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    • 专利摘要:
    systems and methods for reducing sludge produced by wastewater treatment plants. the invention relates to methods and systems for improved sludge removal while maintaining effluent quality. methods including directing a wastewater inlet stream to one are treated, the stream having a flow of at least 20,000 gallons per day (76,000 l per day); the wastewater inlet stream having at least 50 mg / l solids and a dbo of 100 mg / l; removal of solids and dbo from the wastewater inlet stream at the treatment plant to provide a final effluent stream; the final effluent stream having less than 10% of the solids from the wastewater stream and less than 10% dbo from the wastewater stream; removal of solids and dbo producing less than approximately 0.25 mg of secondary sludge (0.25 g / g) per milligram of dbo removal.
    公开号:BR112012018986B1
    申请号:R112012018986-7
    申请日:2011-03-15
    公开日:2020-09-29
    发明作者:Robert G. Whiteman
    申请人:Robert G. Whiteman；
    IPC主号:
    专利说明:

    Background
    [001] Wastewater generated by water from industries and municipalities is commonly collected and sent to a treatment plant for the removal of various physical, chemical and biological pollutants before being discharged into a receiving water body. To carry out the necessary treatment, many public and private treatment plants employ both physical and biological treatment methods. Physical methods include screening, grinding and physical sedimentation which are effective processes for removing larger and heavier solids in wastewater. However, smaller, lighter solids and other pollutants soluble in wastewater resist removal by physical methods. For these pollutants, biological treatment methods such as activated sludge and gouging filters are commonly used.
    [002] The regulations for pollutant discharge from municipal wastewater treatment systems have become more restrictive in recent years. In response, many municipalities have developed new wastewater treatment systems or adapted existing systems to reduce the discharge of pollutants. Pollutants can be in many ways, the most common being Biochemical Oxygen Demand (BOD), Chemical Oxygen Demand (COD), Total Suspended Solids (TSS), ammonia, total nitrogen, nitrate, nitrite and phosphorus.
    [003] Biological treatment systems, such as conventional activated sludge systems and membrane bioreactors are a method to reduce pollutants in a wastewater tributary. The term "affluent" refers to waste water or other raw (untreated) or partially treated-flowing liquid to a reservoir, basin, treatment process or treatment facility or treatment plant. The biological treatment systems are designed and function to retain an adequate amount of the activated sludge in such a way that the pollutant load contained in the water body treated by the system will be adequately reduced. The net amount defined as the weight or mass of useless active sludge produced is related to the Solid Retention Time (TRS) of the system. The minimum RRT required to treat various pollutants under various conditions is generally well known. Conventional activated sludge systems conserve activated sludge using clarification or sedimentation devices and can maintain adequate activated sludge by using clarification or sedimentation devices and can maintain an appropriate TRS to treat pollutants as long as the sludge concentration flow activated and the sedimentability of the activated sludge or clarifiers that goes to the sedimentation basins are within reasonable limits defined by the design parameters, which depend on the area of the sedimentation basins or clarifiers and on the characteristics of the activated sludge. Membrane bioreactor systems conserve activated sludge using membrane filtration equipment and can function successfully at significantly higher activated sludge concentration than is typical for conventional activated sludge systems, but are more limited in their use. ability to process occasional high flow rates.
    [004] When the pollutant load or hydraulic capacity limits are reached, the treatment plants are at risk of violating the licensed limit, with possibilities for federal or state lawsuits, and restrictions or prohibitions of domestic and industrial growth within the service area of the treatment service collection system. Typically, wastewater treatment plants undergo physical expansion to suit the needs of the increased hydraulic load. However, physical expansion is expensive and often requires additional area, which may not be available, adjacent to existing facilities, particularly in large cities, where the cost of the area is high.
    [005] Therefore, it is desirable to find a way to increase the volumetric or mass pollutant load and the hydraulic capacity of the installations without the need to expand the physical installations. A significant advantage of the present invention over prior art methods of sludge processing is that the volumetric load of pollutants can be increased substantially with the addition of a biofermenter in existing physical facilities. In addition, it is also a feature and an advantage of the present invention that the improved sludge process produces a biological sludge with improved sedimentation characteristics. Improved sedimentation characteristics allow increases in hydraulic load without requiring an increase in the size of the physical elements of the activated sludge system because the net loss and / or sludge production are lower. Another advantage is a reduction in operating costs, such as chemical products, labor, energy and transportation because there is less biological sludge to be handled in the sludge management and disposal processes, which typically represents 40 to 50% operating costs of a wastewater treatment plant. Precisely for this reason, the new wastewater treatment facilities can be built in smaller sizes, with a very reduced need for sludge management facilities and consequently at lower capital costs than the known systems. For existing wastewater treatment systems that require an upgrade, it may be possible to eliminate the needs for capital expansion or the backward parts of the expansion or the entire expansion. Additionally, the time between biological sludge dumps can be extended by 25-50% for the processing of activated sludge in an aerobic or anaerobic digester, and from that processing, for the dewatering step such as by drying bed, filter press or centrifuge, by 25-50%. This additional time means less labor requirements, less equipment, less energy use and less use of chemicals. summary
    [006] The invention refers to an improved method for removing sludge while maintaining the quality of the effluent. The method includes directing a wastewater input stream to a treatment plant, the stream having a flow of at least 20,000 gallons per day (76,000 L per day); the wastewater inlet stream having at least 50 mg / L of solids and a BOD of 100 mg / L; removal of solids and BOD from the wastewater inlet stream at the treatment plant to provide a final effluent stream; the final effluent stream having less than 10% solids from the wastewater stream and less than 10% of the BOD from the wastewater stream; removing solids and BOD producing less than approximately 0.25 pounds of secondary sludge per pound (0.25 g / g) of the removed BOD. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 200 mg / L and the removed solid can be less than approximately 0.25 pounds of secondary sludge per pound (0 , 25 g / g) of the removed BOD. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 400 mg / L and the removed solid can be less than approximately 0.25 pounds of secondary sludge per pound (0 , 25 g / g) of the removed BOD. In the method, the wastewater inlet stream can have at least approximately 50 mg / L of solids and a BOD of 100 mg / L and the removed solid can be less than approximately 0.125 pounds of secondary sludge per pound (0.125 g / g) the removed BOD. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 200 mg / L and the removed solid can be less than approximately 0.125 pounds of secondary sludge per pound (0.125 g / g) the removed BOD.
