CA1281027C - Two stage blender - Google Patents
Two stage blenderInfo
- Publication number
- CA1281027C CA1281027C CA000545495A CA545495A CA1281027C CA 1281027 C CA1281027 C CA 1281027C CA 000545495 A CA000545495 A CA 000545495A CA 545495 A CA545495 A CA 545495A CA 1281027 C CA1281027 C CA 1281027C
- Authority
- CA
- Canada
- Prior art keywords
- impeller
- blender
- stage
- mixture
- mixing zone
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/57—Mixing high-viscosity liquids with solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/60—Pump mixers, i.e. mixing within a pump
- B01F25/64—Pump mixers, i.e. mixing within a pump of the centrifugal-pump type, i.e. turbo-mixers
- B01F25/641—Multi-staged turbo-mixers
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Abstract of Disclosure A two stage blender is capable of handling high viscosity liquid-powder mixtures. The mixture discharged from the first stage is directed to the second stage, from which it is discharged at a relatively high discharge pressure. The second stage further enhances the natural vacuum created within the first stage, so that powder is fed at a constant ratio for a wide variety of liquid flows. Selected internal parts of the blender are designed to permit cleaning the blender in place.
Description
~.28~
TWO STAGE BLENDER
Backqround of the Invention.
1. Fi~ld c~ the lAVe~t j~n. This invention pertains to mixing apparatus, and moxe particularly to ~ apparatus for continuously blending powders with a liquid.
20 Description of the Prior Art. Exemplary apparatus for blending liquids and particulate solids i8 disclosed in U. S. Patent No. 3,606~270. That blender has met with considerable comm~rcial success.
However the blender of the 3 1 60~ r 270 patent is somewhat limited in its ability to handle high viscosi~y liquid-powder end products. That is because, as the end product viscosity increases, the blender outlet pressure decreases and the vacuum created in the eye of the blender impeller becomes quite low.
Conseyuently, the amount of powder drawn into the impeller decreases and yields a higher ratio of liquid to powder than is desired. To alleviate that problem, the screen that normally surrounds the impeller periphery may be removed, but then the mixing action produced by the liquid and powder flowing thxough the screen becomes unavailable. Accordingly, blender performance and product consistency occasionally become unacceptable at high end product viscosities.
Thus, a need exists for a blender capable of ~ .
' , handling high viscosity liquid-powder end products.
Summary of the_Invention In accordance with the present invention, a liquid-solid particulate blender is provlded that efficiently mixes and discharges high viscosity end products. This is accomplished by apparatus that includes a second stage mlxing zone that assists drawing the liquid-powder mixture from the first stage and that increases the blender outlet pressure.
In the first stage mixing zone the liquid and powder are blended in a known fashion. Liquid is pumped tangentially around a diffuser tube and into the first stage mixing zone in the same direction as the rotation of a blender impeller. ~he liquid is introduced at the leading edge of the impeller, which has a central recess radially inwardly from the impeller vanes. The impeller accelerates the liquid radially outwardly, thereby creating a vacuum at the central recess. The natural suction created at the impeller recess pulls the powder from a storage hopper to the recess through the diffuser tuhe. Powder and liquid mixing occur as they are accelerated radially outwardly by the impeller~ The mixture is orced through an annular screen surrounding the impeller periphery, thereby further mixing the ingredients.
The liquid and powder leaving the first stage mixing zone are discharged to the second stage mixing zone that is in series with the first stage. The mixture is directed downwardly and radially inwardly after leaving the first stage annular screen. Simple baffles create an in~ernal passage through which the mixture from the first stage enters the central recess of a second stage impeller. The second stage impeller again accelerates the mixture radially outwardly and through a second stage annular screen. As a result of .,........................... ~ . ' '. .: .
.
. . .
~B10~7 the operation of the second stage mixing zone, the vacuum produced at the first stage impeller recess is enhanced, and the flow of powder into the Eirst stage mixing ~one remains relati~ely constant, even with high S viscosity end products. Moreover, the second stags increases the blender outlet pressure to provide increased flow notwithstanding high viscosity end products.
Further in accordance with the present invention, the baffles between the first and second mixing zones are designed to permit cleaning in place the blender first stage mixing zone. For that purpose, a clearance is provided between the first stage impeller and the baffle member ad3acent thereto.
Accordingly, the blender may be flushed and cleaned without complete disassembly, thereby reducing lost production time.
