TH132848A - Systems for treating water used for industrial purposes. - Google Patents

Abstract

DC60 (26/09/56) This invention provides a method and system for low-cost water treatment that will be used. In the process of the industry Basically this invention system consists of a quarantine. At least one, at least one coordination system, at least one dosing system, at least one mobile suction device, and at least one filter device. Coordination system The necessary processes can be controlled according to the system requirements (eg water quality or purity). This invention method and system purify water and remove solids. Suspended without needing to filter the water entirely. But only a small part of the filter is less than the filter. Flow type by filter system for general water treatment up to 200 times

Claims (9)

Disclaimer (all) which will not appear on the advertisement page. : ------ 18/02/2019 ------ (OCR) Page 1 of 4 pages. 1.Systems for low cost water treatment used in industrial processes The system consists of: - One reservoir for the containment of at least 15,000 m 3 and includes a substrate for receiving precipitated particles. The floor underneath is made up of a membrane or a plastic cover that can be cleaned with a mobile suction device; - at least one set of water supply hoses to that containment chamber; - one coordinate system for maintaining the water quality of the containment within the limits of the determinants identified by that coordination system; - At least one dosing system for feeding or dosing of oxidizing agents, disinfectants, binding aids or coagulation aids. Into the water in the reservoir; - at least one mobile suction device for moving along the bottom of the reservoir and sucking part of the water from the bottom of the reservoir containing precipitated particles; - One actuator to drive the mobile suction device along the floor below the containment. The actuator will work in conjunction with a mobile suction device; - a filter device for filtering a portion of water containing sludge that is drawn by a mobile suction device; - collection tube between the mobile suction equipment And filtering equipment thereof; - return hoses from the strainer to the reservoir; And - the supplied water outlet pipes to feed treated water from the reservoir to the downstream industrial processes; Where the coordinate system controls the excitation of the dosing device, the mobile suction device And the filtering device according to the data based on the control factor that was obtained By coordinating system to adjust the determinants in the specified limits; And controls the flow of treated water to downstream industrial processes according to information on downstream industrial processes obtained by the Coordinator. 2. System according to claim 1, where the bottom of the containment container is covered with membrane-containing material. (membrane), geo membrane (geo-membrane), geotextile membrane (geotextile membrane), plastic-surface screw materials, or any combination of these materials on page 2 of four pages. 3. System according to claim 1, where the chemical dosing system consists of a sprayer, a sprayer, a manual dosing, a heavy brew dosing, or a combination of these systems. 4. Systems according to claim 1, where the propulsion device consists of a rail system, a cable system, a hand propulsion system, a motor buoy system, a remote-guided system, a motorized boat, a floating device that Have these engines or systems combined 5. System according to claim 1, where the filter device consists of a cartridge filter 1, a sand filter, a micro-filter, an ultra filter ( ultra-filter), nano-filter (nano-filter), or a combination of these filter devices. 6. The system according to claim 1, where the collector father is composed of hoses, hard pipes, piping systems or any combination of these systems. 7. System according to claim 1, where systematic or more dosing equipment is positioned around the containment loop. 8. System according to claim 7, where the dosing device is equipped with an injection machine. It is positioned along the containment loop for fluxing or dosing of chemicals into the quarantine. 9. System according to claim 8, whereby the coordination system controls the stimulation of the dosing device, based on the information obtained, based on the control factor, to dispense periodic disinfectants into the field. Retained over 7 months to produce an Oxidation Reduction Potential (ORP) of at least 500 mV with a total treatment time of each 7-month period depending on the temperature of the water to be treated, where: i. For women with high temperature up to 35 ° C (? C), the total treatment time consists of Including at least a period of breath. 1 hour for each 0C Of lead temperature; i i.For nostrils above 35? c and less than 70? c, the total treatment time is made up of the peak time of the number of hours calculated by the following equation: page 3 of the number. 4 Pages [35 hrs] - [(Water temperature in degrees Celsius - 35) X 1 hrs / 0C] = Ear time in hours; Or ii i. For women whose temperature is 70? c or greater, the total treatment time is 1 hour. 0. System according to claim 1, where the coordination system controls the actuation of the dosing device based on the obtained data, based on the control factor to add the oxidizing agent to the field. Water retention to prevent the iron and manganese concentrations not more than 1.0 ppm1. 