Hose-end chemical delivery system

Abstract

A chemical delivery system having a body defining a main fluid flow passage through which a fluid passes and a storage tank for holding a chemical. An inlet nozzle delivers a quantity of the fluid in the main fluid flow passage to the storage tank to be mixed with the chemical and an outlet nozzle returns a quantity of the mixed fluid to the main fluid flow passage.

Description

BACKGROUND OF THE INVENTION

This invention relates generally to chemical delivery systems and, more particularly, to a hose-end chemical delivery system.

Hose-end chemical delivery systems for spraying chemicals such as insecticides, herbicides, and fertilizers are known in the art. For example, U.S. Pat. No. 4,475,689 describes a variable dilution ratio hose-end sprayer having a rotatable selector dial. Formed in the rotatable selector dial is a plurality of orifices. The orifices are adapted to intersect an output fluid passageway that extends from a fluid container to a mixing chamber. The mixing chamber is provided for mixing selected amounts of fluid from the fluid container with water that enters the mixing chamber from the hose to which the delivery system is attached. The diameter of each orifice of the rotatable selector dial is proportioned to provide a desired final dilution ratio of the fluid to be siphoned from the fluid container. The orifices extend through the selector dial and lie on a circle concentric with the axis of the selector dial. The orifices also have a radius selected to intersect the axis of the output fluid passageway.

SUMMARY OF THE INVENTION

An improved chemical delivery system is described having a body defining a main fluid flow passage through which a fluid passes and a storage tank for holding a chemical. An inlet nozzle delivers a quantity of the fluid in the main fluid flow passage to the storage tank to be mixed with the chemical and an outlet nozzle is used to return a quantity of the fluid mixed with the chemical from the storage tank to the main fluid flow passage. An adjustment dial having a plurality of orifices of varying diameter that are capable of being individually placed into relation with the inlet nozzle may be used to control the amount of fluid that enters the inlet nozzle from the main fluid flow passage. Furthermore, an outlet nozzle trap in fluid communication with a vent port of the outlet nozzle may be placed in fluid communication with a fill control port of the inlet nozzle. The fill control port is used to direct fluid to the outlet nozzle trap to control venting of air from the storage tank to the main fluid flow passage via the vent port.

A better understanding of the objects, advantages, features, properties and relationships of the invention will be obtained from the following detailed description and accompanying drawings which set forth illustrative embodiments and which are indicative of the various ways in which the principles of the invention may be employed.

BRIEF DESCRIPTION OF THE DRAWINGS

For a better understanding of the invention, reference may be had to preferred embodiments shown in the attached drawings in which:

FIG. 1 illustrates a cross-sectional view of an exemplary hose-end chemical delivery system constructed in accordance with the principles of the subject invention;

FIG. 2 illustrates a top view of an exemplary cap of the hose-end chemical delivery system of FIG. 1 ;

FIG. 3 illustrates a top view of an exemplary selector dial of the hose-end chemical delivery system of FIG. 1 ;

FIG. 4 illustrates a cross-sectional view of an exemplary inlet nozzle of the hose-end chemical delivery system of FIG. 1 ;

FIG. 5 illustrates a cross-sectional view of an exemplary outlet nozzle of the hose-end chemical delivery system of FIG. 1 ;

FIG. 6 illustrates a side view of an exemplary output dip tube screen of the hose-end chemical delivery system of FIG. 1 ;

FIG. 7 illustrates a top view of the dip tube screen of FIG. 6 ; and

FIG. 8 illustrates a cross-sectional view of a further exemplary hose-end chemical delivery system constructed in accordance with the principles of the subject invention.

DETAILED DESCRIPTION

Turning now to the figures, wherein like reference numerals refer to like elements, there is illustrated in FIGS. 1 and 8 an exemplary hose-end chemical delivery system 50 comprising a cap 26 and a storage tank 24 . As will be appreciated, the storage tank 24 is adapted to contain a chemical to be sprayed, for example, a water soluble fertilizer. To sealingly secure the storage tank 24 to the cap 26 , the exterior of the storage tank 24 may be provided with threads 58 adapted to mate with threads 56 formed on the interior of the cap 26 . Additional means for securing the storage tank 24 to the cap 26 , such as providing a snap-fit connection, are also contemplated.