Other objects and advantages of the invention will become apparent to those skilled in the art from reading the disclosureO
Brief DescriPtion of the Drawings - Figr 1 is a partial longitudinal cross-sectional view of the blender of the present invention;
Fig. 2 is a cross-sectional view taken along lines 2-2 of Fig. 1; and Fig. 3 is a set of performance curves for a prior blender and for the blender of the present invention.
Detailed Description of the Invention Although the disclosure hereof is detailed and exact to enable those skilled in the art to practice the invention, the physical embodiments herein disclosed merely exemplify the invention which may be embodied in other specific structure. The scope of the invention is defined in the claims appended hereto.
,. . . . . . . . .
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: ' ` .'............................. ~ : - ', ' , ~X~ 2~
Referring to Figs. 1 and 2, a two-stage blender 1 is illustrated that includes the present invention. The blender is particularly useful for mixing liquid and solid ood and beverage ingredients into a high viscosity edible end product. However, it will be understood that the invention is not limited to sanitary applications.
The blender 1 is used in connection with an electric motor, drive system r and storage hopper that are not illustrated in Figs. 1 and 2. The motor, drive, and hopper are described in U.S. Patent No.
3,606,270 t which is incorporated by reference herein.
The blender may be supported on a stana~ not shown, by posts 3 that are attached to a bottom ring 5.
Located above the blender 1 is the hopper for storing particulate solids, which may be in the form of powders. The powder enters the blender by means of diffuser tube 7. The lower end 9 of the diPfuser tube 7 is provided with an annular flange 11. The upper surface of the flange 11 is shaped with a radius 21 that approximates the radius 23 of the inner surface of the blender casinq inlet 15 adjacent the flange 11.
The diffuser tube 7 is concentrically located within the blender casing inlet 15.
The blender 1 includes a first stage mixing zone 16 bounded by the casing 44. Although in the disclosed con~truction the casing 44 is one piece, an alternate construction could employ a two-piece casing split, for example, along line 45.
The components within the first stage mixing zone 16 comprise a first stage impeller 27, which, as best shown in Fig. 2, may h~ve four vanes 28. The vanes 28 extend radially outwardly from a central hub 30 having ~ length less than the height of the vanes, thereby forming a central recess 33. As .
; . . , ' ' .28~ 7 illustrated, the low~r end 9 of the diffuser tube 7 extends into the recess 33. The impeller 27 is attached to a drive shaft 29 for rotation therewith by an electric motor and drive system. The first stage impeller 27 is secured to the end of the shaft 29 by a screw 31 through a washer 71. Surrounding the periphery of the impeller 27 is a first stage annular screen 37. The first stage annular screen 37 rests on an upper baffle member 35 that has four equally spaced tabs 72 on the outer circumference,of the upper baffle member 35. A pin 73 is fixedly attached to the first stage annular screen 37 extending below the bottom of the first stage annular screen 37 and abutting against one of the four equally spaced tabs 72 of the circular lS plate 35 to prevent rotation of the first stage annular scr~en 37. The casing 44 bounding the first stage mixing zone 16 is fabricated with a wall 38 that i radial~y spaced outwardly from the screen 37 to create a first discharge volume 39.
In accordance with the present invention, the blender 1 further includes a second stage mixing zone 41. The second stage mixing zone 41 is bounded by the common casing 44 and includes a second impeller 43 secured for rotation to the shaft 29. The second stage impeller 43 is separated from the first stage impeller 27 by spacer 74 that fits concentrically around shaft 29. The second stage impeller 43 is genexally similar to the first stage impeller 27, having a central recess 48 and several vanes 52 radiating therefrom. However, the second stage impeller vanes 52 extend radially inwardly farther than the vanes 28 of the first stage impeller 27, so that the second stage recess 48 is smaller than the first stage recess 33. The periphery of the impeller 43 is surrounded by a second stage annular screen 45. The second stage annular screen 45 -'' ' ' ' . , :
f~
rests on a circular plate 70 to which is fixedly attached the support ring 5. The shaf t 29 extends through a sealing means 50 in the circular plate 70.
Casin~ 44 has a wall portion 46 that is radially spaced outwardly from the screen 45 to create a second discharge outlet 47 ~he casing 44 and the support ring 5 may be releasably joined to each other by means of a quick-couple connector 49.
In the illu~trated construction, a passage 51 is formed between -the first and second mixing zones 16 and 41 by means of internal baffles. The baffles comprise an upper baffle member 35 that has four eyually spaced tabs 72 on its outer circumference. The baffles further include a generally horizontal lower member SS which provlde four spacer supports 76 to provide an axial spacing from the upper baffle member 35 and is preferably concentric with the upper baffle member 35. A downwardly sloped wall portion 57 of the casing 44 completes the contours of the passage 51.
