WO2016010409A1

WO2016010409A1 - System for molecular dissociation by means of electric induction

Info

Publication number: WO2016010409A1
Application number: PCT/MX2014/000112
Authority: WO
Inventors: Emilio DEL BUEY PENDÁS; Lucero ACOSTA MORENO
Original assignee: Agua, Fuego, Aire Y Tierra Ingeniería, S.A. De C.V
Priority date: 2014-07-18
Filing date: 2014-07-18
Publication date: 2016-01-21
Also published as: MX2014008777A

Abstract

The invention relates to a sequential system of electrostatic cells, for the ionisation and creation of magnetic fields, the purpose of which is to separate water molecules from pollutants resulting from human activities of a domestic, municipal, industrial, hospital-related, agricultural, oil-related or other nature.

Description

MOLECULAR DISSOLATION SYSTEM BY ELECTRICAL INDUCTION

BACKGROUND

Various methods and treatment plants for reducing wastewater contamination are known, however many of these methods are inefficient. There are biological, chemical, mixed, electro-coagulation, ionic flocculation technologies, but they show various limitations, especially in terms of quality and volume.

DESCRIPTION

The MOLECULAR DISSOLATION SYSTEM BY ELECTRICAL INDUCTION consists of a sequential system of electrostatic cells, ionization and creation of magnetic fields. It also consists of the manufacture of electrodes of different metal composition that are applied to separate the molecule from water all the components outside it.

This system consists of a set of diverse equipment according to the characteristics and volume of the water, oils or sludge to be treated. In the restoration of contaminated soils, consisting of shovels with shovels where treated water is added to an alkali (1), 2, 3, 4 is dissolved in one (2). Internally it has plates and ionization bars (3), the content in sedimentation vats (4) is poured and the water enters the wastewater treatment for recovery and the mud or soil is clean. Subsequently the soil treatment is carried out according to the drawings described below. In both drawings, Fig. 12 corresponds to the beginning of the process, mentioned in the previous paragraph.

The equipment that makes up the system is described in detail in the diagrams attached in the Drawings that are part of this description, in accordance with the following parts: a) Dynamic and static screens (Fig. 1) to retain solid macro up to three millimeters.

b) Centrifuges (Fig. 2), placed as a second or fourth step to separate a certain degree of coagulated material.

c) Magnetic aligners made of neodymium for molecules (Fig. 3), which place the molecules of other compounds present in an oriented position to facilitate coagulation.

d) Intense dissociation units (Fig. 4) to achieve a first coagulation phase. Direct energy from 8 to 15 volts is applied. A more detailed description of the Units of intense dissociation is shown in Drawing 3/3 which is a fiberglass tank that is made up of the following parts: toroidal flanged cover (A), in some cases it has a chimney (B) , estopero with negative charge (C), water outlet (D), power supply from 0 to 15 volts and 0 to 30 amps (E), sludge drain (F), drain valve (G), bottom It is toroidal (H), water inlet (I), electric induction plates with various alloys (J) and a rapier with positive inlet (K).

e) (¿dissociation eldas (Fig. 5) placed in PVC or fiberglass containers, which are handled with direct energy sources with different voltage and plates of different metals, such as aluminum, steel, titanium, among others. These plates vary in quantity according to the volume and quantity of contaminants that need to be separated from the water molecules. f) Ozone contact tank (Fig. 6) with generator of different production capacity. This tank serves as an oxidizer and sterilizer. Due to its properties, it attacks biological matter such as viruses, bacteria, spores and cysts. It also oxidizes metals and other inorganic matter.

g) Settler (Fig. 7) calculated and manufactured to allow time to settle pollutant angles.

h) Filters of silica sand (Fig. 8) for the retention of particles that did not settle with a size of 30 or 20 microns. This part implies backwash.

i) Activated carbon tank (Fig. 9) in bulk to clarify, remove odor and improve water conditions due to its absorption capacity. It implies backwash.

j) Three containers with polypropylene membranes (Fig. 10) for fine filtration with measurements of 10, 5 and 1 microns. Said membranes retain the already coagulated material,

k) Another line with micro-filtering equipment (Fig. 10), which can be according to the case: ultra-filtration, micro-filtration and reverse osmosis.