As illustrated, the chemical delivery system 50 is adapted to be connected to a source of fluid, such as water. To this end, the cap 26 may be provided with a threaded, female connector 3 that is adapted to mate with a threaded, male connector of a conventional garden hose. Preferably, the connector 3 is attached to the remaining components of the cap 26 by means of a swivel connector. A seal 2 may be provided to prevent fluid leakage from the area of any such swivel attachment. When the chemical delivery system 50 is attached to a garden hose, fluid flows in the directions indicated by the fluid flow passage 1 that is illustrated in FIGS. 1 and 8 .

To prevent the backflow of fluid from the chemical delivery system 50 to the fluid supply, a vacuum breaker 18 may be provided within the main fluid flow passage formed in the cap 26 . In this regard, the main fluid flow passage extends between the input, illustrated as connector 3 , and an output. While not intended to be limiting, the illustrated output comprises a threaded, male connector 8 adapted to releasably mate with a spray head 27 . As will be appreciated, the vacuum breaker 18 operates in connection with a vacuum breaker exhaust 4 , formed in the cap 26 adjacent to the vacuum breaker 18 , that provides a vent to the atmosphere if a pressure reversal occurs. A seal 17 may be positioned between the vacuum breaker 18 and the interior of the main fluid flow passage to prevent leakage of fluid through the vacuum breaker exhaust 4 .

While not required, the cap 26 may further include a shut off valve 5 , illustrated in FIGS. 1 , 2 , and 8 . The shut off valve 5 allows a user to manually control the amount of fluid that is permitted to flow through the main fluid passage of the cap 26 . The shut off valve 5 may be a ball valve such as illustrated in the figures, a pistol grip lever actuated valve (e.g., like a gas pump valve), or the like without limitation. A seal 6 may be positioned adjacent to the shut off valve 5 to prevent fluid leakage. Further associated with the main fluid passage and positioned between the inlet (e.g., connector 3 ) and the outlet (e.g., connector 8 ) is a flow restrictor 7 . The flow restrictor 7 functions to restrict the amount of fluid that flows through the main fluid passage to thereby create back pressure that further functions to divert fluid into the storage tank 24 and to siphon fluid from the storage tank 24 .

More specifically, fluid diverted from the main fluid passage is directed to an inlet nozzle 12 that is in fluid communication with the main fluid passage. The inlet nozzle 12 may be in direct fluid communication with the main fluid flow passage as illustrated in FIG. 8 . Alternatively, as illustrated in FIG. 1 , the fluid communication between the main fluid passage and the inlet nozzle 12 may be via an orifice formed in the main fluid passage on the upstream side of the flow restrictor 7 , an upper inlet nozzle 13 , and an adjustment dial 15 . In this regard, the adjustment dial 15 may be provided as a means for allowing a user to manually adjust the amount of fluid that is permitted to flow into the inlet nozzle 12 (i.e., to thereby control the rate of chemical mixing). To this end, the adjustment dial 15 includes a plurality of orifices 28 having various diameters (e.g., having diameters that range from approximately 0.030 to 0.060 inches) that may be selectively disposed between the upper nozzle 13 and the inlet nozzle 12 .

As illustrated in FIGS. 2 and 3 , the plurality of orifices 28 are arranged around the adjustment dial 15 such that the orifices 28 lie on a circle concentric with the axis of the adjustment dial 15 . The orifices 28 also have a radius selected to intersect the axis of the nozzles 12 and 13 . Associated with each of the orifices 28 may be a setting indicator 25 that is visible to the user such that the user may discern which of the orifices is presently associated with the inlet nozzle 12 .

