PROCESS FOR THE REMOVAL OF IMPURITIES FROM HARD WATER AND THE FORMULATION IT EMPLOYS

Abstract

The present invention consists of a process for removing impurities from hard water. Using chemical agents, it removes impurities by mixing a chemical preparation and employing decantation in the first stage of impurity removal. Subsequent validation of the results allows for the removal of other types of impurities present in the water, such as arsenic, cadmium, cyanide, copper, chromium, mercury, nickel, lead, and zinc. Finally, it removes contaminants and microorganisms from the following group: fats and oils, suspended solids, organic carbon, total nitrogen, total phosphorus, worm eggs, E. coli, and fecal enterococci. The resulting sediments are used as biofertilizers, and the treated water can be discharged into conventional municipal sewer systems or, if necessary, treated with ozone (O3) for human consumption.

Description

PROCESS FOR THE ELIMINATION OF IMPURITIES FROM HARD WATER AND THE FORMULATION IT USES FIELD OF INVENTION The present invention consists of a process for the elimination of impurities from hard water, in such a way that by means of chemical agents, it allows the elimination of impurities, by mixing a chemical preparation and using decantation as the first stage of the elimination of impurities, subsequently the validation of results allows to carry out elimination stages of other types of impurities present in the water such as heavy metals and finally the elimination of organic matter present in hard water, for which reason it is considered an invention of chemical type. BACKGROUND In the state of the art, there are various processes to eliminate impurities contained in hard water, some of which are the following: Patent WO1995022509A1 discloses a process for electrolytic purification of contaminated water using oxygen diffusion cathodes which consists of carrying out the oxidation of the contaminating components of the contaminated water in an electrolytic cell equipped with one or more anodes and is characterized by the fact that oxygen diffusion is also carried out in one or more cathodes of said electrolytic cell subjected to a voltage lower than 100 V to reduce this gas to an oxidizing species in solution, selected from hydrogen peroxide or hydroxyl and / or peroxydryl radicals.The equipment for carrying out the process consists of a continuously fed electrolytic cell consisting of an anode (1) and two oxygen diffusion cathodes (2) and sealed on both sides with frames (3), the compartments (4) being delimited between the frames and the cathodes, which are fed with gaseous oxygen and / or gaseous mixtures containing it by means of the inlets (6) and the compartments (5) being similarly delimited between the cathodes and the anode, through which the contaminated water that enters through the inlets (7) and exits through the outlets (8) circulates. It allows the treatment of contaminated water that contains toxic, non-biodegradable or refractory substances to conventional oxidation methods. The previous invention, despite achieving the same technical effect, has a substantial difference with respect to the proposed invention and that is the use of physical anodes and cathodes for the functionality of the invention, which is not the case with this invention.The technology published in WO2007113681A2 contains a system for the treatment and recirculation of water and other solvents. This system integrates four stages comprising biological, physical, chemical, and natural processes to treat water. It operates with electrical, mechanical, or wind power, and is characterized by its energy savings. The design allows for easy assembly or disassembly. It can integrate a shower, sink, and / or washing machine into a single cubicle and can be installed anywhere. The wastewater discharged by this system has a positive impact on the environment. Its construction can be made of various materials and combined with conventional and modern elements to form different shapes. It can also contain modern and luxurious elements, or simply be functional.The invention of this system lies not only in its design, but also in the use of natural elements for water treatment, as well as magnetic and electromagnetic fields. The difference between the previous process is the use of energy sources as a potential characteristic element, but in the proposed invention, this aspect is irrelevant. The invention disclosed as W02008041051A2 presents a wastewater purification process, using chemical hyperoxidation, in a short time, where the invention refers to a compact short-time procedure for the treatment of wastewater that is characterized by comprising a Dissolved Air Flotation (DAF) stage, a second stage of chemical hyperoxidation, by means of which, in a time not exceeding 3 minutes, the soluble contaminant load of the water (COD, BOD5) is eliminated by oxidation and a third stage consisting of specialized filtration with membranes that operate at pressures less than 200 psig and pore sizes between 100 and 8 angstroms. Whose demands are claimed 1. A process for purifying wastewater characterized by the fact that it comprises the following stages: a. Flotation and removal of insoluble materials by Dissolved Air Flotation b. Oxidation of the soluble contaminant load of the water (COD, BOD5) by chemical hyper-oxidation applied for a time between 30 seconds and 3 minutes, c. Elimination of colloidal compounds and dissolved solids by specialized filtration with membranes at pressures less than 200 psig. 2. The process for purifying wastewater according to claim 1, characterized in that the hyperoxidant used in step b) is hypochlorous acid in combination with activated metals for their electron exchange. 