Rotating spray bar assembly, processing systems having a rotating spray bar assembly, and methods of processing
09578885 ยท 2017-02-28
Assignee
Inventors
- Battle Glascock (Soddy Daisy, TN, US)
- Robert C. Bullard (Signal Mountain, TN, US)
- James A. Faller (Chattanooga, TN, US)
- Jonathon R. Bullard (Chattanooga, TN, US)
Cpc classification
B05B1/169
PERFORMING OPERATIONS; TRANSPORTING
B05B1/1636
PERFORMING OPERATIONS; TRANSPORTING
B05B13/0447
PERFORMING OPERATIONS; TRANSPORTING
B05B3/14
PERFORMING OPERATIONS; TRANSPORTING
B05B3/0422
PERFORMING OPERATIONS; TRANSPORTING
B05B1/20
PERFORMING OPERATIONS; TRANSPORTING
B05B13/0405
PERFORMING OPERATIONS; TRANSPORTING
B05B1/3026
PERFORMING OPERATIONS; TRANSPORTING
B05B12/04
PERFORMING OPERATIONS; TRANSPORTING
B05B1/1672
PERFORMING OPERATIONS; TRANSPORTING
International classification
B05B17/00
PERFORMING OPERATIONS; TRANSPORTING
A23B4/16
HUMAN NECESSITIES
B05B3/04
PERFORMING OPERATIONS; TRANSPORTING
B05B3/12
PERFORMING OPERATIONS; TRANSPORTING
B05B1/16
PERFORMING OPERATIONS; TRANSPORTING
B05B1/30
PERFORMING OPERATIONS; TRANSPORTING
Abstract
Rotating spray systems and related methods for enhancing spray performance can include one of more rotating spray assemblies formed of a plurality of individual, linear distribution manifolds to define a rotary cage. The rotary cage is fluidly coupled to a rotating distribution block on a distribution valve, with each linear distribution manifold being fluidly coupled to one of a plurality of distribution conduits defined in the rotating distribution block. The distribution valve further includes a fixed distribution block having an arcuate aperture defined therein. The rotating distribution block rotates relative to the fixed distribution block to individually and sequentially engage each distribution conduit with the arcuate aperture. When the individual distribution conduits are fluidly engaged with the arcuate aperture, pressurized fluid supplied to the distribution valve is supplied to the corresponding linear distribution manifold for spraying by one or more spray nozzles fluidly connected to each linear distribution manifold.
Claims
1. A spray system, comprising: at least one spray bar assembly, said spray bar assembly comprising: a rotary cage including a plurality of linear distribution manifolds, each linear distribution manifold including a manifold inlet and a manifold flow channel, wherein a plurality of manifold apertures are defined along each manifold flow channel and each manifold aperture includes a spray nozzle mounted therein; a distribution valve including a fixed distribution block and a rotary distribution block, the fixed distribution block including an arcuate aperture and the rotary distribution block including a plurality of distribution conduits, wherein the quantity of distribution conduits is equal to the quantity of linear distribution manifolds and each linear distribution manifold is fluidly coupled to the associated distribution conduit; a means for rotating the rotary distribution block relative to the fixed distribution block; and a pressurized fluid supply fluidly coupled to the arcuate aperture; wherein the rotary distribution block is rotated relative to the fixed distribution block such that individual distribution conduits are sequentially, fluidly engaged with the arcuate aperture such that the pressurized fluid supply is introduced into each linear distribution manifold for dispensing from the associated spray nozzles and that dispensing of the pressurized fluid supply is prevented from each linear distribution manifold when the corresponding distribution conduit is not fluidly engaged with the arcuate aperture.
2. The spray system of claim 1, wherein the arcuate aperture has an angular outlet range of 90 degrees.
3. The spray system of claim 1, wherein at least two of the distribution conduits are simultaneously fluidly engaged to the arcuate aperture as the rotary distribution block rotates relative to the fixed distribution block.
4. The spray system of claim 1, further comprising at least two spray bar assemblies, each spray bar assemblies mounted such that the rotary cages are in parallel relation.
5. The spray system of claim 1, further comprising at least two spray bar assemblies, wherein the arcuate apertures of the at least two spray bar assemblies have differing angular outlet ranges.
6. The spray system of claim 1, wherein the rotary distribution block causes the pressurized fluid supply to be dispensed from the spray nozzles in only a downward trajectory as dictated by the arcuate aperture.
7. The spray system of claim 1, wherein the pressurized fluid comprises at least one peroxycarboxylic acid having between about 2 to 12 carbon atoms.
8. The spray system of claim 1, wherein the rotary distribution block is rotated by the means for rotating at a rate of between about 10 rpm to about 100 rpm.
9. The spray system of claim 1, wherein the means for rotating is selected from the group consisting essentially of: a motor directly coupled to the rotary cage, a belt drive assembly, a chain drive assembly and a gear assembly driven by a motor.
