Apparatus, methods, and system for treatment of stormwater and waste fluids
09663936 ยท 2017-05-30
Assignee
Inventors
Cpc classification
Y10T29/49716
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
E03F5/14
FIXED CONSTRUCTIONS
C02F1/40
CHEMISTRY; METALLURGY
B01D21/2483
PERFORMING OPERATIONS; TRANSPORTING
C02F2303/24
CHEMISTRY; METALLURGY
International classification
E03F5/14
FIXED CONSTRUCTIONS
B01D21/24
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A stormwater treatment unit comprising a containment vault having an inlet and an outlet separates debris from a flow of stormwater through the unit. The water flow is controlled by a wall which directs flow from the inlet to the outlet through a reservoir of fluid in the unit. Debris separation by density occurs whereby lighter elements such as oil float on top of the fluid and heavier elements such as sediment collect at the bottom of the unit or in collectors in the reservoir. A wire mesh, deflector, and/or ripple boards placed beneath the inlet further increase efficiency of the separation, and a vent pipe is placed above the outlet to release pressure built up in the outlet during operation. A stormwater treatment system and method of retrofitting an existing stormwater trunk line locates the stormwater treatment unit in an off-line position from an existing drainage trunk line.
Claims
1. A fluid treatment apparatus for treating an inlet fluid, comprising: a separation container connected to an inlet pipe and to an outlet pipe wherein said outlet pipe is at a position lower in said container than said inlet pipe; a wall within said container between said inlet pipe and said outlet pipe; said wall defining a top space between a top of said wall and a top interior surface of said container; said wall defining a bottom space between a bottom of said wall and a bottom interior surface of said container; and a first collector within said container and located under said inlet pipe comprising a plurality of sediment receptacles, wherein said first collector comprises a grooved collector.
2. The fluid treatment apparatus of claim 1, wherein the sediment receptacles are arranged in a periodic pattern.
3. The fluid treatment apparatus of claim 1, wherein said grooved collector presents a saw-toothed cross section.
4. The fluid treatment apparatus of claim 1, further comprising a second collector within said container and located at a lower level than said first collector.
5. The fluid treatment apparatus of claim 1, further comprising a drain pipe extending downward from said outlet pipe.
6. The fluid treatment apparatus of claim 5, wherein an opening in said drain pipe faces upward.
7. The fluid treatment apparatus of claim 5, further comprising a vent pipe extending upward from said outlet pipe.
8. The fluid treatment apparatus of claim 1, wherein said first collector is adjacent said wall.
9. The fluid treatment apparatus of claim 1, wherein said first collector is a stainless steel collector.
Description
BRIEF DESCRIPTION
(1)
(2)
(3)
(4)
(5)
(6)
(7)
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
(8) Embodiments of the present invention are hereafter described in detail with reference to the accompanying figures and are provided for purposes of illustration only and not for the purpose of limiting the invention as defined by the appended claims and their equivalents. Descriptions of well-known functions and constructions are omitted for clarity and conciseness. The figures are meant to illustrate features of exemplary embodiments of the invention and are not drawn to scale.
(9)
(10) Stormwater treatment unit 100 is housed in containment vault 101. Preferably, the dimension of the vault is 6 long7 wide84 tall, and the vault is made of liquid-impermeable concrete with walls that are 6 thick. The dimensions of the vault can be adjusted depending on the application and can be made of other suitable materials such as metal or plastic. The interior of the vault defines a chamber 150.
(11) Containment vault 101 has three openings connecting to chamber 150: inlet 110, outlet 120, and access opening 105. Inlet 110 is placed on one side of chamber 150 and is preferably 12 in diameter and is fitted with a similarly sized pipe 111. Outlet 120 is placed on the opposite side of chamber 150 and is preferably 12 in diameter and is also fitted with a similarly sized pipe 121. Access opening 105, preferably in the form of a manhole, is preferably located at the top of vault 101 and is fitted with a cover. Preferably, materials for the pipes can be PVC, metal, or other types of materials suitable for use with the fluids and contaminants anticipated. Inlet 110, outlet 120, and the pipes 111 and 121 can be of other suitable sizes to accommodate different volumes of fluid and flow rates.