To allow the user to selectively associate one of the orifices 28 with the inlet nozzle 12 , the adjustment dial 15 is adapted to be rotatable. To maintain the orifices 28 in the proper orientation with respect to the nozzles 12 and 13 , the adjustment dial 15 may be provided with a detent mechanism. While not intended to be limiting, the illustrated detent mechanism is comprised of indentations 29 arranged in a concentric circle about the dial 15 that cooperate with a spring loaded pin 16 that is mounted within the cap 26 . The adjustment dial 15 may be rotated about a retaining screw 14 that is adapted to mate with an adapter plate 9 that is provided to maintain the adjustment dial 15 , inlet nozzles 12 and 13 , and an outlet nozzle 10 within the cap 26 . A seal 33 may be provided between the adjustment dial 15 and the inlet nozzle 12 to prevent fluid leakage. For the same purpose, a seal 34 may also be positioned between the inlet nozzle 12 and the adapter plate 9 .

As noted previously, fluid is directed from the main fluid passage to the adjustment dial 15 and, in turn, the input nozzle 12 via atop inlet nozzle 13 . Seals 31 and 32 maybe used to prevent leakage of fluid from areas adjacent to this flow passage. In this regard, the dual seals 31 and 32 associated with the top inlet nozzle 13 (as well as the dual seals 33 and 34 associated with the nozzle 12 ) are especially useful to prevent leakage when the adjustment dial 15 is being rotated during those times that the system 50 is under pressure from the source of fluid. To further enhance the usefulness of the seals, it is preferred that the inlet nozzles (as well as the outlet nozzle) be designed so as to add increasingly positive pressure to the seals as pressure is increased. To this end, as illustrated in FIG. 4 , the top inlet nozzle 13 may include a pressure chamber 30 and the lower inlet nozzle 12 may include a pressure chamber 34 . Optional cavities 51 and 53 may be formed in the upper inlet nozzle 12 and lower inlet nozzle 14 , respectively, to provide an additional seal when the adjustment dial 15 is being rotated while the system is under fluid pressure.

The pressure chamber 30 communicates with fluid in the main flow line such that flow line pressure captured in the pressure chamber 30 forces the top inlet valve to move the top inlet lower seal 32 into further engagement against the adjustment dial 15 . Similarly, the pressure chamber 34 communicates with pressure in the storage tank 24 such that storage tank pressure captured in the pressure chamber 34 forces the lower inlet valve to move the bottom inlet nozzle seal 33 against the adjustment dial. It will be appreciated that, as pressure increases in either the main flow line or the storage tank, a stronger seal is created against the adjustment dial 15 .

For use in mixing fluid with chemical contained within the storage tank 24 , an inlet dip tube 19 , that extends towards the bottom of the storage tank 24 , is connected to a dip tube connection 36 of the inlet nozzle 12 . As illustrated in FIGS. 1 and 8 , an agitation nozzle 20 is further connected to end of the inlet dip tube 19 such that fluid exiting the agitation nozzle 20 will cause chemical contained within the storage tank 24 to mix with fluid that has been delivered to the storage tank 24 . As particularly illustrated in FIG. 8 , plural agitation nozzles 20 may be used and arranged, for example, circumferentially about the end of the inlet dip tube 19 .

To layer fluid over the top of the chemical solution located at the bottom of the storage tank 24 , a fluid control port 47 is provided. The fluid control port 47 may be formed as part of the inlet dip tube 19 as illustrated in FIG. 8 and/or as part of the inlet nozzle 12 as illustrated in FIG. 1 . This manner of delivering fluid to the top of the storage tank 24 helps to stabilize the chemical solution to create a more even injection rate. In addition, this manner of delivering fluid to the storage tank 24 helps to clear the expansion tank 24 of any dye when the chemical has been exhausted during spraying. This is particularly useful since it eliminates the situation where a user thinks chemical remain in the storage tank 24 just because the fluid remains dyed. It is to be appreciated that the control port 47 is optional.

