Patent Abstract:
The wastewater treatment systems have a plurality of treatment zones including a first reactor for supporting biofilms for reducing a concentration of organics and solids from wastewater to be treated and for cyclically nitrifying and denitrifying the wastewater therein. A second reactor is for supporting biosolids, the supporting means including elements for digesting suspended solids in water exiting the first reactor. A portion of the water exiting the second reactor is recycled to the first reactor.

Full Description:
CROSS-REFERENCE TO RELATED APPLICATION  
       [0001]     This application is a continuation of and incorporates by reference co-pending application Ser. No. 10/294,450, filed Nov. 14, 2002, now U.S. Pat. No. 6,811,700, entitled “Integrated Hydroponic and Fixed-Film Wastewater Treatment Systems and Associated Methods,” which application claimed priority to provisional application Ser. No. 60/333,203, filed on Nov. 14, 2001, entitled “Integrated Hydroponic and Fixed-Film Wastewater Treatment Systems and Associated Methods,” both of which are commonly owned with the present invention and which are incorporated herein by reference. 
     
    
     BACKGROUND OF THE INVENTION  
       [0002]     1. Field of the Invention  
         [0003]     The present invention relates to wastewater treatment systems and methods, and, more particularly, to such systems and methods for wastewater treatment that are nonchemically based.  
         [0004]     2. Description of Related Art  
         [0005]     Wastewater treatment via “natural” means, i.e., without the addition of chemicals, has been accomplished with the use of aquatic and emergent macrophytes (plants) that, in concert with the attendant microorganisms and macroorganisms associated with macrophyte roots and stems, substantially mineralize biodegrade organic materials and substantially remove certain excess nutrients, such as nitrogen and, to a lesser extent, phosphorus. These macrophytes have typically been located in artificial marshlands, also known as constructed wetlands, which are designed for gravity flow. A negative aspect of such systems is that they are very land-intensive, requiring roughly on the order of 100 times as much land area as a conventional treatment plant, or, in terms of capacity, as much as 30-40 acres per 10 6  gallons of wastewater treated per day unless other treatment processes are incorporated into the constructed wetlands  
         [0006]     Subsurface-flow wetlands, which comprise aquatic plants positioned above a gravel filter are also known for use in wastewater treatment. These systems have been shown to frequently fail, however. Failure is manifested as the upstream gravel tends to become clogged with biosolids, permitting the influent to bypass the clogged region and pass substantially untreated to a downstream region. Additionally, surfaced wastewater is a breeding ground for disease vectors and nuisance insects. Ultimately the gravel becomes so clogged that design wastewater treatment is substantially compromised. Plants also appear to have little treatment role in subsurface flow wetlands because the plant root systems are inhibited by conditions in the gravel filter from growing sufficiently long to extend into the gravel, and thus have minimal contact with the influent.  
         [0007]     Several varieties of aquatic and emergent macrophytes are known to be used in wetland and aquatic wastewater treament systems, including, but not limited to, cattails, bulrushes, sedges, and water hyacinths. In wetland treatment systems these plants may be packed in unlined or lined trenches or basins filled with a granular porous medium such as gravel or crushed stone. It has also been suggested to use recycled, shredded scrap tires in the place of the gravel. Another suggested wetland system variant is to place a semipermeable barrier between a lower level into which effluent enters and the plant root system for directing the wastewater flow across the entire plant bed.  
         [0008]     In yet another variant floating aquatic macrophytes, typically water hyacinths, are placed in shallow lagoons where plant roots, with attendant microorganisms and macroorganisms, extending into the water column are a principal design treatment mechanism. Although this root zone treatment method can provide advanced secondary treatment effluent, its application is limited by climate to approximately 5% of the United States. The large treatment footprint of water hyacinth treatment systsems prohibits enclosure in greenhouses for almost all economically viable applications.  