(12) In a preferred embodiment, inlet 110 is positioned at about five inches higher than outlet 120. Inlet 110 and outlet 120 are thus very similar in height, allowing for a shallow installation of the unit in areas with a high water table that cannot support a large difference in height between inlet 110 and outlet 120.
(13) Outlet pipe 121 extends through outlet 120 and bends downward toward the bottom of chamber 150 in vault 101. Inlet 122 of pipe 121 faces downward towards the bottom of chamber 150. Outlet pipe 121 is separated from chamber 150 by wall 140. Wall 140 preferably extends from above outlet 120 to a position midway between outlet 120 and the bottom of chamber 150 allowing liquid in chamber 150 to flow to pipe 121. The height of inlet 122 is at or above the lower end of wall 140. Optionally, portions of outlet pipe 121 below outlet 120 may be perforated to further diffuse the draw of liquid by allowing liquid to enter through the sides of pipe 121.
(14) If the outlet 123 of pipe 121 extends lower than water level 160 (as is normally expected to allow flow through pipe 121), the flow of water in pipe 121 could create a siphon that would draw down the water level 160 in chamber 150 to the height of inlet 122 of outlet pipe 121. Vent pipe 130 connects to and extends upward from outlet pipe 121. Vent pipe 130 allows airflow into pipe 121 to avoid the creation of a siphon during high volume flows. Alternatively, pipe 121 could be perforated below water level 160 to allow airflow if water level 160 falls below the bottom of outlet 120 and reduce or avoid a siphon effect.
(15) A space exists between the top of wall 140 and the top of chamber 150 to allow air flow near vent pipe 130 and to prevent the siphoning effect. Wall 140 further serves as a physical barrier to protect pipe 121 from the pressure of inlet water and debris flowing from inlet pipe 111. Wall 140 is preferably made of stainless steel, plastic, or other material suitable for use with the fluids and contaminants anticipated.
(16) Wire mesh 171 is located beneath inlet pipe 111 and is preferably above the lowest part of the outlet 120. Due to the equalization of pressures, water level 160 should normally be at the level of the lowest part of outlet 120 as a higher water level should cause a flow out of outlet pipe 121. Wire mesh 171 is preferably located above water line 160 and separates out large debris from the inlet stream of stormwater. Wire mesh 171 is preferably a metal grate or wire mesh with suitably-sized holes to collect debris from the inlet fluid at the top of the wire mesh while allowing smaller debris, particles, and fluids to flow through. Wire mesh 171 collects leaves and other large clumps of biomass above the water level, and prevents the collected debris from soaking in the liquid in chamber 150 or floating at the water level 160. By keeping the biomass on wire mesh 171 out of the pool of water, the decomposition process for that biomass is slowed and the leaching of ammonium nitrate, other nitrates, and other components from the organic matter is reduced. By keeping trash and other larger debris on wire mesh 171 out of the pool of water, the leaching of chemicals, contaminants and pollutants into the water is reduced.
(17) In the preferred mode of operation of stormwater treatment unit 100, inlet water flows into chamber 150 from inlet pipe 111 from the side, flows into the pool of water in chamber 150 and flows out of chamber 150 through outlet pipe 121. Preferably, chamber 150 is pre-filled with water to a level above inlet 122. The inlet water, which could be from stormwater, run-offs, or other sources, contains varying degrees of debris, biomass, and other solid, semisolid and particulate materials. These materials include heavier-than-water elements such as sand and metals and lighter-than-water elements such as plastics, grease, oil and other hydrocarbons. Stormwater treatment unit 100 works by separating elements in the contaminated water by density. As the inlet water flows through wire mesh 171, heavier elements settle as sediment to the bottom of chamber 150; lighter elements float on top of water line 160 as floating debris 165.
(18) If oil, or other petroleum product, is introduced to the unit as part of floating debris 165, the oil acts as a cover reducing, if not eliminating, the flow of air (e.g., oxygen) into the collected fluid in the unit and, thus, retards the growth of bacteria, algae, and the like in the collected fluid. The reduction in such growth of microorganisms lengthens the maintenance cycle of the unit and reduces a health hazard for maintenance workers and the environment.