    [007] In another embodiment, the invention refers to an improved method for removing sludge while maintaining the quality of the effluent. The method includes directing a wastewater input stream to a treatment plant, the stream having a flow of at least 20,000 gallons per day (76,000 L per day); the wastewater inlet stream having at least 50 mg / L of solids and a BOD of 100 mg / L; removal of solids and BOD from the wastewater inlet stream at the treatment plant to provide a final effluent stream; the final effluent stream having less than 10% of the solids in the wastewater stream and less than 10% of the BOD of the wastewater stream; the removal of solids and BOD producing less than approximately 0.25 pounds of biological sludge per pound (0.25 g / g) of the removed BOD. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 200 mg / L and the removed solid can be less than approximately 0.25 pounds of biological sludge per pound (0 , 25 g / g) of the removed BOD. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 400 mg / L and the removed solid can be less than approximately 0.25 pounds of biological sludge per pound (0 , 25 g / g) of the removed BOD. In the method, the wastewater inlet stream can have at least approximately 50 mg / L of solids and a BOD of 100 mg / L and the removed solid can be less than approximately 0.125 pounds of biological sludge per pound (0.125 g / g) the removed BOD. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 200 mg / L and the removed solid can be less than approximately 0.125 pounds of biological sludge per pound (0.125 g / g) the removed BOD.
    [008] In another embodiment, the invention refers to an improved method for removing sludge while maintaining the quality of the effluent. The method includes directing a wastewater input stream to a treatment plant, the stream having a flow of at least 20,000 gallons per day (76,000 L per day); the wastewater inlet stream having at least 50 mg / L of solids and a BOD of 100 mg / L; removing solids and BOD from the wastewater inlet stream at the treatment plant to provide a first final effluent stream; the first final effluent stream having less than 10% of the solids in the wastewater stream and less than 10% of the BOD of the wastewater stream; treatment of the wastewater stream by the addition of a batch of biofermenter treatment, in which the weight of sludge removed is reduced by at least approximately 10% without increasing the solids and BOD in the final effluent stream. In the method, the treatment batch can be added to the anaerobic digester, the equalization basin and / or the primary clarifier. In the method, the weight of the removed sludge can be reduced by at least approximately 25% without increasing the solids and the BOD in the final effluent stream. In the method, the weight of the removed sludge can be reduced by at least approximately 50% without increasing the solids and BOD in the final effluent stream.
    [009] In yet another embodiment, the invention refers to an improved method for removing sludge while maintaining the quality of the effluent. The method includes directing a wastewater input stream to a treatment plant, the stream having a flow of at least 20,000 gallons per day (76,000 L per day); the wastewater inlet stream having at least 50 mg / L of biological solids and the BOD of 100 mg / L; removing biological solids and BOD from the wastewater input stream at the treatment plant to provide a final effluent stream; the final effluent stream having less than 10% of the biological solids from the wastewater stream and less than 10% of the BOD from the wastewater stream, the removal of solids and the BOD producing less than approximately 0.25 pounds of biological solids per pound (0.25 g / g) of BOD removed. In the method, the sludge can be a primary sludge, a biological sludge, and or the sludge can comprise a primary sludge and a biological sludge. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 200 mg / L and the removed solid can be less than approximately 0.25 pounds of biological solids per pound (0 , 25 g / g) of the removed BOD. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 400 mg / L and the removed solid can be less than the approximately inlet wastewater stream can have at least approximately 50 mg / L of solids and a BOD of 100 mg / L and the solids removed are less than approximately 0.125 pounds of biological solids per pound (0.125 g / g) of BOD removed. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 200 mg / L and the removed solid can be less than approximately 0.125 pounds of biological solids per pound (0.125 g / g) the removed BOD.
    [0010] In an additional embodiment, the invention refers to an improved method for removing sludge while maintaining the quality of the effluent. The method includes directing a wastewater input stream to a treatment plant, the stream having a flow of at least 20,000 gallons per day (76,000 L per day); the wastewater inlet stream having at least 50 mg / L of solids or a BOD of 100 mg / L; removal of solids and BOD from the wastewater inlet stream at the treatment plant to provide a final effluent stream; the final effluent stream having less than 10% of the solids in the wastewater stream and less than 10% of the BOD of the wastewater stream; the removal of solids and BOD producing less than approximately 0.25 pounds of secondary sludge per pound (0.25 g / g) of the removed BOD. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 200 mg / L and the removed solid can be less than approximately 0.25 pounds of secondary sludge per pound (0 , 25 g / g) of the removed BOD. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 400 mg / L and the removed solid can be less than approximately 0.25 pounds of secondary sludge per pound of BOD removed. In the method, the wastewater inlet stream can have at least approximately 50 mg / L of solids and a BOD of 100 mg / L and the removed solid can be less than approximately 0.125 pounds of secondary sludge per pound (0.125 g / g) the removed BOD. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 200 mg / L and the removed solid can be less than approximately 0.125 pounds of secondary sludge per pound (0.125 g / g) the removed BOD.
    [0011] In yet another embodiment, the invention refers to an improved method for removing sludge while maintaining the quality of the effluent. The method includes directing a wastewater input stream to a treatment plant, the stream having a flow of at least 20,000 gallons per day (76,000 L per day); the wastewater inlet stream having at least 50 mg / L of solids or a BOD of 100 mg / L; the removal of solids and BOD from the wastewater inlet stream at the treatment plant to provide a final effluent stream; the final effluent stream having less than 10% of the solids in the wastewater stream and less than 10% of the BOD of the wastewater stream; the removal of solids and BOD producing less than approximately 0.25 pounds of biological sludge per pound (0.25 g / g) of the removed BOD. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 200 mg / L and the removed solid can be less than approximately 0.25 pounds of biological sludge per pound (0 , 25 g / g) of the removed BOD. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 400 mg / L and the removed solid can be less than approximately 0.25 pounds of biological sludge per pound (0 , 25 g / g) of the removed BOD. In the method, the wastewater inlet stream can have at least approximately 50 mg / L of solids and a BOD of 100 mg / L and the BOD removed. In the method, the wastewater inlet stream can have at least approximately 100 mg / L of solids and a BOD of 200 mg / L and the removed solid can be less than approximately 0.125 pounds of biological sludge per pound (0.125 g / g) the removed BOD. Brief description of the drawings FIG. 1 is a flow diagram of the conventional activated sludge process. FIG. 2 is a diagram illustrating a conventional wastewater treatment process. FIG. 3 is a diagram illustrating an example of a wastewater treatment sequence and process. FIG. 4 is a diagram illustrating an example of a wastewater treatment sequence and process. Detailed description of the preferred designs and modalities present.
