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PuK - Process Technology & Components 2024

A technical trade magazine with a history of more than 60 years.

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Vacuum technology<br />

Screw spindle vacuum pumps<br />

Fig. 6: Simulation domain for a pressure-driven flow through a channel with structured<br />

surfaces<br />

a) L/h=1 b) L/h=10<br />

Fig. 7: Mass flow rate through a channel with structured surfaces related to the respective<br />

mass flow rate through a channel with smooth surfaces as a function of the inlet pressure p 1<br />

for different profile parameters α = β [Saz20].<br />

Fig. 7a shows this for a length to<br />

height ratio of one, which corresponds<br />

approximately to an orifice<br />

flow. It can be seen that all four<br />

curves cause an increased throttling<br />

effect with decreasing pressure,<br />

which can be explained analogously<br />

to Fig. 3 by the fact that the proportion<br />

of gas-surface interactions increases.<br />

Furthermore, the throttling<br />

effect depends on the shape of the<br />

surface structure. A very wide profile<br />

angle causes only a slight reduction<br />

in the mass flow rate, while a profile<br />

angle α = β = 45° already causes<br />

a reduction in the mass flow rate of<br />

about 10 % in the orifice flow. If the<br />

profile angle is reduced further, the<br />

flow stagnates. This can also be seen<br />

in Fig. 7b, where the same situation<br />

is shown for a length to height ratio<br />

of ten and the molecules therefore<br />

have to pass through a significantly<br />

longer channel. Here, a reduction of<br />

about 25 % can already be achieved<br />

for smaller profile angles. It is also<br />

noticeable that the effect becomes<br />

smaller for increasing inlet pressures,<br />

so that a transfer to the vacuum<br />

pump is particularly interesting<br />

for the low-pressure side of the machine.<br />

This results in promising synergy<br />

possibilities with the previously<br />

described approach by Kösters<br />

and Eickhoff, as larger machine gaps<br />

could be realised on the low-pressure<br />

side in order to prevent overcompression<br />

during start-up. As soon<br />

as the pressure on the low-pressure<br />

side is low enough, the increased gap<br />

size would be compensated for with<br />

the help of the surface structures by<br />

reducing the mass flow rate even further<br />

than is already the case due to<br />

the rarefied gas flow with technically<br />

smooth walls.<br />

Since there is always a superposition<br />

of a pressure-driven Poiseuille<br />

flow and a shear-driven Couette flow<br />

in the gaps of vacuum pumps, the<br />

DSMC method is used to analyse the<br />

effect of such a surface structure on<br />

a pure Couette flow. The corresponding<br />

simulation domain is shown in<br />

Fig. 8. With a gap height of h = 0.3<br />

mm, a profile depth Λ = 0.03 mm is<br />

used. Since the gap length and the<br />

gap width in vacuum pumps are<br />

much greater than the gap height,<br />

an infinitely wide and long channel is<br />

simulated for simplification, so that<br />

symmetrical boundary conditions are<br />

used in the depth direction (z) and<br />

cyclic boundary conditions in the flow<br />

direction (x) to reduce the computational<br />

effort. The latter have the property<br />

that the left and right cells are<br />

linked to each other as if the channel<br />

were continuing. Accordingly, a particle<br />

that crosses the cyclic boundary<br />

condition on the right-hand side<br />

is initialised again on the left-hand<br />

side and vice versa. The lower wall<br />

has a wall velocity of U = 10 m/s in<br />

the positive x-direction. In the reference<br />

plane shown in green, the mass<br />

flow rate is determined by calculating<br />

the sum of the particle masses in the<br />

positive x-direction minus the sum<br />

of the particle masses that cross the<br />

plane in the negative direction within<br />

a time step and then dividing by the<br />

time step:<br />

Eq. 1<br />

Regardless of the pressure range,<br />

the mass flow rate<br />

for a pure<br />

Couette flow with technically smooth<br />

surfaces can be calculated via<br />

Eq. 2<br />

incorporating the density ρ and the<br />

smallest cross-section area A = h b<br />

[Ple22a, Ple22b].<br />

Fig. 8: DSMC simulation domain of a pure<br />

Couette flow through a channel with onesided<br />

surface structure.<br />

Fig. 9 shows the simulated mass<br />

flow rate of a Couette flow for different<br />

profile angles α = β in relation to<br />

the mass flow rate through a channel<br />

with smooth walls with the same<br />

gap height as a function of the pres-<br />

50 PROCESS TECHNOLOGY & COMPONENTS <strong>2024</strong>

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