(19) Due to the height of the lower end of wall 140, liquid from the midsection of chamber 150 is drawn into inlet 122. Due to the separation process, the liquid drawn into inlet 122 contains less of the lighter elements and heavier elements than the original stormwater. Preferably, wall 140 is positioned high enough to avoid pipe 121 drawing sediment (not shown) from the bottom of chamber 150.
(20) In maintenance, stormwater treatment unit 100 is cleaned periodically depending on the capacity of the unit, volume of stormwater processed, and the contamination levels. Dried leaves, other biomass, and trash can be collected from wire mesh 171. Floating debris 165, such as oil and grease, can be skimmed from the surface of water level 160. Collected sediment can be vacuumed or otherwise removed from the bottom of chamber 150. Optionally, a vacuum can be used to collect other portions of the liquid in chamber 150. As such, the open and modular design of unit 100 keeps the unit accessible for easy maintenance and cleaning.
(21) Referring to
(22) In another embodiment of the invention, a deflector (not shown) is located beneath inlet pipe 111 and above wire mesh 171. Incoming storm water pours on to the deflector and is scattered. The deflector helps slow the inlet water pouring out of pipe 111 and prevents the inlet water from taking a deep plunge that would drive materials through wire mesh 171 and cause large turbulence that would disrupt the settling of sediment at the bottom of chamber 150. In another embodiment of the invention, the deflector may be a sprinkler board that diverts the flow of water and spreading the water throughout the length and width of the chamber. Numerous other water deflecting configurations attached to inlet pipe 111 or positioned in the stream of inlet water will be apparent to one of ordinary skill in the art.
(23) In a preferred embodiment of the invention, collectors 172 and 173 are located beneath wire mesh 171. Collectors 172 and 173 are preferably made of stainless steel and shaped with grooves to present a saw tooth cross-section to slow the rush of the inlet water into chamber 150 and help collect sediment. Collectors 172 and 173 increase surface area contact with the inlet water and may be angled, textured, coated, magnetized or use other cross-sectional shapes, to collect certain materials. In a preferred embodiment, the grooves of collector 172 are four inches deep and the grooves of collectors 173 are twelve inches deep. Alternatively, collectors 172 and 173 may include a pattern of projections that induces turbulence to collect certain materials such as is used in mining operations. Collectors 172 and 173 could also be magnetized to collect certain metals. In a further embodiment of the invention (not shown), collectors 173 are placed above water line 160. In a still further embodiment of the invention, multiple levels of collectors 172 and 173 are used to cascade inlet water. The height of collectors 172 and 173 may be adjustable.
(24) Optionally, collector 155 is located at the bottom of chamber 150 and collects sediment in a manner similar to that of collectors 172 and 173. Collector 155 is also preferably made of stainless steel and shaped with grooves to create a saw tooth cross-section. Collector 155 has increased surface area contact with the flowing fluid and may be angled, textured, coated, magnetized, or utilize other cross-sectional shapes to collect certain materials from the fluid. The grooves of collector 155 are preferably two inches deep.
(25) Also optionally, filler blocks 158 are placed in the bottom corners of chamber 150. Filler blocks 158 shape the bottom of chamber 150 to help reduce turbulence in the water flow and further aid in the efficiency of collecting the sediments and increasing the distance between collected sediment at the bottom of chamber 150 and inlet 122.
(26) In a further embodiment of the invention, the position or dimensions of wall 140 are adjustable to adjust the flow of water to inlet 122 and adjust the efficiency of the treatment process or extract water from different levels within chamber 150i.e., closer to water level 160 versus closer to the bottom of chamber 150. In another embodiment of the invention, wall 140 is perforated to allow a selective extraction from different levels within chamber 150. In yet another embodiment of the invention (not shown), inlet 122 and vent pipe 130 are omitted, leaving outlet pipe 121 flush with the opening of outlet 120 to extract fluid from chamber 150 through the perforated wall. Different levels of fluid in chamber 150 may be extracted depending on the placement of perforations in the wall.
(27)
(28) Stormwater treatment system 200 can be built to modify an existing drainage trunk line with trunk line inlet 201 and trunk line outlet 202. In an exemplary embodiment, drainage flow chambers 280 and 290 and stormwater treatment unit 270 are added to the existing trunk line. The side view of the system shown in
(29) Chamber 280 includes baffle 281 which comprises a short angled wall for diverting flow from inlet 201 to connecting pipe 271. Connecting pipe 271 connects chamber 280 with treatment unit 270. Connecting pipe 272 connects treatment unit 270 with chamber 290. A conventional backflow preventer 291 is preferably provided in or near the junction of pipe 272 and chamber 290. Treatment unit 270 may have a conventional design or a design in accordance with the present invention (as shown).