The lower member 55 has pxovisions to receive a pin 74 that is fixedly attached to the upper portion of the second stage annular screen 45 to prevent rotation of the second stage annular screen.- Slots 75 are formed in casing 44 to prevent the rotation of the lower member 55.
Further in accordance with the present invention, the first stage mixing 20ne 16 is constructed so that the components thereof may be cleaned in place. For that purpose, the impeller 27 and upper baffle member 35 are located with respect to each other such that a radial clearance 58 and an axial clearance 60 exist between the impeller 27 and upper baffle member 35. The clearances 58 and 60 are sized to permit only minimal amounts of the powder-liquid mixture to pass through the clearances, but to allow ' ' . ':
` '' ' ' . ' - .
~'~ 8~ ~ 7 passage of sufficient flushing fluid to permit cleaning the components without disassembling them. As a result~ the first stage mixing zone of the blender 1 of the present invention may be cleaned with only minimum loss of production time.
In operation, the blender 1 of the present invention mixes liquids and powders into end products having higher viscosities than can be handled by single stage blenders. I.iquid is introduced into the blender first stage 16 through th~ hollow cylindrical space 13 that is located between the dif~user tube 7 and the blender casing inlet 15. The entering liquid has a rotational component of motion about the central axis 17 and a downward component of motion, as indicated by arrows 1~. When the liquid strikes the radius 21 of the flanga 11, it is deflected radially outwardly, as indicated by the arrow 25. The rotational motion of the incoming liquid is in the same direction as the rotation of the impeller 27.
The impeller 27 imparts a radially outward acceleration to the liquid. Simultaneously, the impeller creates a natural vacuum within the recess 33, thereby drawing particulate solids from the hopper through the diffuser tube 7 and into the recess 33, as indicated by arrow 34. The solids are then accelerated outwardly by the 1mpeller vanes 28, arrow 36, and they are mixed with the liquid. The mixture is forced through the first stage screen 37, which further mixes the ingredients. As illustrated by arrows 59, the mixture discharged from the first stage mixing zone 16 is diverted downwardly by the casing wall 38 into the passage 51. The baffles composed oE the members 35 and 55 and the casing wall 57 direct the mixture radially inwardly toward axis 17 and into the recess 48 of the second stage mixing zone lmpeller 43, as indicated by ~8~ 7 arrows 61. From the second mixing zone recess 48, the impeller 43 again accelerates the mixture radially outwardO Finally, the mixture is forced through the second stage screen 45 and into the discharge outlet 47, arrow 63.
The addition of the second stage 41 of the blender 1 of the present invention enhances the vacuum produced at the first stage recess 33, thereby drawin~
the particulate solids through the diffuser tube 7 in a uniform manner, even with high viscosity end products.
Referring to Fig. 3, the improved performance of tha two stage blender 1 is graphically illustrated. Curves 67a and 69a qualitatively depict, for two certain typical operating conditi~ns, the changes in vacuum at the first stage recess 33 with change in product flow.
The decrease in vacuum with increased product flow corresponds to a decreased powder-to-liquid ratio, i.e., with less vacuum, less powder is pulled from the hopper at a particular liquid flow. Consequently, the ~0 end product consistency and ingredient ratio may fall outside the formula speci~ication. Curves 67b and 69b ~-qualitatively depict the performance of the two stage blender 1 of the present invention under the same operating conditions as curves 67a and 69a, respectively. The volume at the first stage mixing recess 33 remains relatively constant with increased product flow, thus insuring proper ingredient ratios even at high end product viscosities. Further, the second stage 41 increases the discharge pressure at the discharge outlet 47, thereby overcomincJ the problems associated with mixing high viscosity end products in a single stage blender.
Thus, it is apparent that there has been provided, in accordance with the invention, a two stage blender that fully satisfies the aims and advantages - . ', ~8~27 g set forth above. While the specification has been described in conjunction with specific embodiments thereof, it is evident that many alternatives, modifications, and variations will be apparent to those skilled ln the art in light of the foregoing description. Accordingly, it is intended to embrace all such alternatives, modifications, and variations as fall within the spirit and broad scope of the appended claims.
.
. . :
- , .
TWO STAGE BLENDER
Backqround of the Invention.
1. Fi~ld c~ the lAVe~t j~n. This invention pertains to mixing apparatus, and moxe particularly to ~ apparatus for continuously blending powders with a liquid.
20 Description of the Prior Art. Exemplary apparatus for blending liquids and particulate solids i8 disclosed in U. S. Patent No. 3,606~270. That blender has met with considerable comm~rcial success.
