The present invention relates to liquid dispensing systems for dispensing two or more liquids into a container at high filling speeds to improve homogeneous mixing of such liquids.
Liquid dispensing systems for simultaneously dispensing two or more liquids (e.g., a concentrate and a diluent) into a container are well known. Such liquid dispensing systems typically comprise so-called co-injection nozzles for concurrently but separately dispensing two or more liquids at high filling speeds.
When the liquids to be dispensed are significantly different in composition, viscosity, solubility, and/or miscibility, it is difficult to ensure homogeneous mixing of such liquids in the container. Further, it is inevitable that when dispensed into the container at relatively high filling speed, the liquids tend to splash, and one or more of the liquids may form hard-to-remove residues on the container wall, which may further exacerbate the issue of in-homogenous mixing. Still further, most of the co-injection nozzles commercially available today are not suitable for high-speed liquid filling, because they contain various moving parts (e.g., O-rings, seal gaskets, bolts, screws, etc.) that may become loose under high pressure, and they also may create dead spaces where liquids can be trapped, which may pose challenges for cleaning and result in poor sanitization. Further, when the liquids are dispensed at high filling speeds, it is difficult to ensure precision dosing of such liquids and 100% shut-off of the liquid flow when the dosing is completed.
Therefore, there is a need for liquid dispensing systems with co-injection nozzles that can accommodate high speed liquid filling, with improved homogeneity in the mixing results and reduced formation of residues on the container wall. There is also a need for liquid dispensing systems with improved precision dosing and complete shut-off.
The present invention meets the above-mentioned needs by providing a liquid dispensing system for dispensing two or more liquids into a container, comprising:
Preferably, the first liquid source is controlled by a servo-driven pump, more preferably a servo-driven positive displacement pump, most preferably a servo-driven rotary positive displacement pump.
Preferably, the second liquid source is controlled by a servo-driven pump, more preferably a servo-driven piston pump, most preferably a servo-driven piston pump with a rotary valve.
These and other aspects of the present invention will become more apparent upon reading the following detailed description of the invention.
Features and benefits of the various embodiments of the present invention will become apparent from the following description, which includes examples of specific embodiments intended to give a broad representation of the invention. Various modifications will be apparent to those skilled in the art from this description and from practice of the invention. The scope of the present invention is not intended to be limited to the particular forms disclosed and the invention covers all modifications, equivalents, and alternatives falling within the spirit and scope of the invention as defined by the claims.
As used herein, articles such as “a” and “an” when used in a claim, are understood to mean one or more of what is claimed or described. The terms “comprise,” “comprises,” “comprising,” “contain,” “contains,” “containing,” “include,” “includes” and “including” are all meant to be non-limiting.
As used herein, the terms “substantially free of” or “substantially free from” means that the indicated space is present in the volume of from 0% to about 1%, preferably from 0% to about 0.5%, more preferably from 0% to about 0.1%, by total volume of the unitary dispensing nozzle.
The unitary dispensing nozzle used in the present invention is made as an integral piece, without any moving parts (e.g., O-rings, sealing gaskets, bolts or screws). Such an integral structure renders it particularly suitable for high speed filling of viscous liquid, which typically requires high filling pressure. Such a unitary dispensing nozzle can be made by any suitable material with sufficient tensile strength, such as stainless steel, ceramic, polymer, and the like.
Preferably, the unitary dispensing nozzle of the present invention is made of stainless steel.
The unitary dispensing nozzle of the present invention may have an average height ranging from about 3 mm to about 200 mm, preferably from about 10 to about 100 mm, more preferably from about 15 mm to about 50 mm. It may have an average cross-sectional diameter ranging from about 5 mm to about 100 mm, preferably from about 10mm to about 50mm, more preferably from about 15 mm to about 25 mm.
Such dispensing nozzle provides two or more fluid passages for simultaneously or substantially simultaneously dispensing two or more liquids of different composition, viscosity, solubility, and/or miscibility into a container. For example, one of the liquids can be a minor liquid feed composition, and the other can be a major liquid feed composition (i.e., the liquid making up the majority weight of the final liquid mixture). The container has an opening into which the two or more liquids are dispensed, while the total volume of the container may range from about 10 ml to about 10 L, preferably from about 20 ml to about 5 L, more preferably from about 50 ml to about 4 L.
The nozzle 10 contains a plurality of first flow passages 11 for flowing a first fluid (e.g., a major liquid feed composition) therethrough. Each of the first flow passages 11 is defined by a first inlet 11A located at the first end 12 and a first outlet 11B located at the second end 14, as shown in
The first and second outlets 11B and 13B can have any suitable shapes, e.g., circular, semicircular, oval, square, rectangular, crescent, and combinations thereof. Preferably but not necessarily, both the first and second outlets 11B and 13B are circular, as shown in
The plurality of major feed flows can be configurated to form a diverging “liquid shroud” around the minor feed flow. Alternatively, the plurality of major feed flows may be substantially parallel to each other, thereby forming a parallel “liquid shroud” around the minor feed flow. Such a parallel arrangement of the major feed flows is particularly preferred in the present invention because it provides a greater local turbulence around the minor feed flow inside the container and enables a better, more homogenous mixing result.
