Nutrient removal filtration system and method

Information

  • Patent Grant
  • 11253798
  • Patent Number
    11,253,798
  • Date Filed
    Tuesday, June 23, 2020
    3 years ago
  • Date Issued
    Tuesday, February 22, 2022
    2 years ago
  • Inventors
  • Original Assignees
    • Oldcastle Infrastructure, Inc. (Auburn, WA, US)
  • Examiners
    • Upton; Christopher
    Agents
    • Steinberger; Brian S.
    • Steinberger; Hilary F.
    • Law Offices of Brian S. Steinberger, P.A.
Abstract
Systems, devices, and methods for providing nutrient removals in an up flow filtration storm water system for treating water to very high clean levels using filtration media. A filtration media can be supported by a screen above a floor in a vault allows for incoming storm water to pass into a void space above the floor into the screen and filtration media and then out an outlet to the vault. The filtration media can include recyclable and/or natural particles. Layers of river rocks can be placed on top of and below the filtration media. The captured debris can drop to the floor. The long lasting filtration media can be cleaned by being backwashed.
Description
FIELD OF INVENTION

This invention relates to storm water treatment, and in particular to systems, devices, and methods for providing nutrient removals in an up flow filtration storm water system for treating water to high clean levels using filtration media and a screen, where captured debris slide down a sloped floor to a low point where the debris can be liquefied by water sprayers followed by being easily vacuum removed.


BACKGROUND AND PRIOR ART

Federal clean water requirements require water bodies such as lakes and rivers that must meet strict minimal water quality specifications. To achieve these requirements, storm water drainage pipes often require treatment before conveying storm water into receiving water bodies. As a result, a wide variety of technologies have been developed to treat storm water and improve the water quality.


Common storm water treatment systems are hydrodynamic separators such as baffle type boxes and vortex systems. Hydrodynamic separators can treat relatively large water flows and are good for removing solids that are relatively large in size. However, these types of systems are limited to the size of the pollutants being removed, and are not very efficient for removing dissolved pollutants such as dissolved phosphorus and nitrogen, etc.


To achieve water treatment beyond what can be accomplished by a hydrodynamic separator, another class of storm water treatment systems commonly referred to as filtration systems are used. Filtration systems typically will pass the water flow through a filter media such as sand, zeolite, activated carbon, and the like. Filter media is typically selected to do more than remove solids from the water flow. Depending on the pollutants of concern, filter media can be selected to remove specific dissolved pollutants such as nutrients, metals, or a wide variety of chemical contaminates.


However, a problem with using filter media in a storm water treatment system is the significant influence of friction between the water and the media. In addition, changing the direction of water flow as it passes through a filtration system reduces the kinetic energy of the water flow which will reduce the volume water flow. During big rain events a storm water filtration system in a storm water pipe can significantly inhibit the passage of water and cause flooding upstream from the filtration system. If the filtration system becomes clogged with debris the water flow can be completely stopped.


Typical filter media treatment has required the use of cartridge systems. See for example, U.S. Pat. No. 8,658,044 to Cobb, assigned to Contech Engineered Solutions LLC, and U.S. Published Patent Application 2015/0129473 to Kent. Generally in these types of systems, multiple individual cartridges are filled with media. Water flow is then passed through each of the cartridges and the cartridges collectively treat the water flow. The problem is that the size of the cartridges are limited to a size that can be removed from the vault during servicing. Additionally, there are void spaces between the cartridges, and these spaces are not able to be engaged in the treatment process.


The inventor of the subject application has used media in filters inside of storm water vaults. See for example, U.S. Pat. Nos. 8,034,234 and 8,231,780 to Happel, which are both incorporated by reference. In these patents filtration media cartridges are not being used. However, these patents and all the prior art have additional problems of what happens to the debris which will land spread out across the entire floor of the vault. Having to service debris that is located everywhere on the floor makes it difficult and time consuming to later remove that debris. For example, vacuum lines would need to be used throughout the entire floor. Additionally, the debris can remain in large sizes.


Thus, the need exists for solutions to the above problems with the prior art.


SUMMARY OF THE INVENTION

A primary objective of the present invention is to provide systems, devices, and methods for providing nutrient removals in an up flow filtration storm water system for treating water to high clean levels using filtration media and a screen, where captured debris slide down a sloped floor to a low point where the debris can be liquefied by water sprayers followed by being easily vacuum removed.


A secondary objective of the present invention is to provide systems, devices, and methods for providing nutrient removals in an up flow filtration storm water system for treating water to very high clean levels with filtration media, that can remove pollutants, such as nutrients, oils, phosphorus and nitrogen, where the filter media only needs to be back flushed during servicing and not removed as is required with cartridge filters.


A third objective of the present invention is to provide systems, devices, and methods for providing nutrient removals in an up flow filtration storm water system for treating water to very high clean levels with filtration media, that can remove pollutants, such as nutrients, oils, phosphorus and nitrogen, where the filter media servicing requires less labor, time and media replacement costs as compared to cartridge filters.


A fourth objective of the present invention is to provide systems, devices, and methods for providing nutrient removals in an up flow filtration storm water system for treating water to very high clean levels using filtration media, that can remove pollutants, such as nutrients, oils, phosphorus and nitrogen, where space under the filtration media can be serviced without having to send a technician into the vault saving time and labor.


A fifth objective of the present invention is to provide systems, devices, and methods for providing nutrient removals in an up flow filtration storm water system for treating water to very high clean levels using filtration media, that can accommodate different media types, and be easy to replace and changed out forming a train.