    [0012] Various embodiments of the present invention provide wastewater treatment systems and methods. Many embodiments of the invention are able to receive an affluent that exceeds one or more environmental standards and discharge an effluent that meets current environmental standards, including limitations on BOD, COD, TSS, ammonia, nitrate, nitrite, total nitrogen, and phosphorus levels . Such environmental discharge standards are controlled under or by the National Pollutant Discharge Elimination System (NPDES). Aspects of the invention can be selected to maximize treatment efficiency and minimize operating costs during “normal” operation, while still producing acceptable discharge quality with the same system even during periods of high intake.
    [0013] Specifically, the present invention relates to a method of treating wastewater, in which the liquid biological sludge discharged or produced is reduced. Summary.
    [0014] The practice of the present invention employs, unless otherwise indicated, the conventional techniques of wastewater treatment technologies, which are within the common skills of a qualified Class 1 or Class A technical operator or an Environmental Engineer graduate. Such techniques and the definition of technical terms are fully explained in the literature, such as, Operation of Wastewater Treatment Plants Manuals, A Field Study Training Program, 4th Edition, Volumes 1 and 2, California State University, Sacramento, 1993; Industrial Waste Treatment, A Field Study Training Program, California State University, Sacramento, 1991; Advanced Waste Treatment, A Field Study Training Program, Second Edition, California State University, Sacramento, 1993; and Operation and Maintenance Wastewater Collection Systems, A Field Study Training Program, Fourth Edition, Volumes 1 and 2, California State University, Sacramento, 1993, for operator certification.
    [0015] Waste water can be treated close to where it is generated (in septic tanks, biofilters or aerobic treatment systems), or collected and transported via a pipe network and the pump stations referred to as a collection system for a facility wastewater treatment. Wastewater collection and treatment are typically subject to local, state and federal regulations and standards. Industrial sources of wastewater often require specialized treatment processes.
    [0016] Typically, wastewater treatment involves three stages, called primary, secondary, and tertiary treatments.
    [0017] The primary or sedimentation stage / treatment consists of temporarily keeping the tributary wastewater in a static basin where heavy solids can settle to the bottom while fats, oils, grease and lighter solids float on the surface. The decanted and floating materials are removed and the remaining liquid can be discharged or subjected to secondary treatment.
    [0018] The term "affluent" refers to a waste water or other raw (untreated) or partially treated liquid, flowing into a reservoir, basin, treatment process or treatment plant or treatment facility.
    [0019] In the primary stage, wastewater flows through large tanks, commonly called "primary clarifiers" or "primary sedimentation tanks". The term "clarifier" refers to settling tanks or sedimentation basins ”, which are tanks or basins in which wastewater is kept for a period of time, during which the heaviest solids settle to the bottom and the lightest material floats on the water surface. The tanks are quite large so that the sludge can settle and float the material, such as grease and oils that can reach the surface and be skimmed. The main objective of the primary sedimentation step is to produce both a generally homogeneous liquid capable of being treated biologically and a sludge that can be separately treated or processed. Primary settling tanks are usually equipped with mechanically driven scrapers that constantly direct the collected sludge towards a hopper at the bottom of the tank from where it can be pumped to additional sludge treatment steps.
    [0020] The term "sludge", includes "primary sludge," "secondary sludge" or "biological sludge" and differently "solids", these three words are used interchangeably and depending on the context, refer to the excessive biomass produced during secondary (biological) treatment of biodegradation of organic matter.
    [0021] The term “primary sludge” refers to liquid semi-waste that results from sedimentation using primary treatment, without additional treatment. It typically includes organic material, paper, faecal matter / solids that decant and are removed from the bottom of the primary clarifier or dredged from the equalization basin or a pretreatment. Primary sludge can also include secondary sludge where co-sedimentation of secondary and primary sludge is practiced in primary clarifiers
    [0022] The terms "secondary sludge" or "biological sludge" refer to excessive biomass produced during the secondary (biological) treatment of the biodegradation of organic matter. Secondary sludge includes activated sludge, mixed sludge, and chemically precipitated sludge.
    [0023] The term "solids" refers to primary sludge, secondary sludge or both.
    [0024] The term "biosolids" refers to a primary solid product, produced by wastewater treatment processes.
    [0025] The concentration / reduction of solids via anaerobic digestion combines the primary and secondary sludge. Aerobic processes usually only process the secondary.
    [0026] Sludge is typically removed from wastewater to maintain the accumulation of solids in the biological process. After sludge removal, it can undergo a sludge management process that can take many forms from the initial treatment to reduce the sludge volume using aerobic or anaerobic digestion, followed by chemical agents using concentration step (flocculants or polymers) in machines, such as centrifuges, belt presses for final disposal via land application and incineration and landfill. Sludge disposal and the subsequent management process is important to maintain the food-to-microorganism ratio (F: M ratio) in an activated sludge plant, as the F: M ratio is a major parameter in determining and controlling effluent quality. The term "F: M ratio" refers to the ratio between food and microorganism, which is a measure of the food supplied to bacteria in an aeration tank.
    [0027] The secondary treatment removes the dissolved and suspended biological matter. Secondary treatment is typically performed by native microorganisms, floating in a managed habitat, namely the biological waste treatment system. Secondary treatment requires a separation process to remove microorganisms from treated water prior to discharge or tertiary treatment.
    [0028] Tertiary treatment is sometimes defined as nothing more than primary and secondary treatments. Treated water is sometimes disinfected chemically or physically (for example, by lagoons and microfiltration) prior to discharge into a stream, river, bay, lagoon, or wetland, or it can be used for irrigation of a golf course, gardens or park. If it is clean enough, it can also be used to refill the water table or for agricultural purposes.
    [0029] Generally, affluent wastewater can also be pre-treated. Pretreatment removes materials, such as large objects that can be easily collected from raw sewage before they damage or clog the pumps and skimmers of primary treatment clarifiers. This is most commonly done with a mechanically clean automated bar screen on modern plants that serve large populations, while on smaller or less modern and manually cleaned plants the screen can be used. They typically walk by cleaning a mechanical bar screen according to the accumulation in the bar screens and / or flow rate. The solids are collected and then disposed of in a landfill or incinerated.