3. The process for purifying wastewater according to claim 2, characterized in that the metals activated for their electron exchange are preferably iron and aluminum. 4. The process for purifying wastewater according to claim 1, characterized in that the filtration stage is carried out in a staggered manner using membranes of different pore sizes. 5. The process for purifying wastewater according to claim 4, characterized in that the membranes used have a pore size from 100 angstroms to sizes of 8-11 angstroms. This invention is similar to the proposed technology but differs from the use of specific membranes and air-induced flotation, which makes the proposed process much simpler. Patent WO2014131931A1 discloses a method for removing heavy metals from contaminated water and a device for implementing said method. This method consists of a method for removing heavy metals from contaminated water using a green filter, in which aquatic plant organisms and microorganisms participate. A tank sized according to the volume of water to be decontaminated is required, whether of industrial, urban waste, or agricultural origin. Decontamination occurs using a plant filter composed of a parent plant species from the genus Typha sp. and a companion species selected from the genera Phragmites spp., Iris sp., Sparganium sp., Cyperus spp., Scirpus spp., and Typha ssp.and Nelumbo sp., along with microorganisms from the Vesiculo-Arbuscular fungi group and / or Raoultella terrigena bacteria, previously inoculated into the plant roots, which allows for the reduction or elimination of heavy metals. Finally, the combined filter of several species of aquatic plants allows for a reduction in the quality of the final water. It is important to note that in Mexico, fecal coliforms are used as an indicator to determine pathogen contamination. The maximum permissible limit for wastewater discharges into national waters and resources, as well as discharges into soil (used in agricultural irrigation), is 1,000 and 2,000 as the most probable number (MPN) of fecal coliforms per 100 mi for the monthly and daily averages, respectively. DESCRIPTION The characteristic details of this novel process for removing impurities from hard water are clearly shown in the following description and in the accompanying figures, where the same reference signs are used to indicate the parts and figures shown. Brief description of the figures Figure 1 is a plan view of the process for removing impurities from hard water and the formulation it uses. Figure 2 is a diagram representing the process for removing impurities from hard water and the formulation it uses. Based on the figures above, the process for removing impurities from hard water comprises the following stages. A. STAGE 1. In this stage, a sample of one liter of water to be treated is placed in a container 1 2, its weight and pH level are determined, and there can be three variants: a. If the pH is acidic or neutral, continue with step 1; b. If the pH is alkaline, it is acidified using a range of 0.3 to 0.4 grams to dissolve in the container to cause acidification with a formulation 4 such that in the case of organic matter it is achieved with sulfuric acid in combination with muriatic acid in a ratio of 1:1;in the case of industrial waste materials, nitric acid is combined with muriatic acid and then this stage continues and, in the case of edible fats, tartaric acid or food grade citric acid is used and this stage is followed by adding a formulation 3 of the base formulation in a present concentration of ± 10% and it is vigorously stirred in a range between 10 and 60 rpm, in a temperature range between 20 ° C and 95 ° C, during a time range between 10 and 70 minutes approximately ± 0.1 Volts is released, which when the oscillation is mechanically stopped, it self-consumes in such a way that a reaction is caused where the impurities made up of organic compounds are trapped by chemical reaction and cause that due to weight they are deposited at the bottom of container 1 and are removed by decantation, leaving in container 1 only the water product of the reaction;immediately afterwards and using laboratory tests and at least a set of parameters 5 are determined such as pH, clarity, oxygen concentration, brightness, and conventionally these parameters are compared against a pre-established parameter that allows their reuse, which could be an Official Standard or a reference parameter determined for the territory where the technology is applied (hereinafter referred to as Standard); if