TH67424B - Sustainable methods and systems for low-cost treatment of water affected by bacteria and microalgae. - Google Patents

Abstract

DC60 (26/09/56) This invention reveals a system for the treatment and treatment of water bodies for use in low density recreation The system of this invention generally consists of the containment section, the co-ordination system, the dosing system, the mobile suction device, the non-interference suction device. moving without disturbance and filter equipment coordination system can receive information about Determinants of regulated water quality and can periodically stimulate the necessary processes. to adjust the water quality determinants to stay within the relevant limits The revealed system will filter only a small fraction of the total water volume by less than that filtered by the flow with the filter system of Up to 200 times as much as conventional swimming pools, this exposed method and system also uses less chemicals than the system. General swimming pool water treatment The system of this invention can be used to treat recreational water bodies. and provides a sustainable method for producing water that meets the Environmental Protection Agency's requirements. (Environmental Protection Agency) (EPA) on recreational water for bathing in contact with all parts of the body

Claims (3)

Claims (all) which will not appear on the classifieds page. :------11/10/2017------ (OCR) Page 1 of 7 Pages Claims 1. Sustainable methods for treating and treating water bodies affected by germs. bacteria and microalgae at low cost by filtering a small fraction of the whole body of water. This method includes: a. Collection of water with total dissolved solids (TDS) concentrations up to 50,000 ppm; b. one where the reservoir has a bottom surface. that can be thoroughly cleaned by a non-interference suction device; C. Restricting the density of water players to a maximum of 0.05 water players per cubic meter in such water contained in such reservoir d. in such quarantine with the total duration of Oxidation potential (ORP) is treated during this period by periodically adding disinfectant to the water to generate an ORP of approximately 500 mV, provided that the total ORP treatment during this period It depends on the temperature of the water to be treated. and consist of a minimum period of approximately 1 hour for each water temperature °C up to a maximum temperature of 45 °C; e. stimulation of the following processes through a coordinated system to purify such water; and Remove solids from such water by filtering only a small fraction of the total volume of such water in the containment. such collection, whereby the coordination system will obtain information about the correct water quality determinants controlled by the coordination system. and will trigger processes i, ii and iii to adjust the factor Set it within its limits: i. Suction of a portion of such water containing precipitated particles. with suction device moving to prevent the precipitating material from becoming thicker exceeds the average of 3 mm; i i. filtration of the part of the water sucked by the mobile suction device; and ii i. return of filtered water to such reservoir 2. Claim 1 method, where: a. If the water collected at stage a) has a dissolved solids concentration are total less than or equal to 10,000 ppm, the Langelier Saturation Index must be less than 3; or page 2 of number 7 p. b. If the water collected at stage a) has a total dissolved solids concentration greater than 10,000 ppm, the Stiff & Davis Saturation Index must be lower than 3. 3. Claim 2 method, where the Langlier saturation index is maintained below 2 by a process chosen from pH adjustment, antiscaling addition. antisealant or softening process 4. Claim 2 method, where the Stiff & Davis saturation index is maintained below 2 by a process selected from pH adjustment, Addition of antiscaling agent or water softening process 5. Claim 3 method, where the antiscaling agent consists of compounds such as phosphonates, phosphonic acid, PBTC (phosphonic acid). Phobutan- Tricarboxylic (phosphobutan-tricarboxylic acid), chromate (chromate), zinc polyphosphate (zinc polyphosphate), nitrite (nitrite), silicate (silicate), organic matter, caustic soda, polymers such as malic acid. (malic acid), sodium polyacrylate (sodium polyacrylate), ethylene diamine tetracetic acid, benzotriate Seoul 6. Claim 1 method wherein the data obtained by the coordination system is obtained from the experimental method. The bacteria are selected from chlorine and chlorine compounds; ozone (ozone); biguanide products (biguanide); halogen compounds (halogen); Bromine or a combination of these compounds 8. Claim 1 method, where the mobile suction device moves along the bottom of the retention section and sucks up the water containing the precipitated particles. 