A sixth objective of the present invention is to provide systems, devices, and methods for providing nutrient removals in an up flow filtration storm water system for treating water to very high clean levels using filtration media, with hydrology that varies depending of flow rate.


A seventh objective of the present invention is to provide systems, devices, and methods for providing nutrient removals in an up flow filtration storm water system for treating water to very high clean levels using filtration media, that can be placed in line with existing pipes.


An eighth objective of the present invention is to provide systems, devices, and methods for providing nutrient removals in an up flow filtration storm water system for treating water to very high clean levels using a fluidized media bed that resists clogging.


A ninth objective of the present invention is to provide systems, devices, and methods for providing nutrient removals in an up-flow filtration storm water system for treating water to very high clean levels using filtration media, with easy to remove sediments falling into a settling chamber below media.


A tenth objective of the present invention is to provide systems, devices, and methods for providing nutrient removals in an up flow filtration storm water system for treating water to very high clean levels using filtration media, that can be added to existing treatment systems to improve removal efficiencies of baffle boxes, detention ponds, and spinner systems.


An eleventh objective of the present invention is to provide systems, devices, and methods for providing nutrient removals in an up-flow filtration storm water system for treating water to very high clean levels using filtration media, that is able to pass larger flows.


The novel filtration system can be used for removing a wide array of pollutants, including but not limited to the dissolved phosphorus, dissolved nitrogen, total suspended solids (TSS), nutrients, metals, bacteria, and oil.


A nutrient removal filtration system, can include a generally horizontal screen supported above a bottom of an in-flow vault, with a void space formed between the bottom and the screen, a filtration media resting on the screen, wherein storm water flowing into the vault through an inlet passes into the void space and up through the screen and filtration media and out the vault through an outlet, so that contaminants, metals, nutrients and solids are removed from the storm water by the filtration system, and a sloped floor on the bottom with a lower end adjacent to the inlet and a higher end adjacent to the outlet so that sediment and debris dropping from the filtration media lands on the sloped floor and slides downward toward the lower end of the sloped floor.


The nutrient removal filtration system can include a sprayer for directing water toward the lower end of the sloped floor to liquefy the debris.


The nutrient removal filtration system can include a source of high pressure water from outside the vault, and at least one for running the water to the sprayer.


The nutrient removal filtration system can include a vacuum for removing the liquefied debris from the lower end of the floor.


The filtration media can be selected from at least one of loose recyclable particles and loose natural particles.


The nutrient removal filtration system can include a first layer selected from at least one of loose rocks above the filtration media, and a screen on top of the filtration media, and a second layer of loose rocks between the filtration media and the screen.


The nutrient removal filtration system can include a baffle wall fixed to a front end of the filtration media supported on the screen, so that the baffle wall direct inlet water to flow to the void space under the screen.


The nutrient removal filtration system can include a floating skimmer movably attached to the baffle wall adjacent to the inlet to the vault.


A nutrient removal filtration system, can include a generally horizontal screen supported above a bottom of a treatment vault, with a void space formed between the bottom and the screen, a filtration media resting on the screen, wherein storm water flowing into the vault through an inlet passes into the void space and up through the screen and filtration media and out the vault through an outlet, so that contaminants, metals, nutrients and solids are removed from the storm water by the filtration system, a first side sloped floor on the bottom of the vault with an upper end adjacent to one side of the vault and a lower end adjacent to a middle portion of the vault, and a second side sloped floor on the bottom of the vault with an upper end adjacent to another side of the vault and a lower end adjacent to the middle portion of the vault, wherein sediment and debris from the screen and media falls and slides downward toward the lower end of the first sloped floor, and slides downward toward the lower end of the second sloped floor.


The nutrient removal filtration system can include a sprayer system for directing water, contaminants, metals, nutrients and solids toward the lower end of the first sloped floor and the lower end of the second sloped floor, and to move the debris toward a vacuum line in the vault.


The nutrient removal filtration system can include a source of high pressure water from outside the vault and lines for running the water to the sprayer.


The nutrient removal filtration system can include a left slope in the floor having a lower end adjacent to a left end of the vault and a high end adjacent to a middle of the vault, and a right slope in the floor having a lower end adjacent to a right end of the vault and a high end adjacent to the middle of the vault,


The filtration media can be selected from at least one of loose recyclable particles and loose natural particles.


The nutrient removal filtration system can include a first layer selected from at least one of loose rocks above the filtration media, and a screen on top of the filtration media, and a second layer of loose rocks between the filtration media and the screen.


The nutrient removal filtration system can include a baffle wall fixed to a front end of the filtration media supported on the screen, so that the baffle wall direct inlet water to flow to the void space under the screen.


The nutrient removal filtration system can include a floating skimmer movably attached to the baffle wall adjacent to the inlet.


A method of removing from a storm water vault, can include the steps of providing a generally horizontal screen supported above a floor of an in-flow vault, with a void space formed between the floor and the screen, providing a filtration media resting on the screen, providing the floor with at least one slope and with at least one high end and at least one lower end, directing storm water flowing into the vault through the inlet to pass into the void space and up through the screen and filtration media and out the vault through an outlet, directing debris from the screen and filtration media to slide down the at least one slope on the floor to the at least one lower end, and removing the debris from the at least one lower end of the at least one slope on the floor.


The at least one slope in the floor can include the lower end adjacent to the inlet and the higher end adjacent to the outlet so that sediment and debris dropping from the filtration media lands on the sloped floor and slides downward toward the lower end of the sloped floor.