the laboratory parameters 5 do not comply with the standards required by the Standard then formulation 3, formulation 4 is added to the base formulation in such a way that in the case of organic matter it is obtained with sulfuric acid in combination with muriatic acid in a ratio of 1:1;In the case of industrial waste materials, nitric acid is combined with muriatic acid and then this stage continues, and in the case of edible fats, tartaric acid or food grade citric acid is used and this process is iterated by adding product 6 to formulation 4 until parameters 5 have complied with the Standard; Once this has happened, the treated water is directed to a first filter 7, which allows the elimination of sediments that are fine particles of metals, calcium or sedimentable solids, and parameters 5 are validated again and the sediments are used for the production of biofertilizers; the water separated in this stage is delivered to the next stage without the presence of sediments; in this stage the presence of Arsenic, Cadmium, Cyanide, Copper, Chromium, Mercury, Nickel, Lead and Zinc is reduced until it meets the parameters of the standard; B. STAGE 2. At this stage, the pH, BOD (biochemical oxygen demand of water, the amount of oxygen that biology presents in the water measured in milligrams of oxygen per liter of water) and COD (Chemical oxygen demand of water is measured in milligrams per liter in the amount of oxygen that the water chemically demands) are measured in the water, determining its acidity or alkalinity in a conventional way and it is determined by means of laboratory parameters 5, if there is the presence of one or some of the contaminants and microorganisms of the following group: fats and oils, suspended solids, organic carbon, total nitrogen, total phosphorus, hemminth eggs, E coli and fecal Enterococci and it is validated that they do not have their presence by laboratory parameters 5;Acidic waters are neutralized in the same way as alkaline waters and at this stage the presence of microorganisms is eliminated where potentially now it is warned by the parameters if there is any other contaminant in such a way that it warns us that the treated water only exchanges the contaminant between the sludge and the water itself, if this is the case then the method is not effective in this situation; on the other hand, if the contaminants have been successfully removed, then the sediments can be allowed to be delivered for the production of biofertilizers;Once the sludge has settled, it should preferably be filtered and the mixture left to rest for at least 24 hours to achieve the pH level to neutralize or stabilize, only in the case of not being able to wait this time then neutralization is caused with the added formulation 4 and the water treated in this stage is then delivered to the next stage; C. STAGE 3.- Once the water is received without contaminants, sediments and microorganisms, it is determined if the water complies with the 5 parameters required by the Standard to be used for human consumption. If it does not, then the water is used for conventional discharges, with the certainty that metals, harmful microorganisms, contaminated sediments have been eliminated and the water is safe for discharges to the subsoil; but in the case that it complies with the 5 parameters required by the Standard, then O3 is added to the water, and the corresponding laboratory validations are applied. If it complies with the Standard, it is packaged for human consumption and if it does not, then it is delivered to the next stage; and D. STAGE 4. At this stage, it is considered that the treated water cannot be discharged into the drains of the conventional network nor can it be treated for human consumption, which indicates the presence of some pathogen that is not metal, is not a microorganism, is not a sediment, but nevertheless still contaminates the water, therefore new laboratory parameters 5 are carried out, to determine an efficient variant of formulation 4 such that in the case of organic matter it is achieved with sulfuric acid in combination with muriatic acid in a ratio of 1:1; in the case of industrial waste materials, nitric acid is combined with muriatic acid and then this stage continues and, in the case of edible fats, tartaric acid or food grade citric acid is used; and the process is iterated until stage 1. In order to provide sufficiency to the previous description and demonstrate the inventive activity of the method below, a set of examples are presented that are merely illustrative, but not limiting, so that the examiner can notice the efficiency and novelty of the method once the accompanying evidence has been analyzed. FORMULATION The base formulation consists of the following compounds, in the following proportions: num Element Range (mg / Kg) Minimum Maximum 1 Aluminum 0.0043 0.0095 2 Barium 0.0057 0.008 3 Boron 0.002 0.009 4 Chromium 0.005 0.009 5 Cadmium 0.0001 0.0009 6 Calcium 43.9373 45.9572 7 Copper 0.007 0.01 8 Phosphorus 0.3579 0.3579 9 Iron 0.1687 0.176 10 Magnesium 0.4591 0.46 11 Nickel 0.005 0.01 12 Lead 0.003 0.003 13 Potassium 0.0958 0.098 14 Sodium 0.0543 0.056 