9. Method Fulfillment of claim 1, where such water is treated within the time interval to generate an ORP of approximately 500 mV, is the total treatment period during the water temperature dependent time interval. to such therapy without maintaining the permanent concentration of the disinfectant in the total amount of such water. Page 3 of 7 Page 1 0. Methods in accordance with Claim 1, where such reservoirs comprise a total volume of at least 15,000 m3. affected by bacteria and microalgae at low cost by filtering a small fraction of the whole body of water. This method includes: a. Collection of water with total dissolved solids (TDS) concentrations up to 50,000 ppm; b. one where the reservoir has a bottom surface. that can be thoroughly cleaned by a non-interference suction device; C. Limiting the density of water players to a maximum of 0.05 water players per cubic meter in such water contained in such reservoirs d. in such quarantine with the total duration of An oxidation reduction potential (ORP) is treated during this period by periodically adding a disinfectant to the water to generate an ORP of at least 500 mV, provided that the total ORP treatment is based on The temperature of the water to be treated and consist of a minimum period of approximately 1 h for each water temperature °C up to a maximum temperature of 45 °C; e. stimulation of the following processes through a coordinated system to purify such water; and Remove solids from such water by filtering only a small fraction of the total volume of such water in the containment. Such collection, whereby the coordination system obtains information about the correct water quality determinants. controlled by the coordination system. and will trigger processes i, ii and iii to adjust the factor Set it within its limits: i. Suction of a portion of such water containing precipitated particles. with suction device moving to prevent the precipitated material exceeding the average thickness of 3 mm; i i. filtration of the part of the water sucked by the mobile suction device; and ii i. Return of filtered water to such reservoir 1 2. Claim 1 method, provided that the total ORP treatment time is discontinued during a period of 7 days, page 4 of Number 7 Page 1 3. Claim method 12, where: a. If the water collected at stage a) has a total dissolved solids concentration less than or equal to 10,000 ppm, the saturation index The lier (Langelier Saturation Index) must be less than 3; or b. If the water collected in step a) has a total dissolved solids concentration greater than 10,000 ppm, the Stiff & Davis Saturation Index must be lower. 3 1 4. Claim 13 method, where the Langlier saturation index is maintained below 2 by a selected process of pH adjustment, antiscaling addition. Antiscalant or water softening process 1 5. Claim 13 method, where the Stiff & Davis saturation index is maintained below 2 by a process selected from pH adjustment, Add antiscaling or water softening process 1 6. Claims 14 method, where the antiscaling agent is composed of compounds such as phosphonates, phosphonic acid, PBTC (phosphobutan- tricarboxylic, chromate, zinc polyphosphate, nitrite, silicate, organic matter, caustic soda, malic acid polymer, sodium polyacrylate, sodium salt of Ethylene diaminetetraacetic acid, benzotriazol or a combination of these compounds 1 7. Claim method 12 wherein the data obtained by the coordination system were obtained from Method 1 8. Claim 12 method wherein the disinfectant is selected from chlorine and chlorine compounds; ozone; biguanide products; halogenated compounds; bromine compounds or a combination of these compounds 1 9. Claim 12 method, where the mobile suction device moves along the bottom of the reservoir and sucks up part of the precipitated water. Page 5 of 7 Page 2 0 The method according to claim 12, where such water is treated within a time interval to generate an ORP of at least 500 mV, is the total treatment period during the period depending on the water temperature at which will such therapy without maintaining a permanent concentration of the disinfectant in the aforementioned total volume of water. 2 1. Method pursuant to Claim 12, provided that the reservoir comprises a volume of at least 15,000 m3. 2 2. Method Fulfillment of Claim 12, provided that the total ORP treatment time was terminated during a period of 7 days 2. 3. Systems for the treatment and treatment of aquatic organisms affected by bacteria and algae. Small size with low cost by filtering a small part of the whole body of water This system consists of: a reservoir for water retention, a reservoir with a volume greater than 50,000 m3 and is assembled with a membrane or septum to accept precipitated particles fixed to the bottom surface of the reservoir. keep; - at least one feed pipe for supplying the exiting water to the reservoir; - a coordinated system for keeping water in reservoirs within specified water quality limits; - At least one dosing device for feeding or dispensing disinfectants or antiscaling agents. into the water in the reservoir; - Mobile suction device for moving along the bottom storage and suction of water from the bottom of the reservoir containing precipitated particles; - a drive device for driving the mobile suction device along the lower part of the reservoir, the drive device is operationally coupled with the mobile suction device; - Filter devices with a maximum filtration capacity of up to 2.5% of the total volume of the water body over a period of 24 hours for filtration of the part of the water with precipitated particles sucked up by the mobile suction device; - one or more collection pipes coupled between the mobile suction device and the filter device; and - the return pipe from the filter device to the containment where the coordination system is structured to receive data obtained by visual observations, experimental methods, algorithms, or detection devices based on water quality determinants and to control the actuation of dosing devices, devices Mobile suction and filtering equipment to adjust the factor. Page 