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Gas Flow 
1 
Gigin Ginanjar 
01312003
Content 
2 
• 3.Gas Flow 
– 3.1 Flow Regimes 
– 3.2 Definition of Throughput and Pumping Speed 
– 3.3 Conductance 
• 3.3.1 Definition 
• 3.3.2 Combination 
• 3.3.3 Long Tubes 
• 3.3.4 Orifice 
– 3.4 Calculating Pumping Speed at Different Places
3.1 Flow Regime (1) 
3 
• Flow Regime: Flow that through all different type of flow (because 
vacuum system) 
• Vacuum system start form turbulent flow ,when pressure fall flow 
change to laminar flow. Both flow are viscous ; molecules striking each 
other and pushing each other 
• Transition from turbulent to viscous flow depend on Reynold number; 
which function of flow velocity, mass density, tube diameter
3.1 Flow Regime (2) 
4 
• Knudsen number 
퐾푛 = 
퐿 
푑 
L=mean free path ;mfp [L1] 
d=characteristic dimension of the system [L1] 
• In viscous flow mfp< character dimension ; gas 
to gas collision ; Kn <0.01 
• If pressure reduce then mpf = characteristic 
dimension; gas to wall interaction 
• In region 1>Kn>0.01 transition region; 
• Kn>1 Flow considered molecular flow; In 
molecular flow gas –wall collision predominate, 
The wall interaction is diffuse reflection
Molecular interaction with surface 
Diffuse reflectance . The length of the arrow for desorption 
is proportional to the probability of desorption in 
that direction 
5 
Specular reflectance: The angle of reflection equals the 
angle of incidence 
Example Flashlight to mirror 
Cosine distribution 
Example Flashlight to wall with mate finish 
Wrong: ping pong ball bouncing in the table 
Right : Glue many ping pong ball on a table 
And attempt to bounce to another surface 
Wrong: Incoming ball is very large compare 
to roughness of surface 
Right : Consider that molecule do not bounce. 
Consider absorption, there resident time and desorbs 
Molecular interaction with surface
Molecular flow 
Molecular Flow; random traversing back & forth 
of the molecules from wall to wall with progress 
of molecules through the vacuum lines a matter 
of statistics 
Molecule arriving from region 1 move region 2 
To gases not collide effected one and another 
Higher gas density region 1 
More molecule move right than to left 
6 
Three different regions with P1>P2>P3 
Section A
3.2 Definition of Throughput and Pumping Speed 
7 
The rate flow trough the passage is depends on 
-Capacity of the pump 
-Geometrical shape 
-Type of flow 
-Gas Characteristic 
Gas Flow rate – Mass Flow Rate Q 
- Volumetric Flow Rate S 
Mass Flow Rate Q or Throughput 
The net number of molecules passing a given plane per unit time 
Unit : pressure volume per unit time, example torr-liter per second
8 
Steady state condition : the pressure at given location not changing 
as function of time 
Pseudo-Steady state condition: no leak valve but gas evolving from the walls 
act similar to leak valve
Volumetric flow Rate 
Volumetric flow Rate S or pumping Speed: the actual amount of substance 
which moved a distance d is not specify size that depends on Pressure 
9 
Unit volumetric flow is volume per unit time example liter/sec 
Volumetric flow rate and mass flow rate are related to pressure by equation 
푄 = 푆 푥푃
3.3 Conductance 
10 
• 3.3.1Definition 
Conductance property of component which usually fills a certain amount 
of three dimensional space whereas volumetric flow rate is property of a 
position in space ( plane) 
퐶 = 
푄 
푃1 − 푃2 
Unit for Conductance same as volumetric flow is volume per unit time 
example liter/sec
Combination 
11 
• 3.3.2 Combination Q = constant 
푃1 − 푃2 = 
푄 
퐶1 
푃3 − 푃4 = 
푄 
퐶3 
푃2 − 푃3 = 
푄 
퐶2 
푃1 − 푃4 = 푄 
1 
퐶1 
+ 
1 
퐶2 
+ 
1 
퐶3 
푃1 − 푃4 = 푄 
1 
퐶푡 
1 
퐶푡 
= 
1 
퐶1 
+ 
1 
퐶2 
+ 
1 
퐶3 
퐶푡 = 퐶1 + 퐶2 + 퐶3 
Conductance in series 
Conductance in parallel 
Remember ,Q=Mass Flow Rate/throughput
Long Tubes 
12 
• 3.3.3 Long Tubes 
Long tubes has length significantly greater than its diameter 
Viscous flow od dry at 20oC 
퐶푣 = 
3000 < 푃 > 퐷4 
퐿 
Molecular flow od dry at 20oC 
퐶푚 = 
80퐷3 
퐿 
<P>= Average Pressure , Torr 
D= tube diameter, inches 
L=Tube Length ,inches
Orifice 
13 
• 3.3.4 Orifice 
Conductance of orifice is not infinity 
퐶0 = 11.6 퐴 
1 
퐶푡 
= 
1 
퐶표 
+ 
1 
퐶푙 
A =Area in cm2
Condutance ? 