15 Silicon 0.0972 0.098 16 Zinc 0.0062 0.007 This formulation is added in case of having obtained pH measurements is alkaline, it is acidified using a range of between 0.3 to 0.4 grams to dissolve in the container to cause acidification MODIFIED FORMULATION (4) a. Organic matter is obtained with sulfuric acid in combination with muriatic acid in a 1:1 ratio; b. industrial waste materials, nitric acid is combined with muriatic acid in a 1:1 ratio; ίο c. food fats, tartaric acid or food grade citric acid is used in a 1:1 ratio; Example 1. Black water efficiency test. In a sample of water contaminated with sewage, which presents at least an organic load in a range between 18 to 20 grams per liter, before adding the formulation, the water is passed through a conventional strainer to eliminate those impurities that are physically visible to the human eye and the weight and pH are obtained, thus obtaining an alkaline pH or an acidic pH as a result. The base formulation is then added to the water in an amount ranging from 0.75 to 5 grams per liter; once added, it is stirred for approximately 20 seconds at 30 rpm mechanically, until a homogeneous mixture is achieved in the container (no granules, no visible lumps). This mixture is left to stand for a period of 10 to 15 minutes and the phenomenon that is observed is flocculation since as the mixture settles, the water being treated separates and the solids that were trapped or encapsulated by the reaction with the base formulation are retained at the bottom of the container. The formulation for this sample was applied at room temperature between 29 ° C and 31 ° C. A laboratory test is performed to obtain the observed parameters and the initial comparison is made against the result with the mixture and shown in Table 1. Table 1. Initial vs. final laboratory results in a unit of contaminated water with organic load between 18-20 grams per unit. Item Initial Final pH 12.0 7.9 Clarity 0% 95% Oxygen mg / l 30°C average 7.3 9.7 Brilliance None high Once these results are obtained, the water is separated by decantation, removing the liquid from the container and leaving the sediment at the bottom. The water obtained, in this case, was alkaline, regardless of whether the result was acidic; in both cases, it is neutralized. When determining whether the water still contains contaminants, the result is negative, and the sediment is then delivered for use as biofertilizer. The treated and neutralized water obtained is passed through a first filter and, in this example, compared with the standard to determine whether it is intended for discharge into the site's conventional networks. Example 2. Test on vinasse from the tequila industry. The tequila industry constantly faces the problem of managing vinasse, which generally has a high content of organic matter and nutrients such as nitrogen, sulfur, and phosphorus. It also contains a large amount of potassium. Among the most important organic compounds are alcohols, organic acids, and aldehydes. It also contains recalcitrant phenolic compounds, such as melanoidins. They are acidic (pH between 3 and 4). In this invention, they are initially passed through a first filtration to eliminate impurities visible to the human eye and for this example in a container with approximately 1 liter of water loaded with saturation vinasse, which is the direct product of the tequila industry, it is mixed with the base formulation in an amount between a range between 0.75 to 5 grams per liter; Once added, it is stirred for approximately 20 seconds, at about 30 rpm mechanically, until a homogeneous mixture is achieved in the container, it is left to rest for a period between 10 and 15 minutes and the phenomenon that is observed is flocculation since as the mixture comes to rest, the water that is being treated is separated and the solids that were trapped or encapsulated by the reaction with the base formulation are retained in the lower part of the container.The formulation for this sample was applied at room temperature between 33°C and 95°C in the container, and the separation of organic matter from the water contained in the vinasse is observed; Table 2 shows the laboratory results prior to and after application of the formulation: Table 2. Initial vs. final laboratory results in a unit of contaminated water with organic load between 50-80 grams per unit. Item Initial Final pH 3.7 6.4 Clarity 0% 98% Oxygen mg / la 64°C average 1.7 1.7 Brilliance None Brilliant The resulting water still has an acidic pH, so it is neutralized and the organic compounds in the container are separated by decantation. Two more filtrations are performed on the treated water to obtain a higher concentration of 5 Oxygen by adding Ozone and the following results are obtained, observed in table 3 Item Initial Final pH 6.4 7.1 Clarity 98% 99% Oxygen mg / l 34°C average 1.7 6.9 Brilliance Brilliance Very Brilliance Once these results are obtained, the organic part is analyzed to see if it is free of contaminants, then it is used to make biofertilizers. For the 10th aqueous part, it can be discharged directly into the town's conventional networks or, failing