To further assist in the even mixing of the chemical and the fluid, especially in the case of water soluble fertilizers, the storage tank 24 may be provided with a domed bottom into which the nozzle 20 extends. In this manner, the agitation caused by fluid exiting the nozzle 20 occurs at the bottom most portion of the storage tank 24 . Additionally, the domed bottom improves the strength of the storage tank 24 in a pressurized environment. To allow a storage tank 24 with a domed bottom to sit with stability, a ring 48 may be provided that is adapted to mate with the bottom of the storage tank 24 , for example, by being snap-fit thereto. Still further, to facilitate the mixing of the chemical and fluid, the storage tank 24 may include a portion 24 a that is positioned above the domed bottom that generally protrudes inwardly as is illustrated in FIG. 8 . In particular, the portion 24 a functions to provide a more steep funneling effect to the storage tank 24 to prevent the settling of chemical against the interior surface of the storage tank 24 away from the nozzles 20 .

For use in venting air during filling of the storage tank 24 and for returning fluid mixed with chemical to the main fluid passage once the filling process is complete, an outlet nozzle 10 , having a mounted outlet dip tube 23 , is placed in fluid flow communication with the main fluid passage via an orifice positioned in the main fluid passage located downstream of the flow restrictor 7 . The outlet nozzle 10 , an example of which is illustrated in FIG. 5 , may have a first body section and a second body section that defines a fluid flow passage 40 that is in fluid communication with the main fluid passage. As seen in FIG. 1 , the first body section of the outlet nozzle 10 may be disposed between the main fluid passage and the adapter plate 9 and dual seals 41 and 42 may be provided to prevent fluid leakage from areas where the elements meet. The second body section of the outlet nozzle 10 extends from the adapter plate 9 towards the storage tank 24 and carries an outlet nozzle trap 11 . Preferably, the top of the outlet nozzle trap 11 engages the bottom of the adapter plate 9 .

Alternatively, the outlet nozzle 10 may also be placed in direct fluid communication with the main fluid passage as illustrated in FIG. 8 . Furthermore, the outlet dip tube 23 may be disposed apart from the inlet dip tube 19 , as illustrated in FIG. 1 , or may disposed within the interior of the inlet dip tube 19 , as illustrated in FIG. 8 . In the latter instance, both the inlet dip tube 19 and the outlet dip tube 23 may pass through the outlet nozzle trap 11 .

The outlet nozzle trap 11 preferably has a perforated opening 43 leading to the interior of the tank 24 . In the case where the fill control port 35 is formed in the inlet nozzle 12 and the inlet nozzle 12 is spaced from the outlet nozzle trap 11 , the fill control port 35 serves to direct fluid to the outlet nozzle trap 11 via the perforated opening 43 as is illustrated in FIG. 1 . Alternatively, the fill control port 35 may lead directly to the interior of the outlet nozzle trap. In this regard, the fill control port 35 may be formed as part of the inlet nozzle 12 or be formed adjacent to the inlet nozzle 12 as is illustrated by way of example in FIG. 8 . Regardless of the method for diverting fluid to the outlet nozzle trap 11 , the diverted fluid inhibits the venting of air from the storage tank 24 via a vent port 44 associated with the outlet nozzle 10 . As such, the sizing of the fill control port 35 relative to the size of the outlet nozzle vent 44 will regulate the amount of air capable of being vented via the vent 44 which, in turn, regulates the speed by which the storage tank 24 fills. As will be appreciated, controlling the fill speed in turn controls the initial injection rates, mixing, etc. Furthermore, the action between the fill control port 35 and the vent port 44 helps to eliminate plugging and spurting. For example, if back pressure develops due to air resistance at the screen 21 , the system will function to automatically force more air or fluid out of port 44 . Without such a system, back pressure would develop until enough force was created to push the resisting element through the screen 21 which, when the release occurred, would cause spurting. If the resisting element were not forced through the screen, a plug would occur.

Once the fluid in the storage tank 24 reaches the level of the end of outlet dip tube 23 , fluid mixed with chemical may now be siphoned into the main fluid passage from the storage tank 24 . In this regard, fluid is drawn into the outlet dip tube 23 via a bottom outlet nozzle 22 that is attached to the bottom of the outlet dip tube 23 . Injection of the fluid mixed with chemical into the main fluid passage at a time before the tank is full is made possible by the back pressure created by means of the fluid directed into the outlet nozzle trap 11 .