(30) In the operation of system 200, inlet water from trunk line inlet 201 is diverted via baffle 281 into pipe 271 and into stormwater treatment unit 270. The water is treated in unit 270 and returns to chamber 290 via pipe 272. The treated water flows from chamber 290 into trunk line outlet 202. Backflow preventer 291 reduces or prevents the return of outlet water to stormwater treatment unit 270 via outlet pipe 272.
(31) In a preferred embodiment of the invention, chambers 280 and 290 are lined with collectors 282 and 292, respectively, at the bottom of the chambers. Collectors 282 and 292, similar to collectors 172, 173, and 155 in
(32)
(33) Drainage flow chamber 380 is connected to inlet 301 from an existing drainage trunk line, outlet 303 to an existing drainage pipeline, and pipe 371 to a stormwater treatment unit 370. Baffle 381 in chamber 380 diverts the ordinary flow of inlet water from inlet 301 to pipe 371 for water treatment. An overflow of inlet water passes over baffle 381 to outlet 303. Baffle 381 is preferably built with 6 thick concrete or concrete blocks, but may be built with other suitable materials with other dimensions. In a preferred embodiment, baffle 381 extends to a height no higher than the top of pipe 371 and collector 381 is positioned at the bottom of chamber 380.
(34) In operation, as the inlet water enters drainage flow chamber 380 from inlet 301, the water is blocked off from outlet 303 by baffle 381 and is diverted to pipe 371 into a stormwater treatment unit 370 for treatment. If an overflow condition starts to build in stormwater treatment unit 370 causing the water level in pipe 371 to rise to the top of the pipe, the water level in chamber 380 rises to the top of baffle 381 and the excess inlet water flows over the top of baffle 381 into outlet 303 of the drainage trunk line. Effectively, chamber 380 with baffle 381 acts as an overflow prevention system for the unit 370. Preventing overflow in stormwater treatment unit 370 is an important aspect of the system because an overflow condition may cause debris, sediment, contaminants, pollutants and the like collected by the unit to be flushed out of the unit and back into the drainage system reducing, or entirely negating the unit's performance. Alternatively, in cases where an unexpected volume of stormwater flows through inlet 301 exceeding the capacity of pipe 371, the water level in chamber 380 will rise and the excess flow will pass over baffle 381 to outlet 303.
(35)
(36) Stormwater treatment system 400 comprises two off-line stormwater treatment units 470A and 470B arranged in a parallel configuration. Flow drainage chambers 480A is connected to trunk line inlet pipe 401 and, via pipe 403, to chamber 480B. Chamber 480B is connected via pipe 404 to chamber 490. Chamber 490 is connected to trunk line outlet pipe 402 of the existing drainage trunk line.
(37) Flow drainage chambers 480A and 480B, with collectors 482A and 482B is positioned at the bottom of the chambers, respectively, divert water flow via baffles 481A and 481B, respectively, to pipes 471A and 471B, respectively. Pipes 471A and 471B connect to the inlets of stormwater treatment units 470A and 470B, respectively. The outlets of units 470A and 470B are connected to outlet pipe 472.
(38) In operation, inlet water from inlet 401 is diverted by baffle 481A to pipe 471A to water treatment unit 470A. If an overflow condition occurs in chamber 480A, the excess inlet water overflows baffle 481A to pipe 403 and enters flow drainage chamber 480B. Baffle 481B diverts the inlet water into water treatment unit 470B. If an overflow condition occurs in chamber 480B, the excess inlet water overflows baffle 481B to pipe 404.
(39) Treated water flows out of units 470A and 470B into pipe 472, through backflow preventer 491 and into chamber 490, includes collector 492 at the bottom of chamber 490. In an exemplary embodiment of the invention, pipe 472 is 18 in diameter. Backflow preventer 491 is a conventional backflow preventer to reduce or prevent water from flowing from chamber 490 into pipe 472. Optionally, the outlets of units 470A and 470B may also be equipped with backflow preventers.