The at least one sloped floor can include a first side sloped floor on the bottom of the vault with an upper end adjacent to one side of the vault and a lower end adjacent to a middle portion of the vault, a second side sloped floor on the bottom of the vault with an upper end adjacent to another side of the vault and a lower end adjacent to the middle portion of the vault, a left sloped floor having a low end adjacent to the inlet to the vault and a high end adjacent to a center of the vault, and a right sloped floor having a low end adjacent to the outlet to the vault and a high end adjacent to the center of the vault, so that sediment and debris from the screen and media falls and slides downward toward the lower end of the first side sloped floor and downward to the lower end of the left sloped floor, and the sediment and debris from the screen and media falls and slides downward toward the lower end of the second sloped floor and downward to the lower end of the right sloped floor.


The method can include the steps of liquefying the debris with a sprayer, and vacuuming the liquefied debris from the vault.


Further objects and advantages of this invention will be apparent from the following detailed description of the presently preferred embodiments which are illustrated schematically in the accompanying drawings.





BRIEF DESCRIPTION OF THE FIGURES


FIG. 1A is an upper front right perspective with partial front right cut-away view of the nutrient removing filtration system with floating skimmer and baffle wall.



FIG. 1B is a front right perspective view of the filtration system of FIG. 1A.



FIG. 2A is another upper front right perspective view of the filtration system of FIG. 1A without the floating skimmer.



FIG. 2B is a front right perspective view of the filtration system of FIG. 2A.



FIG. 3A if a front side view of the filtration system of FIG. 1A.



FIG. 3B is an inlet end view of the filtration system of FIG. 3A along arrow 3B.



FIG. 3C is a bottom view of the filtration system of FIG. 3A along arrow 3C.



FIG. 4A is another front side view of the filtration system of FIG. 1A showing the sloped floor without the floating skimmer, baffle wall, screen, filtration media and rock layers,



FIG. 4B is an inlet end view of the filtration system of FIG. 4A along arrow 4B.



FIG. 4C is a top view of the filtration system of FIG. 4A along arrow 4C.



FIG. 5 is an upper front right perspective view partial cut-away of the FIG. 1A filtration system showing the baffle wall and screen and sloped floor without the filtration media.



FIG. 6A is a front side view of a second embodiment of the nutrient removal filtration system with a first slope floor and second sloped floor.



FIG. 6B is a top view of the filtration system of FIG. 6A along arrow 6B.



FIG. 6C is an inlet end view of the filtration system of FIG. 6A along arrow 6C.



FIG. 6D is an outlet end view of the filtration system of FIG. 6A along arrow 6D.





DESCRIPTION OF THE PREFERRED EMBODIMENTS

Before explaining the disclosed embodiments of the present invention in detail it is to be understood that the invention is not limited in its applications to the details of the particular arrangements shown since the invention is capable of other embodiments. Also, the terminology used herein is for the purpose of description and not of limitation.


In the Summary above and in the Detailed Description of Preferred Embodiments and in the accompanying drawings, reference is made to particular features (including method steps) of the invention. It is to be understood that the disclosure of the invention in this specification does not include all possible combinations of such particular features. For example, where a particular feature is disclosed in the context of a particular aspect or embodiment of the invention, that feature can also be used, to the extent possible, in combination with and/or in the context of other particular aspects and embodiments of the invention, and in the invention generally.


In this section, some embodiments of the invention will be described more fully with reference to the accompanying drawings, in which preferred embodiments of the invention are shown. This invention may, however, be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will convey the scope of the invention to those skilled in the art. Like numbers refer to like elements throughout, and prime notation is used to indicate similar elements in alternative embodiments.


A list of components will now be described.



1 first embodiment filtration removal system



2 vault front end



3 inlet/inflow pipe



4 vault sides



5 access hatches



6 vault floor



8 vault rear end



9 outlet/outflow pipe



10 floating skimmer



15 baffle wall



17 baffle support



19 support angle



20 screen panel



30 first rock layer or screen



35 limestone layer



40 filtration media



50 second rock layer



55 limestone layer



60 sloped floor



65 slope support(s) for sloped floor



70 sprayers



80 water lines



100 second embodiment filtration removal system



110 first side sloped floor



120 second side sloped floor



130 left sloped floor



140 right sloped floor



150 middle baffle



FIG. 1A is an upper front right perspective with partial front right cut-away view of the nutrient removing filtration system 1 with floating skimmer 10 and baffle wall 15. FIG. 1B is a front right perspective view of the filtration system 1 of FIG. 1A. FIG. 2A is another upper front right perspective view of the filtration system 1 of FIG. 1A without the floating skimmer 10. FIG. 2B is a front right perspective view of the filtration system 1 of FIG. 2A.



FIG. 3A if a front side view of the filtration system 1 of FIG. 1A. FIG. 3B is an inlet end view of the filtration system 1 of FIG. 3A along arrow 3B. FIG. 3C is a bottom view of the filtration system 1 of FIG. 3A along arrow 3C.



FIG. 4A is another front side view of the filtration system 1 of FIG. 1A showing the sloped floor 60 without the floating skimmer 10, baffle wall 15, screen panel 20, filtration media 40 and rock layers 30, 50, FIG. 4B is an inlet end view of the filtration system 1 of FIG. 4A along arrow 4B. FIG. 4C is a top view of the filtration system 1 of FIG. 4A along arrow 4C.



