JP2016175056A - Water treatment system - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a safe, economical water treatment system that corresponds easily to a plant scale and is easy to maintain, the system efficiently collecting metal ions, halogen ions, hydrogen ions, substances free of electric charges, organic compounds, and radioactive substances from various dirty waters, making germs and viruses extinct.SOLUTION: A water treatment system includes a vacuum evaporation type reciprocating pump 11 to evaporate dirty water under vacuum, a separator 12 to separate a gas inflow by magnetization into a main straight flow, an anode-side branch flow, and a cathode-side branch flow, and a collecting apparatus 13 to divide its inside into a straight flow chamber 38, an anode-builtin chamber 39, and a cathode-builtin chamber 40 where the main straight flow, the anode-side branch flow, and the cathode-side branch flow proceed respectively. The main straight flow goes directly to an outlet 41, and halogen ions, negative-charged organic compounds and the like adhere to an anode 46, while metal ions, positive-charged organic compounds and the like adhere to a cathode 47.SELECTED DRAWING: Figure 1

Description

  The present invention relates to a water treatment system, and in particular, various types of dirty water, such as dirty river water and ground water, and sewage and contaminated water discharged from houses, various factories, and various plants, Is the process of applying vacuum vaporization, magnetic field separation, and electricity collection to dirty seawater around factories and plants, and from the dirty water, metal ions, halogen ions, hydrogen ions, non-charged substances, organic compounds Further, the present invention relates to a water treatment system in which radioactive substances are removed and purified, and bacteria and viruses are killed and purified.

  Usually, a filter is used for purification of tap water in a house, and a filter, a filtration tank, a sedimentation tank, etc. are used for purification of well water. On the other hand, sewage and contaminated water discharged from various factories and plants often contain metal ions, halogen ions, hydrogen ions, non-charged substances (atoms, molecules) and organic compounds. They cannot be removed with filters, filtration tanks or sedimentation tanks.

  (Non) Patent Literature n

  The object of the present invention is to efficiently collect and collect metal ions, halogen ions, hydrogen ions, non-charged substances, organic compounds, radioactive substances, etc. from various types of dirty water with little energy consumption. Bacteria and viruses contained in the dirty water can be killed in the process of vaporization under reduced pressure, the dirty water is purified safely and economically, the water treatment facility is embodied in a simple structure, and the dirty water The processing capacity and number of units are increased or decreased according to the amount of emissions, and it is easily adapted to the scale of the factory or plant, making inspection and repair simple and easy, and maintaining functions by replacing parts for long and easy maintenance. And the provision of a water treatment system where the cost of it is reduced and becomes more economical.

  The water treatment system of the present invention sucks dirty water containing at least metal ions, halogen ions, hydrogen ions, non-charged substances, organic compounds, etc., vaporizes them by vacuum, discharges them, and then A reversible vacuum type reciprocating pump to flow, an intake opening at one end, and a wide air supply opening at the other end, and the ions in the gas flow flowing into the inside from the reduced pressure vaporizing reciprocating pump through the air opening and positive and negative Applying a magnetic field in the direction of separation that gives force to the charged organic compound according to the left-hand rule for Lorentz force, the gas flow is branched into the main straight flow, anode side branch flow, and cathode side branch flow, and the air supply opening And a separation device that flows next to each other, and has a wide intake opening at one end, and the inside is connected to the intake opening, and the straight passage chamber, the anode built-in chamber, and the cathode The main straight flow is divided into the straight passage chamber, the anode side branch flow is flown into the anode internal chamber, the cathode side branch flow is flowed into the cathode internal chamber, and the straight passage chamber is divided. Then, the main straight flow is allowed to flow directly to the outlet thereof, and in the chamber with a built-in anode, the halogen ions, negatively charged organic compounds, etc. are attached to the anode, and in the chamber with a built-in cathode, the metal is placed on the cathode. And a separate collection device for depositing ions, positively charged organic compounds and the like.

  In the water treatment system of the present invention, the dirty water is used to remove metal ions, halogen ions, hydrogen ions, non-charged substances and organic compounds from the dirty water, and to kill and remove bacteria and viruses. Is continuously subjected to vacuum vaporization, magnetic field fractionation, and electricity collection, i.e., the contaminated water is first vaporized under reduced pressure to charge the organic compound, and the metal ions, halogen ions, hydrogen ions, and charges are charged. It is not a gas flow in a state of mixing substances that do not have, and positive and negative charge organic compounds, etc., then, by separating the magnetic field, applying a magnetic field to the gas flow and atoms that do not have charge or atoms that are not charged either positive or negative, It is divided into a flow of molecules, a flow of metal ions and positively charged organic compounds, and a flow of halogen ions and negatively charged organic compounds. Next, water molecules that do not have the electric charge and atoms and molecules that are not charged either positively or negatively in the electricity collection are flowed to the next and processed, while the halogen ions and negatively charged organic compounds are applied to the anode. Since the metal ions and positively charged organic compounds are collected on the cathode, the metal ions, halogen ions, hydrogen ions, non-charged substances, and organic compounds that are difficult to remove with filters and filtration tanks. Efficiently separates and collects from the dirty water with low energy consumption, cleans the dirty water safely and economically, materializes the water treatment facility in a simple structure, and discharges the dirty water The processing capacity and number of units are increased or decreased according to the conditions, and it is easily adapted to the scale of the factory or plant, making inspection and repair simple and easy. It is easy and easy to maintain, and the cost of it is reduced, making it more economical. In the process of purifying contaminated water, bacteria and viruses are killed in the process of vaporization under reduced pressure. The radioactive material is removed in the same manner and can be safely and economically used for the purification treatment of contaminated water, and is practically useful for the purification treatment of dirty water.

