 AM
> >   Subject: Helium thermal properties
> >
> >
> >   Hello all !
> >   I´ve been diving since 86, and nowadays i made my
> > own mixes, but now, i decided to go certified.
> >   My instructor, talking about thermal loss in a
> > trimix class, explain me that the heat exchange is a
> > direct relationship with gas density.
> >   I´ve read and learn in the past (including in
> > phisics class at regular school) that heat exchange
> > depends of  thermal conductivity of the media (Q =
> > mc delta t) where "c" is the thermal conductivity.
> >   Can you help me with that ?
> >   Am i right ?
> >
> >   thanks
> >
> >   Marcelo Moorea
> >
>
>
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