    [0030] Pre-treatment may also include a sand or sand channel or chamber where the speed of incoming wastewater is carefully controlled to allow sand, sand and stones to settle.
    [0031] After tertiary treatment, the accumulated sludge must be treated and disposed of in a safe and effective manner. The goal of digestion is to reduce the amount of organic matter and the number of disease-causing microorganisms present in solids. The most common treatment options include anaerobic digestion, aerobic digestion, and composition. Incineration can also be used.
    [0032] The choice of solid wastewater treatment method depends on the amount of solids generated and other specific local conditions. However, in general, composting is most often used for smaller scale applications followed by aerobic digestion and then for final anaerobic digestion for larger municipal applications.
    [0033] Anaerobic digestion is a bacterial process that is carried out in the absence of oxygen. The process can be thermophilic digestion, in which the sludge is fermented in tanks at a temperature of 55 ° C, or mesophilic, at a temperature of approximately 36 ° C. Although allowing for a shorter retention time (and thus smaller tanks), thermophilic digestion is more expensive in terms of energy consumption for sludge heating.
    [0034] A main feature of anaerobic digestion is the production of biogas (with the most useful component being methane), which can be used in generators for the production of electricity and / or in boilers for heating purposes.
    [0035] Aerobic digestion is a bacterial process that occurs in the presence of oxygen. Under aerobic conditions, bacteria quickly consume organic matter and convert it into carbon dioxide. The operating costs for aerobic digestion are significant because of the energy used by blowers, pumps and engines that have to add oxygen to the process even with the recent advent of stone fiber filter technology that uses natural air currents for oxygenation. Aerobic digestion can also be achieved by using jet aerators to oxidize sludge, which is also expensive, but less expensive than traditional processes.
    [0036] Composting is also an aerobic process that involves mixing sludge with carbon sources, such as sawdust, straw or wood chips. In the presence of oxygen, the bacteria digest both the wastewater solids and the added carbon source and thus produce a large amount of heat.
    [0037] Sludge incineration is less common due to concerns about gaseous emissions and the supplementary fuel (typically natural gas or fuel oil) needed to burn the low calorific sludge and vaporize the waste water. Multiple fireplace floor incinerators with a high residence time as well as fluidized bed incinerators are the most common systems used to burn wastewater sludge. The shared burning in municipal waste plants for power generation is occasionally done, this option is less expensive assuming that the facilities already exist for solid waste as well as there is no need for auxiliary fuel.
    [0038] When liquid sludge is produced, additional treatment may be necessary to make it suitable for final disposal. Typically, the sludge is thickened (dehydrated) to reduce the volumes transported out of the site for disposal. There is no process that completely eliminates the need to dispose of biosolids. There is, however, an additional step that some cities are taking to overheat the wastewater sludge and convert the "cake" into small pelleted granules that have a high concentration of nitrogen and other organic materials and are used as fertilizers. This product can then be sold to local farmers and pasture farms as a soil regulator or fertilizer, reducing the amount of space needed to dispose of sludge in landfills. The fluid removed, called centered, is typically reintroduced into the wastewater process.
    [0039] There are different types of wastewater treatment systems and processes. In the example of wastewater treatment the system is an activated sludge process, which is illustrated in FIG. 1 with a flow diagram. Generally, during the pretreatment stage, the tributary is first evaluated to remove roots, rags, cans, and larger debris, which can then be towed to a landfill or for possible grinding and returned to the plant flow. Then, the sand and gravel are removed from the tributary during the sand removal step and the wastewater is pre-aerated to cool the wastewater and help remove the oil. The tributary is then passed through a flow meter that measures and records the flow. After pretreatment, the affluent is subjected to primary treatment, including sedimentation and flotation that removes sedimentable and floating materials after the primary treatment, wastewater enters secondary treatment (also known as biological treatment) to remove compounds by biodegradation. soluble or dissolved organics while suspended solids are removed via flake entrapment with no biodegradation after some time. After secondary treatment, wastewater enters tertiary treatment where wastewater is disinfected to kill pathogenic organisms, and is usually re-aerated before effluent is discharged.
    [0040] FIG. 2 illustrates another example of the wastewater treatment process. Specifically, this is an example of a pure oxygen system. The pure oxygen system is a modification of the activated sludge process. The main difference is the method of delivering dissolved oxygen to the activated sludge. In other activated sludge processes, air is compressed and released under water to produce an air-water interface that transfers oxygen to water (dissolved oxygen). If compressed air is not used, surface aerators agitate the water surface to bring air into the water to obtain oxygen transfer in the pure oxygen system, the only real differences being that pure oxygen is released below the surface or directed to the water by means of surface aerators instead of air and the aerators are covered. In this process, the tributary is subjected to primary clarification. As shown in FIG. 2, the affluent is pre-treated, then subjected to a primary clarifier, pure oxygen reactors, and a secondary clarifier. The effluent can be contacted with chlorine and disposed of in receiving waters. The sludge can be returned to the pure oxygen reactors or combined with the sludge thickened from the primary clarifier and submitted to the primary and secondary anaerobic digester. The solids can then be dehydrated.
    [0041] Other wastewater treatment processes are known in the art and can be used according to the methods of the present invention.
    [0042] Wastewater Treatment Methods.
    [0043] In one embodiment, the invention is a method for treating wastewater, in which the liquid sludge discharged and / or produced in the method is reduced.
    [0044] In the method, a biofermentation system, which has been described in great detail in U.S. Publication No. 2003/0190742, the contents of which are incorporated here in their entirety are placed on-site at the wastewater treatment plant.
    [0045] The on-site system is for the growth of microbes at the site or the location of contaminated wastewater and generally includes a main tank, a water inlet, an outlet for the treatment batch, a mixing apparatus, and a temperature control device. The nutrient, water and an inoculum comprising microbes are deposited in the on-site system. The inoculants are grown in the on-site system to provide a batch of treatment that includes an increased number of microbes. At least a portion of the treatment batch is directly applied to contaminated wastewater, in such a way that the microbes are not isolated, concentrated or lyophilized between the growth and application stages. Microbes reduce contaminants in contaminated wastewater. In large activated sludge plants or single-stage lagoons a holding tank can be used to transfer the treatment batch where the treatment batch can be diluted to create a larger pumping volume and for dosing purposes to achieve continuous discharge from the batch of treatment.
