TH132847A - Sustainable methods and systems for low-cost treatment of water affected by bacteria and microalgae. - Google Patents

Abstract

DC60 (26/09/56) This invention discloses a system for treating and curing water for use in Recreation at low density Typically, the invention system consists of a storage compartment, a coordinate system, a chemical dosing system, a mobile non-interrupting suction device, a suction device. Move without interference And filter device Coordination system Able to receive information about Factors of Controlled Water Quality And can periodically stimulate necessary processes To adjust the determinants of water quality within the relevant limits Exposed systems filter Only a small part of the total volume of water By less than those filtered by flow with a filter system of A typical swimming pool can be up to 200 times higher. The methods and systems revealed also use less chemicals in the system. General swimming pool water treatment The invention system can be used to treat recreational water bodies. And provide sustainable methods for producing water that comply with the requirements of the Environmental Protection Agency. (Environmental Protection Agency) (EPA) about recreational water used for bathing with All body parts

Claims (3)

Disclaimer (all) which will not appear on the advertisement page. : ------ 11/10/2017 ------ (OCR) Page 1 of 7 pages Disclaimer 1. Sustainable methods for treating and treating water affected by infection. bacteria And microalgae at low cost by filtering a small fraction of all the water. This method includes: a. Collection of water with a high concentration of total dissolved solids (TDS) up to 50,000 ppm; b. One where the container has a bottom surface That can be cleaned thoroughly by a non-interrupting suction device; C. Limiting the density of water players to as many as 0.05 water players per cubic meter in such water contained in that containment d. Within a 7 day period of treatment of such water. In that containment with the total duration of During this period the oxidative oxidation potential (ORP) was treated by adding disinfectants to the water periodically to produce an ORP of approximately 500 mV. It depends on the temperature of the water to be treated. It consists of a minimum time of approximately 1 hour for each water temperature of Celsius (ํ C) to a maximum temperature of 45 ํ C; e. The following processes are activated through a coordinating system to purify the water and Solids are removed from such water by filtering only a small fraction of the total water content in the containment container. This is kept, whereby the system receives information about the determining factor of the correct water quality. Controlled by the aforementioned coordination system And will stimulate processes i, ii and iii to adjust the factor Define it within its limits: i. Suction of that part of water containing precipitated particles. With a suction device Moving to prevent the precipitated material being thick 3 mm above the average; i i. Filtration of the water part picked up by the mobile suction device; And ii i. Recovery of filtered water back to such containment 2. Method of claim 1, where: a. If the water collected in stage a) contains the dissolved solid concentration, If all is less than or equal to 10,000 ppm, the Langelier Saturation Index must be less than 3; Or page 2 of 7 pages b. If the water collected in step a) contains the total dissolved solids concentration above 10,000 ppm, the Stiff & Davis Saturation Index ) Must be below 3. 3. Method according to claim 2, where the Langlier saturation index is maintained below 2 by a process selected from pH adjustment, anti-scale addition. (antisealant) or softening process 4. Method according to claim 2, where the stiffand Davis saturation index is maintained below 2 by a process selected from pH adjustment, Adding anti-scale additives Or soft water process 5. Method according to claim 3, where the anti-slag consists of compounds such as Phosphonate (phosphonate), phosphonic acid (phosphonic acid), PBTC (phosphonic acid). Phobutan - Tricarboxylic (phosphobutan-tricarboxylic acid)), chromate (chromate), zinc polyphosphate, nitrite (nitrite), silicate, organic substance, caustic soda, polymers such as malic acid (malic acid), sodium polyacrylate (sodium polyacrylate), sodium salt of ethylene diamine tetracetic acid, benzothiazide. Seoul (benzotriazole) or combination of these compounds 6. Method according to claim 1 where the information obtained by the coordination system is obtained from the experimental method 7. Method according to claim 1, whereby the killing drug The bacteria were selected from chlorine and chlorine compounds; Ozone (ozone); Baiguanide products (biguanide); Halogen compounds; Bromine or combination of these compounds 8. Method according to claim 1, where the mobile suction device moves along the lower part of the reservoir and the suction part of the water containing the precipitated particles 9. Method In accordance with claim 1, where the water was treated within the period for establishing an ORP of approximately 500 mV, it was the total treatment period during the time dependent on the water temperature. To treat it Without maintaining the persistent concentration of disinfectant in the total amount of such water Page 3 of the number 7 Page 1 0. Method for claim 1 where the containment contains a volume of at least 15,000 meters 3. 