FIG. 5 is an upper front right perspective view partial cut-away of the FIG. 1A filtration system 1 showing the baffle wall 15 and screen panel 20 and sloped floor 60 without the filtration media 40.


Referring to FIGS. 1A to 5, the filtration system 1 can be located inside a vault having a vault front end wall 2 having an inlet (inflow pipe) 3, vault sides 4, vault floor 6 and vault rear end wall 8 having an outlet (outflow pipe) 9, and access hatches 5 on top of the vault. Storm water can pass into the vault through inlet (inflow pipe) 3 and out the vault through outlet (outflow pipe) 9.


A fixed baffle wall 5 supported by baffle wall support(s) 17 can direct the storm water into a void space between a raised screen panel 20 and the vault floor 6. Attached to an upper end of the baffle wall 5 can be a floating skimmer 10, such as but not limited to the floating skimmer shown and described in U.S. Pat. No. 8,231,780 to Happel, who is the same inventor of the subject application, and which is incorporated by reference. The floating skimmer 10 can rise with the level of storm water in the vault to further prevent incoming storm water from spilling over the top of the upper rock layer 30. The invention is used where incoming storm water is directed down the baffle 15 to pass into the void space between vault floor 6 and screen panel 20 and move upward into the screen panel 20 and rock layers 30 and 50 which sandwich filtration media 40.


The screen panel 20 can be supported above vault floor 6 by support angle(s) 19. The screen panel 20 can be a metal screen having openings of approximately ¼ inch. On top of the screen panel 20 can be a lower layer of rocks 50, such as but not limited to river rocks, such as #57 stone, and the like, followed by filtration media 40 with an upper layer of rocks 30, such as but not limited to river rocks, such as #57 stone, on top of the filtration media layer 40. The filtration media can be approximately 2 inches to approximately 4 inches deep, with individual particles sizes of approximately ⅛ inch to approximately inch in size. Each of the rocks in the upper rock layer 30 and lower rock layer 50 can be up to approximately twice the size of the particles used in the filtration media.


The filtration media can include particles described in U.S. Pat. Nos. 7,955,507 and 8,002,984 both to Wanielista et al., which are both incorporated by reference.


The filtration media can include a sorption media composition consisting of: at least two of a recycled material and a naturally occurring material. The recycled material can be selected from a group consisting of tire crumb, wood sawdust and compost. The naturally occurring material can be selected from a group consisting of sand, limestone, sandy clay, expanded clay, and peat


The filtration media can include the combination of one or more recycled materials in combination with one or more naturally occurring materials. The one or more recycled materials can be selected from a group consisting of selected from a group consisting of tire crumb, sawdust, orange peel, coconut husks, leaf compost, crushed oyster shell, soy bean hulls, tree bark, wood chips, paper, alfalfa, mulch, cotton and wheat straw. The one or more of a naturally occurring materials can be selected from a group consisting of peat, sand, zeolites, limestone, sulfur and clay mixed with the one or more recycled materials.


The filtration media can include other types of material such as but not limited to zeolite, corn cob, wood chips, expansion shale, perlite and combinations thereof.


The rocks used in the rock layers 30, 50 can provide a horizontal conveyance for water passing upward. The top rock layer 30 can be primarily used as a weight to hold down the loose particles in the filtration media layer 40. A second screen panel can be used instead of the top rock layer 30. The bottom rock layer 50 can support the particles of filter media 40 from falling through.


The flow of storm water through the filtration system can function similarly the Floating Skimmer Apparatus with Up-Flow Filter shown and described in reference to U.S. Pat. No. 8,034,234 to Happel, which is the same inventor as in the subject invention, which is incorporate by reference.


The subject invention incorporates a novel sloped floor 60 supported from the vault floor 6 by slope supports 65, with the raised screen panel 20, and rock layers 30, 50 which sandwich a filtration media 40 therebetween. Water lines 80 can direct pressurized water from outside the vault to sprayers 70 that can be located under the screen panel 20 at the low point of the sloped floor 60 and at different positions above and the sloped floor between the vault front end 2 and the vault rear end 8. The lines of sprayers 70 can include


The novel invention allows for the void space between the screen panel 20 and the vault floor 6 to be more easily serviced.


Debris passing into the vault can easily become captured in this space. In addition pollutants and nutrients can be prevented from rising upward through the screen panel 20, lower rock layer 50, filtration media layer 40 and top rock layer 30. The sloped floor 60 allows for sediment and debris and other pollutants to drop from the screen panel 20, rock layers 30, 50 and filtration media 40 to land on the sloped floor 60 and slide downward toward the lower end of the sloped floor 60. The sprayers 70 can further move the debris and pollutants to slide down the sloped floor 60. The sprayers 70 can have pressures of approximately 300 PSI and up.


The sprayers 70 can liquefy the captured debris which will also allow it to easily slide down the sloped floor 60. A vacuum truck with vacuum line having a lower end positioned adjacent the low point of the sloped floor 60 so that the small and liquefied debris can be easily vacuumed out of the vault.


The sprayers 70 can be attached to sidewalls of the vault, as well as to the floor. The sprayers 70 that can be single pipes with holes, and connected to water lines 80. The locations and positions of the sprayers 70 can be arranged in various configurations and arrangements, as shown and described in U.S. patent application Ser. No. 14/288,455 filed May 28, 2014, to the same inventor of the subject application, which is incorporated by reference.


The filtration media 40 and rock layers 30, 50 can be periodically cleaned by backwashing water through the vault, which can include running water from above the top layer of rocks 30 through the filtration media 40 and bottom rock layer 50.


