Feeder device and method for adding solid material to a liquid of variable flow rate

• US 4,759,907 A
• Filed: 10/31/1986
• Issued: 07/26/1988
• Est. Priority Date: 10/31/1986
• Status: Expired due to Fees

• Current Assignee: Eltech Systems Corporation (Industrie De Nora S.p.A)
• Original Assignee: Eltech Systems Corporation (Industrie De Nora S.p.A)
• Inventors: Kawolics, Richard J., Zivich, Philip J., Nelson, Bonnie I.
• Primary Examiner(s): Richman, Barry S.
• Assistant Examiner(s): McMahon, Timothy M.
• Application Number:
  US06/925,356
• Time in Patent Office: 634 Days
• Field of Search: 422/7, 422/19, 422/264, 422/264 B, 422/265, 422/276, 422/277, 422/285, 422/278, 210/198.1, 210/199, 210/752, 210/754-759, 137/268, 137/101.27, 4/226, 4/228, 4/231
• US Class Current: 422/7
• CPC Class Codes: B01F 21/22 using additional holders in conduits, containers or pools for keeping the solid material in place, e.g. supports or receptacles
• CPC Class Codes: B01F 21/4021 in the form of tablets stored in containers, canisters or receptacles
• CPC Class Codes: B01F 25/316 with containers for additional components fixed to the conduit
• CPC Class Codes: B01J 4/008 Feed or outlet control devices
• CPC Class Codes: C02F 1/688 Devices in which the water progressively dissolves a solid compound
• CPC Class Codes: Y10T 137/4891 With holder for solid, flaky or pulverized material to be dissolved or entrained

Abstract

A feeder device for controlled dissolution of a solid treating agent in a liquid of variable flow rate is designed such that the concentration of treating agent in the effluent liquid can be substantially constant, irrespective of the actual flow rate of the liquid. Further, the value of this concentration may be adjusted to varying levels and adapted to meet specific needs and requirements of the particular liquid system in which this feeder device may be employed. The constancy of concentration of the agent is obtained by the provision of a proportional weir, positioned in connection with a dissolution chamber, useful for maintaining a liquid volume in this dissolution chamber which can be linearly proportional to the flow rate of the liquid therethrough. In this liquid volume, dammed up by the weir, the solid treating agent, generally a substance containing hypochlorite, sulfite, sulphate or permanganate, can be present at least partly as a soluble solid. An amount of the agent not yet solubilized, proportional to the depth of the liquid, is contacted by and then dissolved in the liquid. Thus, the desired proportionality between this amount or the dissolution rate of the treating agent and the flow rate of the liquid is established.

Claims

1. A feeder device for controlled addition of a treating agent to a flowing liquid of variable flow rate, wherein the device is adapted for the outflow of the liquid from the feeder device by gravity, the feeder comprising:

a housing element having a longitudinal axis for temporarily confining a flowing liquid;

a liquid inlet means and a liquid outlet means in said housing element;

a dissolution chamber within said housing element between said inlet means and outlet means, said dissolution chamber having an elevated bottom and comprising holding means for solid treating agent;

an entrance zone having a bottom and being located between said inlet means and said dissolution chamber;

raised surface means rising from said entrance zone to said dissolution chamber and providing an inlet flow baffle, said raised surface means extending from said entrance zone to said dissolution chamber elevated bottom;

at least one proportional weir between said inlet means and said outlet means including a proportional weir located between said dissolution chamber and said outlet means and being designed such that the amount of liquid present in the dissolution chamber in proportional to the flow rate of flowing liquid, thereby contacting with, and dissolving in the liquid an amount of treating agent proportional to its flow rate;

and with the weir being consturcted so as to be adjustable or exchangeable to provide for a desired concentration of treating agent in the liquid leaving said feeder device.

2. The feeder of claim 1, wherein there is contained in said holding means one or more one or more solid organic or inorganic treating agent, with the inorganic agent being selected from substance containing hypochlorite, sulfite, sulphate, permanganate, or mixtures of the foregoing.

3. The feeder of claim 1, wherein the holding means is comprised of at least one hollow cylinder having one or more lateral openings at a lower portion thereof through which liquid may contact said solid treating agent contained within said cylinder.

4. The feeder of claim 3, wherein the holding means comprises removable top cover for recharging said cylinder with treating agent and the bottom of said holding means rests upon the floor of said dilution chamber.

