High viscosity product pumping method and apparatus

Information

  • Patent Grant
  • 6254367
  • Patent Number
    6,254,367
  • Date Filed
    Tuesday, October 5, 1999
    25 years ago
  • Date Issued
    Tuesday, July 3, 2001
    23 years ago
Abstract
The required larger than normal pressure drop between the infeed and pump inlets of a positive displacement gear or lobe type pump pumping a high viscosity fluid such as pastry dough is obtained by the introduction of a vacuum inside the pump at or near the rotary nip points of the gear or lobe type pump to provide a means for the removal of any gas present in the vicinity of the nip point.
Description




FIELD OF THE INVENTION




The present invention relates to an improved method and equipment for pumping high viscosity products such as pastry dough and more particularly to such a method and apparatus that utilizes the introduction of a vacuum into the pump to assist in the generation of a higher than normal pressure drop from the infeed or hopper reservoir to the pump inlet.




BACKGROUND OF THE INVENTION




Automated machinery to produce bread and other pastry products conventionally use single or twin auger pumps. Such auger pumps not only move the dough, but also uniformly damage the dough due to shearing action and then homogenize the degraded dough throughout the dough mass their use to produce a high quality product id somewhat less than fully desirable.




In order to solve the problem of dough damage and degradation, attempts have been made to utilize positive displacement gear or lobe type pumps that impart less damage to the dough for pumping such viscous masses. The problem with such positive displacement pumps resides in their inability to maintain a proper prime to the pump because of the high viscosity of the dough. Maintenance of the prime to the pumps for the pumping of such highly viscous materials requires that the lobe or gear pump produce a larger than normal pressure drop from the infeed or hopper reservoir to the pump inlet to assure that adequate viscous fluid is continuously drawn into the pump.




Thus, a positive displacement gear or lobe type pump that does not damage the pastry dough to the extent that an auger type pump does while being capable of maintaining its prime would provide significant advantages in the pastry dough pumping arena.




OBJECT OF THE INVENTION




It is therefore an object of the present invention to provide a positive displacement gear or lobe type pump and method of operating same that, while providing all of the advantages of such a pump, can readily maintain it prime even when pumping very high viscosity fluids such as pastry dough.




SUMMARY OF THE INVENTION




According to the present invention, the required larger than normal pressure drop between the infeed and pump inlets in a positive displacement gear or lobe type pump pumping a high viscosity fluid such as pastry dough is accomplished by the introduction of a vacuum inside the pump at or near the rotary nip points of the gear or lobe type pump to provide a means for the removal of any gas present in the vicinity of the nip point.











DESCRIPTION OF THE DRAWINGS





FIG. 1

is a cross-sectional view of a typical rotary pump used to move fluids.





FIG. 2

is a cross-sectional view of a gear or lobe type pump incorporating the improvement of the present invention.





FIG. 3

is a phantom side view of one possible variant of the vacuum tube utilized in the pump and pumping method of the present invention of the present invention.





FIG. 4

is a cross-sectional view of the vacuum tube of

FIG. 3

along the line


4





4


of FIG.


3


.





FIG. 5

is a schematic diagram of the complete vacuum system of the present invention.











DETAILED DESCRIPTION




As shown in

FIG. 1

, a so-called positive displacement gear or lobe pump


10


comprises a housing


12


having two counter rotating lobed gears


14


and


16


mounted on shafts


18


and


20


therein. High viscosity material


22


is supplied to pump


10


via hopper inlet reservoir


24


. At this point, material


22


is under low pressure, as represented by the larger balls in

FIG. 1

, i.e. the pressure provided is solely due to the weight of material


22


in reservoir


24


. As gears


14


and


16


counter rotate, lobes


26


and


28


alternately engage portions


30


and


32


of high viscosity material


22


forcing them about the interior of housing


12


and delivering them to discharge port


34


in the form of compressed, high pressure material


36


represented by the smaller balls in FIG.


1


. Compression and pressure increase is of course due to the relatively smaller surface area of outlet


34


versus that of inlet reservoir


24


.




As described hereinabove, the problem with the operation of such pumps involves their inability to maintain the prime, i.e. the feed of viscous material


22


from reservoir


24


into the area where it may be engaged by lobes


26


and


28


, since viscous material


22


does not readily flow due to its high viscosity. Additionally, gas pockets


38


tend to impose a back pressure on incoming material


22


inhibiting its engagement with lobes


26


and


28


.




