The present invention relates to liquid dispensing systems, and more particularly, to liquid dispensing systems having nozzles for dispensing small controlled quantities of highly viscous liquids.
In many industries there is a need for dispensing small, controlled quantities of highly viscous liquids. In the food industry, by way of example, in the commercial production of pizzas, it is required to dispense droplet sized quantities of sauces onto the pizza dough. Because of the thick nature of the sauce, it is difficult to rapidly dispense closely controlled droplets as desired. Moreover, while it is desirable to dispense relatively small liquid droplets of such sauces and other highly viscous liquids, heretofore it has been difficult to dispense such small droplets on a rapid and repeatable basis. If the sauce contains solids that can clog the nozzle passages, the flow passages must be sized larger making it even more difficult to control the dispensing of small droplets and often resulting in undesirable splattering of discharging sauce. Furthermore, when the dispensing device uses an air operated liquid control piston, rapid operation of the piston is limited by the compressibility of the controlling air. Additionally, when air operated devices are spring returned, the springs return force can be limited up to roughly half of the air pressure's force used to open the device, which resists rapid piston closure.
It is an object of the invention to provide a liquid dispensing system having spray nozzles effective for reliably dispensing precisely controlled small droplet sized quantities of highly viscous liquids.
Another object is to provide a liquid dispensing system as characterized above that is effective for rapidly depositing precisely controlled pixel sized droplets without undesirable splattering of the liquid.
A further object is to provide a liquid dispensing system of the above kind in which the spray nozzles are operable with larger inlet passages less susceptible to clogging from the solids content in the liquid.
Yet another object is to provide such a liquid dispensing system which can be selectively operated for dispensing different sized precisely controlled small droplets.
Another object is to provide such a liquid dispensing system that can be operated more rapidly.
A further object is to provide a liquid dispensing system of such type that have air actuated pistons with return springs the function of which is less resistant to air pressures used in operating the system.
Still another object is to provide a liquid dispensing system of the foregoing type that is relatively simple in design and lends itself to economical manufacture and efficient usage.
Other objects and advantages of the invention will become apparent upon reading the following detailed description and upon reference to the drawings.
While the invention is susceptible of various modifications and alternative constructions, certain illustrative embodiments thereof have been shown in the drawings and will be described below in detail. It should be understood, however, that there is no intention to limit the invention to the specific forms disclosed, but on the contrary, the intention is to cover all modifications, alternative constructions, and equivalents falling within the spirit and scope of the invention.
Referring now more particularly to
Each illustrated module 12 has a respective spray nozzle 30 mounted in depending relation to an underside of the module nozzle support body 20 having an upstream liquid inlet 31 in an upper side communicating with the liquid supply passage 22. For controlling liquid from the common liquid supply passage 22 to the spray nozzle inlet 31 of the module 12, a piston 32 is supported in each module body 20 above the spray nozzle inlet 31 for reciprocating movement between a raised inlet open position and a lowered inlet closed position.
Each piston 32 in this case is supported for selective relative movement in a carrier 33 mounted in sealed relation within a vertical opening 34 of the respective module body 20 with a downstream end of the piston 32 extending through the liquid supply passage 22 for engagement with the spray nozzle inlet 31. For biasing the piston 32 in a lowered position closing the spray nozzle inlet 31, a return spring 35 is disposed within a spring chamber 36 of the module body 20 in interposed relation between a head 32a of the piston 32 and a retention sleeve 37 secured within an upper end of the body opening 34 and retained by a retention cap 38 threadedly engaged within an upper end of the body opening 34. The retention sleeve 37 in this case extends downwardly about the return spring 35 and the piston head 32a, as best depicted in
Pursuant to an important feature of this embodiment, each module body has a pressurized air passage system controlled by a respective valve such that pressurized air that moves the piston to an open position also augments rapid movement of the piston to closure. In the illustrated embodiment, operation of the piston 32 of each module 12 between open and closed positions is controlled by a respective solenoid valve 43, as best depicted in
When the solenoid valve 43 in this case is in its natural or non-energized state, inlet pressure at solenoid valve port air inlet 55a is blocked by a mechanism 43a in this case in the form of a stem, of the solenoid valve 43 (