         [0009]     It is also known to combine plant root zone treatment with conventional activated sludge technology. The principal advantages of combining root zone treatment with activated sludge are improved nutrient removal capability over root zone treatment alone and improved treatment stability in small, activated sludge treatment systems. Among the problems encountered with root zone/activated sludge technology is that the clarifiers employed do not scale well when the size of the system is reduced beyond a certain point. In addition, operator qualifications are high for activated sludge systems, adding to the expense of running the system. Root zone/activated sludge technology has been known to digest in situ a large fraction of the biosolids produced and maintained within the treatment system, thereby reducing system biosolids yield. The mechanism for yield reduction is thought to be the retention of biosolids flocs on plant roots with subsequent consumption and mineralization of flocs by the invertebrate community attendant to the root zone. Reduction of yield is desirable only to a certain point, however. As reactors in series are added, thereby increasing biosolids contact with the root zone, yield may be reduced to the point where an insufficient quantity of biosolids remain to be recycled from the clarifier to the reactors in series. Lack of recycled biosolids substantially degrades the treatment performance of the activated sludge treatment element. This design trap is inherent to root zone/activated sludge treatment systems. Preliminary studies have been performed on various aspects of the present invention by the inventors and other colleagues, as reported in “Final Report on the South Burlington, Vermont Advanced Ecologically Engineered System (AEES) for Wastewater Treatment,” D. Austin et al.,  2000 ; and “Parallel Performance Comparison between Aquatic Root Zone and Textile Medium Integrated Fixed Film Activated Sludge (IFFAS) Wastewater Treatment Systems,” D. Austin, Water Environment Federation, 2001; both of these documents are incorporated herein by reference in their entirety.  
       SUMMARY OF THE INVENTION  
       [0010]     The present invention provides a wastewater treatment system and method that are less land intensive than previous systems, as well as combining the advantages of a plurality of remediation techniques. The present invention has a smaller footprint than previously disclosed wetlands, reduces undesirable characteristics of an influent, and has a low yield, i.e., low proportion of matter needing disposal.  
         [0011]     An additional feature of the invention provides a unified environment that includes a remediation system.  
         [0012]     The wastewater treatment systems and methods of the present invention are amenable to the treatment of, for example, but not intended to be limited to, domestic wastewater, industrial waste or process water, stormwater, urban runoff, agricultural wastewater or runoff, and even biological sludges. The systems are capable of handling a flow range of approximately 2000-2,000,000 gal/day. The types of contaminants that can be treated in the system include suspended particles, nutrients, metals, simple organics (oxygen-demanding substances), and synthetic or complex organics. The undesirable characteristics typically desired to be remediated include, but are not intended to be limited to, average biological oxygen demand (BOD), average total suspended solids (TSS), total nitrogen, and concentration of oil and grease. The systems of the present invention can reduce BOD to &lt;10 mg/L, TSS to &lt;10 mg/L, and total nitrogen to &lt;10 mg/L.  
         [0013]     The water treatment system of the present invention comprises a wastewater inlet, a treated water outlet, and a plurality of treatment modules between the inlet and the outlet. Each module is for treating the water with a selected process. Each module is in fluid communication with at least one other module for permitting sequential treatment of the wastewater by a plurality of processes.  
         [0014]     Influent wastewater is first directed to a a pretreatment process, such as covered anaerobic reactor or screening process, which serves to perform an initial organic and solids removal. A means is provided for removing odors from gases or fumes that are produced herein.  
         [0015]     Following pretreatment for a predetermined period, the wastewater is channeled to a fixed-film reactor, which achieves removal of organics and solids and denitrification. This fixed-film reactor is characterized in a low yield unit process, in which yield is defined as kilograms of VSS exiting the system divided by kilograms of BOD entering the system. In alternate embodiments of the system, plural fixed-film reactors may be provided in series.  
         [0016]     A given fixed-film reactor may operate in a substantially aerobic or anoxic mode, or alternate between anoxic and aerobic modes. A given fixed film reactor may operate as a complete or partial mix bulk liquid reactor. Alternatively, the reactor may operate in a fill and drain mode.  