6 of the number 7 determines the water quality within the specified limit, the water quality factor is composed of the potential Oxidation reduction (ORP), temperature, and precipitated particle thickness 2 4. Claims 23 system in which membranes or membranes are covered. The lower part of the reservoir is composed of a geomembrane. geo-membranes, geotextile membranes, plastic membranes or a combination of these materials 2 5. System according to Claim 23 wherein the dosing device consists of an injector, sprayer, manual dosing, weighing dispenser, tubing or a combination of these 2 6. Systems according to claim 23 where propulsion equipment consists of rail systems, cable systems, manual propulsion systems, robotic systems, remotely guided systems, motorized boats or motorized floating devices. or a combination of these systems 2. 7. Systems according to Claim 23, where the mobile suction device is assembled in an operational pair. with equipment driven by cord, rope, line, cable, flexible string or a combination of these materials 2 8. Claim 23 system where the mobile suction is combined with an operating The device is driven by solid wire (rod), bar, pole, rigid shaft or a combination of these materials 2. 9. System according to claim 23, where the filter device consists of a filter element. cylinder (cartridge filter), sand filter, micro-filter, ultra filter (ultra-filter), nano-filter or a combination of these filters 3 0. Claim 23 system, where the coordination system is structured to control the Activate the dosing device according to the data obtained to dispense the disinfectant periodically into the reservoir water over a period of 7 days to generate an ORP of at least approximately 500 mV for the total treatment duration at each of the 7 intervals. days, depending on the temperature of the water to be treated and shall consist of a minimum period of approximately 1 hour for each water temperature °C (°C) up to a maximum temperature of 45 °C; Page 7 of number 7 Page 3 1. System according to claim 23 wherein the disinfectant is selected from chlorine, chlorine compounds, ozone, biguanide products, halogen compounds, bromine compounds or compounds. These together 3. 2. System according to claim 23, where the antiscaling agent is composed of compounds such as Phosphonate, Phosphonic Acid, PBTC (Phosphobutan-Tricacic Acid). carboxylic, chromate, zinc polyphosphate, nitrite, silicate, organic matter, caustic soda, malic acid polymer, sodium polyacrylate, acid sodium salt. ethylenediaminetetraacetic, benzotriazol or a combination of these 3 3. Claim 23 system in which the determinants of water quality are also included. one or more in pH, total dissolved solids, Langlier saturation index or the saturation index Stiff & Davis ------------ ------11/10/2017------(OCR) Page 1 of 7 Pages Claim 1. A sustainable method for treating and treating water bodies affected by bacteria. and microalgae at low cost by filtering a small fraction of the whole body of water. This method includes: a. Collection of water with total dissolved solids (TDS) concentrations up to 50,000 ppm; b. one where the reservoir has a bottom surface. that can be thoroughly cleaned by a non-interference suction device; C. Restricting the density of water players to a maximum of 0.05 water players per cubic meter in such water contained in such reservoir d. in such quarantine with the total duration of Oxidation potential (ORP) is treated during this period by periodically adding disinfectant to the water to generate an ORP of approximately 500 mV, provided that the total ORP treatment during this period It depends on the temperature of the water to be treated. and consist of a minimum period of approximately 1 hour for each water temperature °C up to a maximum temperature of 45 °C; e. stimulation of the following processes through a coordinated system to purify such water; and Remove solids from such water by filtering only a small fraction of the total volume of such water in the containment. such collection, whereby the coordination system will obtain information about the correct water quality determinants controlled by the coordination system. and will trigger processes i, ii and iii to adjust the factor Set it within its limits: i. Suction of a portion of such water containing precipitated particles. with suction device moving to prevent the precipitating material from becoming thicker exceeds the average of 3 mm; i i. filtration of the part of the water sucked by the mobile suction device; and ii i. return of filtered water to such reservoir 2. Claim 1 method, where: a. If the water collected at stage a) has a dissolved solids concentration are total less than or equal to 10,000 ppm, the Langelier Saturation Index must be less than 3; or page 2 of number 7 p. b. If the water collected at stage a) has a total dissolved solids concentration greater than 10,000 ppm, the Stiff & Davis Saturation Index must be lower than 3. 