that, it can be used for irrigation without risk of contamination. Example 3. Example in sample with sargassum. For this sample, it is necessary to remove the impurities that are physically visible to the naked eye through filtration. It is advisable to avoid crushing the sargassum due to its high proliferation, and for reasons observed, it is necessary to avoid crushing as much as possible. In this example, a 3-liter sample with an organic matter content of between 5 and 30 grams per liter is used; among this organic matter, the sargassum has been previously crushed to include the presence of plant reproductive material. It is then mixed with the base formulation in an amount ranging from 0.75 to 5 grams per liter; once added, it is stirred for approximately 20 seconds, at about 30 rpm mechanically, until a homogeneous mixture is achieved in the container, it is left to rest for a period of between 10 and 15 minutes and the phenomenon that is observed is flocculation since as the mixture rests, the water that is being treated is separated and the solids that were trapped or encapsulated by the reaction with the base formulation are retained in the lower part of the container. The formulation for this sample was applied at room temperature between 26 ° C and 32 ° C, in the container, the separation of organic matter from the water contained in the vinasse is then observed; Table 4 shows the laboratory results prior to and final to the application of the formulation: Table 4. Initial vs. final laboratory results in a unit of water contaminated with organic load between 5-30 grams per unit. Item Initial Final pH 6.7 6.9 Clarity 70% 99% Oxygen mg / l 29°C average 6.7 6.7 Brilliance Poor Brilliance The resulting water still has a nearly neutral pH and, as the organic compounds are separated in the container, they are separated by decantation. It is added with ozone and the analysis shows that there are presence of contaminants and in this case it is the organic material of reproduction of sargassum in the water, therefore it is added to the base formulation, the added formulation, in such a way that the process is iterated and now it is observed that it no longer has the contaminants observed in the first pass of the process and therefore, there is treated and added water that potentially in this case, is intended for human consumption. It is important to note that at the second iteration, the plants and organic matter that is capable of reproduction, are completely inert, because the compounds of the formulation added with acids, have destroyed any possibility of life in the resulting organic matter, by up to 99%. The potentially obtained elements can be classified as harmful and non-harmful, described as follows, and these have this characteristic, depending on the quantity resulting from the application of the method and the formulation. The elements involved and their main action are described below: • Phosphorus: is a water softener and is used as a fertilizer. • Iron: It is not harmful to health in the maximum amount allowed by the NOM, even if it is obtained in a much lower amount than allowed. • Magnesium: Magnesium powder is not suspected of being highly harmful to the environment; in the form of magnesium oxide, a toxicity of 1000 ppm has been established. • Copper: It can be found in many foods, drinking water, and the air. Because we absorb a significant amount of copper every day through food, drinking, and breathing, copper absorption is necessary because copper is a trace element essential for human health. • Calcium: Calcium chloride is found in seawater; calcium ions dissolved in water form deposits in pipes and boilers when the water is hard, i.e., when it contains too much calcium and magnesium. This can be avoided with water softeners. • Zinc: Many foods contain certain concentrations of zinc, the concentration in water may be higher when stored in metal tanks. • Chromium: It is not harmful in small quantities but in large quantities it causes negative effects on health such as skin rashes, general discomfort, weakening of the immune system, among others. • Nickel: Concentrations of nickel in surface waters can lead to decreased algae growth. And like other elements, excess nickel is quite harmful to health. • Cobalt: Cobalt is part of vitamin B12 and in high quantities causes asthma. • Barium: used in salt purification and water softening. • Lead: Lead can enter drinking water through pipes when it rusts, which is why it is highly harmful to health. • Aluminum: This element, in large quantities in water, can cause poisoning in fish, and therefore, birds that eat these fish are also poisoned. • Cadmium: Cadmium has the benefit of concentrating the mind in the human body, but in high concentrations it is very harmful to health as it severely damages the lungs. • Boron: This element consumed in large quantities can have very bad consequences such as infection in the stomach, liver, kidneys and brain which can cause death. • Silicon: Occupational exposure to this element can cause bronchitis and lung disease. However, no negative effects have been reported in the environment.

