Since the first two losses are essentially constant at high vacuum for a given sensor, we can measure these losses and subtract them from the input power which leaves only the rate of heat transmission through the

gas (Eg).

In the viscous flow regime, the Eg loss is directly dependent on the thermal conductivity of the gas (Kg), the surface area of the membrane, the differential temperature and is inversely proportional to distance between the membrane and the lid. It can be written as

Eg = (Kg DT As)/Dx

The thermal conductivity of the gas is essentially constant when in viscous flow where the Knudsen number (Kn) is less than 0.01. In the viscous flow regime there is no change in sensor output with pressure since all of the losses are constants with pressure.

In the molecular flow regime where (Kn > 1) the thermal conductivity of the gas becomes directly proportional to the gas pressure as shown below. We can expect then that Eg will be constant at high pressures and directly proportional to the pressure at low pressures. The energy loss Eg, changes between these two controlling equations as the system passes through the transition region (0.01 < Kn < 1).

 

 

Eg = arLt(273/Th)1/2(Th-Ta)AgP

 

Where

 

 

 

ar

=

accommodation coefficient

 

Lt

=

free molecule thermal conductivity

 

Th

=

temperature of heated membrane

 

Model 2002 Vacuum Gauge

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Image 20
Teledyne 2002 instruction manual Eg = Kg DT As/Dx

2002 specifications

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