14 
• example 
A Tube 10 inches long and 
0.5 inches diameter 
80(0.5)3 
퐶푙 = 
10 
=1.0 liter/sec 
퐶0 = 11.6 휋 0.25 푥 2.54 2 =14.7 liter/ sec 
1 
퐶푡 
= 
1 
1.0 
+ 
1 
14.7 
=1.07 
퐶푡 =0.94 liter/sec 
A Tube 4 inches long 
and 6 inches diameter 
퐶푙 = 
80(4)3 
6 
=853.33 liter/sec 
퐶0 = 11.6 휋 2 푥 2.54 2 = 940.45 liter/ sec 
1 
퐶푡 
= 
1 
853 
+ 
1 
940 
=0.00223 
퐶푡 = 447.39 liter/sec
3.4 Calculating Pumping Speed at Different Places 
15 
• f 푃1 = 
푄 
푆푙 
푃표 = 
푄 
푆푝 
퐶 = 
푄 
푃1 − 푃표 
퐶 = 
1 
1 
푆1 
− 
1 
푆푝 
1 
푆1 
= 
1 
푆푝 
+ 
1 
퐶푡 
1 
푆푎 
= 
1 
푆푏 
+ 
1 
퐶푎푏 
From equation previously 
Conductance equation 
Pumping speed 
Generalized equation
Example 
16 
• Example 
Pump with pumping speed 200 liters/sec 
Attached to chamber via 6 inch tube with 10 inches diameter 
Conductance = 951 liters /sec 
Pumping speed enter the chamber? 
1 
푆푐 
= 
1 
200 
+ 
1 
951 
푆푐=0.936 liters/ sec 
6 inches long and 10 inches diameter 
퐶푙 = 
80(6)3 
10 
=1728 liter/sec 
퐶0 = 11.6 휋 2 푥 2.54 2 = 2116.01 liter/ sec 
1 
퐶푡 
= 
1 
1728 
+ 
1 
2116.01 
= 
퐶푡 = 951.21 liter/sec

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Vacuum Class -Gas flow - gigin 1

  • 1. Gas Flow 1 Gigin Ginanjar 01312003
  • 2. Content 2 • 3.Gas Flow – 3.1 Flow Regimes – 3.2 Definition of Throughput and Pumping Speed – 3.3 Conductance • 3.3.1 Definition • 3.3.2 Combination • 3.3.3 Long Tubes • 3.3.4 Orifice – 3.4 Calculating Pumping Speed at Different Places
  • 3. 3.1 Flow Regime (1) 3 • Flow Regime: Flow that through all different type of flow (because vacuum system) • Vacuum system start form turbulent flow ,when pressure fall flow change to laminar flow. Both flow are viscous ; molecules striking each other and pushing each other • Transition from turbulent to viscous flow depend on Reynold number; which function of flow velocity, mass density, tube diameter
  • 4. 3.1 Flow Regime (2) 4 • Knudsen number 퐾푛 = 퐿 푑 L=mean free path ;mfp [L1] d=characteristic dimension of the system [L1] • In viscous flow mfp< character dimension ; gas to gas collision ; Kn <0.01 • If pressure reduce then mpf = characteristic dimension; gas to wall interaction • In region 1>Kn>0.01 transition region; • Kn>1 Flow considered molecular flow; In molecular flow gas –wall collision predominate, The wall interaction is diffuse reflection
  • 5. Molecular interaction with surface Diffuse reflectance . The length of the arrow for desorption is proportional to the probability of desorption in that direction 5 Specular reflectance: The angle of reflection equals the angle of incidence Example Flashlight to mirror Cosine distribution Example Flashlight to wall with mate finish Wrong: ping pong ball bouncing in the table Right : Glue many ping pong ball on a table And attempt to bounce to another surface Wrong: Incoming ball is very large compare to roughness of surface Right : Consider that molecule do not bounce. Consider absorption, there resident time and desorbs Molecular interaction with surface
