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Publication numberUS2116380 A
Publication typeGrant
Publication dateMay 3, 1938
Filing dateJul 21, 1936
Priority dateAug 13, 1935
Publication numberUS 2116380 A, US 2116380A, US-A-2116380, US2116380 A, US2116380A
InventorsGeorg Bauer Stefan
Original AssigneeGeorg Bauer Stefan
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Emulsification of liquids and apparatus therefor
US 2116380 A
Abstract  available in
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Claims  available in
Description  (OCR text may contain errors)

May 3, 1938. s' G. BAUER 2,116,380

EMULSIFICATION OF LIQUIDS AND APPARATUS THEREFOR Filed July 21, 1936 2 Fig.4, I O 4 "(II/I1, I

VIA/II Patented May 3, 1938 UNITED STATES- EMULSIFICATION 0F LIQUIDS AND APPARATUS THEREFOR Stefan Georg Bauer, Cambridge, England Application July 21, 1936, Serial No. 91,792 In Great Britain August 13, 1935 1 Claim.

This invention is for improvements in or relating to the emulsification or intimate admixture of high viscosity semi-liquid masses by means of a gear pump.

5 The invention has for its object to provide an improved form of apparatus for this purpose which will enable emulsions or mixtures of high quality and stability to be very readily produced.

According to the invention, an apparatus-for the. emulsification or intimate admixture of high viscosity semi-liquid masses comprises a gear pump constructed with suflicient clearance between the casing and the teeth of the gears to provide a definite leakage path for-the mass -under treatment in the pump back from the ,outlet end thereof towards the inlet end of the pump (that is, in counter-course with the body of material being carried round between the teeth of the gears), and incorporating a spring- 90 loaded outwardly opening non-return valve in the outlet of the pump for establishing and maintaining during the operation of the pump and therefore while the outlet thereof is in open pump-discharging condition, a positive pressure difierence at the outlet end of the pump as comparedwith the pressure at the inlet end thereof; sufiicient, having regard to the magnitude of the clearance referred to and to the viscosity of the mass under treatment in the pump, to ensure 30 a constant return flow of a substantial proportion of the said mass along the leakage path.

The spring-loaded outwardly opening non-return valve in the outlet of the pump is preferably provided with means for adjusting the loading of l-Sand the wall of the casing, so as to provide a definite leakage path forthe return flow of a substantial proportion of the material undergoing treatment in the pump, and in association with such relatively large clearance space, with 50 a spring-loaded non-returnyalve in the dis- 'charge outlet of the pump, there is sometimes the difficultythat owing to the'magnitude of the clearance space, 'co'uple'd with the normally loaded condition of the'non-return valve, the body 55 of air' which-initially occupies the interior of the the spring and thereforethe operative opening pump at the commencement of operation thereof refuses to be displaced past the valve by the pumping action of the gears and in consequence the pump is prevented from drawing the material to be treated into it. In this way, the 5 effectual starting of the pump is prevented.

To overcome this difiiculty, the non-return valve is given an elongated tapered form, with the taper directed of course towards the interior of the pump, and is formed in its surface, where- 10 at it seats 'upon the seating surface of the valve, with a spiral groove which extends continuously along the surface of the valve from the end thereof toward the interior of the pump to the end remote therefrom; With the provision of 15 such a groove in the surface of the valve, any air that is present in the pump interior at the commencement of operation of the pump is permitted to pass out of the pump by the action of the gears thereof, while owing to the extended nature cf the groove consequent upon its spiral formation and the elongated form of the valve, the material to be treated, which of course is much more highly viscous than air, is prevented from expression past the valve so as to escape the ac- 2r tion of the gears of the pump or interfere with the establishment of the positive pressure differonce referred to above as between the outlet end of the pump and the inlet end thereof. In consequence, the pump starts immediately.

In' the prior use of a gear pump for emulsification purposes, a positive pressure difference at the outlet end of the pump has been maintained during the operation of the pump by reason of .a pressure head of the material discharged from the pump and in course of being re-cycled back to the inlet end of the pump. It will be understood, however, that in accordance with the present invention this pressure diiference is maintained of such a magnitude, in relation to the 40 size of the clearance space between the teeth of the pump and the casing and having regard to the viscosity of the material under treatment, as to ensure a constant return flow of a substantial proportion of thematerial along the leakage path referred to within the pump. By

this means, it is usually possible, to effect even the highest desired degrees of emulsification or intimacy of interadmixture of the material under treatment in one straight-through operation in contrast to re-cycling the material a number of times through the pump. Also, a very perfect emulsion or mixture is producible at an exceedingly high rate of production.

The invention will now be further described with reference to the accompanying drawing which illustrates one embodiment by way of example.

In this drawing,

Figure 1 is a transverse section through the improved emulsifying machine according to this invention;

Figure 2 is a longitudinal section through the machine on the section line 2-2 of Figure 1, and

Figure 3 is a fragmentary transverse section through the throttled outlet of the machine, showing a form of means for adjusting the loading of the valve.