    [0046] Importantly, the use of the on-site biofermentation system takes into account sufficient, repeated inoculation of functional microbes (whether it is an exogenous or native source) that allows a microbial population to be established quickly and free from competition from an undesirable native population, such as filamentous or Zoogloeal type microbes, which cause the cluster. There is a tremendous commercial need to resolve such problems as filamentous microbes or Zoogloeal clusters, which can increase the total operating cost of a wastewater treatment facility by as much as 20 to 25%. The first area of increased treatment costs arises because of the need to use settling aids or chemicals to clarify the water and concentrate the biomass in the secondary clarifier. Examples of such chemicals include polymers, bentonite, alum, or ferric salts. The second area of increased costs arises due to the poor dehydration of the growth of filaments and Zoogoeal, thus increasing the amount of equipment needed to process the sludge and the amount of polymer in the dewatering, and consequently the costs. The third area of increased cost arises when more labor is needed as the operation becomes less efficient and transportation costs and increased eviction fees. The biofermentation system provides a process that applies control or displaces unwanted microbes, such as filamentous or Zoogloeal microbes that cause sedimentability and agglomeration problems. The fermentation process is used to reduce or eliminate the use of the polymer to improve sedimentation, minimize the use of dewatering chemicals, and minimize the need for sludge management, labor costs, transportation and handling fees. discard.
    [0047] Additionally, the biofermentation process takes into account the provision of an effective concentration of desired microbes at a point of application sufficient to significantly treat wastewater at the point of application. Optimally, the inoculum is grown at a concentration of approximately 108-109 colony forming units per milliliter (cfu / ml) to achieve a minimum preferable inoculation of approximately 103 to 104 cfu / ml at the point of application.
    [0048] The types of microbe or microbes present in the inoculum depend on the type of waste water to be treated. The inoculum may contain a single strain or multiple strains supplied as a liquid or dry product. The dried product is commonly freeze-dried or air-dried. Additionally, microbes can be microbes exogenous to wastewater or native microbes can be isolated from wastewater under treatment.
    [0049] The terms microorganism, microbe, or organism, as used here, are exchangeable and include fungi, yeasts, bacteria, and other small unicellular organisms of biodegradability.
    [0050] Preferably, sludge reduction microorganisms, which can be purchased from Advanced Biofermentation Services Inc., Fleming Island, FL, are used for wastewater treatment in wastewater treatment plants where the efficiency of BOD removal is low, the system is overloaded, and / or at any treatment plant to reduce operating costs related to sludge management, which typically represents approximately 40 to 50% of the operating costs of any facility.
    [0051] Examples of some microbes with particular biodegradation characteristics are given in Table 1. Table 1
    Notes: Spp. = the species, these may vary, Subfiles is a species of Bacillus; Putida is a species of Pseudomonas; CO2 = carbon dioxide.
    [0052] The determination which culture or manufacturer's formulation is most effective for treating particular wastewater can be made using standard respirometric techniques. The principle of respirometry is to measure the activity of a biomass exposed to a test substrate compared to a control containing biomass and a known substrate that gives a predictable result. The substrate to be tested can vary from a specific chemical waste stream or combined wastewater. Respirometry experiments can be adjusted to stimulate aerobic or anaerobic environments. Typical applications of re-spirometry include the assessment of the following: treatability of municipal and industrial wastewater, toxicity of specific waste streams or chemicals; bio-degradability of chemicals; biochemical oxygen requirement (BOD); and oxygen absorption rates (TAO).
    [0053] Aerobic microorganisms use 0 oxygen to grow and metabolize organic substrates. For aerobic microbes, it is considered that the oxygen absorption rate (TAO) is directly related to organic stabilization, and consequently, related to the formulation's ability to biodegrade organic waste.
    [0054] Respirometry equipment and treatability procedures for both aerobic and anaerobic studies can be obtained from manufacturers in the United States, such as Challenge Environmental Systems of Fayetteville, Ark .; Arthur Technology of Fond du Lac, Wis .; and Bioscience Management of Bethlehem, Pa. Examples of aerobic treatability studies can be found in technical documents, such as Whiteman, GR, TAPPI Environmental Conference- “Application of Selected Microbial Formulations in the Pulp and Paper Industry,” TAPPI Environmental Proceedings, Book 1, pages 235-238, April 1991; Whiteman, G. R., Gwinnett Industrial Conference- “Optimizing biological Processes-A Look Inside The Black Box,” April 1995; and Whiteman, G. R., TAPPI Environmental Conference- “Improving Treatment“ Performance with Natural Bioaugmentation ”, TAPPI Environmental Proceedings, Vancouver, BC, 1998; the disclosures of which are incorporated herein by reference.
    [0055] Once the effectiveness of each isolate, isolate, and / or the formulation has been compared using respirometry techniques, then the best can be selected as the inoculum of the fermentation process described here. Ready, prepared cultures can be purchased from Advanced Biofermentation Services Inc., Fleming Island, FL.
    [0056] The term "nutrients" refers to substances that must support living plants and organisms. The main nutrients are carbon, hydrogen, oxygen, sulfur, nitrogen, and phosphorus. Nutrients include both macronutrients and micronutrients. The typical composition of a microbe is shown below in Table 2, in which it is evident that different microbes have different compositions. Microbes also have different capacities to assimilate nitrogen into amino acids, the basic building blocks of proteins or purine or pyrimidine bases of ribonucleic acid (RNA) and deoxyribonucleic acid (DNA). Therefore, different microbes have different requirements for macronutrients (nitrogen and phosphorus) and micronutrients (for example magnesium, calcium, potassium, sodium, manganese, cobalt, nickel, zinc, iron, chloride and sulfur) to optimize the fermentation process. See Introductory Microbiology by Levy, et al., The disclosure of which is incorporated here by reference for information on macronutrients and micronutrients including concentrations of fastidious (difficult to grow) microbes, how to determine whether a particular micronutrient is needed, and explanations the role of nutrients in general. Table 2


    [0057] Active biomass, mainly composed of bacteria, in a biological treatment facility contains 8 to 15% nitrogen for most bacteria, most typically 12 to 12.5% phosphorus and 2 to 5% phosphorus, most typically 2.3 to 2.6%. Phosphorus is important in the formation of adenosine triphosphate (ATP) which is how microbes store energy.