Claims

1. A process for removing impurities from hard water comprising a formulation to remove metals, impurities and organic remains characterized in that it comprises the following stages: A. STAGE 1. In this stage, a one liter sample of water to be treated is placed in a container, its weight and pH level are determined and there can be three variants: a. If the pH is acidic or neutral, stage 1 continues; b. If the pH is alkaline, it is acidified using a range of 0.3 to 0.4 grams to dissolve in the container to cause acidification with a formulation such that in the case of organic matter it is achieved with sulfuric acid in combination with muriatic acid in a ratio of 1:1;in the case of industrial waste materials, nitric acid is combined with muriatic acid and then this stage continues and, in the case of edible fats, tartaric acid or food grade citric acid is used and this stage is followed by adding a formulation of the base formulation in a present concentration of ± 10% and it is vigorously stirred in a range between 10 and 60 rpm, in a temperature range between 20 ° C and 95 ° C, for a time between 10 and 70 minutes approximately ± 0.1 Volts is released, which when the oscillation is mechanically stopped, it self-consumes in such a way that a reaction is caused where the impurities made up of organic compounds are trapped by chemical reaction and cause that due to the weight they are deposited at the bottom of the container and are removed by decantation, leaving in the container only the water product of the reaction;immediately afterwards and using laboratory tests and at least a set of parameters are determined such as pH, clarity, oxygen concentration, brightness, and conventionally these parameters are compared against a pre-established parameter that allows their reuse, which could be an Official Standard or a reference parameter determined for the territory where the technology is applied (hereinafter referred to as Standard); if the laboratory parameters do not comply with the standards required by the Standard, then the formulation is added to the base formulation in such a way that in the case of organic matter it is obtained with sulfuric acid in combination with muriatic acid in a proportion of 1:1;In the case of industrial waste materials, nitric acid is combined with muriatic acid and then this stage continues; in the case of edible fats, tartaric acid or food grade citric acid is used and this process is iterated by adding the product to the formulation until the parameters have met the Standard; Once this has happened, then the treated water is directed to a first filter, which allows the elimination of sediments that are fine particles of metals, calcium or settleable solids, and again the parameters are validated and the sediments are destined for the elaboration of biofertilizers; the water separated in this stage is delivered to the next stage without the presence of sediments; in this stage the presence of Arsenic, Cadmium, Cyanide, Copper, Chromium, Mercury, Nickel, Lead and Zinc is reduced until it meets the parameters of the standard;B. STAGE 2. At this stage, the pH, BOD (biochemical oxygen demand of water, the amount of oxygen that biology presents in the water measured in milligrams of oxygen per liter of water) and COD (Chemical oxygen demand of water is measured in milligrams per liter in the amount of oxygen that water chemically demands) are measured in the water, determining its acidity or alkalinity in a conventional way and it is determined by means of laboratory parameters, if there is the presence of one or some of the contaminants and microorganisms of the following group: fats and oils, suspended solids, organic carbon, total nitrogen, total phosphorus, hemminth eggs, E coli and fecal Enterococci and it is validated that they are not present by laboratory parameters;Acidic waters are neutralized in the same way as alkaline waters and at this stage the presence of microorganisms is eliminated where potentially now it is warned by the parameters if there is any other contaminant in such a way that it warns us that the treated water only exchanges the contaminant between the sludge and the water itself, if this is the case then the method is not effective in this situation; on the other hand, if the contaminants have been successfully removed, then the sediments can be allowed to be delivered for the production of biofertilizers;once the sludge has settled, it should preferably be filtered and the mixture should be allowed to rest for at least 24 hours to achieve the pH level to neutralize or stabilize, only in the case of not being able to wait this time then the neutralization is caused with the added formulation 4 and the water treated in this stage is then delivered to the next stage is supplied to the next stage; C. STAGE 3.- Once the water is received without contaminants, without sediments and without microorganisms, it is determined if the water complies with the parameters required by the Standard to use water for human consumption, if it is not, then the water is used for conventional discharges, with the certainty that metals, harmful microorganisms, contaminated sediments have been eliminated and the water is safe for discharges that go underground;but in the case that it meets the parameters required by the Standard, then O3 is added to the water, and the corresponding laboratory validations are applied in case of complying with the Standard, it is packaged for human consumption and if it does not, then it is delivered to the next stage; and D. STAGE 4. At this stage, it is considered that the treated water cannot be discharged into the drains of the conventional network and cannot be treated for human consumption, which indicates the presence of some pathogen that is not metal, is not a microorganism, is not a sediment, but nevertheless still contaminates the water, therefore new laboratory parameters are carried out, to determine a variant that is efficient in the formulation in such a way that in the case of organic matter it is obtained with sulfuric acid in combination with muriatic acid in a proportion of 1: 1;In the case of industrial waste materials, nitric acid is combined with muriatic acid, and this stage is then continued. In the case of edible fats, tartaric acid or food-grade citric acid is used; and the process is iterated back to stage 1.