10. A method of spraying items, comprising: supplying a pressurized fluid to a distribution valve, said distribution valve including a fixed distribution block and a rotating distribution block, wherein the pressurized fluid is directed into an arcuate aperture on the fixed distribution block; rotating the rotating distribution block relative to the fixed distribution block such that a plurality of distribution conduits defined in the rotating distribution block are sequentially introduced to the arcuate aperture; directing the pressurized fluid through each distribution conduit when each distribution conduit is fluidly engaged with the arcuate aperture, each distribution conduit being fluidly coupled to a linear distribution manifold, wherein the linear distribution manifold defines a rotary cage that rotates in conjunction with the rotating distribution block; and spraying the pressurized fluid from a plurality of spray nozzles on each linear distribution manifold when the corresponding distribution conduit is fluidly engaged with the arcuate aperture.
11. The method of claim 10, wherein the step of spraying further comprises: spraying the pressurized fluid in only a downward trajectory.
12. The method of claim 10, further comprising: providing the pressurized fluid, wherein the pressurized fluid comprises at least one peroxycarboxylic acid having between about 2 to 12 carbon atoms.
13. The method of claim 10, further comprising: conveying a suspended carcass past the rotary cage.
14. The method of claim 10, further comprising: rotating the rotation distribution block at a rate of between about 10 rpm to about 100 rpm.
15. A spray bar assembly, comprising: a rotary cage including a plurality of linear distribution manifolds, each linear distribution manifold including a manifold flow channel, wherein each manifold flow channel includes a plurality of spray nozzles fluidly coupled thereto; and a distribution valve including a fixed distribution block and a rotary distribution block, the fixed distribution block including an arcuate aperture and the rotary distribution block including a plurality of distribution conduits, wherein the quantity of distribution conduits is equal to the quantity of linear distribution manifolds and each linear distribution manifold is fluidly coupled to the associated distribution conduit, such that rotation of the rotary distribution block relative to the fixed distribution block sequentially, fluidly engages each distribution conduit to the arcuate aperture.
16. The spray bar assembly of claim 15, wherein the arcuate aperture has an angular outlet range of about 90 degrees.
17. The spray bar assembly of claim 16, wherein the angular outlet range is selected such that the arcuate aperture is simultaneously, fluid engaged to two or more distribution conduits.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The present invention can be more completely understood in consideration of the following detailed description of various embodiments of the invention in connection with the accompanying drawings, in which:
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(28) While the present invention is amenable to various modifications and alternative forms, specifics thereof have been shown by way of example in the drawings and will be described in detail. It should be understood, however, that the intention is not to limit the present invention to the particular embodiments described. On the contrary, the intention is to cover all modifications, equivalents, and alternatives falling within the spirit and scope of the present invention as defined by the appended claims.
DETAILED DESCRIPTION OF THE DRAWINGS
(29) With reference to
(30) As shown in
(31) As illustrated in
(32) With reference to
(33) Referring again to
(34) As illustrated in
(35) Fixed distribution block 254 and rotating distribution block 256 are each formed of a ceramic material. As illustrated in
(36) As shown in
(37) As seen in
(38) As shown in
(39) In operation, a user actuates either locally, via a switch or button, or remotely, via a control system, the drive assembly 206. Rotational energy from the drive assembly 206 is imparted to the rotary cage 204 such that the rotary cage 204, the rotating distribution block 256 and the union shaft 242 are caused to rotate about axis x as shown in
(40) Dependent upon the angular outlet range 266 and the number of linear distribution manifolds 214 that comprise the rotary cage 204, one or more of the distribution conduits 284 can be fluidly engaged with the arcuate aperture 258 at any time such the pressurized fluid can be simultaneously sprayed from one or more of the linear distribution manifolds 284 at any one time. For example, arcuate aperture 258 with the angular outlet range 266 of approximately 90 degrees as shown in
(41) The processing liquid or gas can comprise a chemical intervention solution that provides the appropriate application for the material being processed. In the situation of a food product, the processing liquid can comprise a chemical intervention solution chosen from chlorine, bromine, cetylpyridinium chloride (CPC), an organic acid, a peroxycarboxylic acid, trisodium phospate, acidified sodium chlorite, and chlorine dioxide.
(42) In some preferred embodiments, the processing liquid comprises at least one peroxycarboxylic acid having 2-18 carbon atoms. In some aspects, the peroxycarboxylic acid solution is chosen from peroxyformic acid, peroxypropionic acid, peroxyacetic acid, peroxybutanoic acid, peroxypentanoic acid, peroxyhexanoic acid, peroxyheptanoic acid, peroxyoctanoic acid, peroxynonanoic acid, peroxydecanoic acid, peroxyundecanoic acid, peroxydodecanoic acid, peroxylactic acid, peroxymaleic acid, peroxyascorbic acid, peroxyhydroxyacetic acid, peroxyoxalic acid, peroxymalonic acid, peroxysuccinic acid, peroxyglutaric acid, peroxyadipic acid, peroxypimelic acid, peroxysubric acid, peroxycitric acid and mixtures thereof. Preferably, the intervention solution comprises an equilibrium peroxyacetic acid or a pH modified peroxyacetic acid.