         [0017]     Water exiting the fixed-film reactor then is pumped or flows by gravity to a hydroponic reactor, in which aquatic plants are suspended atop the liquid for achieving aquatic-root-zone treatment. The hydroponic reactor is substantially aerobic, and operates to achieve VSS digestion in addition to continued removal of nutrients started in the fixed-film reactor. The hydroponic reactor has an inlet and an outlet. Herein the term hydroponic reactor will be taken to comprise aerated reactors that have a rigid rack set at the water surface to support plants that send down roots into the wastewater column. The rack covers substantially the entire water surface. Plants substantially cover the surface of the rack. In alternate embodiments plural hydroponic reactors in series may be provided.  
         [0018]     Digestion of VSS in the hydroponic reactors, or plurality of reactors, is designed to produce an hydroponic effluent VSS concentration of approximately 50 mg/L or less, which is sufficiently low to permit economically viable filtration. Filtration of hydroponic effluent to advanced standards may be achieved by a plurality of technologies.  
         [0019]     Recycling may be directed to an anaerobic pretreatment module or to the fixed-film reactor, prior to channeling water exiting the hydroponic reactor to a filtering and disinfection module.  
         [0020]     The features that characterize the invention, both as to organization and method of operation, together with further objects and advantages thereof, will be better understood from the following description used in conjunction with the accompanying drawing. It is to be expressly understood that the drawing is for the purpose of illustration and description and is not intended as a definition of the limits of the invention. These and other objects attained, and advantages offered, by the present invention will become more fully apparent as the description that now follows is read in conjunction with the accompanying drawing. 
     
    
     BRIEF DESCRIPTION OF THE DRAWINGS  
       [0021]      FIG. 1  is a schematic diagram of the first embodiment of the present invention.  
         [0022]      FIG. 2  is a side cross-sectional view of a hydroponic reactor.  
         [0023]      FIG. 3  is a schematic diagram of the second embodiment of the present invention. 
     
    
     DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS  
       [0024]     A description of the preferred embodiments of the present invention will now be presented with reference to  FIGS. 1-3 .  
         [0025]     A schematic of a first embodiment  10  of the present invention ( FIG. 1 ) illustrates the flow of wastewater through the system, entering a pretreatment module  11 , into which influent  90  is channeled and permitted to reside for a predetermined period. The pretreatment module  11  may comprise, for example, a covered anaerobic reactor, which serves to perform an initial organic and solids removal. In this vessel  1  the solids from the influent settle, and anaerobic bacteria feed on the solids and wastes in the liquid. A means is provided for removing odors from gases or fumes that are produced herein.  
         [0026]     The wastewater  90  is then channeled to an inlet  12  of a fixed-film reactor, such as, but not intended to be limited to, a moving bed bioreactor (MBBR)  13 , which as discussed previously achieves removal of organics and solids and denitrification. The fixed-film reactor  13  in this system  10  comprises a containment vessel that contains manufactured medium  14 , which may be rigidly fixed, fluidized, or randomly packed. The medium  14  provides a large surface area that serves as a substrate for biofilm growth. Nitrification occurs in the biofilms growing on the fixed-film medium  14 , and denitrification occurs during recycling to an anoxic environment or by inducing a transient anoxic condition within the reactor. Sloughing of biofilms in the fixed-film reactor  13  is substantially continuous, thereby eliminating the need for recycling biosolids as in prior known devices.  
         [0027]     The fixed-film reactor  13  provides treatment stability early in the operational life of the system  10 . Bacteria quickly colonize the media  14 , providing effective BOD treatment as heterotrophic bacteria colonize media surfaces. Denitrification can be achieved, as will be discussed in the following, by recycling nitrified effluent to an anoxic or aerobic fixed-film process  13 , thereby meeting design treatment goals prior to plant maturation in the hydroponic reactor  19  discussed in the following.  
         [0028]     Mixing in the reactor  13 , which may be effected by mechanical means, such as a propeller  15 , or by aeration  16 , is designed to ensure that wastewater  90  is exchanged over the entire medium surface area in a period that may range from minutes to several hours depending upon the characteristics of the reactor  13  and the medium  14 . Preferably the mixing occurs substantially continuously during the operation of the system  10 .  
