Floating Wetland Structures and Assemblies
20200146222 ยท 2020-05-14
Inventors
Cpc classification
Y02P60/21
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
B63B35/38
PERFORMING OPERATIONS; TRANSPORTING
B63B35/44
PERFORMING OPERATIONS; TRANSPORTING
B63B2035/4493
PERFORMING OPERATIONS; TRANSPORTING
B63B3/02
PERFORMING OPERATIONS; TRANSPORTING
International classification
Abstract
A floating wetland structure designed for placement in a body of water includes: at least one surface module having an upper surface at or above the water level; at least one submerged module below the water level; and a frame interconnecting the surface module and submerged module. The frame maintains the surface module as horizontally offset from the submerged module such that an open water area is defined. The floating wetland structure can have an alternating arrangement of surface modules and submerged modules. The frame may include lengthwise extending members and laterally extending members. Horizontally extending lower members may be interconnected with the upper members by vertically extending members that maintain the submerged module below the water level.
Claims
1. A floating wetland structure for placement in a body of water having a water level, the floating wetland structure comprising: a frame; and a plurality of modules comprising: at least one surface module having an upper surface for placement at or above the water level; and at least one submerged module for placement below the water level.
2. The floating wetland structure according to claim 1, wherein the frame maintains at least two modules of the plurality of modules as horizontally offset from each other such that a spacing are maintained to define an open water area.
3. The floating wetland structure according to claim 1, wherein at least a portion of the plurality of modules has an alternating arrangement of surface modules and submerged modules.
4. The floating wetland structure according to claim 1, wherein the frame comprises lengthwise extending members and laterally extending members.
5. The floating wetland structure according to claim 1, wherein the frame comprises at least one horizontally extending upper member, at least one horizontally extending lower member, and at least one vertically extending member interconnecting the upper member and lower member.
6. The floating wetland structure according to claim 5, wherein the frame comprises multiple vertically extending members interconnecting the upper member and lower member such that the submerged module is maintained below the water level by the vertically extending members.
7. The floating wetland structure according to claim 6, wherein the vertically extending members each have approximately the same length such that the submerged module is maintained in a horizontal disposition below the water level.
8. The floating wetland structure according to claim 6, wherein the vertically extending members have different lengths such that the submerged module is maintained in a sloped disposition below the water level.
9. The floating wetland structure according to claim 1, wherein at least one module of the plurality of modules comprises multiple layers of buoyant panel material.
10. The floating wetland structure according to claim 1, wherein the at least one surface module has an upper surface with holes for placing plants.
11. The floating wetland structure according to claim 1, wherein the plurality of modules comprises multiple surface modules and multiple submerged modules, and defines multiple open water areas.
12. The floating wetland structure according to claim 11, wherein a riparian edge of the multiple surface modules is higher than a close-packed arrangement without open water areas.
13. The floating wetland structure according to claim 1, wherein a biofilm is supported by the submerged module.
14. A floating wetland structure according to claim 1, wherein plant life is supported by the surface module.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0019] The previous summary and the following detailed descriptions are to be read in view of the drawings, which illustrate particular exemplary embodiments and features as briefly described below. The summary and detailed descriptions, however, are not limited to only those embodiments and features explicitly illustrated.
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DETAILED DESCRIPTIONS
[0030] The previous summary and the following detailed descriptions are to be read in view of the drawings, which illustrate particular exemplary embodiments and features as briefly described below. The summary and detailed descriptions, however, are not limited to only those embodiments and features explicitly illustrated.
[0031] These descriptions are presented with sufficient details to provide an understanding of one or more particular embodiments of broader inventive subject matters. These descriptions expound upon and exemplify particular features of those particular embodiments without limiting the inventive subject matters to the explicitly described embodiments and features. Considerations in view of these descriptions will likely give rise to additional and similar embodiments and features without departing from the scope of the inventive subject matters. Although the term step may be expressly used or implied relating to features of processes or methods, no implication is made of any particular order or sequence among such expressed or implied steps unless an order or sequence is explicitly stated.
[0032] Any dimensions expressed or implied in the drawings and these descriptions are provided for exemplary purposes. Thus, not all embodiments within the scope of the drawings and these descriptions are made according to such exemplary dimensions. The drawings are not made necessarily to scale. Thus, not all embodiments within the scope of the drawings and these descriptions are made according to the apparent scale of the drawings with regard to relative dimensions in the drawings. However, for each drawing, at least one embodiment is made according to the apparent relative scale of the drawing.
[0033] Like reference numbers used throughout the drawings depict like or similar elements. Unless described or implied as exclusive alternatives, features throughout the drawings and descriptions should be taken as cumulative, such that features expressly associated with some particular embodiments can be combined with other embodiments.