    [0058] Microbes are composed of proteins, carbohydrates, fatty materials called lipids, or combinations of these substances. In particular, proteins are used to produce enzymes that are the basis of the biodegradation process. A series of reactions make up the process of biodegradation of any particular organic substance. A specific enzyme performs each reaction. These enzymes are composed of amino acids and sometimes cofactors, usually metals, that make up the reactive sites of enzymes where the biodegradation and conversion of an organic substance takes place. Optimally, micronutrients are present in an amount sufficient to optimize the biodegradation process or fermentation. Micronutrients include substances, such as vitamins, coenzymes, metals, or the inorganic compounds needed, such as cofactors for the production of enzymes, coenzymes or for cell growth. For example, sulfur is necessary for the assimilation of essential amino acid cysteine and methionine. Information on the role of such micronutrients, such as coenzymes, including folic acid, pantothenic acid (Coenzyme A), vitamin B12 (cobamide), biotin, nicotinic acid or nicotinamide (NAD), vitamin B1 (thiamine, vitamin B2 (riboflavin, vitamin B6 (pyridoxine), lipoic acid and ascorbic acid is found in Biochemistry, Second Edition, Albert L. Lehninger, Wort Publishers Inc, 1975, ISBN: 0-87901-047- 9, and Introductory Microbiology by Levy, et al., John Wiley & Sons Inc, 1973, ISBN 0- 471-53155-3, the disclosures of which are incorporated herein by reference.
    [0059] As mentioned earlier, the type of microbe or microbes used in the wastewater treatment process of the present invention depends on the type of wastewater problem to be addressed. The microbes most commonly used are bacteria, and most commonly, aerobic, mesophilic bacteria are used. Aerobic bacteria use oxygen to metabolize organic matter, as measured, for example, by biochemical oxygen requirement (BOD), chemical oxygen requirement (COD), total organic carbon (TOC), or total carbon (TC). It is also possible to use optional bacteria, which can metabolize with or without oxygen, or anaerobic bacteria, which do not use oxygen. Bacteria are also classified according to the temperature at which they grow optimally. Optimal temperatures are, for thermophiles: 55 to 75 ° C .; for mesophiles: 30 to 45 ° C .; and for mandatory psychrophiles: 15 to 18 ° C.
    [0060] The application or use of such a local biofermentation process and system results in a lower net sludge loss and / or production from any municipal or industrial wastewater treatment plant.
    [0061] A preferred wastewater treatment sequence and the processes according to the present invention are generally illustrated in FIGS. 3 and 4. The methods, however, are not limited to any particular system illustrated in the drawings or detailed above, any apparatus that allows the performance of a method of the invention can be used instead.
    [0062] In relation to FIG. 3, wastewater treatment according to the methods of the present invention includes pre-treatment, primary treatment (chemical and physical), secondary treatment (removal of suspended and dissolved organic solids), tertiary treatment, sludge treatment, dumping of sludge and liquid dump.
    [0063] The treatment steps specific to the wastewater treatment method of the present invention are shown in FIG. 4.
    [0064] The pretreatment stage includes sorting and removing sand, equalizing and storing and separating oil. The primary chemical treatment includes at least 2 stages of neutralization and chemical addition and coagulation. The primary physical treatment includes multiple flotation, sedimentation and filtration steps. Secondary treatment of dissolved organics includes activated sludge, anaerobic lagoon, aerated drip filter pond, stabilization basin, rotating biological contactor and filter. The suspended solid removal of the secondary treatment includes sedimentation of the solids or the internal aeration basin having a mute cycle (SBR) or the use of membranes. Then, wastewater undergoes tertiary treatment, which includes coagulation and sedimentation, filtration, carbon absorption, ion exchange and membrane. The sludge that results from the treatment steps is then available for sludge treatment. Specifically, sludge can be treated by digestion or liquid combustion. The sludge can also be made thick (dehydrated) by gravity or flotation to reduce the volumes transported out of the site for disposal. Also, the sludge can be treated by pressure filtration, vacuum filtration, centrifugation or pond formation or drying beds. After the sludge treatment, the sludge can be disposed of by incineration, ocean dumping and landfill. The treated diluted wastewater can also be disposed in the receiving waters, controlled or transported the discharge, the application of an oceanic discharge surface or the leakage of water tables, evaporation and incineration. Concentrated organic wastewater can be disposed of by deep well injection or incineration.
    [0065] Surprisingly, the wastewater treatment process that incorporates the local biofermentation system using microbes reduces the sludge of the present invention results in a net loss and / or lower sludge production.
    [0066] Specifically, typically, for every 1 pound (lb) of BOD treated by the secondary system, one would expect that 0.5 pound (lb) of sludge would be wasted and / or produced. Based on loads from the BOD of the tributary and typical removal of 90% of the BOD by most biological systems this would be equivalent to the 0.45 pound sludge produced by 1 pound of BOD entering the plant.
    [0067] The biological sludge production rates vary for the different constituents of wastewater, for example, fat, oil and / or grease (FOG) could produce 0.7 to 0.8 pounds of sludge / lb from the reduced BOD, while chemicals such as benzene or phenol can be as low as 0.25 pounds of sludge / lb of reduced BOD.
    [0068] However, when a biofermentation system that uses as its treatment batch sludge reduction microbes is installed on site in the wastewater treatment plant, according to the methods of the present invention, for every 1 lb of DBO treated by the secondary system, 0.125 pounds of sludge is wasted and / or produced. Based on the tributary BOD loads and typical 90% BOD removal by most biological systems this would be equivalent to 0.112 lb of the sludge produced per lb of DBO entering the plant, which is significantly less than one of those normally versed in the technique would wait based on the amount of the affluent entering the treatment plant.
    [0069] Without being tied to a particular mechanism, it is believed that the lower net sludge loss and / or production can be attributed, for example to the increased number of microbes present in the system and available for the biofermentation process as described in Publ. U.S. No. 2003/0190742. By increasing the number of viable microbes in the biological system, this essentially reduces the F: M ratio, which means more viable microbes with less food to eat. This in turn would result in the cellular metabolism of microbes that use BOD for cell maintenance instead of cell growth. The latter, therefore, would result in less biological sludge production. In addition, or alternatively, the benefit of reducing filamentous microbes (in the activated sludge system) results in better sludge sedimentation taking into account more sludge to be transported in the biological system, thus reducing the F: M ratio by increasing the TRS. This F: M reduction and increases in TRS are a classic method of reducing net sludge loss as sludge self-digests in the biological system resulting in lower net sludge loss. Examples. Example 1. Gray City
    [0070] The goal of this study was to improve BOD treatment efficiency and hydraulic capacity at the activated sludge wastewater treatment plant in the City of Gray, as the conventional treatment system was often overloaded on a daily basis in design ability.