I) Ultraviolet light equipment (Fig. 11) to sterilize the water already recovered with light and quartz enclosed in a stainless steel container.

Depending on the type of water to be treated, there will be five different modalities:

First Modality.- The MOLECULAR DISSOLATION SYSTEM BY ELECTRICAL INDUCTION FOR RAINWATER WATER POTABILIZATION consists of a sequential system of electrostatic cells, ionization and creation of magnetic fields. It also consists of the manufacture of electrodes of different metal composition that are applied to separate the molecule from water all the components outside it. This system consists of a set of diverse equipment according to the characteristics and volume of the water, oils or sludge to be treated.

The equipment that makes up the system is described in detail in the diagrams that are attached in the Drawings that are part of this description, in accordance with the following parts: m) to retain solid macro of up to n) second or fourth step to pull apart

certain degree of coagulated material,

o) Magnetic aligners made of neodymium for molecules (Fig. 3), which place the molecules of other compounds present in an oriented position to facilitate coagulation.

p) Intense dissociation units (Fig. 4) to achieve a first coagulation phase. Direct energy from 8 to 15 volts is applied. A more detailed description of the Units of intense dissociation is shown in Drawing 3/3 which is a fiberglass tank that is made up of the following parts: toroidal flanged cover (A), in some cases it has a chimney (B) , estopero with negative charge (C), water outlet (D), power supply from 0 to 15 volts and 0 to 30 amps (E), sludge drain (F), drain valve (G), bottom It is toroidal (H), water inlet (I), electric induction plates with various alloys (J) and a rapier with positive inlet (K).

q) Dissociation cells (Fig. 5) placed in PVC or fiberglass containers, which are handled with direct energy sources with different voltage and plates of different metals, such as aluminum, steel, titanium, among others. These plates vary in quantity according to the volume and quantity of contaminants that need to be separated from the water molecules. r) Ozone contact tank (Fig. 6) with generator of different production capacity. This tank serves as an oxidizer and sterilizer. Because of its properties it attacks biological matter such as viruses, bacteria, spores and cysts. It also oxidizes metals and other inorganic matter.

s) Sedimentator (Fig. 7) calculated and manufactured to allow time to settle contaminant clots.

t) Filters of silica sand (Fig. 8) for the retention of particles that did not settle with a size of 30 or 20 microns. This part implies backwash.

u) Activated carbon tank (Fig. 9) in bulk to clarify, remove odor and improve water conditions due to its absorption capacity. It implies backwash.

v) Three containers with polypropylene membranes (Fig. 10) for fine filtration with measurements of 10, 5 and 1 microns. Said membranes retain the already coagulated material,

w) Another line with micro-filtering equipment (Fig. 10), which may be as appropriate: ultra-filtration, micro-filtration and reverse osmosis,

x) Ultraviolet light equipment (Fig. 1 1) to sterilize the water already recovered with light and quartz enclosed in a stainless steel container.

Second Modality.- THE MOLECULAR DISSOLATION SYSTEM BY ELECTRICAL INDUCTION FOR THE TREATMENT OF WASTEWATER

It consists of a sequential system of electrostatic cells, ionization and creation of magnetic fields.

The equipment that makes up the system is described in detail in the diagrams attached in the Drawings that are part of this description, in accordance with the following parts: a) Dynamic and static sieves (Fig. 1) to retain macro solids of up to three millimeters.

e) Dissociation cells (Fig. 5) placed in PVC or fiberglass containers, which are handled with direct energy sources with different voltage and plates of different metals, such as aluminum, steel, titanium, among others. These plates vary in quantity according to the volume and quantity of contaminants that need to be separated from the water molecules.

f) Ozone contact tank (Fig. 6) with generator of different production capacity. This tank serves as an oxidizer and sterilizer. Because of its properties it attacks biological matter such as viruses, bacteria, spores and cysts. It also oxidizes metals and other inorganic matter.

g) Sedimentator (Fig. 7) calculated and manufactured to allow time to settle contaminant clots.

h) Filters of silica sand (Fig. 8) for the retention of particles that did not settle. This part implies backwash. i) Activated carbon tank (Fig. 9) in bulk to clarify, remove odor and improve water conditions due to its absorption capacity. It implies backwash. Third Modality.- THE MOLECULAR DISSOLATION SYSTEM BY ELECTRICAL INDUCTION FOR THE POTABILIZATION OF SEA WATER

It consists of a sequential system of electrostatic cells, ionization and creation of magnetic fields. It also consists of the manufacture of electrodes of different metal composition that are applied to separate the molecule from the water † all the components outside it.