2. A formulation for removing impurities from hard water, characterized in that it comprises: a. Aluminum in a proportion within a range of 0.0043 to 0.0095 mg / kg of the total formulation; b. Barium in a proportion within a range of 0.0057 to 0.008 mg / kg of the total formulation; c. Boron in a proportion within a range of 0.002 to 0.009 mg / kg of the total formulation; d. Chromium in a proportion within a range of 0.005 to 0.009 mg / kg of the total formulation; e. Cadmium in a proportion within a range of 0.0001 to 0.0009 mg / kg of the total formulation; f. Calcium in a proportion ranging from 43.9373 to 45.9572 mg / kg of the total formulation; g. Copper in a proportion ranging from 0.007 to 0.01 mg / kg of the total formulation; h.Phosphorus in a proportion between 0.3579 and 0.3579 mg / kg of the total formulation; i. Iron in a proportion between 0.1687 and 0.176 mg / kg of the total formulation; j. Magnesium in a proportion between 0.4591 and 0.46 mg / kg of the total formulation; k. Nickel in a proportion between 0.005 and 0.01 mg / kg of the total formulation; i. Lead in a proportion between 0.003 and 0.009 mg / kg of the total formulation; m. Potassium in a proportion between 0.0958 and 0.098 mg / kg of the total formulation; n. Sodium in a proportion ranging from 0.0543 to 0.056 mg / kg of the total formulation; or Silicon in a proportion ranging from 0.0972 to 0.098 mg / kg of the total formulation; e.g.Zinc in a proportion ranging from 0.0062 to 0.007 mg / kg of the total formulation; which allows the removal of organic matter when the formulation is used in combination with sulfuric acid and muriatic acid in a 1:1 ratio; because it reacts by breaking lipid bonds and separating fat, inhibiting its action by breaking it down into its separate compounds.

3. The formulation for removing impurities from hard water as claimed in claim 2, characterized in that it allows the removal of industrial waste materials, combining nitric acid with muriatic acid in a 1:1 ratio; because it reacts by neutralizing the pH, leaving it between 5.5 and 8; 4. The formulation for removing impurities from hard water as claimed in claim 2, characterized in that it allows for the removal of food fats, using tartaric acid or food-grade citric acid in a 1:1 ratio; because it reacts by breaking lipid bonds and separates the fat, inhibiting its action by decomposing it into its separate compounds and, in the case of the presence of anilines, neutralizes the compound that causes the coloration; 5. The use of the formulations of claims 2 to 4, which is applied with the process of claim 1, characterized in that it is in powder form; 6. The use of the formulations of claims 2 to 4, which is applied with the process of claim 1, characterized in that it is in capsule presentation; 7. The use of the formulations of claims 2 to 4, which is applied with the process of claim 1, characterized in that it is in gel presentation; 8. The use of the formulations of claims 2 to 4, which is applied with the process of claim 1, characterized in that it is in tablet form; 9. The use of the formulations of claims 2 to 4, which is applied with the process of claim 1, characterized in that it is in pellet presentation;