However the blender of the 3 1 60~ r 270 patent is somewhat limited in its ability to handle high viscosi~y liquid-powder end products. That is because, as the end product viscosity increases, the blender outlet pressure decreases and the vacuum created in the eye of the blender impeller becomes quite low.
Conseyuently, the amount of powder drawn into the impeller decreases and yields a higher ratio of liquid to powder than is desired. To alleviate that problem, the screen that normally surrounds the impeller periphery may be removed, but then the mixing action produced by the liquid and powder flowing thxough the screen becomes unavailable. Accordingly, blender performance and product consistency occasionally become unacceptable at high end product viscosities.
Thus, a need exists for a blender capable of ~ .
' , handling high viscosity liquid-powder end products.
Summary of the_Invention In accordance with the present invention, a liquid-solid particulate blender is provlded that efficiently mixes and discharges high viscosity end products. This is accomplished by apparatus that includes a second stage mlxing zone that assists drawing the liquid-powder mixture from the first stage and that increases the blender outlet pressure.
In the first stage mixing zone the liquid and powder are blended in a known fashion. Liquid is pumped tangentially around a diffuser tube and into the first stage mixing zone in the same direction as the rotation of a blender impeller. ~he liquid is introduced at the leading edge of the impeller, which has a central recess radially inwardly from the impeller vanes. The impeller accelerates the liquid radially outwardly, thereby creating a vacuum at the central recess. The natural suction created at the impeller recess pulls the powder from a storage hopper to the recess through the diffuser tuhe. Powder and liquid mixing occur as they are accelerated radially outwardly by the impeller~ The mixture is orced through an annular screen surrounding the impeller periphery, thereby further mixing the ingredients.
The liquid and powder leaving the first stage mixing zone are discharged to the second stage mixing zone that is in series with the first stage. The mixture is directed downwardly and radially inwardly after leaving the first stage annular screen. Simple baffles create an in~ernal passage through which the mixture from the first stage enters the central recess of a second stage impeller. The second stage impeller again accelerates the mixture radially outwardly and through a second stage annular screen. As a result of .,........................... ~ . ' '. .: .
.
. . .
~B10~7 the operation of the second stage mixing zone, the vacuum produced at the first stage impeller recess is enhanced, and the flow of powder into the Eirst stage mixing ~one remains relati~ely constant, even with high S viscosity end products. Moreover, the second stags increases the blender outlet pressure to provide increased flow notwithstanding high viscosity end products.
Further in accordance with the present invention, the baffles between the first and second mixing zones are designed to permit cleaning in place the blender first stage mixing zone. For that purpose, a clearance is provided between the first stage impeller and the baffle member ad3acent thereto.
Accordingly, the blender may be flushed and cleaned without complete disassembly, thereby reducing lost production time.
Other objects and advantages of the invention will become apparent to those skilled in the art from reading the disclosureO
Brief DescriPtion of the Drawings - Figr 1 is a partial longitudinal cross-sectional view of the blender of the present invention;
Fig. 2 is a cross-sectional view taken along lines 2-2 of Fig. 1; and Fig. 3 is a set of performance curves for a prior blender and for the blender of the present invention.
Detailed Description of the Invention Although the disclosure hereof is detailed and exact to enable those skilled in the art to practice the invention, the physical embodiments herein disclosed merely exemplify the invention which may be embodied in other specific structure. The scope of the invention is defined in the claims appended hereto.
,. . . . . . . . .
' '~
: ' ` .'............................. ~ : - ', ' , ~X~ 2~
Referring to Figs. 1 and 2, a two-stage blender 1 is illustrated that includes the present invention. The blender is particularly useful for mixing liquid and solid ood and beverage ingredients into a high viscosity edible end product. However, it will be understood that the invention is not limited to sanitary applications.
The blender 1 is used in connection with an electric motor, drive system r and storage hopper that are not illustrated in Figs. 1 and 2. The motor, drive, and hopper are described in U.S. Patent No.
3,606,270 t which is incorporated by reference herein.
The blender may be supported on a stana~ not shown, by posts 3 that are attached to a bottom ring 5.
Located above the blender 1 is the hopper for storing particulate solids, which may be in the form of powders. The powder enters the blender by means of diffuser tube 7. The lower end 9 of the diPfuser tube 7 is provided with an annular flange 11. The upper surface of the flange 11 is shaped with a radius 21 that approximates the radius 23 of the inner surface of the blender casinq inlet 15 adjacent the flange 11.
The diffuser tube 7 is concentrically located within the blender casing inlet 15.