1 1. A sustainable method for treating and preserving water that has Affected by bacteria And microalgae at low cost by filtering a small fraction of the entire water body. This method includes: a. Collection of water with a high concentration of total dissolved solids (TDS) up to 50,000 ppm; b. One where the container has a bottom surface That can be cleaned thoroughly by a non-interrupting suction device; C. Limiting the density of water players to a maximum number of 0.05 water players per cubic meter in such water contained in that containment d. Within a period of 7 days. In that containment with the total duration of Oxidation Reduction Potential (ORP) was treated during this period by periodically adding disinfectant to the water to produce an ORP of at least 500 mV where the total ORP treatment is dependent on The temperature of the water to be treated It consists of a minimum time of approximately 1 hour for each water temperature of Celsius (ํ C) to a maximum temperature of 45 ํ C; e. The following processes are activated through a coordinating system to purify the water and Solids are removed from the water by filtering only a small fraction of the total amount of such water in the reservoir. It is kept, whereby the system receives information about the determining factor of the correct water quality. Controlled by the aforementioned coordination system And will stimulate processes i, ii and iii to adjust the factor Define it within its limits: i. Suction of that part of water containing precipitated particles. With a suction device Moving in order to prevent the precipitated material having a thickness of more than 3 mm in average; i i. Filtration of the water part picked up by the mobile suction device; And ii i. Return of filtered water to the said containment 1 2. Method according to claim 1, whereby the total ORP treatment time is terminated during a 7 day period page 4 of Number 7 Page 1 3. Method according to claim 12, where: a. If the water collected in a) stage has the total dissolved solid concentration less than or equal to 10,000 ppm, the saturated Lier (Langelier Saturation Index) must be less than 3; Or b. If the water collected in step a) has total dissolved solids concentration above 10,000 ppm, the Stiff & Davis Saturation Index must be low. Over 3 1 4. Method according to claim 13, where the Langlier saturation index is maintained below 2 by a selected process from pH adjustment, anti-scale addition. (antiscalant) or soft water process 1 5. Method to claim 13, where the stiff & davis saturation index is maintained below 2 by a process selected from pH adjustment, Add anti-slag Or softening process 1 6. Method according to claim 14, where the anti-slag consists of compounds such as phosphonate, phosphonic acid, PBTC (phosphobutan - Tricarboxylic), chromate, zinc polyphosphate, nitrite, silicate, organic matter, caustic soda, malic acid polymers, sodium polyacrylate, sodium salt of Ethylenediaminetetetraacetic acid, benzothiazole or combination of these compounds 1 7. Method according to claim 12, where information obtained by the coordination system. This is obtained from Experiment Method 1 8. Method for claim 12 where disinfectants are selected from chlorine and chlorine compounds; ozone; Baiguanide products; Halogenated compounds; Bromine compounds Or combination of these compounds 1 9. Method according to claim 12, where the mobile suction device moves along the lower part of the reservoir and the suction part of the water containing precipitated particles Page 5 of the number 7 Page 2 0 The method, according to claim 12, is where the water is treated within the period to establish an ORP of at least 500 mV for the total treatment period during the period depending on the water temperature at Will such therapy The persistent concentration of disinfectant in the total volume of the aforementioned water is not maintained. 2. 1. Method of claim 12, where the containment area is at least 15,000 m. 3. 2 2. Method. In accordance with claim 12, whereby the total ORP treatment time is discontinued over a period of 7 days 2 3. System for the treatment and treatment of water affected by bacteria and algae. Small size at low cost by filtering a small fraction of all the water. This system consists of: a reservoir for the retention of water, a reservoir with a volume of more than 50,000 m3 and a composite membrane or duct to receive precipitated particles that are fixed to the bottom surface of the containment. Keep; - at least one set of supply hoses for feeding the exuding water to the reservoir; - a coordinated system for keeping the water in the reservoir within the specified water quality limits; - at least one dosing device for feeding or dispensing disinfectant or anti-calc Into the water in the catchment; - Mobile suction device for moving along the lower part Containment And suction part Of the water from the bottom of the reservoir containing precipitated particles; - Actuator for driving the mobile suction device along the lower part of the container, the actuator is operated in parallel with the mobile suction device; - a filter device with a filtration capacity of up to 2.5% of the total volume of the water in a 24-hour period for the filtration of water parts containing precipitated particles sucked by a mobile suction device; - one or more collector tubes coupled between the mobile suction and the strainer; And - the pipe returns from the filter to the containment Where the coordination system is structured to obtain data obtained by the naked eye, experimental methods, algorithm, or detectors based on water quality determinants and to control the actuation of chemical dosing devices, devices. Mobile suction And a filter device to adjust the factor, page 6 of the number 7, set the water quality within the specified limits, the water quality determinant includes the Oxidation, Reduction (ORP), Temperature, and Thickness of Precipitated Particles 2 4. System according to claim 23 where membranes or coverings are covered. The lower part of the containment contains the Gio membrane. (geo-membranes), geotextile membranes, plastic substrates. 