TRANSITION GAS-FLOW IN DRAG PUMPS AND CAPILLARY LEAKS

Authors
Citation
Jc. Helmer et G. Levi, TRANSITION GAS-FLOW IN DRAG PUMPS AND CAPILLARY LEAKS, Journal of vacuum science & technology. A. Vacuum, surfaces, and films, 13(5), 1995, pp. 2592-2599
Citations number
14
Categorie Soggetti
Physics, Applied","Materials Science, Coatings & Films
ISSN journal
07342101
Volume
13
Issue
5
Year of publication
1995
Pages
2592 - 2599
Database
ISI
SICI code
0734-2101(1995)13:5<2592:TGIDPA>2.0.ZU;2-X
Abstract
Modern turbomolecular pumps include a drag stage in the exhaust, opera ting roughly in the pressure range of 10 mTorr-10 Torr. Flow condition s range from molecular flow at the drag inlet, to viscous flow at the outlet, known as ''transition'' flow. In general, models of transition flow in drag pumps have not been developed. Moreover, the model of a Gaede Dump given in journals and textbooks up to the present, gives va lues of compression ratio that are orders of magnitude too high. In 19 13, Gaede proposed a differential equation for transition flow in a dr ag pump. He did not solve the general equation, and the model was inco mplete. We have developed a new model that takes transition flow in a differential element and integrates it over the length of the pump. Th is model is modified by a ''pumping leak'' expression for the gas stri pper, which separates the inlet from the outlet. The result is compare d with experimental measurements, and good agreement is obtained over the entire pressure range from molecular, through transition, and into viscous flow. Up to a critical pressure in viscous flow, compression ratio is constant as a function of exhaust pressure, within a factor o f 2. Within this factor, increasing compression arises from the reduce d pressure drop across the inlet aperture as its conductance increases in the transition flow regime. Above the critical pressure, compressi on drops rapidly as laminar backflow increases. This critical pressure is controlled by the dimensions of the channel. Below the critical pr essure, compression is determined by the pumping leak, and is somewhat independent of molecular weight. If the surface velocity is zero, the model reduces to a capillary leak. Predictions of our model agree wit h Knudsen's data for capillary leaks in transition flow, in addition t o giving a better account of the ''conductance minimum.'' ''Slip flow' ' is not an obvious factor, and it cannot be distinguished from the ri ght combination of viscous and molecular flow. (C) 1995 American Vacuu m Society.