1. System according to claim 1, where the coordination system controls the actuation of the dosing device according to the obtained data, depending on the control factor for the addition of the coagulation aid And / or coagulation aid in the quarantine to prevent the turbidity of the water more than 5 NTU1. 2. System according to claim 1 where the coordinate system controls the actuation of the mobile suction device based on the obtained data, depending on the control factor, to prevent the thickness of the sludge layer on the floor. The bottom of the containment exceeds the average value of 100 mm 1. 3. System according to claim 1, where the system is closed circuit 1 4. System according to claim 1 where disinfectants contain ozone, bicuanide, bromine, halogen, or a combination of these 1. 5. System according to claim 1, where oxidizing agents are composed of halogen compounds, I \ 'salts, pormanganates, peroxides, ozone, sodium persynthetic, potassium peroxide. Sulfates, oxidants produced by electrolysis or combined compounds 1 6.System according to claim 1, where the binding agent or binding agent is composed of cat, ionic polymers, non-ionic polymers, aluminum salts, Aluminum Chlorhydrate, Sulfate, Aluminum Sulphate, Quart and / or Polyquat, Calcium Oxide, Calcium Hydrox P.4 of 4 Sides, Ferrous Sulfate, Fir Rick chloride, polyacrylamide, sodium aluminate, sodium shilicate, chitosan, gelatin, bent tour, alginate, omega, derivatives, of starch. Or these compounds add up to 1 7. System according to claim 1, where that system is a continuous water treatment system 1. 8. System according to claim 1, wherein the industrial process includes Reverse osmosis process, process of producing fresh water from salted water (desalination), evaporation process, purification process, algae culture process, aquaculture process, mining process. Or these processes mix up 1 9. System according to claim 1, where the information received by the coordinate is data from the naked eye, experimental method, algorithm or detector ------ ------ ------ 19/10/2017 ------ (OCR) Page 1 of 7 pages. 1. Methods for preparing water for use in industrial processes. Where the water will be made Let the bridging and suspended solids in the water be removed by filtering a small fraction of the total water, this method includes: a.Water collection with a total dissolved solids (TDS) concentration of up to 60,000 ppm, where: i.If the collected water has total dissolved solids concentration less than or equal to 10,000 ppm, the Langelier Saturation Index must be less than 3, or i. i. If the collected water has a total dissolved solid concentration greater than 10,000 ppm, the Stiff & Davis saturation index values (Stiff & Davis). Davis) must be less than 3; b. Such water retention in one or more reservoirs. Where the containment is below that Can be cleaned thoroughly by a mobile suction device; c. Within a period of 7 days, treatment of the aforementioned water in the aforementioned containment during this period is by adding disinfectant to the said water to create an Oxidation Reduction Potential (ORP) of at least approximately 500 mV. The total time of ORP treatment over the whole period of moisture depends on the water temperature. To treat such therapy, where: i. For water up to 35 ° C (ํ C), the total ORP treatment time includes a minimum inhalation time of approximately 1 hour for each ํ C of water temperature; i i. For water above 35 ํ C and less than 70 ํ C, the total ORP treatment time includes the minimum duration of hours calculated by the following equation: [35 hrs]. - [(Water temperature in degrees Celsius - 35) X 1 h / ํ C] = minimum duration in hours; Or ii i. For water with a temperature of 70 ํ C or greater, the total ORP treatment time is approximately 1 hour. d. Stimulation of the following processes through one coordinate system to make the water Purify and remove suspended solids by filtering only a small fraction of the total volume of the water. In the containment, the coordinate system receives information on the determinants of the water quality being affected. Controlled by the aforementioned coordination system, the aforementioned determinants of water quality include the concentration of Iron and manganese, turbidity and sludge layer thickness And stimulate one or more processes of 7 pages than in process i to V to adjust such water quality determinants within the limits of those values: i. Adding an oxidant to the water in such containment to control the risk of oxidation. Iron and manganese concentrations in the water. Where the oxidant is added to the water In quantities sufficient to maintain and / or prevent iron and manganese concentrations greater than 1 ppm; i i.Adding coagulation aids, binding agents or their mixtures Into the said water in the containment To control the turbidity of the water, where a sufficient amount of agglutination agent, binding agent or its mixtures is added to the water. To prevent the