3. Claim 2 method, where the Langlier saturation index is maintained below 2 by a process chosen from pH adjustment, antiscaling addition. antisealant or softening process 4. Claim 2 method, where the Stiff & Davis saturation index is maintained below 2 by a process selected from pH adjustment, Addition of antiscaling agent or water softening process 5. Claim 3 method, where the antiscaling agent consists of compounds such as phosphonates, phosphonic acid, PBTC (phosphonic acid). Phobutan- Tricarboxylic (phosphobutan-tricarboxylic acid), chromate (chromate), zinc polyphosphate (zinc polyphosphate), nitrite (nitrite), silicate (silicate), organic matter, caustic soda, polymers such as malic acid. (malic acid), sodium polyacrylate (sodium polyacrylate), ethylene diamine tetracetic acid, benzotriate Seoul 6. Claim 1 method wherein the data obtained by the coordination system is obtained from the experimental method. The bacteria are selected from chlorine and chlorine compounds; ozone (ozone); biguanide products (biguanide); halogen compounds (halogen); Bromine or a combination of these compounds 8. Claim 1 method, where the mobile suction device moves along the bottom of the retention section and sucks up the water containing the precipitated particles. 9. Method Fulfillment of claim 1, where such water is treated within the time interval to generate an ORP of approximately 500 mV, is the total treatment period during the water temperature dependent time interval. to such therapy without maintaining the permanent concentration of the disinfectant in the total amount of such water. Page 3 of 7 Page 1 0. Methods in accordance with Claim 1, where such reservoirs comprise a total volume of at least 15,000 m3. affected by bacteria and microalgae at low cost by filtering a small fraction of the whole body of water. This method includes: a. Collection of water with total dissolved solids (TDS) concentrations up to 50,000 ppm; b. one where the reservoir has a bottom surface. that can be thoroughly cleaned by a non-interference suction device; C. Limiting the density of water players to a maximum of 0.05 water players per cubic meter in such water contained in such reservoirs d. in such quarantine with the total duration of An oxidation reduction potential (ORP) is treated during this period by periodically adding a disinfectant to the water to generate an ORP of at least 500 mV, provided that the total ORP treatment is based on The temperature of the water to be treated and consist of a minimum period of approximately 1 h for each water temperature °C up to a maximum temperature of 45 °C; e. stimulation of the following processes through a coordinated system to purify such water; and Remove solids from such water by filtering only a small fraction of the total volume of such water in the containment. Such collection, whereby the coordination system obtains information about the correct water quality determinants. controlled by the coordination system. and will trigger processes i, ii and iii to adjust the factor Set it within its limits: i. Suction of a portion of such water containing precipitated particles. with suction device moving to prevent the precipitated material exceeding the average thickness of 3 mm; i i. filtration of the part of the water sucked by the mobile suction device; and ii i. Return of filtered water to such reservoir 1 2. Claim 1 method, provided that the total ORP treatment time is discontinued during a period of 7 days, page 4 of Number 7 Page 1 3. Claim method 12, where: a. If the water collected at stage a) has a total dissolved solids concentration less than or equal to 10,000 ppm, the saturation index The lier (Langelier Saturation Index) must be less than 3; or b. If the water collected in step a) has a total dissolved solids concentration greater than 10,000 ppm, the Stiff & Davis Saturation Index must be lower. 3 1 4. Claim 13 method, where the Langlier saturation index is maintained below 2 by a selected process of pH adjustment, antiscaling addition. Antiscalant or water softening process 1 5. Claim 13 method, where the Stiff & Davis saturation index is maintained below 2 by a process selected from pH adjustment, Add antiscaling or water softening process 1 6. Claims 14 method, where the antiscaling agent is composed of compounds such as phosphonates, phosphonic acid, PBTC (phosphobutan- tricarboxylic, chromate, zinc polyphosphate, nitrite, silicate, organic matter, caustic soda, malic acid polymer, sodium polyacrylate, sodium salt of Ethylene diaminetetraacetic acid, benzotriazol or a combination of these compounds 1 7. Claim method 12 wherein the data obtained by the coordination system were obtained from Method 1 8. Claim 12 method wherein the disinfectant is selected from chlorine and chlorine compounds; ozone; biguanide products; halogenated compounds; bromine compounds or a combination of these compounds 1 9. Claim 12 method, where the mobile suction device moves along the bottom of the reservoir and sucks up part of the precipitated water. Page 5 of 7 Page 2 0 The method according to claim 12, where such water is treated within a time interval to generate an ORP of at least 500 mV, is the total treatment period during the period depending on the water temperature at which will such therapy without maintaining a permanent concentration of the disinfectant in the aforementioned total volume of water. 2 1. Method pursuant to Claim 12, provided that the reservoir comprises a volume of at least 15,000 m3. 2 2. Method Fulfillment of Claim 12, provided that the total ORP treatment time was terminated during a period of 7 days 2. 