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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. 2: Suctions speed curve of an SSVP with different housing gap heights [Dre14].<br />

reached. As less and less mass enters<br />

the machine at lower pressures,<br />

an equilibrium is established at this<br />

pressure between the intake mass<br />

flow rate and the mass flow rate that<br />

returns through the gaps, so that<br />

the machine effectively no longer<br />

conveys anything, thus preventing<br />

a further reduction in pressure. The<br />

charac teristic of the machine with initially<br />

increasing suction speed results<br />

from the fluid mechanical properties<br />

within the gap. At high suction pressure,<br />

the molecular density is high,<br />

so that a molecule collides very frequently<br />

with other molecules until<br />

it encounters a boundary (rotor and<br />

housing). In this way, the momentum<br />

and energy transport are dominated<br />

by intermolecular collisions and the<br />

fluid moves as a continuum. When<br />

the pressure is reduced, the molecular<br />

density also decreases so that a<br />

particle can travel a greater distance<br />

until it collides with another particle.<br />

This increases the proportion of gassurface<br />

collisions, which leads to increased<br />

friction. If the pressure is so<br />

low that the number of intermolecular<br />

collisions is negligible compared to<br />

the particle-wall collisions, this is referred<br />

to as a molecular flow. A qualitative<br />

course of the normalised mass<br />

flow rate of a gap through which air<br />

flows is shown in Fig. 3. The normalisation<br />

is chosen so that a normalised<br />

mass flow rate of one corresponds to<br />

an isentropic choked nozzle flow. The<br />

gap height is set to h = 0.3 mm and<br />

T = 293 K is assumed for the ambient<br />

temperature. It is shown that the normalised<br />

mass flow rate with an initial<br />

continuum flow decreases significantly<br />

with decreasing inlet pressure<br />

until a minimum is reached and then<br />

increases again asymptotically with<br />

further pressure reduction towards<br />

molecular flow. The greater proportion<br />

of gas-surface interactions also<br />

increases the influence of relative<br />

wall movement on the mass flow<br />

rate. Such a wall movement is caused<br />

by the rotational speed of the rotors.<br />

Accordingly, the red line results from<br />

a wall movement in the direction of<br />

flow, the green line for a wall movement<br />

against the direction of flow<br />

and the black line describes a purely<br />

pressure-driven flow with static<br />

boundaries.<br />

In order to realise the highpressure<br />

ratios over the machine<br />

(e. g. p at<br />

/p suction<br />

= 10 5 ), the rotors have<br />

a significantly larger wrap than conventional<br />

screw machines in high<br />

pressure applications. This results in<br />

a kind of multi-stage design with several<br />

encapsulated working chambers<br />

in axial direction, which leads to a reduction<br />

in the pressure ratio between<br />

individual working chambers. In order<br />

to avoid continuous gap connections<br />

from the high-pressure to the lowpressure<br />

side, the number of teeth is<br />

limited to a maximum of two, or even<br />

one for some profiles. Internal compression<br />

is usually achieved by successively<br />

reducing the chamber volume<br />

by changing the rotor pitch, but<br />

more recently also by using conical<br />

rotors [Moe23]. The advantage of reducing<br />

the chamber volume continuously<br />

instead of using an end plate is a<br />

more uniform compression along the<br />

rotor and therefore better heat distribution<br />

in the machine. Furthermore,<br />

throttling losses can be reduced by<br />

avoiding control edges [Jou18]. One<br />

problem with the internal compression<br />

of the machines is that the machine<br />

has to cover very large pressure<br />

ranges. In nominal oper ation, a very<br />

large internal compression would<br />

be desirable, which would reduce<br />

the energy consumption on the one<br />

hand and possibly also the size on<br />

the other. For example, a large suction<br />

chamber takes up a lot of mass,<br />

which can then be compressed to a<br />

small volume and then pushed out<br />

on the high-pressure side at a low<br />

Fig. 3: Schematic course of the normalised mass flow rate through the housing gap of an<br />

SSVP as a function of the inlet pressure and the influence of relatively moved walls.<br />

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

47

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