turbidity of the water from more than 5 NTU; ii i. Suction of that part of water containing precipitated particles. It is produced by process i and / or ii with a mobile suction device to control the sludge layer thickness. For that thickness The sediment layer is not greater than the average of 100 mm; i v. Filtration of the said portion of water which is also sucked by a mobile suction device. At least one set of filtering equipment; and v. Returning filtered water to such containment; and e. The use of the treated water in further downstream processes. Where the water that has been Such therapy has been used: i. is a raw material for industrial processes and circulates in an open cycle, or i i. to tug, irrigate, seep or mix 2. Method according to claim 1, where the Langlier saturation index or Stiff & Davis saturation index was maintained at more than 2 eyes by a selective process from pH adjustment, additive. Slag (antisealants) or softening processes 3. Method according to claim 2, where the anti-slag contains phosphonic acid (phosphonic acif), PBTC, phosphobutane acid. Tricarboxylic (phosphobutan-tricarboxylic acid), chromate (chromate), zinc polyphosphate, zinc polyphosphate, nitrite (nitrite), silicate, organic substance, caustic soda, polymer such as malic acid ( malic acid), sodium polyacrylate (sodium page 3 of number 7, polyacrylate), ethylene diamine tetracetic acid sodium salts, benzoate. Triasole (benzotriazole) or a combination of these compounds 4. Method for claim 1 whereby the water collected may be residual liquid from Industrial processes or water collected from natural and / or treated water sources. 5. Method for claim 1 where disinfectants contain ozone, biguanide, bromine, halogen compounds; And all these compounds together 6. Method according to claim 1 where the information received by the aforementioned coordination system is obtained. By experimental method (empirical method) 7.Method according to claim 1, where oxidizing agents (oxidizing agents) include Halogenated compounds; Permanganate salt (permanganate salts), peroxides (peroxides); Ozone; Sodium persulfate (sodium persulfate); Potassium persulfate (potassium persulfate); The oxidant produced moisture by electrolysis method. (electrolytic) or combination of these compounds 8. Method according to claim 1, whereby the binding agent or the binding agent Contains polymers (polymers) such as cat-ionic polymers (cationic polymer); And anionic polymer (anionic polymer); Aluminum salt; Quate (quate); And polyquat (polyquate); Calcium oxide; Calcium hydroxide (calciumhydrozide); Ferrous sulphate (ferrous sulphate); Ferric chloride (ferric chloride); Polyacrylamide (polyacrylamide); Sodium aluminate (sodium aluminate); Sodium silicate (sodium silicate); Sitosan (chitosan); Gelatin (gelatin); Guar gum (guar gum); Alginate (alginate); Moringa seed; Starch derivatives And all these compounds together 9. Methods according to claim 1 that also includes the removal of chlorine. (dechlorinating) the water in the said containment If residual chlorine is detected in such water The chlorine removal process consists of four pages of seven pages, including a reactive carbon filter or chemicals containing sodium bisulfite, sodium metabisulfite, or other compounds. This unites 1 0. Method according to claim 1, where the total ORP treatment time is intermittent over a period of 7 days 1 1. Method for claim 1, where: i. For water up to 35 ° C (ํ C), the total ORP treatment time is approximately 1 hour for each water temperature oC; i i. For water above 35 ํ C and less than 70 ํ C, the total ORP treatment time includes an approximate time of the number of hours calculated by the following equation: [35 hrs] - [(Water temperature in degrees Celsius - 35) X 1 h / ํ C] = duration in hours; Or ii i.For water with a temperature of 70 ํ C or more, the total ORP treatment time is approximately 1 hour. 2. A system for treating water with capital roots used in industrial processes The system consists of: - The water reservoir for the containment of water that contains at least 15,000 m 3 and consists of a matt floor. Lower for receiving particles settling The floor below is made up of memes. A membrane or plastic cover that can be cleaned with a mobile suction device; - at least one set of hoses to feed water to that reservoir; - one coordinate system for keeping the water in the containment chamber having internal water quality The limits of the determining factors specified by the coordination system; - At least one dosing system for feeding or dosing of oxidizing agents, disinfectants, binding agents or coagulation aids. Into water in that containment; - At least one mobile suction device for moving along the bottom of the containment container. And sucking part of the water from the bottom of the reservoir containing the sedimentation particles; - One actuator for driving the mobile suction device along the floor. Bottom of containment The actuator will work in conjunction with a mobile suction device; Page 5 of Page 7 - Filtration device for filtering part of water containing precipitated particles sucked by The mobile suction device; - collection tube between the mobile suction equipment And