  • 6. Molecular flow Molecular Flow; random traversing back & forth of the molecules from wall to wall with progress of molecules through the vacuum lines a matter of statistics Molecule arriving from region 1 move region 2 To gases not collide effected one and another Higher gas density region 1 More molecule move right than to left 6 Three different regions with P1>P2>P3 Section A
  • 7. 3.2 Definition of Throughput and Pumping Speed 7 The rate flow trough the passage is depends on -Capacity of the pump -Geometrical shape -Type of flow -Gas Characteristic Gas Flow rate – Mass Flow Rate Q - Volumetric Flow Rate S Mass Flow Rate Q or Throughput The net number of molecules passing a given plane per unit time Unit : pressure volume per unit time, example torr-liter per second
  • 8. 8 Steady state condition : the pressure at given location not changing as function of time Pseudo-Steady state condition: no leak valve but gas evolving from the walls act similar to leak valve
  • 9. Volumetric flow Rate Volumetric flow Rate S or pumping Speed: the actual amount of substance which moved a distance d is not specify size that depends on Pressure 9 Unit volumetric flow is volume per unit time example liter/sec Volumetric flow rate and mass flow rate are related to pressure by equation 푄 = 푆 푥푃
  • 10. 3.3 Conductance 10 • 3.3.1Definition Conductance property of component which usually fills a certain amount of three dimensional space whereas volumetric flow rate is property of a position in space ( plane) 퐶 = 푄 푃1 − 푃2 Unit for Conductance same as volumetric flow is volume per unit time example liter/sec
  • 11. Combination 11 • 3.3.2 Combination Q = constant 푃1 − 푃2 = 푄 퐶1 푃3 − 푃4 = 푄 퐶3 푃2 − 푃3 = 푄 퐶2 푃1 − 푃4 = 푄 1 퐶1 + 1 퐶2 + 1 퐶3 푃1 − 푃4 = 푄 1 퐶푡 1 퐶푡 = 1 퐶1 + 1 퐶2 + 1 퐶3 퐶푡 = 퐶1 + 퐶2 + 퐶3 Conductance in series Conductance in parallel Remember ,Q=Mass Flow Rate/throughput
  • 12. Long Tubes 12 • 3.3.3 Long Tubes Long tubes has length significantly greater than its diameter Viscous flow od dry at 20oC 퐶푣 = 3000 < 푃 > 퐷4 퐿 Molecular flow od dry at 20oC 퐶푚 = 80퐷3 퐿 <P>= Average Pressure , Torr D= tube diameter, inches L=Tube Length ,inches
  • 13. Orifice 13 • 3.3.4 Orifice Conductance of orifice is not infinity 퐶0 = 11.6 퐴 1 퐶푡 = 1 퐶표 + 1 퐶푙 A =Area in cm2
  • 14. Condutance ? 14 • example A Tube 10 inches long and 0.5 inches diameter 80(0.5)3 퐶푙 = 10 =1.0 liter/sec 퐶0 = 11.6 휋 0.25 푥 2.54 2 =14.7 liter/ sec 1 퐶푡 = 1 1.0 + 1 14.7 =1.07 퐶푡 =0.94 liter/sec A Tube 4 inches long and 6 inches diameter 퐶푙 = 80(4)3 6 =853.33 liter/sec 퐶0 = 11.6 휋 2 푥 2.54 2 = 940.45 liter/ sec 1 퐶푡 = 1 853 + 1 940 =0.00223 퐶푡 = 447.39 liter/sec
  • 15. 3.4 Calculating Pumping Speed at Different Places 15 • f 푃1 = 푄 푆푙 푃표 = 푄 푆푝 퐶 = 푄 푃1 − 푃표 퐶 = 1 1 푆1 − 1 푆푝 1 푆1 = 1 푆푝 + 1 퐶푡 1 푆푎 = 1 푆푏 + 1 퐶푎푏 From equation previously Conductance equation Pumping speed Generalized equation
  • 16. Example 16 • Example Pump with pumping speed 200 liters/sec Attached to chamber via 6 inch tube with 10 inches diameter Conductance = 951 liters /sec Pumping speed enter the chamber? 1 푆푐 = 1 200 + 1 951 푆푐=0.936 liters/ sec 6 inches long and 10 inches diameter 퐶푙 = 80(6)3 10 =1728 liter/sec 퐶0 = 11.6 휋 2 푥 2.54 2 = 2116.01 liter/ sec 1 퐶푡 = 1 1728 + 1 2116.01 = 퐶푡 = 951.21 liter/sec