Further associated with the bottom outlet nozzle 22 is a dip tube screen 21 , illustrated in FIGS. 6 and 7 , having a non-clogging design. In the illustrated embodiment, the screen 21 comprises a screen meshing 46 (for example, of polypropylene) attached to vertical support rods 45 . The relationship of the vertical support rods 45 is such that the narrowest point between adjacent vertical support rods 45 is at the point where the support rods 45 engage the screen meshing 46 . In this manner, anything that is capable of passing through the support rods 45 at their outermost points of association will be able to pass through into the interior of the screen 21 . To provide a more consistent flow into the outlet dip tube 23 , it is preferred that the outlet bottom nozzle 22 extends into the middle of the screen 21 .

While specific embodiments of the invention have been described in detail, it will be appreciated by those skilled in the art that various modifications and alternatives to those details could be developed in light of the overall teachings of the disclosure. For example, it is to be appreciated that various elements, such as the dip tubes, ports, etc., could be eliminated without departing from the spirit of the invention. Accordingly, the particular arrangement disclosed is meant to be illustrative only and not limiting as to the scope of the invention which is to be given the full breadth of the appended claims and any equivalents thereof.

Claims

1. A method for injecting a chemical into a flow of fluid in a main fluid flow passage, comprising:diverting a quantity of fluid from the main fluid flow passage to a storage tank via an inlet nozzle to mix the diverted fluid with a chemical stored within the storage tank; returning a quantity of the fluid mixed with the chemical from the storage tank to the main fluid flow passage via an outlet nozzle; and directing a quantity of fluid from the main fluid flow passage to an outlet nozzle trap associated with the outlet nozzle to fill the outlet nozzle trap to control venting of air from the storage tank to the main fluid flow passage via a vent port associated with the outlet nozzle.

2. The method as recited in claim 1, wherein directing a quantity of fluid from the main fluid flow passage to the outlet nozzle trap comprises directing the quantity of fluid directly into the outlet nozzle trap.

3. The method as recited in claim 1, wherein directing a quantity of fluid from the main fluid flow passage to the outlet nozzle trap comprises directing the quantity of fluid through a port formed in the outlet nozzle trap.

4. The method as recited in claim 3, wherein the quantity of fluid directed to the outlet nozzle trap is diverted from the inlet nozzle.

5. The method as recited in claim 1, further comprising directing the quantity of fluid diverted from the main fluid flow passage to a bottom portion of the storage tank to mix the chemical stored within the storage tank.

6. The method as recited in claim 5, further comprising passing the quantity of fluid diverted from the main fluid flow passage to the bottom portion of the tank through an agitation nozzle.

7. The method as recited in claim 5, further comprising passing the quantity of fluid diverted from the main fluid flow passage to the bottom portion of the tank through a plurality of agitation nozzles.

8. The method as recited in claim 7, wherein the plurality of agitation nozzles are arranged about the bottom of a dip tube connected to the inlet nozzle.

9. The method as recited in claim 1, further comprising layering a quantity of fluid drawn from the main fluid flow passage over a top of the fluid mixed with chemical.

10. The method as recited in claim 9, wherein the quantity of fluid drawn from the main fluid flow passage is layered over the top of the fluid mixed with chemical via a vent formed in the inlet nozzle.

11. The method as recited in claim 9, wherein the quantity of fluid drawn from the main fluid flow passage is layered over the top of the fluid mixed with chemical via a vent formed in a dip tube connected to the inlet nozzle.

12. The method as recited in claim 1, further comprising filtering the quantity of fluid mixed with the chemical that is returned to the main fluid flow passage from the storage tank.

13. The method as recited in claim 12, wherein a mesh screen is attached to a dip tube that is attached to the outlet nozzle for use in filtering the quantity of fluid mixed with chemical that is returned to the main fluid flow passage from the storage tank.