filtering equipment thereof; - return hoses from the strainer to the reservoir; And - the provided water outlet pipe to feed the treated water from the reservoir to the process. Downstream industry; Where the coordination system controls the actuation of the dosing device, the mobile suction device and the filter device according to the data on the derived control factor. By the coordination system To adjust the determinants in the specified limits; And regulate the flow of water through treatment to Downstream industrial processes according to information on the downstream industrial processes obtained By the coordination system 1 3. System according to claim 12, where the bottom of the containment is covered with material that Consists of a membrane (membrane), geo membrane (geo-membrane), geotextile membrane, plastic substrate, or a combination of these materials 1 4.System according to claim 12, where the chemical dosing system consists of a sprayer, a sprayer, a manual dosing, a weighing dosing, a pipe or a combination of these 1. 5. Systems according to claim 12, where the propulsion device consists of a rail system, a cable system, a hand propulsion system, a robotic system, a remote-guided system, a motorized boat, a floating device that Have these engines or systems combined 1 6.The system according to claim 12, where the filter device consists of a cartridge filter, a sand filter, a micro-filter, an ultra filter ( ultra? filter), nano-filter (nano-filter), or a combination of these filter devices. 7. System according to claim 12, where the collection pipes consist of hoses, hard pipes, piping systems or these systems together page 6 of number 7 Page 1. 8. System according to claim 12, where one or more dosing equipment is classified as Location according to containment loop 1 9. System according to claim 18, where the dosing device is equipped with an injection machine. Are positioned along the containment loop for the feeding or dosing of chemicals into the reservoir water 2 0. System according to claim 12, where the coordinate system controls the excitation of the dispensing device. The chemical, based on the data obtained, depends on the control factor to periodically dispense disinfectants into the water. In storage over a period of 7 days to produce an Oxidation Reduction Potential (ORP) of at least 500 mV with a total of 7 day treatment periods depending on the water temperature to be treated, where: i. For water up to 35 ° C (° C) the total treatment time is composed of Include at least 1 hour for each ํ C of water temperature; i i. For water above 35 ํ C and less than 70 ํ C, the total treatment time is The sum of the total duration of hours is calculated by the following equation: [35 hrs] - [(water temperature in degrees Celsius - 35) X 1 h / 0C] = minimum time. In hours; or ii i. For water with a temperature of 70 ํ C or more, the total treatment time Total duration is a minimum of about 1 hour 2. 1. System according to claim 12, where the coordinate system controls the excitation of the dispensing device. The chemical, according to the information obtained, depends on the control factor to add an oxidizing agent to the water in the place. Water retention to prevent the iron and manganese concentrations of water not greater than 1.0 ppm 2. 2. System according to claim 12, where the coordinate system controls the stimulation of the dispensing device. The chemical, according to data obtained, depends on the control factor for adding coagulation aid. And / or a coagulant into the water in the reservoir to prevent the turbidity of the said water more than 5 NTU page 7 of the number 7 page 2 3. System according to claim 12, where the coordinate system controls the excitation of the equipment. Mobile suction according to the obtained data, depending on the control determinant to prevent thickness. Of sediment at the bottom of the containment above the mean of 100 mm2 4. System according to claim 12, where the system is closed circuit 2 5. System according to claim 12, where disinfectants contain ozone, bicuanide, bromine, halogen, or a combination of these 2. 6. System according to claim 12, where oxidizing agents are composed of compounds Such as halogens, permanganate, peroxide, ozone, sodium persulfate, potassium persulfate, oxidant produced by electrolytic methods. Or combination of these 2 compounds 7. System according to claim 12, whereby the binding agent or the binding agent Contains cat ionic polymers, anionic polymers, aluminum salts, aluminum chlorhydrate, alum, aluminum sulfate, quartz and / Or polyquat, calcium oxide, calcium hydroxide, ferrous sulfate, ferric chloride, polyacrylamide, sodium aluminate, sodium silicate, chitosan, j. Latin, tour gum, alginate, moringa seed, starch derivatives. Or combination of these 2 compounds 8. System according to claim 12, where that system is continuous water treatment system 2. 9. System according to claim 12, wherein the industrial process includes Reverse osmosis process, the process of producing fresh water from saltwater (desalination), evaporation process, purification process, algae culture process, aquaculture process, mining process. Or a mix of these processes 3 0. System according to claim 12, where information received by the coordination system is information from Naked-eye observation, experimental method, algorithm or detector ------------ ------ 19/10/2017 ------ (OCR) Page 1 of the number 7 pages. 