The blender 1 includes a first stage mixing zone 16 bounded by the casing 44. Although in the disclosed con~truction the casing 44 is one piece, an alternate construction could employ a two-piece casing split, for example, along line 45.
The components within the first stage mixing zone 16 comprise a first stage impeller 27, which, as best shown in Fig. 2, may h~ve four vanes 28. The vanes 28 extend radially outwardly from a central hub 30 having ~ length less than the height of the vanes, thereby forming a central recess 33. As .
; . . , ' ' .28~ 7 illustrated, the low~r end 9 of the diffuser tube 7 extends into the recess 33. The impeller 27 is attached to a drive shaft 29 for rotation therewith by an electric motor and drive system. The first stage impeller 27 is secured to the end of the shaft 29 by a screw 31 through a washer 71. Surrounding the periphery of the impeller 27 is a first stage annular screen 37. The first stage annular screen 37 rests on an upper baffle member 35 that has four equally spaced tabs 72 on the outer circumference,of the upper baffle member 35. A pin 73 is fixedly attached to the first stage annular screen 37 extending below the bottom of the first stage annular screen 37 and abutting against one of the four equally spaced tabs 72 of the circular lS plate 35 to prevent rotation of the first stage annular scr~en 37. The casing 44 bounding the first stage mixing zone 16 is fabricated with a wall 38 that i radial~y spaced outwardly from the screen 37 to create a first discharge volume 39.
In accordance with the present invention, the blender 1 further includes a second stage mixing zone 41. The second stage mixing zone 41 is bounded by the common casing 44 and includes a second impeller 43 secured for rotation to the shaft 29. The second stage impeller 43 is separated from the first stage impeller 27 by spacer 74 that fits concentrically around shaft 29. The second stage impeller 43 is genexally similar to the first stage impeller 27, having a central recess 48 and several vanes 52 radiating therefrom. However, the second stage impeller vanes 52 extend radially inwardly farther than the vanes 28 of the first stage impeller 27, so that the second stage recess 48 is smaller than the first stage recess 33. The periphery of the impeller 43 is surrounded by a second stage annular screen 45. The second stage annular screen 45 -'' ' ' ' . , :
f~
rests on a circular plate 70 to which is fixedly attached the support ring 5. The shaf t 29 extends through a sealing means 50 in the circular plate 70.
Casin~ 44 has a wall portion 46 that is radially spaced outwardly from the screen 45 to create a second discharge outlet 47 ~he casing 44 and the support ring 5 may be releasably joined to each other by means of a quick-couple connector 49.
In the illu~trated construction, a passage 51 is formed between -the first and second mixing zones 16 and 41 by means of internal baffles. The baffles comprise an upper baffle member 35 that has four eyually spaced tabs 72 on its outer circumference. The baffles further include a generally horizontal lower member SS which provlde four spacer supports 76 to provide an axial spacing from the upper baffle member 35 and is preferably concentric with the upper baffle member 35. A downwardly sloped wall portion 57 of the casing 44 completes the contours of the passage 51.
The lower member 55 has pxovisions to receive a pin 74 that is fixedly attached to the upper portion of the second stage annular screen 45 to prevent rotation of the second stage annular screen.- Slots 75 are formed in casing 44 to prevent the rotation of the lower member 55.
Further in accordance with the present invention, the first stage mixing 20ne 16 is constructed so that the components thereof may be cleaned in place. For that purpose, the impeller 27 and upper baffle member 35 are located with respect to each other such that a radial clearance 58 and an axial clearance 60 exist between the impeller 27 and upper baffle member 35. The clearances 58 and 60 are sized to permit only minimal amounts of the powder-liquid mixture to pass through the clearances, but to allow ' ' . ':
` '' ' ' . ' - .
~'~ 8~ ~ 7 passage of sufficient flushing fluid to permit cleaning the components without disassembling them. As a result~ the first stage mixing zone of the blender 1 of the present invention may be cleaned with only minimum loss of production time.
In operation, the blender 1 of the present invention mixes liquids and powders into end products having higher viscosities than can be handled by single stage blenders. I.iquid is introduced into the blender first stage 16 through th~ hollow cylindrical space 13 that is located between the dif~user tube 7 and the blender casing inlet 15. The entering liquid has a rotational component of motion about the central axis 17 and a downward component of motion, as indicated by arrows 1~. When the liquid strikes the radius 21 of the flanga 11, it is deflected radially outwardly, as indicated by the arrow 25. The rotational motion of the incoming liquid is in the same direction as the rotation of the impeller 27.