14. The method as recited in claim 1, further comprising controlling the amount of fluid diverted from the main fluid flow passage to the storage tank by means of an adjustment dial.

15. A chemical delivery system, comprising:a body defining a main fluid flow passage through which a fluid passes; a storage tank for holding a chemical; an inlet nozzle by which a quantity of the fluid in the main fluid flow passage is delivered to the storage tank to be mixed with the chemical; an outlet nozzle, having a vent port, by which a quantity of the fluid mixed with the chemical is returned to the main fluid flow passage from the storage tank; an outlet nozzle trap in fluid communication with the vent port of the outlet nozzle; and a fill control port for directing fluid from the main fluid flow passage to the outlet nozzle trap to fill the outlet nozzle trap to control venting of air from the storage tank to the main fluid flow passage via the vent port.

16. The chemical delivery system as recited in claim 15, wherein the fill control port is in direct fluid flow communication with the outlet nozzle trap.

17. The chemical delivery system as recited in claim 16, wherein the fill control port is formed in the inlet nozzle.

18. The chemical delivery system as recited in claim 16, wherein the fill control port is formed adjacent to the inlet nozzle.

19. The chemical delivery system as recited in claim 15, further comprising a fluid control port for layering fluid over the fluid mixed with the chemical in the storage tank.

20. The chemical delivery system as recited in claim 19, wherein the fluid control port is formed in the inlet nozzle.

21. The chemical delivery system as recited in claim 19, wherein the fluid control port is formed in a dip tube connected to the inlet nozzle.

22. The chemical delivery system as recited in claim 15, further comprising an inlet dip tube attached to the inlet nozzle and extending into the storage tank.

23. The chemical delivery system as recited in claim 22, further comprising an agitation nozzle attached to the inlet dip tube.

24. The chemical delivery system as recited in claim 22, further comprising a plurality of agitation nozzles attached to the inlet dip tube.

25. The chemical delivery system as recited in claim 15, wherein the storage tank has a domed bottom.

26. The chemical delivery system as recited in claim 25, wherein the storage tank has a funnel shape leading to the domed bottom.

27. The chemical delivery system as recited in claim 25, further comprising a ring stand attachable to the domed bottom of the storage tank.

28. The chemical delivery system as recited in claim 15, wherein the main fluid flow passage comprises a cap attachable to the storage tank.

29. The chemical delivery system as recited in claim 15, further comprising an outlet dip tube attached to the outlet nozzle and extending into the storage tank.

30. The chemical delivery system as recited in claim 29, further comprising an inlet dip tube attached to the inlet nozzle and extending into the storage tank, wherein the outlet dip tube is disposed within the inlet dip tube.

31. The chemical delivery system as recited in claim 30, further comprising a dip tube screen attached to the outlet dip tube opposite the outlet nozzle.

32. The chemical delivery system as recited in claim 31, wherein the dip tube screen is non-clogging.

33. The chemical delivery system as recited in claim 32, wherein the dip tube screen comprises a plurality of support rods and a meshing attached to the plurality of support rods.

34. The chemical delivery system as recited in claim 33, wherein the plurality of support rods are arranged such that a narrowest distance between adjacent support rods is located proximate to the meshing.

35. The chemical delivery system as recited in claim 34, wherein the outlet dip tube extends to an approximate mid-point of the dip tube screen.

36. The chemical delivery system as recited in claim 15, further comprising a flow restrictor disposed with the main fluid flow passage to divert fluid to the storage tank via the inlet nozzle.

37. A system for injecting a chemical into a flow of fluid in a main fluid flow passage, comprising:means for diverting a quantity of fluid from the main fluid flow passage to a storage tank via an inlet nozzle to mix the diverted fluid with a chemical stored within the storage tank; means for returning a quantity of the fluid mixed with the chemical from the storage tank to the main fluid flow passage via an outlet nozzle; and means directing a quantity of fluid from the main fluid flow passage to an outlet nozzle trap associated with the outlet nozzle to fill the outlet nozzle trap to control venting of air from the storage tank to the main fluid flow passage via a vent port associated with the outlet nozzle.