2 5. System according to claim 23, where the dosing device consists of a sprayer, a sprayer, a manual dosing, a weighing dispenser, a hose or a combination of these 2. 6. Systems according to claim 23, where the propulsion equipment consists of a rail system, a cable system, a hand propulsion system, a robotic system, a remote-guided system, a motorized boat or a motorized floating device. 2 7. System according to claim 23, where the mobile suction device is assembled in an operational pair. With a device driven by a cord, rope, line, cable, flexible string, or any combination of these materials2 8. System according to claim 23 Where the mobile sucker is assembled in an operational pair with A rigid wire drive device (rod), bar, pole, rigid shaft, or any combination of these materials. 9. System according to claim 23, where the filter consists of a type filter. Cylinder (cartridge filter), sand filter, micro-filter, ultra filter (ultra-filter), nano-filter (nano-filter) or these filter devices combined 3 0. System according to claim 23, where the coordination system is structured to control the Activate the dosing device according to the data obtained to periodically dispense disinfectant into the containment water over a 7 day period to produce an ORP of at least approximately 500 mV for each total treatment period of 7 days. The day depends on the temperature of the water to be treated. And consisted of a minimum period of approximately 1 hour for each degree Celsius (ํ C) to a maximum temperature of 45 ํ C; Page 7 of Number 7 Page 3 1. System according to claim 23, where disinfectants are selected based on chlorine, chlorine compounds, ozone, bicuanide products, halogen compounds, bromine compounds or compounds. 3 2. System according to claim 23, where the anti-slag consists of compounds such as phosphonate, phosphonic acid, PBTC (phosphobutan-trica Carboxylic), chromate, zinc polyphosphate, nitrite, silicate, organic matter, caustic soda, malic acid polymers, sodium polyacrylate, sodium salt of A Tethylene diamine, tetraacetic, benzothiazole or combination of these compounds 3 3. System according to claim 23, where the water quality determinants also include values. One or more in pH, total dissolved solids, Langlier saturation index value. Or the saturation index Stiff & Davis ------------ ------ 11/10/2017 ------ (OCR) Page 1 of Number 7 Disclaimer 1. Sustainable methods for treating and curing water affected by bacteria. And microalgae at low cost by filtering a small fraction of all the water. This method includes: a. Collection of water with a high concentration of total dissolved solids (TDS) up to 50,000 ppm; b. One where the container has a bottom surface That can be cleaned thoroughly by a non-interrupting suction device; C. Limiting the density of water players to as many as 0.05 water players per cubic meter in such water contained in that containment d. Within a 7 day period of treatment of such water. In that containment with the total duration of During this period the oxidative oxidation potential (ORP) was treated by adding disinfectants to the water periodically to produce an ORP of approximately 500 mV. It depends on the temperature of the water to be treated. It consists of a minimum time of approximately 1 hour for each water temperature of Celsius (ํ C) to a maximum temperature of 45 ํ C; e. The following processes are activated through a coordinating system to purify the water and Solids are removed from such water by filtering only a small fraction of the total water content in the containment container. This is kept, whereby the system receives information about the determining factor of the correct water quality. Controlled by the aforementioned coordination system And will stimulate processes i, ii and iii to adjust the factor Define it within its limits: i. Suction of that part of water containing precipitated particles. With a suction device Moving to prevent the precipitated material being thick 3 mm above the average; i i. Filtration of the water part picked up by the mobile suction device; And ii i. Recovery of filtered water back to such containment 2. Method of claim 1, where: a. If the water collected in stage a) contains the dissolved solid concentration, If all is less than or equal to 10,000 ppm, the Langelier Saturation Index must be less than 3; Or page 2 of 7 pages b. If the water collected in step a) contains the total dissolved solids concentration above 10,000 ppm, the Stiff & Davis Saturation Index ) Must be below 3. 