The machine is in principle agear pump, as already indicated herein. It comprises a pair of intermeshing toothed gears I, 2 rotatable about parallel axes within a pump casing 3 of oval crosssection as shown in Figure 1. Gear I is mounted upon a driving shaft 4, to which it is keyed by a key 5. Gear 2 is mounted upon a stationary shaft 6. Shaft 4 is carried in bearings in the ends of the casing 3. One of these bearings is marked 1. The other is marked 8 (see Figure 2). Bearing 8 is at the inner end of a hollow boss 9 accommodating packing I maintained in position by a gland nut i I screwed on to the exterior of the boss 9.

The casing 3 is, in the constructional form of the invention shown, in two parts, a body part 12 which includes one of the ends of the casing (see Figure 2) and a cover part I3 constituting the other end of the casing. The casing has at one side an inlet H for the material to be emulsified and immediately opposite this inlet at the other side of the casing an outlet ii for the emulsion which has been formed in the machine by the action of the pump gears l, 2 therein,. These gears rotate in the directions of the arrows in Figure 1 and carry the material inflowed through the inlet l4 round with them to the opposite side of the casing, that is to say within the spaces between the teeth of the gears, the intermesh of the teeth of the respective gears at the point of tangency of the pitch circle of the gears providing in effect a fairly tight block to the flow of material across the pump directly, that is to say in by-passage in either direction of thenormal path of conveyance between the gears and the wall of the casing.

According to the invention, however, a definite clearance is provided between the teeth of the gears and the wall of the casing (that is, around the upper half and the lower half respectively of the two gears l, 2), this clearance being of sumcient magnitude, having regard to the viscosity of the material to be treated in the pump and to the loading or opening pressure of the spring-loaded non-return valve, hereinafter referred to, in the outlet thereof, to provide a return leakage path for a substantial proportion of the material back from the outlet end of the pump interior toward the inlet end thereof.

The emulsion outlet I5 is of elongated conical form, as shown inFigure 1, with the taper of the cone towards the interior of the pump and in it is a correspondingly conical non-return valve block l6 spring loaded by a compression spring I! to result in a predetermined positive back pressure or pressure difference in the pump as between the pressure obtaining at the outlet thereof and the pressure obtaining at the inlet end, this back pressure serving to promote the return flow above referred to of the material back along said leakage path toward the inlet end of the pump.

Referring to Figure 3, the loaded valve Ii is here shown as formed, for the purpose hereinbefore described with a continuous spiral groove [8 extending along its surface from end to end of the valve also and as associated with means for adjusting the loading pressure of the valve. These means comprise a compression spring I! interposed between the outer end of the valve and a plunger 20 in turn interposed between the spring and a knob or wheel 2| adjustable along a spigot 22 by screw-threaded engagement therewith, the spigot 22 being screwed into the body of the out-' let as shown.

What I claim as my invention and desire to secure by Letters Patent of the United States is:-

Apparatus for emulsifying or intimately admixing high viscosity semi-liquid masses, comprising a toothed wheel gear pump constructed with suflicient clearance between the casing and the teeth of the'gears to provide a definite leakage path for the mass under treatment in the pump back from the outlet end thereof towards the inlet end of the pump, and incorporating a springloaded outwardly opening non-return valve in the outlet of the pump for establishing and maintaining during the operation of the pump and therefore while the outlet thereof is in open pump-discharging condition, a positive pressure difference at the outlet end of the pump as compared with the pressure at the inlet end thereof, sufficient, having regard to the magnitude of the clearance referred to and to the viscosity of the mass under treatment in the pump, to ensure a constant return flow of a substantial proportion of the said mass along the leakage path.

STEFAN GEORG BAUER.

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2425671 *Sep 17, 1942Aug 12, 1947SoconyProcess of polymerizing
US2522378 *May 22, 1946Sep 12, 1950Owens Corning Fiberglass CorpResolving water and oil emulsions
US2644319 *Jan 4, 1950Jul 7, 1953Millman ClintonDevice for maintaining different temperatures in refrigerators
US2967841 *Mar 25, 1957Jan 10, 1961Du PontProcess for improved dispersion of pigments in enamels
US3349713 *Sep 10, 1965Oct 31, 1967Glanzstoff Koln G M B HProcess and device for mixing liquids of differing viscosities
US3592445 *Nov 26, 1968Jul 13, 1971Smith Kline French LabGelatin dip pot
US4015828 *Oct 30, 1973Apr 5, 1977Imperial Chemical Industries LimitedInjection of additives into liquid streams
US4025056 *Jun 30, 1975May 24, 1977Imperial Chemical Industries LimitedMixing apparatus
US5005982 *Jun 21, 1989Apr 9, 1991Kistner Kenneth JMaterial processor
US5137368 *Jul 18, 1990Aug 11, 1992Specified Equipment Systems Co., Inc.Viscous fluid pumping apparatus and system
Classifications
U.S. Classification366/97, 138/43, 366/272, 241/236, 366/262
International ClassificationB01F5/14, B01F5/00
Cooperative ClassificationB01F5/14
European ClassificationB01F5/14