The novel filtration system 1 avoids technology that avoids typical head losses during high flow events. This enables the placement of filtration media in line with existing pipes without a significant impact on flow. The filtration media bed is in an up flow fluidized configuration which enables the system to be resistant to clogging.


In no flow states, which are between rain events, the filtration media and rock layers remain stable. Typically for nutrient specific granular media, biological activity on the surface of the media and water begin to consume contaminants captured by the media, and over time the denitrification process accelerates. Every time the rain event begins and ends the media can shift and break apart any clogs that may have begun to form in the media


During low to medium flows, all the water flow is directed to force water up through the filtration media and rock layers. Sediments and other solids will settle into the lower void space below the filtration media and rock layers.


During high flows the float skimmer rises and water can flow over the top of the filtration media and rock layers to the outlet of the vault.



FIG. 6A is a front side view of a second embodiment of the nutrient removal filtration system 100 with a first slope floor 110 and second sloped floor 120. FIG. 6B is a top view of the filtration system 100 of FIG. 6A along arrow 6B. FIG. 6C is an inlet end view of the filtration system 100 of FIG. 6A along arrow 6C. FIG. 6D is an outlet end view of the filtration system 100 of FIG. 6A along arrow 6D.


Referring to FIGS. 6A to 6D, the second embodiment filtration system 100 can include similar components to the previous embodiment. Here, the floor can include a first side sloped floor 110 and a second side sloped floor 120, as well as a left sloped floor 130 and a right sloped floor 140.


The first side sloped floor 110 on the bottom of the vault can have an upper end adjacent to one side of the vault and a lower end adjacent to a middle portion of the vault. The second side sloped floor 120 on the bottom of the vault can have an upper end adjacent to another side of the vault and a lower end adjacent to the middle portion of the vault. A left sloped floor 130 can have a low end adjacent to the inlet to the vault and a high end adjacent to a center of the vault supported by a middle baffle 150. A right sloped floor 140 can have a low end adjacent to the outlet to the vault and a high end adjacent to the center of the vault supported by the middle baffle 150.


Sediment and debris from the screen and media can fall and slide downward toward the lower end of the first side sloped floor 110 and downward to the lower end of the left sloped floor 130 in a downward funnel configuration. Sediment and debris from the screen and media can also fall and slides downward toward the lower end of the second sloped floor 120 and downward to the lower end of the right sloped floor 149 also in a downward funnel configuration.


Although not shown, sprayers 80 can be positioned to both liquefy and direct the debris and pollutants to the front inlet end 2 and rear inlet end 8 of the vault for pickup by vacuum lines similar to the previous embodiment.


In addition the rock layers 30, 50 can be replaced with limestone layers 35, 55. In addition a screened panel 20 can also be used in a similar configuration to the previous embodiment.


The storm water treatment vaults can be retrofitted with slope floors (subfloors. Additionally, the floors of the storm water treatment vaults can be concrete poured into sloped surfaces when the vaults are built.


While the invention has been described, disclosed, illustrated and shown in various terms of certain embodiments or modifications which it has presumed in practice, the scope of the invention is not intended to be, nor should it be deemed to be, limited thereby and such other modifications or embodiments as may be suggested by the teachings herein are particularly reserved especially as they fall within the breadth and scope of the claims here appended.