As shown in

FIG. 2

, the present invention solves this priming problem by the introduction of a vacuum tube


40


into the vicinity of nip point


42


, i.e. that point where two lobes


26


and


28


approach each other and where gas pocket


38


occurs. Vacuum tube


40


provides the means to extract from nip point


42


gas entrapped in gas pocket


38


thereby eliminating this cause of back pressure against incoming material


22


and indeed drawing material


22


into nip point


42


by the negative force of the vacuum.




The particular level of vacuum utilized will, of course depend to some degree upon the consistency/viscosity of material


22


being pumped and is readily determinable by the skilled artisan having the instant disclosure before them. A vacuum of about 20 inches of mercury is considered appropriate for pumping materials such as pastry dough.




The structure of vacuum tube


40


is not particularly critical so long as it is capable of extracting entrapped gas/air from the vicinity of nip point


42


. One possible such useful structure for vacuum tube


40


is shown in

FIGS. 3 and 4

. As shown in

FIG. 3

, vacuum tube


40


comprises a mounting ring


44


for securing vacuum tube


40


at the appropriate location within housing


12


at nip point


42


, a vacuum tube housing


46


and a rear support


48


for similarly mounting vacuum tube


40


in housing


12


. Vacuum to the interior of vacuum tube


40


is supplied via apertures


50


whose structure and location are shown most clearly in FIG.


4


. Gas/air and liquid (water) may be provided entering interior


52


of housing


46


through aperture


54


to assist with the removal by flushing of any material


22


entering apertures


50


and permitting their drawing to a tank trap


58


in vacuum line


60


as shown in FIG.


5


.





FIG. 5

depicts a preferred overall vacuum system of the present invention. As shown in

FIG. 5

, the system operates by using a vacuum generator


64


that may be of a simple Venturi type. The generated vacuum is passed through vacuum line


60


and in turn through a vacuum tank trap


58


and thence via vacuum line


60


A to apertures


50


. Vacuum tank trap


58


is equipped with appropriate vacuum control and pressure detection gauges


66


and


68


. In order to provide the flushing air or water that may be required to move material


22


entering apertures


50


and draining this material to vacuum tank trap


58


air/water/oil of appropriate composition and cleanliness can be bled into vacuum tube


40


via line


70


through a regulator


72


from supply tank


74


. In this fashion, any material


22


that enters vacuum tube


40


and vacuum apertures


50


is drained to vacuum tank


58


via vacuum line


60


A with the help of the inserted air/water/oil and vacuum tank


58


periodically cleaned.




From the foregoing description, one skilled in the art can easily ascertain the essential characteristics of this invention and without departing from the spirit and scope thereof make various changes and modifications to the invention to adapt it to various usages and conditions. It is therefor intended that the scope of the invention be limited only buy the scope of the appended claims.



Claims
  • 1. In a positive displacement rotary pump for pumping viscous fluids comprising:A) a housing having; i) an inlet reservoir; and ii) a discharge port; and B) a pair of counter rotating lobed gears within said housing, said counter rotating lobed gears defining a nip point where two lobes of said lobed gears meet; the improvement comprising the inclusion of a vacuum tube in the vicinity of said nip point to provide a means for removal of any gas entrapped in said housing at said nip point.
  • 2. A method for improving the viscous fluid priming characteristics of a positive displacement rotary pump comprising:A) a housing having; iii) an inlet reservoir; and iv) a discharge port; and B) a pair of counter rotating lobed gears within said housing, said counter rotating lobed gears defining a nip point where two lobes of said lobed gears meet; said method comprising the application of a vacuum via a vacuum tube located in the vicinity of said nip point to provide a means for removal of any gas entrapped in said housing at said nip point during pumping.
Parent Case Info

The benefit under 35 USC 119 of United States provisional application 60/106,575 filed Nov. 2, 1998 is hereby claimed.

US Referenced Citations (1)
Number Name Date Kind
5145349 McBurnett Sep 1992
Foreign Referenced Citations (4)
Number Date Country
1273994 Jul 1968 DE
2737761 Mar 1979 DE
2737833 Mar 1979 DE
496360 Nov 1919 FR
Provisional Applications (1)
Number Date Country
60/106575 Nov 1998 US