The impeller 27 imparts a radially outward acceleration to the liquid. Simultaneously, the impeller creates a natural vacuum within the recess 33, thereby drawing particulate solids from the hopper through the diffuser tube 7 and into the recess 33, as indicated by arrow 34. The solids are then accelerated outwardly by the 1mpeller vanes 28, arrow 36, and they are mixed with the liquid. The mixture is forced through the first stage screen 37, which further mixes the ingredients. As illustrated by arrows 59, the mixture discharged from the first stage mixing zone 16 is diverted downwardly by the casing wall 38 into the passage 51. The baffles composed oE the members 35 and 55 and the casing wall 57 direct the mixture radially inwardly toward axis 17 and into the recess 48 of the second stage mixing zone lmpeller 43, as indicated by ~8~ 7 arrows 61. From the second mixing zone recess 48, the impeller 43 again accelerates the mixture radially outwardO Finally, the mixture is forced through the second stage screen 45 and into the discharge outlet 47, arrow 63.
The addition of the second stage 41 of the blender 1 of the present invention enhances the vacuum produced at the first stage recess 33, thereby drawin~
the particulate solids through the diffuser tube 7 in a uniform manner, even with high viscosity end products.
Referring to Fig. 3, the improved performance of tha two stage blender 1 is graphically illustrated. Curves 67a and 69a qualitatively depict, for two certain typical operating conditi~ns, the changes in vacuum at the first stage recess 33 with change in product flow.
The decrease in vacuum with increased product flow corresponds to a decreased powder-to-liquid ratio, i.e., with less vacuum, less powder is pulled from the hopper at a particular liquid flow. Consequently, the ~0 end product consistency and ingredient ratio may fall outside the formula speci~ication. Curves 67b and 69b ~-qualitatively depict the performance of the two stage blender 1 of the present invention under the same operating conditions as curves 67a and 69a, respectively. The volume at the first stage mixing recess 33 remains relatively constant with increased product flow, thus insuring proper ingredient ratios even at high end product viscosities. Further, the second stage 41 increases the discharge pressure at the discharge outlet 47, thereby overcomincJ the problems associated with mixing high viscosity end products in a single stage blender.
Thus, it is apparent that there has been provided, in accordance with the invention, a two stage blender that fully satisfies the aims and advantages - . ', ~8~27 g set forth above. While the specification has been described in conjunction with specific embodiments thereof, it is evident that many alternatives, modifications, and variations will be apparent to those skilled ln the art in light of the foregoing description. Accordingly, it is intended to embrace all such alternatives, modifications, and variations as fall within the spirit and broad scope of the appended claims.
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Claims (6)
1. In a blender for mixing solid particulates and liquids having a rotatable impeller for radially discharging the mixture and having imperforate vanes of a predetermined height with a centrally located recess with respect to the impeller vanes; means for feeding the solid particulates to the impeller recess; means for introducing liquid to the impeller vanes to be mixed with the solids by the impeller; an annular screen surrounding the impeller periphery; and casing means for enclosing the impeller and screen and for discharging the mixed liquid and solids, the improvement comprising:
a. a first annular passage formed in the casing means having a height generally equal to the height of the impeller vanes and uniformly surrounding the annular screen for receiving the mixture discharged radially by the impeller;
b. a second annular passage concentric with the impeller and axially isolated therefrom and communicating with the first annular passage, the second annular passage directing the flow of the mixture radially inwardly;
c. second rotatable impeller means for receiving the mixed product from the second annular passage and for accelerating the product radially outwardly; and d. discharge means surrounding the second impeller means for receiving the mixed end product therefrom, so that the discharge pressure of the end product is increased by the second impeller means to thereby enable the blender to handle high viscosity end products.
a. a first annular passage formed in the casing means having a height generally equal to the height of the impeller vanes and uniformly surrounding the annular screen for receiving the mixture discharged radially by the impeller;
b. a second annular passage concentric with the impeller and axially isolated therefrom and communicating with the first annular passage, the second annular passage directing the flow of the mixture radially inwardly;
c. second rotatable impeller means for receiving the mixed product from the second annular passage and for accelerating the product radially outwardly; and d. discharge means surrounding the second impeller means for receiving the mixed end product therefrom, so that the discharge pressure of the end product is increased by the second impeller means to thereby enable the blender to handle high viscosity end products.