Claims
  • 1. A nutrient removal filtration system, comprising: a generally horizontal lower metal screen having openings of approximately ¼ inch, supported above a bottom of an in-flow vault, with a void space formed between the bottom and the screen;a lower layer of loose rocks on the lower metal screen;a filtration media of particles resting on the lower layer of loose rocks, the filtration media of particles includes a combination of loose recyclable particles and loose natural particles, wherein storm water flowing into the vault through an inlet passes into the void space and up through the screen and filtration media and out the vault through an outlet, so that contaminants, metals, nutrients and solids are removed from the storm water by the filtration system.
  • 2. The nutrient removal filtration system of claim 1, further comprising; an upper layer of loose rocks above the filtration media of particles.
  • 3. The nutrient removal filtration system of claim 2 further comprising: a top metal screen having openings of approximately ¼″ on top of the second layer of loose rocks.
  • 4. The nutrient removal filtration system of claim 2, wherein the upper layer of loose rocks include river rocks.
  • 5. The nutrient removal filtration system of claim 2, wherein each of the lower layer of rocks and each of the upper layer of rocks is up to approximately twice the size of filtration media particles.
  • 6. The nutrient removal filtration system of claim 1, further comprising: a top metal screen having openings of approximately ¼″ above the filtration media.
  • 7. The nutrient removal filtration system of claim 1, wherein the lower layer of loose rocks include river rocks.
  • 8. The nutrient removal filtration system of claim 1, wherein the loose recyclable particles are selected from a group comprising tire crumb, sawdust, orange peel, coconut husks, leaf compost, crushed oyster shell, soy bean hulls, tree bark, wood chips, paper, alfalfa, corn, mulch, cotton and wheat straw, and the loose natural particles are selected from another group comprising peat, sand, zeolites, limestone, sulfur and clay mixed with the one or more recycled materials.
  • 9. The nutrient removal filtration system of claim 1, wherein the filtration media of particles is approximately 2 inches to approximately 4 inches deep.
  • 10. The nutrient removal filtration system of claim 1, wherein the filtration media of particles includes particle sizes of between approximately ⅛ of an inch to approximately ½ inch in size.
  • 11. The nutrient removal filtration system of claim 1, wherein each of the lower layer of rocks is up to approximately twice the size of filtration media particles.
  • 12. A nutrient removal filtration system, comprising: a generally horizontal lower metal screen having openings of approximately ¼ inch supported above a bottom of a treatment vault, with a void space formed between the bottom and the screen;a filtration media of particles resting on the lower metal screen, the filtration media of particles includes a combination of loose recyclable particles and loose natural particle, wherein storm water flowing into the vault through an inlet passes into the void space and up through the screen and filtration media and out the vault through an outlet, so that contaminants, metals, nutrients and solids are removed from the storm water by the filtration system;a floor on the bottom of the vault wherein sediment and debris from the screen and media falls and slides to the floor.
  • 13. The nutrient removal filtration system of claim 12 further comprising: a generally horizontal top metal screen having openings of approximately ¼ inch on top of the filtration media of particles.
  • 14. The nutrient removal filtration system of claim 12, wherein the loose recyclable particles are selected from a group comprising tire crumb, sawdust, orange peel, coconut husks, leaf compost, crushed oyster shell, soy bean hulls, tree bark, wood chips, paper, alfalfa, corn, mulch, cotton and wheat straw, and the loose natural particles are selected from another group comprising peat, sand, zeolites, limestone, sulfur and clay mixed with the one or more recycled materials.
  • 15. The nutrient removal filtration system of claim 12, further comprising: a first layer of a combination of loose rocks and a first limestone layer above the filtration media of particles, anda generally horizontal top metal screen having openings of approximately ¼ inches on top of the filtration media of particles.
  • 16. The nutrient removal filtration system of claim 15, further comprising: a second layer selected from another combination of additional loose rocks and a second limestone layer, between the filtration media and the generally horizontal top metal screen.
  • 17. A nutrient removal filtration system, consisting of: a generally horizontal lower metal screen having openings of approximately ¼ inch, supported above a bottom of an in-flow vault, with a void space formed between the bottom and the screen;a lower layer of loose river rocks on the lower metal screen;
  • 18. A nutrient removal filtration system, consisting of: a generally horizontal lower metal screen having openings of approximately ¼ inch, supported above a bottom of an in-flow vault, with a void space formed between the bottom and the screen;a lower layer of loose river rocks on the lower metal screen;a filtration media of particles resting on the lower layer of loose rocks, the filtration media of particles includes a combination of loose recyclable particles and loose natural particles, wherein storm water flowing into the vault through an inlet passes into the void space and up through the screen and filtration media and out the vault through an outlet, so that contaminants, metals, nutrients and solids are removed from the storm water by the filtration system,wherein the filtration media of particles includes particle sizes of between approximately ⅛ of an inch to approximately ½ inch in size,wherein each of the lower layer of rocks is up to approximately twice the size of filtration media particles; anda generally horizontal top metal screen having openings of approximately ¼ inches on top of the filtration media of particles.
  • 19. A nutrient removal filtration system, consisting of: a generally horizontal lower metal screen having openings of approximately ¼ inch, supported above a bottom of an in-flow vault, with a void space formed between the bottom and the screen;a lower layer of loose river rocks on the lower metal screen;a filtration media of particles resting on the lower layer of loose rocks, the filtration media of particles includes a combination of loose recyclable particles and loose natural particles, wherein storm water flowing into the vault through an inlet passes into the void space and up through the screen and filtration media and out the vault through an outlet, so that contaminants, metals, nutrients and solids are removed from the storm water by the filtration system,wherein the filtration media of particles includes particle sizes of between approximately ⅛ of an inch to approximately ½ inch in size; andan upper layer of loose river rocks on top of the filtration media of particles, wherein each of the lower layer of rocks and each of the upper layer of loose river rocks is up to approximately twice the size of filtration media particle.
CROSS REFERENCE TO RELATED APPLICATIONS

This application is a Divisional of U.S. patent application Ser. No. 15/952,803 filed Apr. 13, 2018, which is a Divisional of U.S. patent application Ser. No. 15/248,202 filed Aug. 26, 2016, now U.S. Pat. No. 10,183,240, which is a Continuation-In-Part of U.S. patent application Ser. No. 14/288,455 filed May 28, 2014, abandoned, which claims the benefit of priority to U.S. Provisional Patent Application Ser. No. 61/828,958 filed May 30, 2013. The entire disclosure of each of the applications listed in this paragraph are incorporated herein by specific reference thereto.