When the solenoid valve 43 is energized, the solenoid shifts actuating mechanism 43a to close exhaust port 55b removing the connection of port 55c to atmosphere and connecting solenoid valve ports 55a, 55c. Pressurized air at the air supply port 50 of module body 20 then communicates with pressure chamber 42 via passages 63, 63a in the module body 20 and solenoid mounting block 44, solenoid valve ports 55a, 55c and passages 62a, 62 causing the piston 32 to stroke upwardly, opening the nozzle inlet 31 and compressing the return spring 35. The upward stroke of the piston head 32a imparts a positive air displacement within the spring chamber 36 resulting in a slight pressure increase. The pressure increase in the spring cavity 36 drains through holes 41 in the spring retention sleeve 37, annular passage 40, outlet passage 60, and air outlet port 52 to atmosphere pressure (
When un-energized, the solenoid valve 43 shifts back to the natural state. Inlet air pressure at solenoid port 55a is again blocked preventing pressurized air from entering the device. Rapid decompression of the pressurized air in piston chamber 42 causes a migration of elevated pressure within passages 62, 62a in the module body 20 and solenoid mounting block 44, ports 55c and 55b of solenoid valve 43, outlet passage 61a and 61 in the solenoid mounting block 44 and module body 20, spring chamber 36, outlet passage 60, and outlet port 52 as the system pressure in piston chamber 42 is released and equalizes with the atmosphere. Migrating pressure in the annular passage 40 communicates through holes 41 in spring retention sleeve 37 causing elevated pressure within spring chamber 36 and acting on the surface area of piston head 32a within the spring chamber 36 resulting in a momentary downward force supplementing the constant downward force from return spring 35 opposing the decompressing pressure in the piston chamber 42, returning piston 32 to its natural state, closing passage 31 and stopping liquid flow through spray nozzle 30, from common liquid supply passage 22. An appreciable decrease in time required to return the piston 32 to its natural state is attributed to the momentary increase in pressure within the spring chamber 36. All passages and cavities downstream of solenoid valve 43 including spring chamber 36 intrinsically return to atmospheric pressure through an outlet port 52 effectively removing the supplemental force the transient pressure applied to piston head 32a.
Further operation of the liquid dispensing module 12 by again energizing solenoid 43 is unaffected by the previous cycles increased pressure in the spring chamber 36 as the increased pressure is transient and quickly returns to atmosphere pressure allowing the increased pressure to have the desired effect on piston's 32 opening stroke without effecting the piston's 32 closing stroke. As it will become apparent, the solenoid valve 43 can be cycled at predetermined rates for the particular dispensing operation with the piston's 32 variable open time providing a varying pixel volume.
In accordance with a further aspect of this embodiment, each spray nozzle module 12 is operative for dispensing controlled small round pixel sized droplets of highly viscous liquid as an incident to cycling of the piston 32 even when the liquid has an appreciable solids content. Each spray nozzle 30 with particular reference to
The cylindrical mounting flange 78 of the core 72 has a concavely configured (relative to the direction of fluid flow) downstream end wall 80 formed with a plurality of circumferentially spaced axially oriented liquid orifices 81. These liquid orifices that communicate between an expansion cavity 82 of the nozzle seat 71 and an annularly configured liquid discharge passage defined between the nozzle core 72 and the nozzle body 70 for directing liquid in a controlled fashion for optimum dispensing in small droplet form as will become apparent. It will be understood that while the illustrated nozzle 30 comprises a multi-part assembly, alternatively, it could have a one-piece construction or fewer or greater assembled parts.
In carrying out this aspect of the present embodiment, the nozzle core 72 has a teardrop shaped pintle 83 which together with the internal circumferential surface of the surrounding nozzle body 70 defines an expanding discharge passage 85 that reduces exit velocity of the dispensed liquid for maintaining a desired flow rate and consistent droplet size of the highly viscous discharging liquid. To that end, the illustrated pintle 83 (see
In operation, with continued reference to
More specifically, the circumferential orifices 81 at the downstream end of the expansion cavity 82 communicate with an inlet section 92 of the discharge passage 85 that is defined between the outwardly directed wall section 91 of the nozzle body 70 and the pintle 83 of the nozzle core 72. The cross-sectional area of the annular inlet section 92 may increase as the section extends in the downstream direction such that the velocity of the fluid in this region continues to be reduced as the cross-sectional area of the discharge passage expands. A slight reduction in the cross-sectional area of the discharge passage 85 in a subsequent stabilizing section 93 of the discharge passage 85 (again defined by the outer surface of the pintle 83 and the inner circumferential surface of the nozzle body 70) immediately downstream of the inlet section 92 can provide a slight increase in pressure. This increase in pressure stabilizes and balances the flow removing individual jet streams caused by the fluid entering the inlet section 92 of the discharge passage 85 through the series of orifices 81 and allows uniform flow along the internal wall surface of the nozzle body 70. The cross-sectional area of the stabilizing section 93 remains constant through this region as the fluid gains stability.