2. A blender for mixing liquid and powder into a high viscosity end product comprising:
a. a first stage mixing zone;
b. means for introducing liquid and powder to the first stage mixing zone;
c. a first imperforate impeller having a hub and upstanding vanes of a predetermined height and radiating from the hub to a predetermined diameter, the impeller being adapted for creating a vacuum to draw powder into the first stage mixing zone and for mixing the liquid and powder in said first stage mixing zone and for radially discharging the mixture therefrom;
d. a second stage mixing zone;
e. a casing wall uniformly surrounding the first stage mixing zone and defining a uniform first annular passage of a height generally equal to the height of the impeller vanes;
f. a second annular passage in axial alignment with and axially separated from the first stage mixing zone, the first and second annular passages cooperating to locate the second stage mixing zone in series with the first stage mixing zone by directing the mixture from the first stage mixing zone to the second mixing zone; and g. means in the second stage mixing zone for receiving and accelerating the mixture from the second passage and for discharging the mixed end product, so that the end product is discharged from the second stage mixing zone at a high discharge pressure to enable the blender to handle high viscosity end products.
a. a first stage mixing zone;
b. means for introducing liquid and powder to the first stage mixing zone;
c. a first imperforate impeller having a hub and upstanding vanes of a predetermined height and radiating from the hub to a predetermined diameter, the impeller being adapted for creating a vacuum to draw powder into the first stage mixing zone and for mixing the liquid and powder in said first stage mixing zone and for radially discharging the mixture therefrom;
d. a second stage mixing zone;
e. a casing wall uniformly surrounding the first stage mixing zone and defining a uniform first annular passage of a height generally equal to the height of the impeller vanes;
f. a second annular passage in axial alignment with and axially separated from the first stage mixing zone, the first and second annular passages cooperating to locate the second stage mixing zone in series with the first stage mixing zone by directing the mixture from the first stage mixing zone to the second mixing zone; and g. means in the second stage mixing zone for receiving and accelerating the mixture from the second passage and for discharging the mixed end product, so that the end product is discharged from the second stage mixing zone at a high discharge pressure to enable the blender to handle high viscosity end products.
3. The blender of claim 2 wherein the second annular passage is defined by a plurality of baffles, the baffles comprising:
a. a generally horizontal upper member concentric with the first impeller and having an outer diameter in general radial alignment with the first impeller vanes outer diameter and an inner diameter in radial clearance relationship with the impeller hub;
b. a generally horizontal lower member axially spaced from and concentric with and parallel to the upper member; and c. an inwardly and downwardly sloped wall portion of the casing wall uniformly bounding the first annular passage.
a. a generally horizontal upper member concentric with the first impeller and having an outer diameter in general radial alignment with the first impeller vanes outer diameter and an inner diameter in radial clearance relationship with the impeller hub;
b. a generally horizontal lower member axially spaced from and concentric with and parallel to the upper member; and c. an inwardly and downwardly sloped wall portion of the casing wall uniformly bounding the first annular passage.
4. The blender of claim 2 further comprising:
a. base means for supporting the blender on a support surface; and b. quick couple means for releasably connecting the casing to the base means.
a. base means for supporting the blender on a support surface; and b. quick couple means for releasably connecting the casing to the base means.
5. A two stage blender for mixing liquid and powders into high viscosity end products comprising:
a. means for introducing the liquid and powders into the blender;
b. a first impeller mounted for rotation around a central axis and having a central recess of a first size for receiving the liquid and powder, the impeller imparting a radially outward acceleration to the powder and liquid to thereby mix them;
c. a casing surrounding the first impeller and defining a uniform annular passage to receive the mixed liquid and powder, the casing being formed with a wall shaped to direct the mixture axially and radially inwardly toward the central axis;
d. a pair of axially spaced baffle members concentric with the central axis for guiding the mixture from the casing annular passage inwardly toward the central axis and actually along the central axis;
e. a second impeller mounted for rotation about the central axis in unison with the first impeller, the second impeller having a central recess of a second size less than the size of the recess of the first impeller for receiving the mixture from the baffle members and for imparting a second outward acceleration to the mixture; and f. discharge means in the casing uniformly surrounding the second impeller for receiving the mixture from the second impeller, so that the mixture is discharged from the blender at a high pressure notwithstanding high end product viscosity.
a. means for introducing the liquid and powders into the blender;
b. a first impeller mounted for rotation around a central axis and having a central recess of a first size for receiving the liquid and powder, the impeller imparting a radially outward acceleration to the powder and liquid to thereby mix them;
c. a casing surrounding the first impeller and defining a uniform annular passage to receive the mixed liquid and powder, the casing being formed with a wall shaped to direct the mixture axially and radially inwardly toward the central axis;
d. a pair of axially spaced baffle members concentric with the central axis for guiding the mixture from the casing annular passage inwardly toward the central axis and actually along the central axis;
e. a second impeller mounted for rotation about the central axis in unison with the first impeller, the second impeller having a central recess of a second size less than the size of the recess of the first impeller for receiving the mixture from the baffle members and for imparting a second outward acceleration to the mixture; and f. discharge means in the casing uniformly surrounding the second impeller for receiving the mixture from the second impeller, so that the mixture is discharged from the blender at a high pressure notwithstanding high end product viscosity.