1. Methods for preparing water for use in industrial processes. Where the water will be made Let the bridging and suspended solids in the water be removed by filtering a small fraction of the total water, this method includes: a.Water collection with a total dissolved solids (TDS) concentration of up to 60,000 ppm, where: i.If the collected water has total dissolved solids concentration less than or equal to 10,000 ppm, the Langelier Saturation Index must be less than 3, or i. i. If the collected water has a total dissolved solid concentration greater than 10,000 ppm, the Stiff & Davis saturation index values (Stiff & Davis). Davis) must be less than 3; b. Such water retention in one or more reservoirs. Where the containment is below that Can be cleaned thoroughly by a mobile suction device; c. Within a period of 7 days, treatment of the aforementioned water in the aforementioned containment during this period is by adding disinfectant to the said water to create an Oxidation Reduction Potential (ORP) of at least approximately 500 mV. The total time of ORP treatment over the whole period of moisture depends on the water temperature. To treat such therapy, where: i. For water up to 35 ° C (ํ C), the total ORP treatment time includes a minimum inhalation time of approximately 1 hour for each ํ C of water temperature; i i. For water above 35 ํ C and less than 70 ํ C, the total ORP treatment time includes the minimum duration of hours calculated by the following equation: [35 hrs]. - [(Water temperature in degrees Celsius - 35) X 1 h / ํ C] = minimum duration in hours; Or ii i. For water with a temperature of 70 ํ C or greater, the total ORP treatment time is approximately 1 hour. d. Stimulation of the following processes through one coordinate system to make the water Purify and remove suspended solids by filtering only a small fraction of the total volume of the water. In the containment, the aforementioned system receives information on the determinants of the water quality being affected. Controlled by the aforementioned coordination system, the aforementioned determinants of water quality include the concentration of Iron and manganese, turbidity and sludge layer thickness And stimulate one or more processes of 7 pages than in process i to V to adjust such water quality determinants within the limits of those values: i. Adding an oxidant to the water in such containment to control the risk of oxidation. Iron and manganese concentrations in the water. Where the oxidant is added to the water In quantities sufficient to maintain and / or prevent iron and manganese concentrations greater than 1 ppm; i i.Adding coagulation aids, binding agents or their mixtures Into the said water in the containment To control the turbidity of the water, where a sufficient amount of agglutination agent, binding agent or its mixtures is added to the water. To prevent the turbidity of the water from more than 5 NTU; ii i. Suction of that part of water containing precipitated particles. It is produced by process i and / or ii with a mobile suction device to control the sludge layer thickness. For that thickness The sediment layer is not greater than the average of 100 mm; i v. Filtration of the said portion of water which is also sucked by a mobile suction device. At least one set of filtering equipment; and v. Returning filtered water to such containment; and e. The use of the treated water in further downstream processes. Where the water that has been Such therapy has been used: i. is a raw material for industrial processes and circulates in an open cycle, or i i. to tug, irrigate, seep or mix 2. Method according to claim 1, where the Langlier saturation index or Stiff & Davis saturation index was maintained at more than 2 eyes by a selective process from pH adjustment, additive. Slag (antisealants) or softening processes 3. Method according to claim 2, where the anti-slag contains phosphonic acid (phosphonic acif), PBTC, phosphobutane acid. Tricarboxylic (phosphobutan-tricarboxylic acid), chromate (chromate), zinc polyphosphate, zinc polyphosphate, nitrite (nitrite), silicate, organic substance, caustic soda, polymer such as malic acid ( malic acid), sodium polyacrylate (sodium page 3 of number 7, polyacrylate), ethylene diamine tetracetic acid sodium salts, benzoate. Triasole (benzotriazole) or a combination of these compounds 4. Method for claim 1 whereby the water collected may be residual liquid from Industrial processes or water collected from natural sources and / or treated water. 