(43) In some aspects, the equilibrium peroxyacetic acid preferably has a pH above about 3.0 and below about 7.0, in some aspects about 3.5 to about 5.5, and in some other aspects about 3.5 to about 5.0, although subranges within these ranges is contemplated.
(44) In some aspects, the pH modified peroxycarboxylic acid preferably has a pH above about 7.0 and below about 10.0, in certain aspects a pH range of about 7.0 to about 9.5, and in some other aspects a pH range of about 7.5 to about 9.0, although subranges within these ranges is contemplated. The pH modified peroxycarboxylic acid can be prepared by combining a peroxycarboxylic acid solution, such as a peroxyacetic acid solution, with one or more buffering agents chosen from sodium hydroxide, potassium hydroxide, the sodium salt of carbonic acid, the potassium salt of carbonic acid, phosphoric acid, silicic acid or mixtures thereof, in a quantity that is necessary to bring the solution to said pH range One of ordinary skill in the art will appreciate that other alkalizing chemistries approved for direct food contact may also be used, whether alone or in combination with any of the foregoing buffering agents. The quantity of the buffering agent in a buffered peroxycarboxylic acid solution will generally be in the range of about 0.01% to about 10% by volume of the total solution, but other volumes of the buffering agent may be utilized depending upon various parameters, such as local water condition, including pH, hardness and conductivity.
Simulations
(45) In order to demonstrate the improved performance of the rotating spray assemblies 202 as compared to the conventional oscillating spray assemblies 110, two simulations were conducted to compare fluid usage and cleaning efficiency between the different spray assembly designs. In preparing the simulations, various assumptions were made including using the same individual spray nozzles within each of the different spray assemblies. Each spray nozzle was simulated to dispense one (1) gpm of fluid at forty (40) psig. The spray pattern for each spray nozzle is as illustrated within
(46) Simulation 1: Prior Art Oscillating Spray Bar Assembly
(47) With respect to the first simulation involving the oscillating spray assemblies 110, the oscillation pattern for each oscillating spray assembly 110 modeled in the simulation is shown in
(48) Simulation 1 consisted of a spray system utilizing twenty-two (22) oscillating spray assemblies 110 with a combined total of two hundred twenty (220) nozzles. Each nozzle had an on time (during the down stroke only) of fifty (50)%. Thus, the oscillating spray assemblies 110 of Simulation 1 had an anticipated fluid use rate of 110 gpm. As can be seen in
(49) Simulation 2: Rotating Spray Assembly
(50) With respect to the second simulation involving the rotating spray assemblies 202, the rotation pattern for each rotating spray assembly 202 is shown in
(51) Simulation 2 consisted of a spray system utilizing four rotating spray assemblies 202 with a combined total of three hundred twenty (320) nozzles. The arcuate aperture 258 of each rotating spray assembly 202 was arranged to provide each nozzle with an on time (spray during ninety (90) of rotation) of twenty five (25)%. Thus, the rotating spray assemblies 202 of Simulation 2 had an anticipated fluid use rate of eighty (80) gpm. As can be seen in
(52) A comparison of the simulations demonstrates that the rotating spray assemblies 202 use less fluid and a smaller footprint while providing superior spray performance than is experienced with the oscillating spray assemblies 110. Specifically, the total anticipated water flow rate for Simulation 1 is one hundred ten (110) gpm, while that of Simulation 2 is eighty (80) gpm, which results in about thirty (30)% less gas or liquid being used. Also, Simulation 2 results in continual impact spraying for about eight (8) seconds with an overlapping spray pattern, while Simulation 1 results in intermittent spray during the down stroke having a total spray impact between about four (4) and about five (5) seconds, resulting in an improvement to expected spray impact of sixty (60) to one hundred (100)%. Thus, Simulation 2 has a continual, uninterrupted surface impact that continually pushes the stream in a downward direction on the material being impacted by the spray and having the highest total surface spray impact dwell time. Further, compared to Simulation 1, Simulation 2 is able to utilize less than half the length of the cabinet that is required for Simulation 1, resulting in a more efficient use of space.
(53) Although specific examples have been illustrated and described herein, it will be appreciated by those of ordinary skill in the art that any arrangement calculated to achieve the same purpose could be substituted for the specific examples shown. This application is intended to cover adaptations or variations of the present subject matter. Therefore, it is intended that the present invention be defined by the attached claims and their legal equivalents.