Downstream of the stabilizing section 93, the liquid enters a final expansion section 95 defined by the inwardly tapered terminal end section 90 of the nozzle core 72 that extends downstream to a nozzle mouth 94 defined at the downstream end of the nozzle body 70. The progressively increasing cross-sectional area of the final expansion section 95 is achieved through the reducing conical diameter of the pintle 83 in the terminal end section 90 while the inner circumferential surface of the nozzle body 70 is maintained at a consistent diameter. The pintle 83 helps stabilize the fluid and enables greater expansion of the liquid than could be achieved with nozzle core having a simple uniform diameter. Sustained contact of the liquid with inner and outer wall surfaces of the discharge passage is a function of the surface tension of the liquid.
The cross-sectional area of the final expansion section 95 at the nozzle mouth 94 defines the exit velocity of the liquid, which is inversely proportional to the cross-sectional area at the nozzle mouth in relation to the area of nozzle inlet 31. The terminal end section 90 of the nozzle core 72 preferably extends slightly beyond the nozzle mouth 94 to assist in breaking the surface tension of the liquid with the inner circumferential surface of the nozzle body 70 without impacting the outer diameter of the discharging liquid stream. Having the inner circumferential surface of the nozzle body 70 at a constant diameter helps establish a consistent diameter of the boundary layer of the liquid when it exits the nozzle, which assists in maintaining the desired droplet diameter independent of the distance of the nozzle from the target.
It has been found that a dramatic reduction in the velocity of the liquid can be achieved through progressively increasing the cross-sectional area of the discharge passage 85. The inward expansion of the discharge passage 85 is achieved by progressively reducing the diameter of the pintle 83 while maintaining the inner circumferential surface of the nozzle body 70. This helps produce discharging liquid with a consistent stream diameter. The reduced velocity of the liquid allows it to be dispensed without splattering. This further allows the utilization of larger nozzle inlet orifices 31 for enabling the dispensing of liquids with larger solids content. Once the discharge passage of the nozzle is initially filled with viscous fluid, the surface tension of the liquid will keep the nozzle 30 charged with liquid ready to be dispensed upon opening of the nozzle inlet 31. Because the liquid can be substantially incompressible, an exact relationship can be maintained between the liquid volume entering the nozzle 30 through the inlet 31 and the liquid exiting the nozzle mouth 94. Cycling the piston 32 to open and close the inlet orifice 31 at a rapid rate, such as 50 milliseconds, has been found to produce small, consistent droplets of liquid that are discharged at a reduced exit velocity. This allows the discharging droplets to be deposited on a target, such as a target about 2 inches from the nozzle, without splattering.
With reference to
In this embodiment, the nozzle seat 102 again is secured within an upstream end 74 of the nozzle body 101 and defines a liquid inlet 31, and the nozzle core 104 has an upstream cylindrical mounting flange 78 positioned within the nozzle body 101 retained in place by the nozzle seat 102. The upstream cylindrical mounting flange 78 of the nozzle core 104 again has a concave configured upstream end wall 80 formed with a plurality of circumferentially spaced axially oriented liquid orifices 81. The orifices 81 communicate between an expansion cavity 82 within the nozzle seat 102 between the nozzle seat liquid inlet 31 and the nozzle core 104 and an annular passage 92 defined between an internal cylindrical wall section 106 of the nozzle body 101 and a pintle 83 of the nozzle core 104. The outer radial sides of the mounting flange liquid orifices 81 in this case are aligned with the nozzle body internal cylindrical wall section 106.
The pintle 83 of the nozzle core 104 again has a tear dropped shape, which together with the internal cylindrical wall section 106 of the nozzle body 101 defines an annular flow passage 85 that reduces velocity of dispensed liquid as it travels through the nozzle body 101. As in the previous embodiment, the illustrated pintle 83 has a relatively small diameter upstream end section 86 extending centrally from the mounting flange 78, a radially outwardly extending curved section 87 adjacent the upstream end, and an inwardly tapered relatively long conical end section 90 that together with the internal cylindrical nozzle wall section 106 of the nozzle body 101 defines an expansion section 95 of the annular flow passage 85. The geometry of the pintle 83 again defines the inner diametric wall of the annular flow passage 85 while providing a structure against which a vacuum due to the flow expansion can be formed. The deceleration of the liquid within the expansion section 95 of the annular flow passage 85 again is a function of the surface tension and the capillary forces ability to draw a vacuum and resist flow.
