19 Jun 031 Lamberston Removal and F0 Straight Section Vacuum Upgrade Mike McGee FNAL.
Why is a Vacuum Needed? To move a particle in a (straight) line over a large distance.
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Transcript of Why is a Vacuum Needed? To move a particle in a (straight) line over a large distance.
Why is a Vacuum Needed?
To move a particle in a (straight) line over a large distance
Why is a Vacuum Needed?
Contamination(usually water)
Clean surface
Atmosphere (High)Vacuum
To provide a clean surface
Pressione Numero molecole/cm3
un pacco di caffè imballato sotto vuoto 104 Pa 2.7 x 1018
un tubo catodico in un televisore 10-4 Pa 2.7 x 1010
un acceleratore di particelle in fisica nucleare 10-8 Pa 2.7 x 106
una camera con il miglior vuoto che attualmente si può produrre in laboratorio 10-12 Pa 2.7 x 102
nostra galassia 10-14 Pa 1-10spazio intergalattico ? 1 al m3
Tabella 1a: La pressione in alcune tipiche applicazioni
Altitudine PressioneAl livello del mare 101000 PaSulla vetta del Monte Bianco 50000 PaAlla quota di crociera di un Jumbo-Jet (20000 m) 5000 PaSu un satellite artificiale alla quota di 35000 km 2 x 10-3 PaSulla superficie della luna 5 x 10-5 Pa
Tabella 1b: Cambiamento della pressione in funzione dell’altitudine
HOW DO WE CREATE A VACUUM?
VACUUM PUMPING METHODS
Sliding VaneRotary Pump
MolecularDrag Pump
TurbomolecularPump
Fluid EntrainmentPump
VACUUM PUMPS(METHODS)
ReciprocatingDisplacement Pump
Gas TransferVacuum Pump
DragPump
EntrapmentVacuum Pump
Positive DisplacementVacuum Pump
KineticVacuum Pump
RotaryPump
DiaphragmPump
PistonPump
Liquid RingPump
RotaryPiston Pump
RotaryPlunger Pump
RootsPump
Multiple VaneRotary Pump
DryPump
AdsorptionPump
Cryopump
GetterPump
Getter IonPump
Sputter IonPump
EvaporationIon Pump
Bulk GetterPump
Cold TrapIon TransferPump
Gaseous Ring Pump
TurbinePump
Axial FlowPump
Radial FlowPump
EjectorPump
Liquid JetPump
Gas JetPump
Vapor JetPump
DiffusionPump
DiffusionEjector Pump
Self PurifyingDiffusion Pump
FractionatingDiffusion Pump
Condenser
SublimationPump
BAROMETER
WATER MERCURY
760mm
Mercury: 13.58 times heavier than water: Column is 13.58 x shorter :10321 mm/13.58=760 mm (= 760 Torr)
10.321mm
29,9in
(Page 12 manual)
PRESSURE OF 1 STANDARD ATMOSPHERE:
760 TORR, 1013 mbar
AT SEA LEVEL, 0O C AND 45O LATITUDE
Pressure Equivalents
Atmospheric Pressure (Standard) =
014.729.9760760760,000101,3251.0131013
gauge pressure (psig)pounds per square inch (psia)inches of mercurymillimeter of mercurytorrmillitorr or micronspascalbarmillibar
THE ATMOSPHERE IS A MIXTURE OF GASES
PARTIAL PRESSURES OF GASES CORRESPOND TO THEIR RELATIVE VOLUMES
GAS SYMBOLPERCENT BY
VOLUMEPARTIAL PRESSURE
TORR PASCAL
NitrogenOxygenArgonCarbon DioxideNeonHeliumKryptonHydrogenXenonWater
N2
O2
ACO2
NeHeKrH2
XH2O
7821
0.930.03
0.00180.00050.0001
0.000050.0000087Variable
5931587.1
0.251.4 x 10-2
4.0 x 10-3
8.7 x 10-4
4.0 x 10-4
6.6 x 10-5
5 to 50
79,00021,000
940331.8
5.3 x 10-1
1.1 x 10-1
5.1 x 10-2
8.7 x 10-3
665 to 6650
(Page 13 manual)
VAPOR PRESSURE OF WATER AT VARIOUS TEMPERATURES
T (O C)
100
25
0
-40
-78.5
-196
P (mbar)
1013
32
6.4
0.13
6.6 x 10 -4
10 -24
(BOILING)
(FREEZING)
(DRY ICE)
(LIQUID NITROGEN)
(Page 14 manual)