3. Systems for the treatment and treatment of aquatic organisms affected by bacteria and algae. Small size with low cost by filtering a small part of the whole body of water This system consists of: a reservoir for water retention, a reservoir with a volume greater than 50,000 m3 and is assembled with a membrane or septum to accept precipitated particles fixed to the bottom surface of the reservoir. keep; - at least one feed pipe for supplying the exiting water to the reservoir; - a coordinated system for keeping water in reservoirs within specified water quality limits; - At least one dosing device for feeding or dispensing disinfectants or antiscaling agents. into the water in the reservoir; - Mobile suction device for moving along the bottom storage and suction of water from the bottom of the reservoir containing precipitated particles; - a drive device for driving the mobile suction device along the lower part of the reservoir, the drive device is operationally coupled with the mobile suction device; - Filter devices with a maximum filtration capacity of up to 2.5% of the total volume of the water body over a period of 24 hours for filtration of the part of the water with precipitated particles sucked up by the mobile suction device; - one or more collection pipes coupled between the mobile suction device and the filter device; and - the return pipe from the filter device to the containment where the coordination system is structured to receive data obtained by visual observations, experimental methods, algorithms, or detection devices based on water quality determinants and to control the actuation of dosing devices, devices Mobile suction and filtering equipment to adjust the factor. Page 6 of the number 7 determines the water quality within the specified limit, the water quality factor is composed of the potential Oxidation reduction (ORP), temperature, and precipitated particle thickness 2 4. Claims 23 system in which membranes or membranes are covered. The lower part of the reservoir is composed of a geomembrane. geo-membranes, geotextile membranes, plastic membranes or a combination of these materials 2 5. System according to Claim 23 wherein the dosing device consists of an injector, sprayer, manual dosing, weighing dispenser, tubing or a combination of these 2 6. Systems according to claim 23 where propulsion equipment consists of rail systems, cable systems, manual propulsion systems, robotic systems, remotely guided systems, motorized boats or motorized floating devices. or a combination of these systems 2. 7. Systems according to Claim 23, where the mobile suction device is assembled in an operational pair. with equipment driven by cord, rope, line, cable, flexible string or a combination of these materials 2 8. Claim 23 system where the mobile suction is combined with an operating The device is driven by solid wire (rod), bar, pole, rigid shaft or a combination of these materials 2. 9. System according to claim 23, where the filter device consists of a filter element. cylinder (cartridge filter), sand filter, micro-filter, ultra filter (ultra-filter), nano-filter or a combination of these filters 3 0. Claim 23 system, where the coordination system is structured to control the Activate the dosing device according to the data obtained to dispense the disinfectant periodically into the reservoir water over a period of 7 days to generate an ORP of at least approximately 500 mV for the total treatment duration at each of the 7 intervals. days, depending on the temperature of the water to be treated and shall consist of a minimum period of approximately 1 hour for each water temperature °C (°C) up to a maximum temperature of 45 °C; page 7 of number 7 page 3 1. System according to claim 23, where disinfectants are selected from chlorine, chlorine compounds, ozone, biguanide products, halogen compounds, bromine compounds or a combination of these 3 2. System according to claim 23, where the antiscaling agent consists of compounds such as Phosphonate, Phosphonic Acid, PBTC (Phosphobutan-Tricarboxylic Acid). ), chromate, zinc polyphosphate, nitrite, silicate, organic matter, caustic soda, malic acid polymers, sodium polyacrylate, sodium salt of ethylenediic acid. aminetetraacetic, benzotriazol or a combination of these 3 3. The system according to claim 23, where water quality determinants are also included. one or more in pH, total dissolved solids, Langlier saturation index or the saturation index Stiff & Davis ------------ 1. A sustainable method for treating and treating water bodies affected by bacteria. and microalgae at low cost by filtering a small fraction of the whole body of water. This method includes: a. Collection of water with total dissolved solids (TDS) concentrations up to 50,000 ppm; b. The retention of such water in at least one reservoir where such reservoir has a bottom surface. that can be thoroughly cleaned by a non-interference suction device; c. Limiting the density of water players to a maximum of 0.05 water players per cubic meter in such water that is confined in the reservoir. d. Within a period of 7 days and for water temperatures up to 45°C, maintain an ORP of such water at at least 500 mV for a period of at least 1 hour for Water temperature in degrees Celsius by adding a disinfectant to the water; e. Stimulating the following processes through coordination wherein the process purifies water and removes suspended solids by filtering only a small fraction of the total water: i. suction part of such water containing precipitated particles produced by previous process With a mobile suction device to prevent thickening of the precipitated material. exceeds the average of 3 mm; i. filtration of the portion of water sucked by a mobile suction device; and ii i. return of filtered water to one or more such reservoirs.