In accordance with that important feature of this embodiment, the spray nozzle 100 is designed for accelerating highly viscous liquids upon discharge from the spray nozzle sufficient for facilitating the rapid discharge of even smaller sized, discreetly controlled droplets of the liquid. To this end, the expanding annular flow passage 85 between the nozzle body cylindrical wall section 106 and the pintle 83 communicates with a reduced diameter discharge orifice 110 of the spray nozzle sized for accelerating the liquid sufficient for enabling the repeated discharge of discreet small sized liquid droplets. In the illustrated embodiment, the nozzle body 101 has an inwardly tapered downstream section 111 that defines the discharge orifice 110 smaller in diameter than the cylindrical wall section 106. It will be understood that alternatively a separate spray tip may be mounted at a downstream end of the cylindrical wall section 106 of the nozzle body 101 for defining the discharge orifice 110. A downstream end of the conical pintle section 90 in this case again extends a short distance beyond the discharge orifice 110 of the spray nozzle for defining an annular discharge passage 113 between the nozzle body discharge orifice 110 and the pintle conical section 90.
While the expanding annular flow passage 85 reduces the liquid flow through the spray nozzle 100, the smaller diameter discharge orifice 110 and resulting smaller diameter annular discharge passage 113 unexpectedly has been found to accelerate the liquid discharge sufficient for enhancing the discreet separation of small droplets during cyclic operation of the spray nozzle 100. While the expanding annular flow passage 85 reduces velocity of the fluid flow through the spray nozzle 100 as in the previous embodiment, the reduced diameter discharge orifice 110 and resulting smaller sized annular flow passage 113 creates a sharp transition between the expanding annular flow passage 85 and atmosphere beyond the spray nozzle 100 that inherently imparts separation between fluid held captive in the nozzle body 101 and the inertia of discharging fluid from the spray nozzle that effects the reliable discharge of small discreet droplets.
The relation between the area of the inlet passage 31 and the annular discharge passage 113 may be controlled based upon the viscosity of the liquid being dispensed for imparting reliable separation of droplets without excessive acceleration that causes undesirable splattering of the liquid. In one embodiment, particularly applicable for dispensing pizza sauces, the ratio of the area of the annular passage 113 that effects accelerated velocity to the area of the inlet 31 of the spray nozzle is 5 to 1. As such, the fluid velocity at discharge will be reduced to ⅕th or 20% of the liquid velocity at the inlet 31. In such case, accelerated discharge of the viscous liquid at the discharge orifice 110 will enhance reliable separation of the discharging droplets without excessive speed that creates splattering of the dispensed droplets. In one embodiment, the nozzle body discharge orifice may be 0.285 inches in diameter, while other embodiments may have different sized discharge orifices depending upon the relation between the areas of the resulting annular flow passage 113 and the liquid inlet 31 and the viscosity of the particular liquid being dispensed.
In operation it will be seen that once the free passage within the spray nozzle 100 is initially filled with viscous liquid, the fluid surface tension will keep the nozzle charged with fluid ready for dispensing from the discharge passage 113. The incompressibility of the fluid maintains an exact relationship between the fluid entering the spray nozzle through the inlet 31 and fluid exiting the annular discharge passage 113. Cycling a poppit or control piston rapidly to open and close the inlet 31 develops small, consistent slugs of fluid at a velocity that enhances droplets separation without splattering of the dispensed liquid.
Hence, the subject spray nozzle 100 has been able to achieve the discharge of smaller and more consistent volumes of vicious liquids. The tension generated by the fluids transition between the low internal velocity within the expansion section 95 and the increased velocity as an incident to discharge from the smaller sized discharge orifice 110 and annular flow passage 113 unexpectedly has been found to provide a more consistent and repeatable break in the discharging fluid stream. While the 5 to 1 area ratio between the annular discharge passage 113 and the liquid inlet 31 has been found to work best for fluids having viscosity typical of pizza sauces, it will be understood that the ratio can be easily adjusted to accommodate different liquids. It will be understood that the optimum volume ratio between the annular passage 113 and a liquid inlet 31 is a balance between the desired consistent, repeatable breaks in the fluid upon discharge and undesirable splattering due to excessive velocity, which can be adjusted for the particular fluid being dispensed.
This present application is a continuation in part of U.S. patent application Ser. No. 17/470,771 filed Sep. 9, 2021, which claims the benefit of U.S. Provisional Patent Application No. 62/076,001, filed on Sep. 9, 2020, and which are incorporated by reference.
Number | Date | Country | |
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63076001 | Sep 2020 | US |
Number | Date | Country | |
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Parent | 17470771 | Sep 2021 | US |
Child | 18110569 | US |