         [0029]     Following flow through the fixed-film reactor  13 , water is channeled from an outlet  17  of the fixed-film reactor  13  to an inlet  18  of a first hydroponic reactor  19  ( FIG. 2 ). A hydroponic reactor  19  herein is intended to comprise a basin  20  having the inlet  18  and an outlet  22 . A rack  23  is positionable at the water&#39;s surface in the basin  20  and is adapted for supporting plants  24  thereon. Preferably the rack  23  covers substantially the entire surface of the basin  20 , and plants  24  cover substantially the entire rack  23 .  
         [0030]     The role of plant roots  25  has been determined to be extremely important in the remediation processes of the present system  10  and its alternate embodiments. Plant roots  25  retain significant quantities of biosolids, also known as volatile suspended solids (VSS). Retention of biosolids on plant roots is a key mechanism of the digestion of biosolids within the hydroponic reactor. The aquatic root zone achieves simultaneous nitrification and denitrification. Significant nitrification occurs when nitrifying biosolids are retained on the plant roots  25 . Denitrification occurs in localized, transient anoxic sites within the root zone. Further, overall reaction rates are higher than in pure aquatic-root-zone treatment. Since the system  10  does not employ a clarifier, as in prior known systems, capital and operating expenses and time are significantly reduced.  
         [0031]     Treatment basin  20  depth  26  in relation to average root depth has a significant effect on treatment performance. At least a 20% penetration of the treatment water column  26  by root mass is believed preferable. As a number of plant species have been found that can reliably produce roots 2 feet in length, a maximum design depth  26  of approximately 6 to 7 feet is feasible for the current system  10 .  
         [0032]     Aeration and/or other means for imparting mechanical energy  27  is important, for mixing the contents of the reactor  19  and for forcing contact between the wastewater and the plant roots  25 , ensuring that the plant root zone significantly contributes to treatment. Mixing force should not, however, be so robust as to cause the roots to splay outward, thereby decreasing exposed root surface area.  
         [0033]     Time spent in the hydroponic reactor  19  should be sufficient to digest volatile organic material present in the wastewater and bacterial biomass generated in the system  10 .  
         [0034]     The yield from the system  10  is very low, since two reactor types  13 , 19  having intrinsically low yields are combined. Values less than 0.1 kg effluent VSS/kg influent BOD 5  are achievable with the present system  10 .  
         [0035]     In a particular embodiment, the fixed-film reactor  13  is embedded into the hydroponic reactor  19 ; however, this is not intended as a limitation, and the principle of having the reactors  13 , 19  in series obtains in any physical arrangement of this system  10 , as schematically illustrated in  FIG. 1 .  
         [0036]     In the embodiment shown in  FIG. 1 , a second hydroponic reactor  19 ′ follows the first  19  in series. Alternatively, one very long hydroponic reactor may also be contemplated.  
         [0037]     Recirculation Q r  comprises an important feature of the system  10  design. Recirculation may be achieved by any pumping means known in the art, and is preferably at least equal to the forward flow rate, and may be up to ten times the forward flow rate. In the embodiment of  FIG. 1 , recirculation occurs following the second hydroponic reactor  19 ′.  
         [0038]     In an alternate embodiment, the hydroponic reactor  19  is substantially toroidal, with a central cylindrical module comprising the fixed-film reactor  13 . One of skill in the art will recognize that other configurations are also feasible.  
         [0039]     This system  10  offers improvements to prior art technologies: By integrating a high-rate fixed-film treatment  13  into an aquatic-root-zone  19  treatment system, the advantages of the combined technologies are retained while substantially eliminating the drawbacks. The improvements include that the fixed-film component  13  provides treatment stability early during start-up of the system  10 . Bacteria colonize the medium  14  quickly in the fixed-film reactor(s)  13 , providing effective BOD treatment as heterophilic bacteria colonize medium  14  surfaces, and then nitrification as the nitrifying bacteria colonize medium  14  surfaces.  