(40) While system 400 contains only two stormwater treatment units arranged in parallel, further units can be added and arranged in the configuration of unit 470B.
(41) The stormwater treatment unit and system has advantageous application to other uses besides stormwater treatment. Filtering run-offs from mining operations, processing fluids used in oil well fracturing operations, recycling cooling fluids for cutting blades, processing contaminated lubricants containing metal shavings, and like applications may be implemented with the treatment units and systems according to the present invention.
(42)
(43) Fluid treatment unit 500 comprises chamber 550, with openings for inlet 511 and outlet 521. Inlet 511 and outlet 521 are separated by wall 540 extending only part way between the top and bottom of chamber 550. The inlet fluid from inlet 511 is pre-separated by wire mesh 571 for larger debris. Vent pipe 530 is located on top of outlet 521 to facilitate the release of any pressure differential in outlet 521. In operation, fluid flowing through unit 500 is separated by density. Lighter components 565 float on top of the reservoir of principal fluid in chamber 550. Heavier components 555 settle and are collected at the bottom of chamber 550. Once the level of fluid 560 in chamber 550 reaches the lower level of pipe 521, processed fluid flows out of pipe 521.
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(45) Fluid treatment unit 600 comprises a chamber defined by wall 601, sump area 655 for collecting debris at the bottom of the chamber, and access opening 605 at the top of the chamber. Inlet pipe 611 is located on one side of the chamber, and outlet manifold 621 with an outlet pipe 623 is located on another side of the chamber. Inlet pipe 611 and outlet pipe 623 are separated by a wall 640 in the chamber having a wall top 641 and a wall bottom 642.
(46) A space exists between wall top 641 and the top of the chamber to allow airflow between the chamber and vent pipes 630. Another space exists between wall bottom 642 and the bottom of the chamber to allow fluid to flow from inlet pipe 611 to outlet manifold 621. Outlet manifold 621 comprises pipe loop 622 and vent pipes 630 and is connected to outlet pipe 623. Pipe loop 622 has a cut-out 625 at the top surface of a bottom portion of the loop.
(47) In a preferred mode of operation, fluid flows into the chamber from inlet pipe 611 into a pool of fluid in the chamber normally at a level reaching the bottom surface of outlet pipe 623. Fluid in the pool flows underneath wall bottom 642 and enters outlet manifold 621 through cut-out 625, which is positioned lower than outlet pipe 623. Fluid that entered outlet manifold 621 through cut-out 625 rises in pipe loop 622 as the fluid level in the chamber rises, until it reaches the level of the bottom surface of outlet pipe 623 and flows out through outlet pipe 623. Only fluid entering outlet manifold 621 through cut-out 625 will be able to access outlet pipe 623. Outlet pipe 623 is positioned lower than inlet pipe 611 so that fluid can flow due to gravity from inlet pipe 611 through the chamber, into the outlet manifold 621 via cut-out 625, and out through outlet pipe 623.
(48) Particles caught in the flow of fluid under wall bottom 642, or swept up from sump area 655, if any, may impact the bottom surface of the bottom portion of pipe loop 622. Such impact can prevent, or at least slow, the flow of such particles into cut-out 625.
(49) Differences in air pressure between the chamber and pipe loop 622 are equalized due to the flow of air over wall top 641 and into vent pipes 630 or from vent pipes 630 over wall top 641 to the chamber.
(50) According to an embodiment of the invention, a method of retrofitting an existing stormwater trunk line is disclosed. First, two separated sections of a trunk line are replaced with two chambers, the second chamber separate and downstream from the first chamber. Next, a stormwater treatment unit, either as disclosed in the present invention or known in the art, is connected to the two installed chambers via an inlet pipe connected to the first chamber and an outlet pipe connected to the second chamber. A baffle is installed in the first chamber with a height no greater than the top of the inlet pipe in the first chamber to direct flow into the inlet pipe. In another embodiment of the invention, a backflow preventer is installed between the outlet pipe and the second chamber.
(51) Although the invention has been described and illustrated with a certain degree of particularity, it is understood that the present disclosure has been made only by way of example, and that numerous changes in the combination and arrangement of parts can be resorted to by those skilled in the art without departing from the spirit and scope of the invention, as hereinafter claimed.