5. The feeder of claim 1, wherein said porportional weir is an adjustable weir which comprises at least one shutter plate arranged essentially perpendicular to the longitudinal axis of said housing element, said at least one shutter plate having an opening for the passage of said a liquid, said opening being essentially a vertical slot of varying width, progressively decreasing in width with increasing relative height along said slot.

6. The feeder of claim 5, wherein said proportional weir comprises two shutter plates arranged in one plane, and setting means for adjusting the distance of said shutter plates to one another.

7. The feeder of claim 6, wherein said setting means comprises two toothed racks, one connected to each shutter plate such that the teeth of said two racks oppose each other, and a toothed wheel engaging both racks, said wheel and said racks being operatively connected to shift said shutter plates relative to one another upon rotation of said toothed wheel.

8. The feeder of claim 1, wherein said device includes a dilution chamber while having said dissolution chamber located between said dilution chamber and said entrance zone, with said dissolution chamber having an elevated bottom with respect to said entrance zone and dilution chamber, with the ratio of the distance across the entrance zone to the height of said elevated bottom being at least 2:

1.

9. The feeder of claim 8, wherein the distance across the entrance zone is the distance from an outlet end of the liquid inlet means to the beginning of the elevated bottom.

10. The feeder to claim 8, wherein the ratio of the distance across the dilution chamer to the height of the elevated bottom is at least 2:

1.

11. The feeder of claim 10, wherein the distance across the dilution chamber is the distance from an outlet end to the end of the elevated bottom.

12. The feeder of claim 1, further comprising a dilution chamber within said housing element, a channel means within said housing element arranged to provide a bypass leading to said dilution chamber, said channel means being arranged between said inlet means and said outlet means so that liquid flowing through said housing element is divided into first and second streams, the first stream passing through said dissolution chamber before entering said dilution chamber and the second stream entering the channel means providing said bypass, said at least one weir further including a second proportional weir arranged between said inlet means and said outlet means in said bypass, said second proporitonal weir being constructed so as to be adjustable.

13. The feeder of claim 12, wherein the proportional weir located between the dissolution chamber and the outlet means is contructed so as to be adjustable for providing variations in the proportionality between the amount of liquid in the dissolution chamber and the liquid flow rate.

14. The feeder of claim 3, wherein said outlet means is arranged at the bottom of said dilution chamber.

15. The feeder of claim 12, wherein said weir between said inlet means and said bypass rests on the bottom of said dissolution chamber.

16. The feeder of claim 15, wherein said inlet means is positioned below the bottom of said dissolution chamber.

17. The feeder of claim 15, wherein said inlet means is comprised of a tube entering said entrance zone, said tube comprising a closed end portion and lateral openings adjacent thereto, said lateral openings being arranged on said end portion of said tube in a position substantially facing said bottom of said entrance zone.

18. The feeder of claim 15, wherein said outlet means is arranged at the bottom level of said dilution chamber.

19. The feeder of claim 18, wherein the bottom of said dilution chamber is at a level corresponding to the bottom level of said entrance zone.

20. A method of adding solid treating agent to a flowing liquid of varying flow rate, comprising:

feeding said liquid of variable flow rate to a feeder device entrance zone

flowing said liquid form said entrance zone over a flow baffle extending from said entrance zone to a dissolution chamber

passing said liquid through said dissolution chamber wherein it is brought into controlled contact with a solid treating agent;

restricting the flow of said liquid through said dissolution chamber; and

establishing a linearly proportional, adjustable relationship between the depth of liquid present within said dissolution chamber and the discharge amount of liquid from said chamber, thus dissolving said treating agent at a rate proportional to said flow rate.

21. The method of claim 20, wherein the liquid is divided into a first and a second stream, said first stream being passed through said dissolution chamber and subsequently combined wiht said second stream that is bypassing said dissolution chamber, the flow ratio between said first and second stream being kept substantially constant at varying total flow rates.

22. The method of claim 20, wherein said steps of establishing a linearly proportional, adjustable relationship and restricting said flow of said liquid through said dissolution chamber includes flowing said liquid through a proportional weir.

23. In a feeder assembly for controlled addition of a treating agent to a flowing liquid of variable flow rate, wherein said assembly has a housing element for temporarily confining a flowing liquid, which housing element includes liquid inlet means, liquid outlet means, a dissolution chamber containing holding means for solid treating agent and said assembly includes at least one weir, the improvement in said assembly which comprises a liquid inlet zone having a floor, within said housing element, which floor is at a first level for said assembly and said liquid inlet zone, said dissolution chamber having a floor at a second level, with said second level dissolution chamber floor being above said assembly floor, and including a raised surface means between floors providing a flow baffle, and with said at least one weir including a weir positioned between said dissolution chamber and said outlet means, which weir is a proportional weir.