6. The blender of claim 5 wherein the baffle members comprise an upper baffle member fabricated with predetermined radial and axial clearances relative to the first impeller to permit passing a flushing fluid through the clearances to enable cleaning the blender in place.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US90136686A | 1986-08-28 | 1986-08-28 | |
| US901,366 | 1986-08-28 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1281027C true CA1281027C (en) | 1991-03-05 |
Family
ID=25414033
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000545495A Expired - Lifetime CA1281027C (en) | 1986-08-28 | 1987-08-27 | Two stage blender |
Country Status (8)
| Country | Link |
|---|---|
| EP (1) | EP0261797B1 (en) |
| JP (1) | JPS63100922A (en) |
| KR (1) | KR880002567A (en) |
| BR (1) | BR8704357A (en) |
| CA (1) | CA1281027C (en) |
| DE (1) | DE3778270D1 (en) |
| ES (1) | ES2030730T3 (en) |
| MX (1) | MX165959B (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE29819508U1 (en) * | 1998-11-02 | 1999-01-14 | VMA-GETZMANN GmbH, 51580 Reichshof | Dispersing device |
| CN100563805C (en) * | 2003-10-16 | 2009-12-02 | 巴塞尔聚烯烃意大利有限责任公司 | The method of continuous production emulsion |
| KR100770166B1 (en) | 2006-11-30 | 2007-10-26 | 지에스칼텍스 주식회사 | Apparatus for manufacturing source particles of separator for fuel cell and method of manufacturing source particles of separator for fuel cell by using the same |
| KR100856702B1 (en) * | 2007-07-30 | 2008-09-04 | 주식회사 피엠씨코리아 | A stirring room and a mixing water tank for rapid mixing |
| US20140262338A1 (en) * | 2013-03-15 | 2014-09-18 | Schlumberger Technology Corporation | Blender system with multiple stage pumps |
| KR101528284B1 (en) * | 2013-12-23 | 2015-06-12 | 주식회사 포스코 | Powder supply system and method thereof |
| CN112023785B (en) * | 2020-08-31 | 2022-07-01 | 广西金天地改性沥青有限公司 | Asphalt heating device |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3606270A (en) * | 1970-05-14 | 1971-09-20 | Ludish Co | Continuous power blender |
| DE2139497C3 (en) * | 1971-08-06 | 1975-02-13 | Franz Morat Gmbh, Kaiseraugst (Schweiz) | Emulsifying and dispersing device |
| GB1451533A (en) * | 1974-01-29 | 1976-10-06 | Schold G R | Apparatus for dispersing a liquid solid particles contained in aglomerated form in the liquid |
| JPS61268344A (en) * | 1985-01-22 | 1986-11-27 | Funken:Kk | Method and apparatus for continuous kneading of powder such as fine powdery coal of oil coke in order to prepare slurry |
-
1987
- 1987-08-21 ES ES198787307436T patent/ES2030730T3/en not_active Expired - Lifetime
- 1987-08-21 DE DE8787307436T patent/DE3778270D1/en not_active Expired - Lifetime
- 1987-08-21 EP EP87307436A patent/EP0261797B1/en not_active Expired - Lifetime
- 1987-08-24 MX MX789087A patent/MX165959B/en unknown
- 1987-08-25 BR BR8704357A patent/BR8704357A/en not_active IP Right Cessation
- 1987-08-27 CA CA000545495A patent/CA1281027C/en not_active Expired - Lifetime
- 1987-08-27 KR KR870009380A patent/KR880002567A/en not_active Application Discontinuation
- 1987-08-28 JP JP62214970A patent/JPS63100922A/en active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| EP0261797A1 (en) | 1988-03-30 |
| BR8704357A (en) | 1988-04-19 |
| MX165959B (en) | 1992-12-11 |
| EP0261797B1 (en) | 1992-04-15 |
| DE3778270D1 (en) | 1992-05-21 |
| JPS63100922A (en) | 1988-05-06 |
| ES2030730T3 (en) | 1992-11-16 |
| KR880002567A (en) | 1988-05-09 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MKLA | Lapsed |