US Referenced Citations (222)
Number Name Date Kind
122209 Ashman Dec 1871 A
232948 Dernham Oct 1880 A
587559 Riley Aug 1897 A
664945 Guion Jan 1901 A
783556 Van Buskirk Feb 1905 A
809201 Lutz Jan 1906 A
838129 Mikolasek Dec 1906 A
920961 Keil May 1909 A
1060338 Gschwind Apr 1913 A
1442348 McDermet Jan 1923 A
2102310 Egan Dec 1937 A
2182795 Day Dec 1939 A
2263259 Boosey Nov 1941 A
2360961 Mayo Oct 1944 A
2436793 Danel Mar 1948 A
2485755 Loosli Oct 1949 A
2559784 Moore Jul 1951 A
2615526 Lane Oct 1952 A
2652946 Beatty Sep 1953 A
2796988 Loffler Jun 1957 A
3091339 Marra May 1963 A
3237915 Palmer Mar 1966 A
3237975 Stahley Mar 1966 A
3282430 Kinne Nov 1966 A
3527348 Henri Sep 1970 A
3631983 Mail Jan 1972 A
4024881 Weiland et al. May 1977 A
4070863 Brown Jan 1978 A
4189386 Aman Feb 1980 A
4198717 Kessel Apr 1980 A
4278190 Oory et al. Jul 1981 A
4297219 Kirk et al. Oct 1981 A
4308141 Clendenen Dec 1981 A
4326952 Blake Apr 1982 A
4422931 Wolde-Michael Dec 1983 A
4509717 Wright et al. Apr 1985 A
4668405 Boze May 1987 A
4689145 Mathews et al. Aug 1987 A
4722800 Aymong Feb 1988 A
4738644 Happel Apr 1988 A
4765889 Grujanac Aug 1988 A
4785966 Waltke Nov 1988 A
4891128 Goronszy Jan 1990 A
4895653 Cherochak Jan 1990 A
5034122 Wiesemann Jul 1991 A
5037541 Ruey-Jang et al. Aug 1991 A
5069781 Wilkes Dec 1991 A
5133619 Murfae et al. Jul 1992 A
5232587 Hegemier et al. Aug 1993 A
5284580 Shyh Feb 1994 A
5372714 Logue, Jr. Dec 1994 A
5378376 Zenner Jan 1995 A
5397464 Hannon Mar 1995 A
5403474 Emery Apr 1995 A
5405539 Schneider Apr 1995 A
5480254 Autry et al. Jan 1996 A
5486287 Murphy et al. Jan 1996 A
5518024 Weeks et al. May 1996 A
5535554 Harris, Jr. Jul 1996 A
5562819 Turner, Jr. et al. Oct 1996 A
5575925 Logue, Jr. Nov 1996 A
5632889 Tharp May 1997 A
5643445 Billias et al. Jul 1997 A
5670039 Harris Sep 1997 A
5779888 Bennett Jul 1998 A
5810510 Urriola Sep 1998 A
5820762 Bamer et al. Oct 1998 A
5855774 Boelter Jan 1999 A
5904842 Billias et al. May 1999 A
5980740 Harms et al. Nov 1999 A
5985157 Leckner et al. Nov 1999 A
6032421 Yamada Mar 2000 A
6077448 Tran-Quoc-Nam et al. Jun 2000 A
6086756 Roy Jul 2000 A
6086758 Schilling et al. Jul 2000 A
6099743 Pedersen Aug 2000 A
6106706 Roy et al. Aug 2000 A
6106707 Morris et al. Aug 2000 A
6149803 DiLoreto, Jr. et al. Nov 2000 A
6178565 Franco Jan 2001 B1
6190545 Williamson Feb 2001 B1
6200484 McInnis Mar 2001 B1
6231758 Morris et al. May 2001 B1
6270663 Happel Aug 2001 B1
6287459 Williamson Sep 2001 B1
6294095 Lewis Sep 2001 B1
6315897 Maxwell Nov 2001 B1
6334953 Singleton Jan 2002 B1
6379541 Nicholas Apr 2002 B1
6428692 Happel Aug 2002 B2
6478954 Turner, Jr. et al. Nov 2002 B1
6517709 Cardwell et al. Feb 2003 B1
6531059 Morris et al. Mar 2003 B1
6537446 Sanguinetti Mar 2003 B1
6551023 Allard Apr 2003 B2
6562233 Schilling et al. May 2003 B1
6638424 Stever et al. Oct 2003 B2
6651825 Turner, Jr. et al. Nov 2003 B2
6666974 Page Dec 2003 B2
6668390 Gonzalez Dec 2003 B1
6733665 Khalil May 2004 B1
6767456 Middleton et al. Jul 2004 B2
6780310 Howe Aug 2004 B1
6797161 Use et al. Sep 2004 B2
6797162 Happel Sep 2004 B2
6800195 Batten et al. Oct 2004 B1
6824677 Martinez Nov 2004 B2
6866153 Turner, Jr. et al. Mar 2005 B2
6869525 Happel Mar 2005 B1
6872029 Allard et al. Mar 2005 B2
6884343 Harris et al. Apr 2005 B2
6936163 Use et al. Aug 2005 B2
6939461 Use et al. Sep 2005 B2
6951607 Use et al. Oct 2005 B2
6974540 Fleischmann Dec 2005 B1
6976808 Allard Dec 2005 B2
6979148 Happel et al. Dec 2005 B2
6986621 Allard Jan 2006 B2
6994783 Use et al. Feb 2006 B2
6998039 Harris et al. Feb 2006 B2
7005060 Pitt et al. Feb 2006 B2
7011743 Use et al. Mar 2006 B2
7083721 McClure et al. Aug 2006 B2
7094337 Williams et al. Aug 2006 B2
7094338 Morris et al. Aug 2006 B2
7112274 Sanguinetti Sep 2006 B1
7128341 Dahl et al. Oct 2006 B1
7128832 Wade Oct 2006 B2
7132045 Trangsrud Nov 2006 B1
7153417 Happel Dec 2006 B2
7156987 Sanguinetti Jan 2007 B1
7270747 Happel et al. Sep 2007 B2
7282142 Kraft Oct 2007 B2
7288188 Al-Assfour Oct 2007 B2
