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VACUUM Classified Abstracts O O II -- Vacuum Apparatus and Auxiliaries -- II Contd. Some Remarks on Ion Pumps Hungary. The working principle of ion-transport and ion-getter pumps is briefly discussed. The function of these pumps depends on the anode-cathode distance, the voltage, the current density, the condition of the cathode surface and the gaseous atmosphere. Sommaire : Le proc6d6 de pompage des pompes ~ transport ionique ou des pompes getter ionique est hri6vement discut6. Some Theoretical and Experimental Observations on the Ultimate Vacuum Obtainable in Vapour Pumps See Abstract No. : 69/I The Theory of High-Speed Oil Diffusion Pumps United Kingdom. This paper is concerned with the action of the top jet of fractionating pumps ill which all jet towers extend to the boiler. This jet is responsible for the high speed of evacuation at low pressures. The magnitude of tile pressure gradient in the central tower which leads to the top jet, and the manner in which the vapour beam spreads as it moves outwards from the jet aperture affects the speed and can result in a substantial loss of speed. A first order theory is developed from which a reIationship between the speed of the top jet and its aperture is established, and theoretical curves for the air speed of a 16-inch pump as a function of the radius of the central tower, which agree with experimental results, show that for maximum speed an optimum aperture exists. Smaller and larger pumps with central tower diameters determined from similar theoretical curves have a high efficiency and are able to produce vacua close to 10 .7 ram. Hg without the aid of traps. The high ultimate vacuum together with the adequate speed of the subsidiary jets and the high limiting fore pressure of these pumps make them particularly suitable for use with particle accelerators. It was found experimentally that the optimum angle between the jet and the horizontal is about 45 ° and that for a particular arrangement the speed is almost independent of the width of the slit, from which the vapour beam emerges, in the range 0.3-0.6 cm. The discussion sets out the advantages of increasing the number of jets in 6-inch. or larger pumps, to four. Sommaire : Cet articIe est une 4rude th6orique du m6canisme de travail des pompes k diffusion ~ huile. On discute aussi les difficult4s rencontr6es, pour obtenir de grandes vitesses de pompage avec l'hydrog6ne. Correct Use of the Formula for Apparent Pumping Speed See Abstract No. : 68/I Improvements Relating to Vacuum Pumps of the Vapour Jet Type United Kingdom. In a conventional vapour pump each jet usually takes the form of a divergent annular nozzle fed by a central vapour tube, the pumped gas being drawn downwards between the outer edge of the nozzle and the surrounding pump wall. In the arrangement described here the annular nozzle is situated close to the pump wall and tile pumped gas passes down through its inner periphery. The nozzle is fed with vapour by a lagged tube external to the pump and is designed so that the inner boundary of the jet converges to an apex in the centre while the outer boundary strikes the cold wall in the normal way. It is claimed that the hollow conical vapour stream so formed constitutes a barrier which largely eliminates the back-diffusion of both, vapour and entrained gas, from the region near the cold wall into the high vacuum side. Somma~ire : La r6alisation d'une pompe k injection 6quipee d'un injecteur produisant un jet conique de vapeur d'un type particulier est d6crite. Ce systgme est dit, de r6duire le risque d'un retour de vapeur et de l'entrainement de gaz dans l'appareil. High Vacuum Diffusion Pump United States. The patent describes a device for preventing displacement of the jet assembly of a diffusion pump during operation or in transit. It consists of a length of spring wire of such a size that its ends stretch across the inside of the pump body, provided at its centre with a loop which locates around a spigot projecting from the top of the uppermost jet cap. The loop is big enough to allow slight radial movement of the jet assembly, so that it may seat squarely on the base, but prevents the possibility of its lifting from the base. Sommaire : On d6crit un syst6me emp6chant le d6placement de l'ensemble de l'4jecteur d'une pompe k diffusion, soft pendant le fonctionuement soft pendant le transport. Distillation System for Recovering Spent Pumping Oils See Abstract No. : 91/III Abstract, No. and References 38/1I Letter by P. F. Varadi Vacu%q~b 4, Jan. 1954 66-67 39/11 40/II Article by L. Riddiford & R. F. Coo J. Sci. Instrum. 3I, Feb. 1954 33-36 41/1I 42/11 W. J. Scott & British Thomson- Houston Co. Ltd. Brit. Pat. 705,160 43/11 J. Wishart & Consolidated Vacuum Corp. U.S. Pat. 2,668,005 44/II April, 1954 Vacuum 231 Vol. IV No. 2

High vacuum diffusion pump

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Page 1: High vacuum diffusion pump

VACUUM

Classified A b s t r a c t s

O

O

I I - - V a c u u m Apparatus and Auxi l iar ies - - I I Contd.

Some Remarks on Ion P u m p s

Hungary. The work ing pr inciple of i on - t r anspo r t and ion-get te r p u m p s is br ief ly discussed. The func t ion of t he se p u m p s depends on t h e anode -ca thode dis tance, t h e vol tage, t he cu r r en t densi ty , t he condi t ion of t he ca thode sur face and t he gaseous a tmosphe re .

Sommaire : Le proc6d6 de p o m p a g e des p o m p e s ~ t r a n s p o r t ionique ou des pompes ge t te r ionique es t h r i 6 v e m e n t discut6.