24. The feeder assembly of claim 23, wherein said raised surface means includes at least one step between said assembly floor and said dissolution chamber floor.

25. The feeder assembly of claim 23, wherein said raised surface means includes at least one step extending upwardly to the threshold of the weir.

26. The feeder assembly of claim 23, wherein said proportional weir is constructed to be linearly proportional and is positioned between said dissolution chamber and said outlet means.

27. The feeder assembly of claim 23, wherein the ratio of the distance across the floor of said liquid inlet chamber to the height between the floors is at least 2:

1.

28. In a feeder assembly for controlled addition of a treating agent to a flowing liquid of variable flow rate, wherein said assemby has a housing element for temporarily confining a flowing liquid, which housing element includes liquid inlet means, liquid outlet means, a dissolution chamber containing holding means for solid treating agent and said assembly includes at least one weir, the improvement in said assembly which comprises a liquid inlet zone having a floor within said housing element which floor is at a first level for said assembly and said liquid inlet zone, said dissolution chamber having a floor at a second level, a bypass chamber within said housing element between said liquid inlet zone and said liquid outlet means and having a floor at said second level, said bypass chamber floor being above said assemby floor and with said assemby including a raised surface means between floors providing a flow baffle.

29. The feeder assembly of claim 28, wherein said raised surface menas includes at least one step between said assembly floor and said bypass chamber floor.

30. The feeder assembly of claim 28, wherein said raised surface mens includes at least one step extending upwardly to the threshold of the weir.

31. The feeder assembly of claim 28, wherein a linearly proportional weir is positioned in assembly adjacent said dissolution chamber.

32. In a feeder assembly for controlled addition of a treating agent to a flowing liquid of variable flow rate, wherein said assembly has a housing element for temporarily confining a flowing liquid, which housing element includes liquid inlet means, liquid outlet means, a dissolutin chamber containing holding means for solid treating agent and said assembly includes at least one weir, the improvement in said assembly which comprises a liquid inlet zone within said housing element, a dissolution chamber within said housing element between said inlet means and outlet means, said at least one weir incuding a proportional weir positioned adjacent said dissolution chamber a with there being as said liquid inlet means a perforate, elongated liquid inlet element extending into said liquid inlet zone, and with there being a raised surface means flow baffle extending between said inlet zone and said dissolution chamber.

33. The feeder assembly of claim 32, wherein said liquid inlet element is positioned in said inlet chamber upstream from said proportional weir.

34. The feeder assembly of claim 32, wherein said liquid inlet element comprises a perforate inlet tube having an at least partially blocked end, with said tube being positioned in said inlet zone above a floor of said zone.

35. The feeder assemby of claim 32, wherein said liquid inlet element extends horizontally into said liquid inlet zone.

36. The feeder assembly of claim 32, wherein said inlet zone has a floor, said dissolution chamber has a floor above said inlet zone floor and said liquid inlet element is positioned below said dissolution chamber floor.

37. The feeder assembly of claim 32, comprising a bypass chamber leading from said inlet chamber to a dilution chamber.

38. In a feeder assembly for controlled addition of a treating agent to a flowing liquid of variable flow rate, wherein said assembly has a housing element for temporarily confining a flowing liquid, which housing element includes liquid inlet means, liquid outlet means, a dissolution chamber containing holding means for solid treating agent, the improvement in said assembly which comprisies a liquid inlet zone having a floor within said housing element, which floor is at a first level for said assembly and said liquid inlet zone, a dissolution chamber with a floor at a second level, with said dissolution chamber floor being above said assembly floor, a raised surface means flow baffle between said floors and with the ratio of the distance across the inlet zone to the height of the raised surface means between the floor levels being at least 2:

1.

39. The feeder assembly of claim 38, wherein said ratio is at least 3:

1.

40. The feeder assembly of claim 38, comprising a bypass chamber having a floor at said second level and leading from said inlet chamber to a dilution chamber.

41. The feeder assembly of claim 38, wherein said dissolution chamber leads to a dilution chamber having a floor at said first level.

42. The feeder assembly of claim 41, wherein the ratio of the distance across the dilution chamber to the height between floor levels is at least 2:

1.