7294256 Happel et al. Nov 2007 B2
7309420 Trangsrud Dec 2007 B1
7328809 Gigas et al. Feb 2008 B2
7396471 Wimberger Jul 2008 B2
7488414 Wimberger Feb 2009 B2
7494585 Nino Feb 2009 B2
7524414 Barragan Apr 2009 B1
7658857 Wacome Feb 2010 B2
7662280 Cooney Feb 2010 B1
7722763 Benty et al. May 2010 B2
7771591 Lucas Aug 2010 B2
7785464 Happel Aug 2010 B2
7815800 Komatsu Oct 2010 B2
7824551 Wanielista et al. Nov 2010 B2
7846327 Happel et al. Dec 2010 B2
7883620 Owen Feb 2011 B2
7897047 Wanielista et al. Mar 2011 B2
7927484 Wanielista et al. Apr 2011 B2
7955507 Wanielista et al. Jun 2011 B2
7959799 Happel et al. Jun 2011 B2
7981283 Happel et al. Jul 2011 B2
7981300 Wacome Jul 2011 B2
8002984 Wanielista et al. Aug 2011 B1
8002985 Wanielista et al. Aug 2011 B1
8017006 Lopez Sep 2011 B2
8034234 Happel Oct 2011 B2
8034236 Happel Oct 2011 B1
8034237 Happel et al. Oct 2011 B2
8038879 Kraft Oct 2011 B2
8051568 Moody et al. Nov 2011 B2
8083937 Happel Dec 2011 B2
8101079 Wanielista et al. Jan 2012 B1
8142666 Happel Mar 2012 B1
8153005 Wanielista et al. Apr 2012 B1
8216453 Moody et al. Jul 2012 B2
8221632 McInnis et al. Jul 2012 B2
8231780 Happel Jul 2012 B2
8252182 Chang et al. Aug 2012 B1
8366923 Happel Feb 2013 B1
8393827 Happel Mar 2013 B1
8425150 Happel Apr 2013 B1
8491797 Happel Jul 2013 B1
8622652 Happel Jan 2014 B1
8651767 Happel Feb 2014 B1
8658044 Cobb Feb 2014 B2
8974144 Happel Mar 2015 B1
9068312 Happel Jun 2015 B1
9340965 Happel May 2016 B2
9534368 Happel Jan 2017 B1
10155670 Happel Dec 2018 B1
10183240 Happel Jan 2019 B1
10202285 Happel Feb 2019 B1
10238993 Happel Mar 2019 B1
10260222 Happel Apr 2019 B1
10287768 Happel May 2019 B1
10384956 Happel Aug 2019 B1
10472815 Happel Nov 2019 B1
20010047954 Happel Dec 2001 A1
20030026659 Wu Feb 2003 A1
20030089652 Matsui et al. May 2003 A1
20030121846 Use et al. Jul 2003 A1
20030132150 Happel Jul 2003 A1
20030136717 Tseng Jul 2003 A1
20030172487 Thompson et al. Sep 2003 A1
20030175079 Happel et al. Sep 2003 A1
20040065601 Martinez Apr 2004 A1
20040222159 Peters et al. Nov 2004 A1
20040226869 McClure et al. Nov 2004 A1
20050051499 Nino Mar 2005 A1
20050069386 Happel et al. Mar 2005 A1
20050183997 Happel et al. Aug 2005 A1
20050218049 Happel Oct 2005 A1
20060016767 Olson et al. Jan 2006 A1
20060096935 Harding May 2006 A1
20060163130 Happel et al. Jul 2006 A1
20060201860 Happel et al. Sep 2006 A1
20060207922 Dussich Sep 2006 A1
20090045135 Khudenko et al. Feb 2009 A1
20090114579 Dyer May 2009 A1
20090134081 Happel et al. May 2009 A1
20090166279 Happel et al. Jul 2009 A1
20100032363 Happel Feb 2010 A1
20100078370 Happel Apr 2010 A1
20110168612 Happel Jul 2011 A1
20110278237 McInnis Nov 2011 A1
20140352729 Happel Dec 2014 A1
20150129473 Kent May 2015 A1
20190078310 Kent Mar 2019 A1
Foreign Referenced Citations (2)
Number Date Country
2916458 Nov 2008 FR
2004353407 Dec 2004 JP
Non-Patent Literature Citations (5)
Entry
Bio-Clean, Submittal Drawings to Lake County, Florida from Bio-Clean, a Forterra Company, regarding Magnolia Lane Drainage, submitted Mar. 7, 2017, 8 pages.
Bio-Clean, Final Project Drawings approved by Lake County, Florida from Bio-Clean, a Forterra Company, regarding Magnolia Lane Drainage, Mar. 23, 2017, 1 page.
Rising and Non-Rising Stem, Telescoping Valves, Halliday Products, retrieved on Jun. 15, 2009, retrieved from www.hallidayproducts.com/ssg.html, 4 pages.
Aluminum Slide and Weir Glass, Water, and Waste Water Valves and Gates, retrieved on Jun. 15, 2009, retrieved from http://ncvg.net/products/alumslideweir.html, 10 pages.
Happel, T., Utility U.S. Appl. No. 14/151,284, filed Jan. 9, 2014; Office Action Summary dated Dec. 24, 2014, 12 pages.
Related Publications (1)
Number Date Country
20200316496 A1 Oct 2020 US
Provisional Applications (1)
Number Date Country
61828958 May 2013 US
Divisions (2)
Number Date Country
Parent 15952803 Apr 2018 US
Child 16908888 US
Parent 15248202 Aug 2016 US
Child 15952803 US
Continuation in Parts (1)
Number Date Country
Parent 14288455 May 2014 US
Child 15248202 US