Some Theoretical and Experimental Observations on the Ultimate Vacuum Obtainable in Vapour P u m p s

See A b s t r a c t No. : 69 / I

The Theory of High-Speed Oil Diffusion P u m p s

United Kingdom. This pape r is concerned wi th the ac t ion of t he top je t of f r ac t iona t ing p u m p s ill which all j e t towers e x t e n d to the boiler. Th i s je t is responsible for t he h igh speed of evacua t ion a t low pressures . The m a g n i t u d e of tile p ressure g rad ien t in t he cent ra l tower which leads to t he top jet , and t he m a n n e r in wh ich t he v a p o u r b e a m spreads as i t m o v e s ou t wa rds f rom the je t ape r tu re affects t he speed and can resu l t in a s u b s t a n t i a l loss of speed. A first order t heo ry is developed f rom which a reIa t ionship be tween t he speed of t he t op je t and i ts ape r tu re is es tabl ished, and theore t ica l curves for t h e air speed of a 16-inch p u m p as a func t ion of t h e rad ius of t he cent ra l tower, wh ich agree wi th e x p e r i m e n t a l resul ts , show t h a t for m a x i m u m speed an o p t i m u m ape r tu re exists . Smaller and larger p u m p s w i th cent ra l tower d i ame te r s de t e rmined f rom similar theore t ica l curves h a v e a h i gh efficiency and are able to p roduce v a c u a close to 10 .7 ram. H g w i t h o u t t he a id of t raps . T h e h igh u l t i m a t e v a c u u m toge the r wi th t he adequa t e speed of t he subs id i a ry je t s and t he h igh l imi t ing fore p ressure of t hese p u m p s m a k e t h e m par t i cu la r ly su i tab le for use wi th par t ic le accelerators. I t was found expe r imen t a l l y t h a t t he o p t i m u m angle be tween t he je t and the hor izonta l is abou t 45 ° and t h a t for a pa r t i cu la r a r r a n g e m e n t t he speed is a lmos t i n d e p e n d e n t of the w id th of t he slit, f rom which t he v a p o u r b e a m emerges, in t h e r ange 0 .3-0.6 cm. T he discuss ion sets ou t t h e a d v a n t a g e s of increas ing t he n u m b e r of j e t s in 6 - inch . or larger p u m p s , to four.

Sommaire : Cet articIe es t une 4rude th6or ique du m6can i sme de t rava i l des p o m p e s k diffusion ~ huile. On d iscute auss i les difficult4s rencontr6es , pour ob ten i r de g randes vi tesses de p o m p a g e avec l 'hydrog6ne .

Correct Use of the Formula for Apparent Pumping Speed See A b s t r a c t No. : 68 / I

Improvements Relating to V a c u u m P u m p s of the Vapour Jet Type

United Kingdom. I n a conven t iona l v a p o u r p u m p each je t usua l ly t akes t he form of a d ive rgen t a n n u l a r nozzle fed by a cent ra l v a p o u r tube , t he p u m p e d gas being d r a w n downwards be tween t he ou te r edge of t he nozzle and t he s u r r o u n d i n g p u m p wall. I n t he a r r a n g e m e n t described here t he a n n u l a r nozzle is s i tua ted close to t he p u m p wall and tile p u m p e d gas passes down t h r o u g h i ts inner per iphery . The nozzle is fed wi th vapou r by a lagged t u b e ex te rna l to t h e p u m p and is designed so t h a t t he inner b o u n d a r y of t he je t converges to an apex in t h e cent re while t he ou te r b o u n d a r y s t r ikes the cold wall in t he n o r m a l way. I t is c la imed that t h e hol low conical v a p o u r s t r e a m so fo rmed cons t i tu te s a barr ier wh ich largely e l iminates t he back-di f fus ion of both , v a p o u r and en t r a ined gas, f rom t he region nea r t he cold wall into t he h igh v a c u u m side.

Somma~ire : L a r6al isat ion d ' u n e p o m p e k in ject ion 6quipee d ' u n in jec teur p r o d u i s a n t un j e t conique de v a p e u r d ' u n t y p e par t icu l ie r es t d6crite. Ce sys tgme est dit, de r6duire le r i sque d ' u n re tour de v a p e u r et de l ' e n t r a i n e m e n t de gaz d a n s l 'apparei l .

High V a c u u m Diffusion P u m p

United States. The patent describes a device for preventing displacement of the jet assembly of a diffusion pump during operation or in transit. It consists of a length of spring wire of such a size that its ends stretch across the inside of the pump body, provided at its centre with a loop which locates around a spigot projecting from the top of the uppermost jet cap. The loop is big enough to allow slight radial movement of the jet assembly, so that it may seat squarely on the base, but prevents the possibility of its lifting from the base.

Sommaire : On d6crit un syst6me emp6chant le d6placement de l'ensemble de l'4jecteur d'une pompe k diffusion, soft pendant le fonctionuement soft pendant le transport.

Distillation System for Recovering Spent Pumping Oils See A b s t r a c t No. : 91 / I I I

Abstract, No. and References

38/1I

Letter by P. F. Varadi

Vacu%q~b 4, Jan. 1954

66-67

39/11

40/II

Article by L. Riddiford &

R . F. Coo J. Sci. Instrum. 3I, Feb. 1954

33-36

41/1I

42/11

W. J. Scott & British Thomson- Houston Co. Ltd.

Brit. Pat. 705,160

43/11

J. Wishart & Consolidated

Vacuum Corp. U.S. Pat. 2,668,005

4 4 / I I

April , 1954 Vacuum 231 Vol. I V No. 2