    [0071] Before treatment, City of Gray had an activated sludge system for conventional wastewater treatment packaging designed to treat 400,000 gallons per day (Ipd) of municipal wastewater with an integrated aerobic digester and 4 drying beds. Typically, the sludge was poured into the drying beds after the first 90 days as was normal practice before the start of winter.
    [0072] A Model 250 biofermentation system, which can be purchased from Advanced Biofermentation Services, Fleming Island, FL and installed as previously described in Publ. U.S. No. 2003/0190742, was adjusted at the site adjacent to the activated sludge system to be treated.
    [0073] The Model 250 biofermenter has been adjusted to feed 30 gallons daily of 1/4 of a batch of resistance treatment, including microbes for BOD removal under the trade name “Biobooster for BOD removal” that can be purchased from Advanced Biofermentation Services, Fleming Island FL. A batch of full potency treatment is defined as adding 10 pounds of bionutrient (the nutrient used to grow microbes) to the biofermenter. As such, 1/4 of a batch of resistance treatment is equivalent to% or 2.5 pounds. The bionutrient used in the process can be purchased from Advanced Biofermentation Services, Fleming Island FL.
    [0074] The biofermentation process was initially adjusted to 90 days before winter. Within 90 days of starting treatment, significant improvements in the treatment process were observed by operators, including improved hydraulic capacity without loss of TSS in the effluent during peak flows (sometimes greater than 1 MGD) and better removal of DBO. Such observation was produced visually and noted by the operators.
    [0075] In the spring of the following year, it was surprisingly noticed that the sludge dumping into the drying beds did not occur and more attention was paid to the sludge dumping process.
    [0076] Several months later, the city observed that there was a 75% reduction in sludge production, which was observed due to the lack of use of drying beds. The city had already started to purchase a new belt press and a construction costing $ 800,000 to replace the drying beds. If the city had realized that biofermentation could reduce liquid sludge dumping and / or its production, then the city would not have approved the expense.
    [0077] Importantly, the City of Gray noticed a 65% reduction in the use of polymer and the hydraulic capacity was increased by 50%. Also, any foam / defoamer problems have been eliminated. All of this resulted in an improved wastewater treatment process. Example 2.
    [0078] The Dublin City Wastewater Treatment Facility (WWTP) has used alum to precipitate suspended solids and the associated BOD outside the final effluent for the past eight (8) years. The plant is a 4.0 MGD drip filter plant, with two sand displacement filters at the end that produce reusable water. WWTP has three licenses: (B1) 4 MGD, 30 DBO, 30 TSS (B2) 4 MGD, 25 DBO, 15 TSS (B3) 4 MGD, 25 DBO, 30 TSS
    [0079] To improve BOD removal, reduce the use of alum in the secondary clarifiers used for clarification, and develop a healthier biology to reach the full potential of the process, a biofermentation process, as described here, has been implemented in the City Dublin WWTP.
    [0080] Specifically, a Model 250 biofermentation system, which can be purchased from Advanced Biofermentation Services, Fleming Island FL and installed as previously described in Publ. U.S. No. 2003/0190742, was adjusted at the location adjacent to the percolation filter system. The Model 250 has been tuned to feed 60 gallons of% potency daily from a batch of treatment using a specific sludge reduction culture called “sludge reduction bio-reinforcement”, which can be purchased from Advanced Biofermentation Services Inc, Fleming Island, FL.
    [0081] The treatment was carried out for 45 days.
    [0082] After 45 days of using the biofermentation process, the city was able to stop using alum, saving the city approximately US $ 100,000.
    [0083] Also, the growth of algae in the rocks of the drip filter increased, the BOD of the effluent was reduced and TSS reached an 85% removal without the use of alum. There was also a noticeable reduction in the amount of biological sludge, which resulted in the use of the press five days a week, producing two reservoirs a day (consuming a roll of 20 yards each), to use the press once or twice a day. week producing one reservoir per day (consuming a 20 yard roll).
    [0084] Notably, after 6 months of operation the presses were used once every two weeks. This represented a reduction of more than 70% in sludge maintenance costs. The digester has also been improved (including primary sludge and secondary sludge). Specifically, the digester sludge was changed from 11/2% solids to 3% solids and a cleaner supernatant coming out of the digesters. Example 3 (Predictive)
    [0085] Method to improve anaerobic sludge digestion.
    [0086] Another recognized application of the surprising results in Dublin is the possibility of improving anaerobic sludge digestion.
    [0087] For the treatment of the anaerobic sludge digester, a biofermenter (purchased from Advanced Biofermentation Services, Fleming Island, FL) was adjusted at the digester site to add a batch of treatment directly to the digester. The dosage rate may vary based on the volume of the digester. However, typically for a digester of less than 1 MGV, the dosage rate is 10 - 60 gallons per day from a batch power of% to V2.
    [0088] To achieve faster rates of metabolism the dosage rates are doubled or quadrupled, as necessary to obtain the desired results.
    [0089] The cost-benefit for the client is dependent on improved quality of the digester supernatant and thickness of the solids that would help dehydration and result in lower costs of chemicals / polymers for dehydration. Also, operating costs would be due to less labor and a lower frequency of disposal. In addition, the efficiency of such anaerobic digesters is improved where the capacity for digestion is limited, thus avoiding capital expenditure or minimizing expenditure needs. Example 4 (Predictive).
    [0090] Method to improve sludge digestion in an equalization basin.
    [0091] Another recognized application of the surprising results in the city of Gray is the possibility of improving the digestion of sludge in the equalization basin, which are typically used by several small towns before treatment in a packaging plant. Also, expensive pretreatment and / or primary clarifiers can be avoided.
    [0092] For the treatment of sludge from the equalization basin a biofermenter (purchased from Advanced Biofermentation Services, Fleming Island, FL) is mounted to the equalization basin location to add a batch of treatment directly to the equalization basin at the plant entrance wastewater.
    [0093] The dosage rate could be based on the volume of the equalization basin or the inlet flow. Typically, however, the inlet flow volume for less than 1 - 3 MGV would be 10-60 gallons per day of one to 1/2% of the batch power. The scale increase for larger plants would be proportional. To achieve faster rates of metabolism the dosage rates can be doubled or quadrupled should be needed to obtain the desired results.