This system consists of a set of diverse equipment according to the characteristics and volume of the water, oils or sludge to be treated. The equipment that makes up the system is described in detail in the diagrams attached in the Drawings that are part of this description, in accordance with the following parts: a) Dynamic and static screens (Fig. 1) to retain solid macro up to three millimeters.

b) Two centrifuges (Fig. 2), placed as a second or fourth step to separate a certain degree of coagulated material.

c) Two magnetic aligners made of neodymium for molecules (Fig.

3), which place the molecules of other compounds present in an oriented position to facilitate coagulation.

d) Two units of intense dissociation (Fig. 4) to achieve a first coagulation phase. Direct energy from 8 to 15 volts is applied. A more detailed description of the Units of intense dissociation is shown in Drawing 3/3 which is a fiberglass tank that is made up of the following parts: toroidal flanged cover (A), in some cases it has c | chimney (B), rapier with negative charge (C), water outlet (D), power supply from 0 to 15 volts and 0 to 30 amperes (E), sludge drain (F), drain valve (G), the bottom is toroidal (H), water inlet (I), electric induction plates with various alloys (J) and a rapier with positive input (K).

e) Dissociation cells (Fig. 5) placed in PVC or fiberglass containers, which are handled with direct energy sources with different voltage and plates of different metals, such as aluminum, steel, titanium, among others. These plates vary in quantity according to the volume and quantity of contaminants that need to be separated from the water molecules. In this case, a minimum of 50 dissociation cells are necessary, depending on the volume of water to be treated.

f) Two ozone contact tanks (Fig. 6) with generator of different production capacity. This tank serves as an oxidizer and sterilizer. For its properties it attacks biological matter such as viruses, bacteria, spores and! cysts It also oxidizes metals and other inorganic matter.

g) Two settlers (Fig. 7) calculated and manufactured to allow time to settle contaminant clots.

h) Three filters of silica sand (Fig. 8) for the retention of particles that did not settle with a size of 30 or 20 microns. This part implies backwash.

i) Three tanks of activated carbon (Fig. 9) in bulk to clarify, remove odor and improve water conditions due to its absorption capacity. It implies backwash.

j) Six containers with polypropylene membranes (Fig. 0) for fine filtration with measurements of 10, 5 and 1 microns. These membranes retain the already coagulated nhaterial.

k) Another line with two micro-filtration equipment (Fig. 10), which may be as appropriate: ultra-filtration, micro-filtration and reverse osmosis. I) Two ultraviolet light equipment (Fig. 1 1) to sterilize the water already recovered with light and quartz enclosed in a stainless steel container.

Fourth modality.- MOLECULAR DISSOLATION SYSTEM BY ELECTRICAL INDUCTION FOR EARTH WASHING consists of a sequential system of plates and bars of ionization, electrostatic cells, ionization and creation of magnetic fields. It also consists of the manufacture of electrodes of different metal composition that are applied to separate the molecule from water all the components outside it.

This system consists of a set of diverse equipment according to the characteristics and volume of the water, oils or sludge to be treated. The equipment that makes up the system is described in detail in the diagrams attached in the Drawings that are part of this description, in accordance with the following parts:

When it comes to land washing, a step prior to Drawing 1/3 described in Drawing 4/4 is necessary, which consists in the restoration of contaminated soils, earth washing, consisting of shovels with shovels where treated water is added to an alkali (1), dissolves 2, 3, 4 to one (2). Internally it has plates and ionization bars (3), the content in sedimentation vats (4) is poured and the water enters the wastewater treatment for recovery and the mud or soil is clean.