5. Method for claim 1 where disinfectants contain ozone, biguanide, bromine, halogen compounds; And all these compounds together 6. Method according to claim 1 where the information received by the aforementioned coordination system is obtained. By an empirical method 7.Method according to claim 1, where oxidizing agents (oxidizing agents) include Halogenated compounds; Permanganate salt (permanganate salts), peroxides (peroxides); Ozone; Sodium persulfate (sodium persulfate); Potassium persulfate (potassium persulfate); The oxidant produced moisture by electrolysis method. (electrolytic) or combination of these compounds 8. Method according to claim 1, whereby the binding agent or the binding agent Contains polymers (polymers) such as cat-ionic polymers (cationic polymers); And anionic polymer (anionic polymer); Aluminum salt; Quate (quate); And polyquat (polyquate); Calcium oxide; Calcium hydroxide (calciumhydrozide); Ferrous sulphate (ferrous sulphate); Ferric chloride (ferric chloride); Polyacrylamide (polyacrylamide); Sodium aluminate (sodium aluminate); Sodium silicate (sodium silicate); Sitosan (chitosan); Gelatin (gelatin); Guar gum (guar gum); Alginate (alginate); Moringa seed; Starch derivatives And all these compounds together 9. Methods according to claim 1 that includes also removal of chlorine. (dechlorinating) the water in the said containment If residual chlorine is detected in such water The chlorine removal process consists of four pages of seven pages, including a reactive carbon filter or chemicals containing sodium bisulfite, sodium metabisulfite, or other compounds. This unites 1 0. Method according to claim 1 where the total ORP treatment time is intermittent over a period of 7 days 1 1. Method for claim 1, where: i. For water up to 35 ° C (ํ C), the total ORP treatment time is approximately 1 hour for each water temperature oC; i i. For water above 35 ํ C and less than 70 ํ C, the total ORP treatment time includes an approximate time of the number of hours calculated by the following equation: [35 hrs] - [(Water temperature in degrees Celsius - 35) X 1 h / ํ C] = duration in hours; Or ii i.For water with a temperature of 70 ํ C or more, the total ORP treatment time is approximately 1 hour. 2. A system for treating water with capital roots used in industrial processes The system consists of: - The water reservoir for the containment of water that contains at least 15,000 m 3 and consists of a matt floor. Lower for receiving particles settling The floor below is made up of memes. A membrane or plastic cover that can be cleaned with a mobile suction device; - at least one set of hoses to feed water to that reservoir; - one coordinate system for keeping the water in the containment chamber having internal water quality The limits of the determining factors specified by the coordination system; - At least one dosing system for feeding or dosing of oxidizing agents, disinfectants, binding agents or coagulation aids. Into water in that containment; - At least one mobile suction device for moving along the bottom of the containment container. And sucking part of the water from the bottom of the reservoir containing the sedimentation particles; - One actuator for driving the mobile suction device along the floor. Bottom of containment The actuator will work in conjunction with a mobile suction device; Page 5 of Page 7 - Filtration device for filtering part of water containing precipitated particles sucked by The mobile suction device; - collection tube between the mobile suction equipment And filtering equipment thereof; - return hoses from the strainer to the reservoir; And - the provided water outlet pipe to feed the treated water from the reservoir to the process. Downstream industry; Where the coordination system controls the actuation of the dosing device, the mobile suction device and the filter device according to the data on the derived control factor. By the coordination system To adjust the determinants in the specified limits; And regulate the flow of water through treatment to Downstream industrial processes, according to information on received downstream industrial processes By the coordination system 1 3. System according to claim 12, where the bottom of the containment is covered with material that Consists of a membrane (membrane), geo membrane (geo-membrane), geotextile membrane (geotextile membrane), plastic substrate, or a combination of these materials 1 4.System according to claim 12, where the chemical dosing system consists of a sprayer, a sprayer, a manual dosing, a weighing dosing, a pipe or a combination of these 1. 5. Systems according to claim 12, where the propulsion device consists of a rail system, a cable system, a hand propulsion system, a robot system, a remote-guided system, a motorized boat, a floating device that Have these engines or systems combined 1 6.The system according to claim 12, where the filter device consists of a cartridge filter, a sand filter, a micro-filter, an ultra filter ( ultra? filter), nano-filter (nano-filter), or a combination of these filter devices. 7. System according to claim 12, where the collection pipes consist of hoses, hard pipes, piping systems or these systems together page 6 of number 7 Page 1. 