3. Method according to claim 2, where the Langlier saturation index is maintained below 2 by a process selected from pH adjustment, anti-scale addition. (antisealant) or softening process 4. Method according to claim 2, where the stiffand Davis saturation index is maintained below 2 by a process selected from pH adjustment, Adding anti-scale additives Or soft water process 5. Method according to claim 3, where the anti-slag consists of compounds such as Phosphonate (phosphonate), phosphonic acid (phosphonic acid), PBTC (phosphonic acid). Phobutan - Tricarboxylic (phosphobutan-tricarboxylic acid)), chromate (chromate), zinc polyphosphate, nitrite (nitrite), silicate, organic substance, caustic soda, polymers such as malic acid (malic acid), sodium polyacrylate (sodium polyacrylate), sodium salt of ethylene diamine tetracetic acid, benzothiazide. Seoul (benzotriazole) or combination of these compounds 6. Method according to claim 1 where the information obtained by the coordination system is obtained from the experimental method 7. Method according to claim 1, whereby the killing drug The bacteria were selected from chlorine and chlorine compounds; Ozone (ozone); Baiguanide products (biguanide); Halogen compounds; Bromine or combination of these compounds 8. Method according to claim 1, where the mobile suction device moves along the lower part of the reservoir and the suction part of the water containing the precipitated particles 9. Method In accordance with claim 1, where the water was treated within the period for establishing an ORP of approximately 500 mV, it was the total treatment period during the time dependent on the water temperature. To treat it Without maintaining the persistent concentration of disinfectant in the total amount of such water Page 3 of the number 7 Page 1 0. Method for claim 1 where the containment contains a volume of at least 15,000 meters 3. 1 1. A sustainable method for treating and preserving water that has Affected by bacteria And microalgae at low cost by filtering a small fraction of the entire water body. This method includes: a. Collection of water with a high concentration of total dissolved solids (TDS) up to 50,000 ppm; b. One where the container has a bottom surface That can be cleaned thoroughly by a non-interrupting suction device; C. Limiting the density of water players to a maximum number of 0.05 water players per cubic meter in such water contained in that containment d. Within a period of 7 days. In that containment with the total duration of Oxidation Reduction Potential (ORP) was treated during this period by periodically adding disinfectant to the water to produce an ORP of at least 500 mV where the total ORP treatment is dependent on The temperature of the water to be treated It consists of a minimum time of approximately 1 hour for each water temperature of Celsius (ํ C) to a maximum temperature of 45 ํ C; e. The following processes are activated through a coordinating system to purify the water and Solids are removed from the water by filtering only a small fraction of the total amount of such water in the reservoir. It is kept, whereby the system receives information about the determining factor of the correct water quality. Controlled by the aforementioned coordination system And will stimulate processes i, ii and iii to adjust the factor Define it within its limits: i. Suction of that part of water containing precipitated particles. With a suction device Moving in order to prevent the precipitated material having a thickness of more than 3 mm in average; i i. Filtration of the water part picked up by the mobile suction device; And ii i. Return of filtered water to the said containment 1 2. Method according to claim 1, whereby the total ORP treatment time is terminated during a 7 day period page 4 of Number 7 Page 1 3. Method according to claim 12, where: a. If the water collected in a) stage has the total dissolved solid concentration less than or equal to 10,000 ppm, the saturated Lier (Langelier Saturation Index) must be less than 3; Or b. If the water collected in step a) has total dissolved solids concentration above 10,000 ppm, the Stiff & Davis Saturation Index must be low. Over 3 1 4. Method according to claim 13, where the Langlier saturation index is maintained below 2 by a selected process from pH adjustment, anti-scale addition. (antiscalant) or soft water process 1 5. Method to claim 13, where the stiff & davis saturation index is maintained below 2 by a process selected from pH adjustment, Add anti-slag Or softening process 1 6. Method according to claim 14, where the anti-slag consists of compounds such as phosphonate, phosphonic acid, PBTC (phosphobutan - Tricarboxylic), chromate, zinc polyphosphate, nitrite, silicate, organic matter, caustic soda, malic acid polymers, sodium polyacrylate, sodium salt of Ethylenediaminetetetraacetic acid, benzothiazole or combination of these compounds 1 7. Method according to claim 12, where information obtained by the coordination system. This is obtained from Experiment Method 1 8. Method for claim 12 where disinfectants are selected from chlorine and chlorine compounds; ozone; Baiguanide products; Halogenated compounds; Bromine compounds Or combination of these compounds 1 9. Method according to claim 12, where the mobile suction device moves along the lower part of the reservoir and the suction part of the water containing precipitated particles Page 5 of the number 7 Page 2 0 The method, according to claim 12, is where the water is treated within the period to establish an ORP of at least 500 mV for the total treatment period during the period depending on the water temperature at Will such therapy The persistent concentration of disinfectant in the total volume of the aforementioned water is not maintained. 2. 1. Method of claim 12, where the containment area is at least 15,000 m. 3. 