Still further, the nozzle 10 is substantially free of any dead space (i.e., spaces that are not directly in the flow passages and therefore can trap liquid residues). Therefore, it is easy to clean and is less likely to cause cross-contamination when switching between different liquid feeds.
Preferably, but not necessarily, the ratio of the total cross-sectional area of the first outlets 11B over the total cross-sectional area of the second outlet 13B may range from about 5:1 to about 50:1, preferably from about 10:1 to about 40:1, and more preferably from about 15:1 to about 35:1. Such ratio ensures a significantly large major-to-minor flow rate ratio, which in turn enables more efficient dilution of the minor ingredient in the container, ensuring that there is no ‘hot spots’ of localized high concentrations of minor ingredient in the container.
The nozzle 20 contains a plurality of first flow passages 21 for flowing a first fluid (e.g., a major liquid feed composition) therethrough. Each of the first flow passages 21 is defined by a first inlet 21A located at the first end 22 and a first outlet 21B located at the second end 24, as shown in
All of the first outlets 21B have a crescent shape, while such crescents are arranged in a concentric manner with substantially the same radius center. In contrast, the second outlet 23B is circular in shape. Further, the second outlet 23B is located at the radius center of the first outlets 21B and is substantially surrounded by the plurality of first outlets 21B, as shown in
The nozzle 20 is also substantially free of any dead space and is therefore easy to clean with a reduced risk of cross-contamination when changing liquid feeds.
Preferably, but not necessarily, the ratio of the total cross-sectional area of the first outlets 21B over the total cross-sectional area of the second outlet 23B may range from about 5:1 to about 50:1, preferably from about 10:1 to about 40:1, and more preferably from about 15:1 to about 35:1.
Both the first and second ends 32 and 34 have relatively planar surfaces. A cylindrical sidewall 36 is located between the first and second ends 32 and 34.
The nozzle 30 contains a plurality of first flow passages 31 for flowing a first fluid (e.g., a major liquid feed composition) therethrough. Each of the first flow passages 31 is defined by a first inlet 31A located at the first end 32 and a first outlet 31B located at the second end 34, as shown in
All of the first outlets 31B have a crescent shape, while such crescents are arranged in a concentric manner with substantially the same radius center. In contrast, the second outlet 33B and the third outlet 35B are circular in shape. Further, the second outlet 33B is located at the radius center of the first outlets 31B, while the third outlet 35B is located adjacent to the radius center of the first outlets 31B. In this manner, both the second and third outlets 33B and 35B are substantially surrounded by the plurality of first outlets 31B, as shown in
The nozzle 30 is also substantially free of any dead space and is therefore easy to clean with a reduced risk of cross-contamination when changing liquid feeds. Preferably, but not necessarily, the ratio of the total cross-sectional area of the first outlets 31B over the total cross-sectional area of the second outlet 33B may range from about 5:1 to about 50:1, preferably from about 10:1 to about 40:1, and more preferably from about 15:1 to about 35:1. Similarly, the ratio of the total cross-sectional area of the first outlets 31B over the total cross-sectional area of the third outlet 35B may range from about 5:1 to about 50:1, preferably from about 10:1 to about 40:1, and more preferably from about 15:1 to about 35:1.
Cherry-Burrell (Wisconsin, USA). The first fluid supplied by the first liquid source 41 may flow through a flowmeter 412, which measures the mass or volumetric flow rate of the first fluid to further ensure precision dosing thereof.
The first valve assembly 47 located at or near the first end of the unitary dispensing nozzle 45 is preferably actuated by a first remotely mounted pneumatic solenoid 420, which in turn is in fluid communication with a pressurized air supply 42. Pressurized air is passed from the air supply 42 through the pneumatic solenoid 420 into said first valve assembly 47 to open and close the one or more first flow passages 452, thereby controlling the flow of the first liquid through the unitary dispensing nozzle 45.
The second fluid supplied by the second fluid source 43 to the unitary dispensing nozzle 45 is preferably a minor liquid feed composition, and more preferably a liquid with significantly higher viscosity than the major liquid feed composition, which can be filled at an average flow rate ranging from 0.1 ml/second to about 1000 ml/second, preferably from about 0.5 ml/second to about 800 ml/second, more preferably from about 1 ml/second to about 500 ml/second.