[0034] Most prior-art treatment wetlands are plant-based systems, in which function is related to plant structure. In a departure from plant-based orthodoxy, the implementations described below take a thermodynamic approach to treatment wetland design. Wetland functions are regulated by microbiota and their metabolism. The energy that supports microbial growth and metabolism is generated in redox reactions, a chemical process in which electrons are transferred from electron donors to electron acceptors. Wetland biogeochemical function is a predictable outcome of the interaction between thermodynamic constraints on microbial communities and supplies of electron donors and acceptors. Thermodynamic-focused design is derived from the theoretical, with mechanistic underpinnings, leading to a priori predictions; whereas, plant-based design is derived from empirical data. A thermodynamic-focused treatment wetland design incorporates the scientific foundations of biological control necessary for maximizing the treatment capacity of natural treatment wetland systems.
[0035] A thermodynamic approach to treatment wetland design, according to various embodiments within the scope of these descriptions, is implemented by an engineered floating treatment wetland (FTW) platform that incorporates wetland elements having specific traits which can be utilized to affect the redox state of the treatment zone, such as submerged surfaces with variable depth and orientation, open-water areas, surface cover, and high ratios of riparian edge to total treatment area. More oxidizing conditions are predominately obtained by incorporating wetland elements associated with photosynthetic oxygen generation and atmospheric diffusion, such as submerged surfaces and open water areas. More reduced conditions are obtained by using floating wetlands as water surface cover to restrict the amount of oxygen entering the water and varying microbial habitat density. Variable configurations of an FTW platform may also beneficially affect temperature and hydrology in the treatment zone.
[0036] Example 1: In a field implementation of thermodynamic-based design, a treatment wetland for treating high-nitrate, nitrified wastewater in a lagoon at a wastewater facility is designed, in at least one embodiment, based on an inflow ranging from 20,000 to 25,000 gallons per day at 60 to 80 mg/l nitrate concentration. The treatment lagoon was sized at 520 m.sup.2, thus requiring nitrate removal rates >10,000 mg/m.sup.2/day for complete reduction of nitrate load, an order of magnitude larger than the upper range of wetland reported denitrification rates at 1020 mg/m.sup.2/day. The thermodynamic-focused treatment wetland's size was more than an order of magnitude smaller than conventional plant-based design would suggest. Operating data indicated nitrate reduction rates >10,000 mg/m2/day and complete nitrate reduction as long as biological oxygen demand (electron donors) was maintained at 25 mg/l or greater.
TABLE-US-00001 TABLE 1 Data from Example 1 INLET OUTLET AVERAGE INLET OUTLET NITRATE NITRATE NITRATE MONTHLY FLOW BOD BOD REMOVAL RATE SAMPLE DATE mg/l mg/l GPD mg/l mg/l mg/m.sup.2/day Jun. 26, 2017 54 <0.5 23699 <6 150 9316 Jul. 10, 2017 63 5.5 22245 <4 16 9311 Jul. 31, 2017 63 <0.1 22245 <4 54 10,201 Aug. 14, 2017 72 <0.1 19217 10,072 Jun. 11, 2018 68 <1 19,466 <4 27 9635 Jun. 27, 2018 58 <0.5 19,466 <4 45 8239 Jul. 9, 2018 61 12 19,082 12 6802 Jul. 26, 2018 62 <1 19,082 <4 26 8612 Aug. 13, 2018 69 <1 17,219 <4 27 8649
[0037] The thermodynamic gradient between more reducing conditions and more oxidizing condition contains a redox zone in which denitrification occurs rapidly and efficiently. The Example 1 data supports the a priori design for that specific thermodynamic zone. As one travels the thermodynamic gradient from more oxidizing to more reducing conditions, the processes involving the use of various electron acceptors during the degradation of organic matter would follow an order from aerobic, to nitrate reduction, manganese reduction, iron reduction, sulfate reduction, and methane reduction. The variations in platform configuration provide incremental adjustments affecting the redox environment providing the ability to create a favorable redox environment for the desired reduction process.
[0038] Dissolved oxygen (DO) concentrations vary within a wetland and are affected by depth, shading, biological oxygen demand (BOD), and numerous other factors. Floating treatment wetlands (FTW)s lower dissolved oxygen levels in the waters underneath their footprint by physically blocking sunlight for photosynthetic production of oxygen and blocking diffusion from the atmosphere. DO levels underneath an FTW are reduced by microbial activity related oxygen consumption associated with plant roots. These FTW traits provide a control mechanism for creating more reducing conditions. For creating more oxidizing conditions, wetland elements such as submerged surfaces and open water areas are employed.