    [0094] The cost benefit to the customer would be dependent on removing the BOD that improves through the equalization basin and reducing the accumulation of solids and avoiding or transferring the need to dredge solids. Dredging is extremely expensive as it involves costs of dewatering equipment, chemicals / polymers for dehydration, labor, transportation and dumping fees. In addition, treatment can result in improving the efficiency of such equalization capacity where such capacity is limited, thus avoiding capital expenditure or minimizing the need for expenses. Example 5 (Predictive).
    [0095] Method to reduce the primary sludge in the primary clarifier before the anaerobic digester.
    [0096] Another recognized application of the surprising results in Dublin would be the possibility of reducing the primary sludge in the primary clarifier before the anaerobic digester as the treatment of the primary sludge is highly expensive.
    [0097] For the treatment of the primary clarifier sludge a biofermenter (purchased from Advanced Biofermentation Services, Fleming Island FL) is mounted on site to add a batch of treatment directly to the primary clarifier sludge at the inlet of the wastewater plant.
    [0098] The dosage rate may vary based on the volume treated by the wastewater treatment plant. Typically, however, the volume treated by the wastewater plant less than 1 - 3 MGV would be 10-60 gallons per day of a 1/4 to 1/2 batch power. The scale increase for larger plants would be proportional. To achieve faster rates of metabolism the dosage rates can be doubled or quadrupled and must be those to obtain the desired results.
    [0099] The cost benefit to the customer would be dependent on the reduction of the maintenance costs of primary sludge sludge, such as the costs of dewatering equipment, chemical / polymer compound for dehydration, labor, transport, and eviction. In addition, a second advantage would be improving the efficiency of such sludge management processes where such capacity is limited, thereby avoiding capital expenditure or minimizing the need for expenditure.
    [00100] All Patents, Patent Applications, Provisional Applications, and Publications mentioned or cited are hereby incorporated by reference in their entirety, including all figures and tables, to the extent that they are inconsistent with the explicit teachings of the this specification.
    [00101] Although various modalities of the invention have been described, it will be apparent to those ordinarily skilled in the art that many other modalities and applications will be possible within the limits of the invention. Consequently, the invention should not be restricted except in light of the appended claims and their equivalents.
    权利要求:
    Claims (1)
    [0001]
    1. Method to reduce sludge production in a wastewater treatment process by at least approximately 10% while reducing solids and BOD in a final effluent stream, CHARACTERIZED by the fact that it comprises treating a wastewater flow in a wastewater treatment plant by adding a batch of treatment from a biofermenter; where the wastewater treatment process comprises: directing the wastewater inlet stream to the treatment plant, the stream having a flow of at least 20,000 gallons per day (76,000 L per day) and the water inlet stream residuals having at least 50 mg / L of solids and a BOD of 100 mg / L; remove solids and BOD from the wastewater stream at the treatment plant to provide the final effluent stream; the final effluent stream having less than 10% of the solids in the wastewater stream and less than 10% of the BOD of the wastewater stream; in which the biofermenter is placed on-site at the wastewater treatment plant; wherein nutrient, water and an inoculum comprising microbes are deposited in an on-site biofermenter and the inoculum is grown in the biofermenter placed on-site to provide a batch of treatment comprising microbes; wherein the inoculum is grown at a concentration of approximately 108 to 109 colony forming units per milliliter (cfu / ml) to achieve a minimum preferable inoculation of approximately 103 to 104 cfu / ml at the point of application of the batch treatment; wherein the biofermenter includes a main tank, an inlet for water, an outlet for the treatment batch, a mixing apparatus, and a temperature control apparatus; and in which at least a portion of the treatment batch comprising microbes is applied directly to contaminated wastewater, such that the microbes are not isolated, concentrated or lyophilized between the stages of growth and application to the wastewater treatment process, and in which the treatment batch is added to an anaerobic digester, an equalization basin, a primary clarifier, an activated sludge system or a percolation filter system.
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    同族专利:
    公开号 | 公开日
    JP2013527023A|2013-06-27|
    EP2528869A2|2012-12-05|
    EP2528869B1|2019-05-01|
    PT2528869T|2019-07-19|
    ES2736248T3|2019-12-27|
    KR20140021953A|2014-02-21|
    KR20210054037A|2021-05-12|
    IN2012MN02051A|2015-06-12|
    CA2787971A1|2011-08-18|
    US20110186510A1|2011-08-04|
    CN102844276A|2012-12-26|
    BR112012018986A2|2018-03-27|
    CN107352752A|2017-11-17|
    PL2528869T3|2019-11-29|
    EP3549916A1|2019-10-09|
    KR20190003816A|2019-01-09|
    US9409803B2|2016-08-09|
    WO2011100089A2|2011-08-18|
    WO2011100089A3|2011-10-06|
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    法律状态:
    2018-04-10| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|
    2019-01-29| B06T| Formal requirements before examination [chapter 6.20 patent gazette]|
    2019-10-08| B06A| Patent application procedure suspended [chapter 6.1 patent gazette]|
    2020-01-14| B15I| Others concerning applications: loss of priority|Free format text: PERDA DA PRIORIDADE US 12/696,919 DE 29/01/2010 REIVINDICADA NO PCT/US2011/021464, CONFORME AS DISPOSICOES PREVISTAS NA LEI 9.279 DE 14/05/1996 (LPI) ART. 167O, DECRETO NO. 635 DE 21/08/1992 E CONVENCAO DA UNIAO DE PARIS (REVISTA EM ESTOCOLMO 14/07/1967), ART. 4O, ALINEA C, ITEM 1. ESTA PERDA SE DEU PELO FATO DO BRASIL NAO ACEITAR RESTABELECIMENTO DE PRIORIDADE (RESERVA DO BRASIL DE ACORDO COM A REGRA 49TER.1 ALINEA (G) E/OU 49TER.2 ALINEA (H) DO REGULAMENTO DE EXECUCAO DO PCT), JA QUE O PRAZO PARA O DEPOSITO INTERNACIONAL COM REIVINDICACAO DE PRIORIDADE ULTRAPASSOU OS 12 MESES. |
    2020-07-07| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|
    2020-09-29| B16A| Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 15/03/2011, OBSERVADAS AS CONDICOES LEGAIS. |
    优先权:
    申请号 | 申请日 | 专利标题
    US12/696.919|2010-01-29|
    US12/696,919|US9409803B2|2010-01-29|2010-01-29|Systems and methods for reducing sludges produced by wastewater treatment facilities|
    PCT/US2011/021464|WO2011100089A2|2010-01-29|2011-03-15|Systems and methods for reducing sludges produced by wastewater treatment facilities|
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