(Page 15 manual)
Vapor Pressure of some Solids
(Page 15 manual)
PRESSURE RANGES
RANGE
ROUGH (LOW) VACUUM
HIGH VACUUM
ULTRA HIGH VACUUM
PRESSURE
759 TO 1 x 10 -3 (mbar)
1 x 10 -3 TO 1 x 10 -8 (mbar)
LESS THAN 1 x 10 -8 (mbar)
(Page 17 manual)
Viscous and Molecular Flow
Viscous Flow(momentum transferbetween molecules)
Molecular Flow(molecules moveindependently)
FLOW REGIMESViscous Flow:
Distance between molecules is small; collisions between molecules dominate; flow through momentum transfer;generally P greater than 0.1 mbar
Transition Flow: Region between viscous and molecular flow
Molecular Flow: Distance between molecules is large; collisions betweenmolecules and wall dominate; flow through random motion;generally P smaller than 10 mbar-3
(Page 25 manual)
MEAN FREE PATH
MOLECULAR DENSITY AND MEAN FREE PATH
1013 mbar (atm) 1 x 10-3 mbar 1 x 10-9 mbar
#mol/cm3
MFP
3 x 10 19
(30 million trillion)4 x 10 13
(40 trillion)4 x 10 7
(40 million)
2.5 x 10-6 in6.4 x 10-5 mm
2 inches5.1 cm
31 miles50 km
kTmolecole) diametro(P
2
12
Il libero cammino medio è inversamente proporzionale alla pressione ed alla sezione d’urto della molecola di gas
A A’P1
P2Flusso
P1 > P2
Portata:
dt
dnkT
dt
dVPQ
Q è costante lungo il tubo e pertantodt
dVP
dt
dVP 2
21
1
Conduttanza:
21 PP
QC
Conduttanza in parallelo:
C1
C2
P1 P2
Q1
Q2
)CC(C
)PP()CC(QQQ
21
212121
Conduttanza in serie:
)CC(C
)PP()CC(QQQ
21
212121
C1C2
P1P2
QP3
Flusso totale = somma dei flussi
1
21
2131
232
121
322211
C
1
C
1C
:seriein econduttanz due le per
C
Q
C
1
C
1QPP
C
QPP
C
QPP
quindi
)PP(C)PP(CQ
Flusso costante:
VELOCITA’ DI POMPAGGIO DI UNA POMPA
C
PCamera
Ppompa
Q
pompa
pompacamera
pompa P
PPC
P
QS
Cam
era
Pom
paVELOCITA’ EFFETTIVA DI POMPAGGIO DI UN SISTEMA:
1
camera
pompa
camera
pompacamera
cameraeff C
1
S
1
P
PS
P
PPC
P
QS
L’effetto della conduttanza è quello di ridurre la velocità di pompaggio efficaceRispetto alla velocità di pompaggio all’imbocco della pompa
FLOW REGIMES
Mean Free PathCharacteristic Dimension
Viscous Flow: is less than 0.01
Mean Free PathCharacteristic Dimension
Molecular Flow: is greater than 1
Mean Free PathCharacteristic Dimension
Transition Flow: is between 0.01 and 1
Conductance in Viscous Flow
Under viscous flow conditions doubling the pipe diameter increases the conductance sixteen times. The conductance is INVERSELY related to the pipe length
(Page 28 manual)
d = diameter of tube in cml = length of tube in cmP1 = inlet pressure in torrP2 = exit pressure in torr
)s/l(2
PP
l
d138C 21
4
EXAMPLE:d = 4 cm P1 = 2 torrl = 100 cm P2 = 1 torr
C=530 l/s
Conductance in Molecular Flow
Under molecular flow conditions doubling the pipe diameter increases the conductanceeight times.The conductance is INVERSELY related to the pipe length.
d = diameter of tube in cml = length of tube in cmT = temperature (K)M = A.M.U.
)s/l(M
T
l
d81.3C
3
EXAMPLE:T = 295 K (22 OC) d = 4 cm M = 28 (nitrogen) l = 100 cmC=7.9 l/s
GAS LOAD
Outgassing
Leaks
Virtual
Real
BackstreamingDiffusion
Permeation
GAS LOAD (Q) IS EXPRESSED IN:mbar liters per second
Pumpdown CurveP
ress
ure
(m
bar
)
Time (sec)
10-11
10 1 10 3 10 5 10 7 10 9 10 11 10 13 10 15 10 17
10+1
10-1
10-3
10-5
10-7
10-9
Volume
Surface Desorption
Diffusion
Permeation