[0039] Submerged surfaces provide more oxidizing conditions, whereas traditional floating wetlands that cover the surface provide more reducing conditions. In a report on vertical profiles of DO in various types of Free Water Surface (FWS) wetlands, substantial differences were reported in DO concentrations among wetland habitat types, with the lowest DO levels associated with emergent and floating vegetative systems with DO levels of 1-2 mg/l, and the highest DO levels found in submerged systems, with mean levels of 10 mg/l. Open water sites' DO levels were intermediate, with mean DO of 6.0 mg/l. FTWs would be comparable to floating vegetative systems. Oxygen levels associated with submerged surfaces were approximately 5 times higher than floating systems.
[0040] Microbial communities associated with submerged surfaces benefit from photosynthetically-generated oxygen being produced within a biofilm. Oxygen supply into and out of a biofilm is a diffusive process, with a DO gradient extending from the bulk water, through a diffusive boundary layer, and into the biofilm, with oxygen moving from high concentration areas to low concentration areas. A shaded (non-illuminated) biofilm would tend to have an oxygen gradient moving from the higher DO levels in the bulk water toward the lower DO levels within the biofilm, resulting in the effective DO concentration available to the microbial community within the biofilm being lower than the DO concentration measured in the bulk water. In a submerged surface biofilm receiving sunlight, oxygen is being produced within the biofilm, and as light intensity increases, the amount of oxygen produced by photosynthesis increases. As light intensity exceeds the compensation point, the point on the light curve where photosynthesis produces an amount of oxygen equal to the oxygen requirements within the biofilm, the biofilm becomes an exporter of oxygen to the bulk waters. In this case, the DO level within the biofilm is higher than measured in the bulk water. In one report, with bulk water oxygen concentration of 200 mol/l (6.4 mg/l), the oxygen concentration was reduced to zero at 0.02 cm depth in a cyanobacterial mat without irradiance, while that with irradiance of 1000 photons/m.sup.2/sec, the oxygen concentration at 0.02 cm deep in the mat rose to approximately 900 mol/l (28.8 mg/l).
[0041] A study in 1996 reporting the effects of light on photosynthesis and photosynthesis-coupled respiration found that areal respiration of an illuminated biofilm was 7.8 times higher at an irradiance of 200 photons/m.sup.2/sec than the areal dark respiration. In addition to increased oxygen supply, higher microbial activity was also ascribed to deeper oxygen penetration into the biofilm in light conditions, with an oxygen penetration depth of only 0.2-0.5 mm in the dark and an oxygen penetration depth of 2.0 mm in light.
[0042] In an experiment that maintained a minimum DO concentration of 1.1 mg/l in the bulk water, another reported that under light conditions, nitrification rates in an algal-bacterial biofilm were 945 mg-N/m.sup.2/day, while under dark conditions nitrification rates were 156 mg-N/m.sup.2/day.
[0043] Riparian edge is widely recognized as an important ecosystem control point, associated with high-biogeochemical activity rates. Another coined the term hotspot in describing the high biogeochemical activity associated with terrestrial-aquatic interfaces, noting that hot spots occur where hydrological flow paths converge with substances or other flow paths containing complementary or missing reactants. The inclusion of open water areas and flow channels in FTW design creates additional riparian edge and provides paths for hydrological flows bringing nutrients/reactants to the reaction site, significantly improving mass transfer relative.
[0044] Temperature control strategiesLiterature reports that FTWs have modest effect on water temperature. The use of submerged-surface FTWs offers a means to affect temperature, both raising the temperature of the top surface biofilm communities and cooling the water column underneath the submerged body. Nitrification rates begin to decline significantly as temperatures drop below 15 degrees C. The benefit from raising the temperature in the reaction site would apply over the entire cold weather range of the temperature/activity curve, shifting the activity curve upwards by the amount of temperature differential at the reaction site. The placement of submerged surfaces a few cm under the water surface reduces the mass of water being heated, resulting in a greater change in temperature in the reduced water volume. The observed difference between the water temperature over the submerged surface and the bulk water varies as a function of submerged surface total area, wind induced mixing, and other factors. The difference of 1-2 degrees Celsius has a significant effect on activity rates over the 0-15 degrees Celsius range.
[0045] The solar heat that would normally enter the water column is captured in the top few cm of the water column and the submerged surface body acts to insulate the water column below. The higher temperature on the top surface results in increased amounts energy being removed from the water column via evaporation, resulting in lower temperatures below the submerged surface body.