         [0040]     The elimination of the clarifier comprises an elimination of what has been heretofore considered a fundamental unit process. Elimination of the clarifier is made possible by the extremely small yield of the present system  10  while maintaining the biological nutrient removal treatment capacity found in clarifier-based treatment technology. For the purposed of filtration, the term “low yield” is defined as the production of effluent VSS concentrations &lt;50 mg/L without accumulation of VSS elsewhere in the system  10 . At these VSS concentrations, several filtration technologies can effectively replace the clarifier, with a filter  28  following the second hydroponic reactor  19 ′. Filtered effluent can be designed to produce TSS values &lt;5 mg/L from a filter influent of VSS of 50 mg/L. Filtrate from such a filtration system  28  can effectively be processed on site in most treatment applications. Recycling may also occur following the filtration system  28  (dotted line in  FIG. 1 ) in an alternate embodiment.  
         [0041]     One embodiment of a filtration system comprises a vertical flow wetland  28 , which includes a basin  30  having an outlet  31  in a bottom thereof. The basin  30  is adapted to contain a particulate medium  32 , 32 ′, and a mat  33  adapted for permitting plants  35  to root  36  therein. The mat  33  is positioned above the particulate medium  32 . The wetland cell  28  is adapted to maintain a population of aquatic invertebrates therein.  
         [0042]     This system  10  is capable of achieving an ammonia concentration of &lt;1 mg/L. A redox (oxidation reduction potential) probe  34  may be employed to regulate pumping. If the redox level is greater than a predetermined limit, the pump is turned off. Pumping only occurs as long as the system is anoxic. Alternatively, the wetland cell may fill and draw per other means of control such as a timer, programmable logic controller, or an on-line monitoring technology othe than a redox probe. The system  10  is capable of producing an effluent having a BOD &lt;5 mg/L, TSS &lt;5 mg/L, total nitrogen &lt;10 mg/L, and turbulence &lt;5 ntu&#39;s.  
         [0043]     Another advantage of this system  10  is its aesthetic features. In use, the reactors  13 , 19  appear to be planters filled with beautiful plants, and the sound of flowing water is known to have beneficial effects to the human psyche.  
         [0044]     A second embodiment of the wastewater treatment system  50  is illustrated schematically in  FIG. 3 . This system  50  is also modular, and contains a first  51  and a second  52  fixed-film reactor such as the reactor  13  described above, connected in series, following the pretreatment vessel  53 . In this configuration the first fixed-film reactor  51  remains in a substantially anoxic condition, while the second  52  remains in a substantially aerobic condition.  
         [0045]     At least one hydroponic reactor  54  follows the second fixed-film reactor  52 , and is substantially the same as that  19  described above. Following aquatic-root-zone treatment, a filtration system  55  removes any remaining suspended solids. Recycling for denitrification follows the filtration system  55  to the first fixed-film reactor  51 .  
         [0046]     Another aspect of the present invention includes a method of designing a site-specific wastewater treatment system. The method comprising the step of determining parameters of wastewater at a site. Such parameters may include, but are not intended to be limited to, measured levels of wastewater characteristics and temporal ranges thereof. One of skill in the art will recognize that flow rate, volume, nutrient level, BOD, TSS, and VSS may be included in such a set of parameters.  
         [0047]     Owing to the modular nature of the systems  10 , 50  of the present invention, a wastewater treatment system can then be configured that is specific to the determined wastewater parameters.  
         [0048]     In the foregoing description, certain terms have been used for brevity, clarity, and understanding, but no unnecessary limitations are to be implied therefrom beyond the requirements of the prior art, because such words are used for description purposes herein and are intended to be broadly construed. Moreover, the embodiments of the apparatus illustrated and described herein are by way of example, and the scope of the invention is not limited to the exact details of construction.  
         [0049]     Having now described the invention, the construction, the operation and use of preferred embodiments thereof, and the advantageous new and useful results obtained thereby, the new and useful constructions, and reasonable mechanical equivalents thereof obvious to those skilled in the art, are set forth in the appended claims.

Technology Classification (CPC): 2