Subsequently the ground treatment is carried out according to drawings 1/3 and 2/3 described below. In both drawings, Fig. 12 corresponds to the beginning of the process, mentioned in the previous paragraph. a) Dynamic and static cranes (Fig. 1) to retain macro solids of up to three millimeters.

d) Intense dissociation units (Fig. 4) to achieve a first coagulation phase. Direct energy from 8 to 15 volts is applied. A more detailed description of the Units of intense dissociation is shown in Drawing 3/4 which is a fiberglass tank that is made up of the following parts: toroidal flanged cover (A), in some cases it has a fireplace j

(B), rapier with negative charge (C), water outlet (D), power supply from 0 to 15 volts and 0 to 30 amps (E), sludge drain (F), drain valve (G) , the bottom is toroidal (H), water inlet (I), electric induction plates with various alloys (J) and a rapier with positive inlet (K).

g) Sedimentator (Fig. 7) calculated and manufactured to allow time to settle contaminant clots. h) Filters of silica sand (Fig. 8) for the retention of particles that are not 30 or 20 microns in size. This part implies

i) Activated carbon tank (Fig. 9) in bulk to clarify, remove odor and improve water conditions due to its absorption capacity.

It implies backwash.

Fifth modality.- THE MOLECULAR DISSOLATION SYSTEM BY ELECTRICAL INDUCTION FOR THE TREATMENT OF HAZARDOUS WASTE consists of a sequential system of electrostatic cells, ionization and creation of magnetic fields. It also consists of the manufacture of electrodes of different metal composition that are applied to separate the molecule from water all the components outside it. This system consists of a set of diverse equipment according to the characteristics and volume of the water, oils or sludge to be treated.

c) Magnetic aligners made of neodymium for molecules (Fig. 3), which place the molecules of other compounds present in a d) first phase of description more

Detailed of the Units of intense dissociation is shown in Drawing 3/3 which is a fiberglass tank that is made up of the following parts: toroidal flanged cover (A), in some cases it has a chimney (B), but with negative charge (C), water outlet (D), power supply from 0 to 15 volts and 0 to 30 amps (E), sludge drain (F), drain valve (G), the bottom is toroidal ( H), water inlet (I), electric induction plates with various alloys (J) and a rapier with positive inlet (K).

f) Ozone contact tank (Fig. 6) with generator of different production capacity. This tank serves as an oxidizer and sterilizer.

Because of its properties it attacks biological matter such as viruses, bacteria, spores and cysts. It also oxidizes metals and other inorganic matter.

improve water conditions due to its absorption capacity. It implies backwash.

j) Ozone contact tank (Fig. 10) with generator of different production capacity. For the second time this tank serves as an oxidant and sterilizer. Because of its properties it attacks biological matter such as viruses, bacteria, spores and cysts. It also oxidizes metals and other inorganic matter. The result of the application of the parts described above and that make up the system results in water suitable for human consumption. i

The physical phenomena that occur in the purification and treatment system are the following: a) Screening

b) Magnetic

c) Electrostatic

d) Coagulation

e) Sedimentation

f) Filtration

g) Ultrafiltration

h) Sterilization with ultraviolet and ozone rays

The use of these physical phenomena manages to separate the water molecules from other contaminating components.

System applications include, among others, the following uses:

1) Healthy and marine waters

2) Domestic wastewater

3) Municipal wastewater

4) Industrial wastewater

5) Hospital wastewater

6) Wastewater from mining activities

7) Rainwater

8) Leaching of solid waste

9) Oils

Claims

CLAIMS The novelty of the system is that it integrates equipment to separate the water molecules contaminated by human or natural factors.

1. - System of molecular dissociation by electrical induction for the purification of rainwater comprising: a dynamic sieve and a static sieve; centrifugal machines; magnetic aligners made of neodymium for molecules, which place the molecules of other compounds present in an oriented position to facilitate coagulation; Intense dissociation units to achieve a first coagulation phase, which are made up of: a fiberglass tank that is made up of a toroidal flanged cover (A), a chimney (B), a rapier with a negative charge (C ), a water outlet (D), a power supply (E), a sludge drain (F), a drain valve (G), a toroidal bottom (H), a water inlet (I ), an electric induction plate with various alloys (J) and a rapier with positive input (K); a dissociation cell placed in PVC or fiberglass containers; a contact tank for ozone with generator of different production capacity; a settling tank; filters of silica sand; a bulk activated carbon tank; three containers with polypropylene membranes for fine filtration with measurements of 10, 5 and 1 microns; a micro-filtration equipment, which may be as appropriate: ultra-filtration, micro-filtration and reverse osmosis; an ultraviolet light equipment to sterilize the water already recovered with light and quartz enclosed in a stainless steel container.