[0046] Various embodiments of floating wet land (FTW) structures are illustrated and described herein. The structures can be deployed at and/or under the surface of a body of water or water way so as to mimic a true wetland. Significant biological activity is promoted over the wetland device during cold weather in which the surrounding waters are lacking in activity. Measurements show that the temperature over such wetland structures can be 5-6 degrees F. higher on a sunny day than the surrounding water. An energy balance around a wetland structure, based on a 300 watts per square meter of solar energy and a 4 inch depth, yields an expected delta temperature of 5.4 degrees F. This phenomenon has been sustainably observed and validated with a mathematical model.
[0047] Many small communities utilize lagoon systems for wastewater treatment. Bacterial activity becomes close to zero as temp approaches 0 degrees C., resulting in an inability of these some treatment systems to meet permit discharge limits in cold weather. It is possible that the several degrees that the inventive structures described and illustrated herein can raise temperatures by concentrating solar energy may have significant value in wastewater treatment.
[0048]
[0049] The floating wetland (FTW) structure 100 includes a skeletal frame 110 (
[0050]
[0051]
[0052] The vertically extending members 124 can be connected to the upper horizontally extending members 120 and lower members 122 by way of various connection types as represented in
[0053]
[0054] The frame members 112 and 114, in both upper and lower horizontally extending examples as represented in
[0055] The multiple layers 126 can be laminated together. The module shown in partial assembly in
[0056] A constructed module 102 is shown in
[0057] While other dimensions and shapes are within the scope of these descriptions, in at least one non-limiting example according to
[0058]
[0059]
[0060] Mutually perpendicular dimensions J and K, as measured in
[0061] While other dimension are within the scope of these descriptions, in at least one non-limiting example of an FTW structure 200 according to
[0062] Strategically positioned FTWs can divide open water into smaller units such that the core wetland become more dominant relative to any one area of open water; and the core wetland's anoxic zone can be projected beyond its own footprint and extend across small strips of open water, expanding the treatment zone. The frame work accomplishes the task of creating an anoxic treatment zone while maintaining a restricted oxygen input into the system.
[0063]
[0064] Microbial communities associated with submerged surfaces benefit from photosynthetically-generated oxygen being produced within the biofilm. Oxygen supply into and out of a biofilm is a diffusive process, with a DO gradient extending from the bulk water, through a diffusive boundary layer, and into the biofilm, with oxygen moving from high concentration areas to low concentration areas. A shaded (non-illuminated) biofilm would tend to have an oxygen gradient moving from the higher DO levels in the bulk water toward the lower DO levels within the biofilm, resulting in the effective DO concentration available to the microbial community within the biofilm being lower than the DO concentration measured in the bulk water. In a submerged surface biofilm receiving sunlight, oxygen is being produced within the biofilm, and as light intensity increases, the amount of oxygen produced by photosynthesis increases. As light intensity exceeds the compensation point, the point on the light curve where photosynthesis produces an amount of oxygen equal to the oxygen requirements within the biofilm, the biofilm becomes an exporter of oxygen to the bulk waters. In this case, the DO level within the biofilm is higher than measured in the bulk water. Another reported that with bulk water oxygen concentration of 200 mol/l (6.4 mg/l), the oxygen concentration was reduced to zero at 0.02 cm depth in a cyanobacterial mat without irradiance, while that with irradiance of 1000 photons/m.sup.2/sec, the oxygen concentration at 0.02 cm deep in the mat rose to approximately 900 mol/l (28.8 mg/l). The oxygen level within the biofilm was 4.5 times greater than the bulk water.
[0065] A natural riparian edge is the interface between land and a body of water. An FTW contributes additional man-made riparian edge when deployed in a body of water. Riparian edge is an important ecosystem control point, associated with high activity rates. The term hotspot is used to describe the high biogeochemical activity associated with terrestrial-aquatic interfaces, noting that hot spots occur where hydrological flowpaths converge with substances or other flowpaths containing complementary or missing reactants. The inclusion of open water areas and flow channels in FTW design creates additional riparian edge and provides paths for hydrological flows bringing nutrients/reactants to the reaction site, significantly improving mass transfer relative to conventional FTW design.
[0066] Examples of implementing multiple wetland habitats design strategies to regulate oxygen levels are illustrated in the contrasting close-packed FTW structure 400 of
[0067] For illustration purposes, the sections of
[0068] The basic FTW structure 500 in
[0069] The above-described embodiments and those inferred in view of these descriptions and referenced drawings are beneficial for water treatment, for example by promoting biofilm activity on submerged surfaces where photosynthetically-generated oxygen is produced by biofilm microbial life.
[0070] Particular embodiments and features have been described with reference to the drawings. It is to be understood that these descriptions are not limited to any single embodiment or any particular set of features, and that similar embodiments and features may arise or modifications and additions may be made without departing from the scope of these descriptions and the spirit of the appended claims.