2 2. Method. In accordance with claim 12, whereby the total ORP treatment time is discontinued over a period of 7 days 2 3. System for the treatment and treatment of water affected by bacteria and algae. Small size at low cost by filtering a small fraction of all the water. This system consists of: a reservoir for the retention of water, a reservoir with a volume of more than 50,000 m3 and a composite membrane or duct to receive precipitated particles that are fixed to the bottom surface of the containment. Keep; - at least one set of supply hoses for feeding the exuding water to the reservoir; - a coordinated system for keeping the water in the reservoir within the specified water quality limits; - at least one dosing device for feeding or dispensing disinfectant or anti-calc Into the water in the catchment; - Mobile suction device for moving along the lower part Containment And suction part Of the water from the bottom of the reservoir containing precipitated particles; - Actuator for driving the mobile suction device along the lower part of the container, the actuator is operated in parallel with the mobile suction device; - a filter device with a filtration capacity of up to 2.5% of the total volume of the water in a 24-hour period for the filtration of water parts containing precipitated particles sucked by a mobile suction device; - one or more collector tubes coupled between the mobile suction and the strainer; And - the pipe returns from the filter to the containment Where the coordination system is structured to obtain data obtained by the naked eye, experimental methods, algorithm, or detectors based on water quality determinants and to control the actuation of chemical dosing devices, devices. Mobile suction And a filter device to adjust the factor, page 6 of the number 7, set the water quality within the specified limits, the water quality determinant includes the Oxidation, Reduction (ORP), Temperature, and Thickness of Precipitated Particles 2 4. System according to claim 23 where membranes or coverings are covered. The lower part of the containment contains the Gio membrane. (geo-membranes), geotextile membranes, plastic substrates. 2 5. System according to claim 23, where the dosing device consists of a sprayer, a sprayer, a manual dosing, a weighing dispenser, a hose or a combination of these 2. 6. Systems according to claim 23, where the propulsion equipment consists of a rail system, a cable system, a hand propulsion system, a robotic system, a remote-guided system, a motorized boat or a motorized floating device. 2 7. System according to claim 23, where the mobile suction device is assembled in an operational pair. With a device driven by a cord, rope, line, cable, flexible string, or any combination of these materials2 8. System according to claim 23 Where the mobile sucker is assembled in an operational pair with A rigid wire drive device (rod), bar, pole, rigid shaft, or any combination of these materials. 9. System according to claim 23, where the filter consists of a type filter. Cylinder (cartridge filter), sand filter, micro-filter, ultra filter (ultra-filter), nano-filter (nano-filter) or these filter devices combined 3 0. System according to claim 23, where the coordination system is structured to control the Activate the dosing device according to the data obtained to periodically dispense disinfectant into the containment water over a 7 day period to produce an ORP of at least approximately 500 mV for each total treatment period of 7 days. The day depends on the temperature of the water to be treated. And consisted of a minimum period of approximately 1 hour for each degree Celsius (ํ C) 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, bicuanide products, halogen compounds, bromine compounds or any combination of these 3. 2. System according to claim 23, where the anti-slag 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, ethylenediaminetic acid sodium salt. Amine, tetraacetic, benzothiazole or combination of these 3 compounds 3. System according to claim 23, where the determinants of water quality also include the value One or more in pH, total dissolved solids, Langlier saturation index value. Or the saturation index Stiff & Davis ------------ 1. Sustainable methods for treating and heal water affected by bacteria. And microalgae at a low cost by filtering a small fraction of the entire water body. The methods include: a. Water collection with a high concentration of total dissolved solids (TDS) up to 50,000 ppm; b. Such water retention in at least one containment with such a reservoir has a bottom surface. That can be cleaned thoroughly by a non-interrupting suction device; c. Limiting the density of water players up to the number of water players 0.05 per cubic meter in such water contained in that containment. d. Within 7 days and for water temperatures up to 45 ° C, maintain the ORP of such water at at least 500 mV for at least 1 hour for Water temperature each degree Celsius By adding disinfectant to water; e. Stimulation of the following processes through coordination. Where the process purifies and removes suspended solids by filtering only a small fraction of the total water: i. Suction of that part of the water containing precipitated particles produced by Previous process With a mobile suction device to prevent thick precipitated materials. Beyond the average 3 mm; i i. Filtration of the sucked water portion by a mobile suction device; and ii i. Returning the filtered water back to one or more such reservoirs.