2. - System of molecular dissociation by electrical induction for wastewater which includes: a dynamic screen and a static screen; centrifugal machines; magnetic aligners made of neodymium for molecules, which place the molecules of other compounds present in a oriented position to facilitate coagulation; Intense dissociation units to achieve a first coagulation phase, which are made up of: a fiberglass tank that is made up of a toroidal flanged cover (A), a chimney (B), a rapier with a negative charge (C ), a water outlet (D), a power supply (E), a sludge drain (F), a drain valve (G), a toroidal bottom (H), a water inlet (I), an electric induction plate with various alloys (J) and a rapier with positive input (K); a dissociation cell placed in PVC or fiber containers

¡¡

glass; u ozone contact tank with generator of different production capacity; a settling tank; filters of silica sand; an i tank

bulk activated carbon!

3.- System of molecular dissociation by electrical induction for the purification of seawater comprising: a dynamic sieve and a static sieve; two centrifugal machines; two magnetic aligners made of neodymium for molecules, which place the molecules of other compounds present in an oriented position to facilitate coagulation; two units of intense dissociation to achieve a first coagulation phase, which are made up of: two fiberglass tanks that are made up of a toroidal flanged cover (A), a chimney (B), a rapier with a negative charge (C ), a water outlet (D), a power supply (E), a sludge drain

¡.

(F), a drain valve (G), a toroidal bottom (H), a water inlet (I), a ί

electric induction plate with various alloys (J) and a rapier with positive input (K); fifty dissociation cells placed in PVC or fiberglass containers; two ozone contact tanks with generator of different production capacity; two settling tanks; three filters of silica sand; three tanks of activated carbon in bulk; six containers with polypropylene membranes for fine filtration with measurements of 10, 5 and 1 microns; a micro-filtration equipment, which can be as appropriate: ultra-filtration, micro-filtration and Inverse osmosis; an ultraviolet light equipment to sterilize the water already recovered with light and quartz enclosed in a stainless steel container.

4.- System of molecular dissociation by electric induction for the washing of earth that includes: a shovel revolver that has plates and bars of internal ionization, a dynamic sieve and a static sieve; centrifugal machines; Magnetic aligners made of neodymium for molecules, the ¹ qua is placed to the molecules of other compounds present in an oriented position to facilitate their coagulation; Intense dissociation units to achieve a first coagulation phase, which are made up of: a fiberglass tank that is made up of a toroidal flanged cover (A), a chimney (B), a rapier with a negative charge (C ), a water outlet (D), a power supply (E), a sludge drain (F), a drain valve (G), a toroidal bottom (H), a water inlet (I), an electric induction plate with various alloys (J) and a rapier with positive input (K); a dissociation cell placed in PVC or fiberglass containers; a contact tank for ozone with generator of different production capacity; a settling tank; filters of silica sand; a bulk activated carbon tank; three containers with polypropylene membranes for fine filtration with measurements of 10, 5 and 1 microns; a micro-filtration equipment, which may be as appropriate: ultra-filtration, micro-filtration and reverse osmosis; an ultraviolet light equipment to sterilize the water already recovered with light and quartz enclosed in a stainless steel container.

5.- System of molecular dissociation by electrical induction for the treatment of hazardous waste, which includes: a dynamic sieve and a static sieve; centrifugal machines; magnetic aligners made of neodymium for molecules, which place the molecules of other compounds present in an oriented position to facilitate coagulation; Intense dissociation units to achieve a first phase of coagulation, which are conformed by: a fiberglass tank that is made up of a toroidal flanged cover (A), a chimney (B), a rapier with negative charge (C), a water outlet (D), an electrical power supply ( E), a sludge drain (F), a drain valve (G), a toroidal bottom (H), a water inlet (I), an electric induction plate with various alloys (J) and a rapier with inlet positive (K); a dissociation cell placed in PVC or fiberglass containers; a contact tank for ozone with generator of different production capacity; a settling tank; a silica sand filter; a bulk activated carbon tank; an ozone generator (L).