8. System according to claim 12, where one or more dosing equipment is classified as Location according to containment loop 1 9. System according to claim 18, where the dosing device is equipped with an injection machine. Are positioned along the containment loop for the feeding or dosing of chemicals to the reservoir water 2 0. System according to claim 12, where the coordinate system controls the excitation of the dispensing device. The chemical, based on the data obtained, depends on the control factor to periodically dispense disinfectants into water. In storage over a period of 7 days to produce an Oxidation Reduction Potential (ORP) of at least 500 mV with a total of 7 days of each treatment period depending on the water temperature to be treated, where: i. For water up to 35 ° C (° C) the total treatment time is composed of Include at least 1 hour for each ํ C of water temperature; i i. For water above 35 ํ C and less than 70 ํ C, the total treatment time is The sum of the total duration of hours is calculated by the following equation: [35 hrs] - [(water temperature in degrees Celsius - 35) X 1 h / 0C] = minimum time. In hours; or ii i. For water with a temperature of 70 ํ C or more, the total treatment time Total duration is a minimum of about 1 hour 2. 1. System according to claim 12, where the coordinate system controls the excitation of the dispensing device. The chemical, according to the information obtained, depends on the control factor to add an oxidizing agent to the water in the place. Water retention to prevent the iron and manganese concentration of water not higher than 1.0 ppm 2. 2. System according to claim 12, where the coordinate system controls the stimulation of the dispensing device. The chemical, according to data obtained, depends on the control factor for adding coagulation aid. And / or a coagulant into the water in the reservoir to prevent the turbidity of the said water more than 5 NTU page 7 of the number 7 page 2 3. System according to claim 12, where the coordinate system controls the excitation of the equipment. Mobile suction according to the obtained data, depending on the control determinant to prevent thickness. Of sediment at the bottom of the containment above the mean of 100 mm2 4. System according to claim 12, where the system is closed circuit 2 5. System according to claim 12, where disinfectants contain ozone, bicuanide, bromine, halogen, or a combination of these 2. 6. System according to claim 12, where oxidizing agents are composed of compounds Such as halogens, permanganate, peroxide, ozone, sodium persulfate, potassium persulfate, oxidant produced by electrolytic methods. Or combination of these 2 compounds 7. System according to claim 12, whereby the binding agent or the binding agent Contains cat ionic polymers, anionic polymers, aluminum salts, aluminum chlorhydrate, alum, aluminum sulfate, quartz and / Or polyquat, calcium oxide, calcium hydroxide, ferrous sulfate, ferric chloride, polyacrylamide, sodium aluminate, sodium silicate, chitosan, j. Latin, tour gum, alginate, horseradish, starch derivatives. Or combination of these 2 compounds 8. System according to claim 12, where that system is continuous water treatment system 2. 9. System according to claim 12, wherein the industrial process includes Reverse osmosis process, the process of producing fresh water from saltwater (desalination), evaporation process, purification process, algae culture process, aquaculture process, mining process. Or a mix of these processes 3 0. System according to claim 12, where information received by the coordination system is information from Naked-eye observation, experimental method, algorithm or detector ------------ 1.Methods for low-cost water treatment By the process in the industry, it makes the water Purify and remove suspended solids in water. Less of the total water, the assembly methods include: a. Collection of water with total dissolved solids (TDS) up to 60,000 ppm; b. One such reservoir. Where the containment has a bottom that can Thoroughly cleaned with a mobile suction device; c.Within 7 days: i. For water up to 35 ° C, the ORP of that water is maintained at least 500 mV for at least 1 hour for each degree Celsius of the water temperature. By adding disinfectant to the water in that water; i i. For water which is above 35 ° C and up to 69 ° C, the ORP of that water will be maintained for at least 500 mV for at least several hours. By adding disinfectant to the water Where the minimum duration of the number of hours is calculated by the following equation: [35 hrs] - [water temperature in degrees Celsius, -35] = minimum duration of hours; or ii. i.For water with a temperature of 70 ° C or greater, the ORP of that water is maintained at at least 500 mV for at least 1 hour d. Stimulation of the following processes through one coordinate system. Whereby the process They produce pure water and remove suspended solids by filtering only a small fraction of the total water: i.Adding an oxidizing agent to avoid the iron concentration and More than 1 ppm manganese; i i.Adding agglutination aid, binding aid or rounded mixture Go down to avoid the turbidity of more than 5 NTU; ii i. Suction of water containing precipitated particles Which is also produced by the previous process Mobile suction device to avoid the precipitation of material thickness greater than the average of 100 mm; i v. Filtration of water which is drawn by a mobile suction device with a filter device. At least one set; and v. Returning filtered water to one or more such reservoirs; e. Use of the said treated water in further downstream processes.