The second liquid source 43 preferably comprises a pressurized header (not shown) for supplying the second liquid at an elevated pressure (i.e., higher than atmospheric pressure). The second liquid supply 43 is preferably controlled by a servo-driven pump 430, which is preferably a servo-driven piston pump, more preferably a servo-driven piston pump with a rotary valve. Most preferred servo-driven pump for controlling the second liquid supply 43 is the Hibar 4S series precision rotatory dispensing pump commercially available from Hibar Systems Limited (Ontario, Canada), which comprises a ceramic 3-way rotary valve that is particularly suitable for handling high viscosity liquids. The servo-driven piston pump 430 is preferably actuated by a second remotely mounted pneumatic solenoid 440, which passes pressurized air from an air source 44 into the rotary valve of the pump 430 to rotate said valve between a dosing mode and a dispensing mode. In said dosing mode, a predetermined amount of said second liquid is dosed by said second liquid source 43 into said servo-driven piston pump 430; and in said dispensing mode, said predetermined amount of the second liquid is dispensed by said servo-driven piston pump 430 to said unitary dispensing nozzle 45.
The second valve assembly 49 located at or near at lease one of the sidewalls of the unitary dispensing nozzle 45 preferably comprises an air-operated valve for opening and closing said one or more second flow passages 454 of the unitary dispensing nozzle 45. The air-operated valve is preferably a pinch valve that opens by flexing an internal membrane (not shown) to allow fluid to flow through, and it is particularly suitable for isolating the fluid from any internal valve parts and ensuring 100% shut-off. Preferably, the air-operated valve is actuated by a remotely mounted pneumatic solenoid. More preferably, the air-operated valve is actuated also by the second remotely mounted pneumatic solenoid 440.
The first valve assembly 57 located at or near the first end of the unitary dispensing nozzle 55 preferably comprises an air cylinder 571 with an internal piston 572 that divides such air cylinder 571 into an upper chamber 571A and a lower chamber 571B, a spring 573, and a fluid plunger 575. The internal piston 572 is capable of moving up and down along the air cylinder 571 when pressurized air is passed into the lower or upper chamber 571A or 571B of said air cylinder 571. The fluid plunger 575 is connected with and actuated by said internal piston 572 and said spring 573. Typically, the fluid plunger 575 is being pushed down by the spring to seat immediately above the one or more first flow passages 552. When the fluid plunger 575 is in this position, it blocks off the one or more first flow passages 552, thereby preventing the low viscosity major feed liquid from flowing through said one or more first flow passages 552.
To open the one or more first flow passages 552, a first remotely mounted pneumatic solenoid (not shown) is triggered to pass pressurized air from an air supply (not shown) into the bottom chamber 571B of the air cylinder 571 to pressurize said bottom chamber 571B. When this occurs, the internal piston 572 raises up along the air cylinder 571. Because the internal piston 572 is directly coupled to the fluid plunger 575, the upward motion of the internal piston 572 moves the fluid plunger 575 up against the closing force of the spring 573. When the fluid plunger 575 is moved up and away from the one or more first flow passages 552 (as shown in
The second valve assembly 59 located at or near a side wall of the unitary dispensing nozzle 55 preferably comprises an air-operated pinch valve 591 having an internal membrane 592. When the pinch valve 591 is filled with pressurized air, the internal membrane 592 closes and cuts off flow of the high viscosity minor feed liquid into the one or more second flow passages 554. When the pressurized air is let out of the pinch valve 591, the internal member 592 flexes to open under the force of the liquid flow, thereby allowing the high viscosity minor feed liquid to flow therethrough into the one or more second flow passages 554. Preferably, flow of pressurized air in and out of the pinch valve 591 is controlled by a remotely mounted pneumatic solenoid.
The dimensions and values disclosed herein are not to be understood as being strictly limited to the exact numerical values recited. Instead, unless otherwise specified, each such dimension is intended to mean both the recited value and a functionally equivalent range surrounding that value. For example, a dimension disclosed as “40 mm” is intended to mean “about 40 mm.”
Every document cited herein, including any cross referenced or related patent or application and any patent application or patent to which this application claims priority or benefit thereof, is hereby incorporated herein by reference in its entirety unless expressly excluded or otherwise limited. The citation of any document is not an admission that it is prior art with respect to any invention disclosed or claimed herein or that it alone, or in any combination with any other reference or references, teaches, suggests or discloses any such invention. Further, to the extent that any meaning or definition of a term in this document conflicts with any meaning or definition of the same term in a document incorporated by reference, the meaning or definition assigned to that term in this document shall govern.
While particular embodiments of the present invention have been illustrated and described, it would be obvious to those skilled in the art that various other changes and modifications can be made without departing from the spirit and scope of the invention. It is therefore intended to cover in the appended claims all such changes and modifications that are within the scope of this invention.
Number | Date | Country | Kind |
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PCT/CN2019/125654 | Dec 2019 | WO | international |
Number | Date | Country | |
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20210187527 A1 | Jun 2021 | US |