It is the general | schematic figure which showed the specific example of the water treatment system of this invention utilized for the purification process of the sewage discharged | emitted from a factory. It is the general | schematic figure which showed another specific example of the water treatment system of this invention of carrying out the purification process of the waste water discharged | emitted from the enlarged factory. It is the general | schematic figure which showed another specific example of the water treatment system of this invention of which it increases in size and raises processing efficiency and purifies the wastewater discharged | emitted from a factory. It is the longitudinal cross-sectional view which showed another decompression vaporization type reciprocating pump utilized in the water treatment system shown by FIG. It is the cross-sectional view which showed the another pressure reduction vaporization type reciprocating pump shown by FIG. It is the longitudinal cross-sectional view which showed another multistage pressure reduction vaporization reciprocating pump utilized by the water treatment system shown by FIG. It is the cross-sectional view which showed the other multistage pressure reduction vaporization type | mold reciprocating pump shown by FIG.

  The water treatment system of the present invention sucks dirty water containing at least metal ions, halogen ions, hydrogen ions, non-charged substances, organic compounds, etc., vaporizes them by vacuum, discharges them, and then A reversible vaporization type reciprocating pump to flow, an intake opening at one end, and a wide air supply opening at the other end, and the ions in the gas flow flowing into the inside from the reduced pressure vaporization reciprocating pump through the intake opening and positive and negative Applying a magnetic field in the direction of separation that gives force to the charged organic compound according to the left-hand rule for Lorentz force, the gas flow is branched into the main straight flow, anode side branch flow, and cathode side branch flow, and the air supply opening And a separation device that flows next to each other, and has a wide intake opening at one end, and the inside is connected to the intake opening, and the straight passage chamber, the anode built-in chamber, and the cathode The main straight flow is divided into the straight passage chamber, the anode side branch flow is flown into the anode internal chamber, the cathode side branch flow is flowed into the cathode internal chamber, and the straight passage chamber is divided. Then, the main straight flow is allowed to flow directly to the outlet thereof, and in the chamber with a built-in anode, the halogen ions, negatively charged organic compounds, etc. are attached to the anode, and in the chamber with a built-in cathode, the metal is placed on the cathode. And a separate collection device for depositing ions, positively charged organic compounds and the like.

Hereinafter, the water treatment system of the present invention will be described based on the specific examples specified and illustrated. FIG. 1 shows the sewage discharged from a factory, which is embodied so that various kinds of dirty water can be purified. Example 10 of the water treatment system of the present invention to be used for purification treatment is shown, and the water treatment system 10 continuously applies vacuum evaporation, magnetic field separation, and electricity collection to the sewage, Then, the vacuum vaporization type reciprocating pump 11, the separation device 12, the separation collection device 13, and the centrifugal separation device (to remove at least metal ions, halogen ions, hydrogen ions, non-charged substances, organic compounds, etc. from the sewage ( (Not shown) are assembled in order, and sewage discharged from the factory is purified. The water treatment system 10 separates and removes metal ions, halogen ions, hydrogen ions, non-charged substances, organic compounds, and the like contained in sewage.
The metal ions are alkali metal ions, alkaline earth metal ions, other metal ions, and the halogen ions are fluorine ions, chlorine ions, bromine ions, iodine ions, etc., and have no charge. Is a water molecule or an atom or molecule that is not charged either positively or negatively, such as water (H ₂ O), oxygen (O ₂ ), nitrogen (N ₂ ), inert gas (rare gas), such as argon (Ar) , Krypton (Kr), xenon (Xe), and the like, and the organic compound is oil, fat or the like.

The oil is vaporized by depressurization in the reduced pressure vaporization type reciprocating pump 11, and the vaporized water molecules are charged positively or negatively in the process of being discharged from the reduced pressure vaporization type reciprocating pump 11 to the separation device 12. Or it attracts and adheres to an anode.
In addition, cations, anions, non-charged atoms and molecules such as water (H ₂ O), oxygen (O ₂ ), and nitrogen (N ₂ ) are agitated and charged even if they are in a crisp state. You will never get or be robbed.

Specifically, atoms attracted to the cathode are firstly hydrogen, an isotope of hydrogen, and hydrogen (H) is taken as an example. When hydrogen (H) is present in the form of ions, it is attracted to the cathode because it is in the form of H ⁺ and has a positive charge. When H ⁺ adheres to the cathode, H ⁺ obtains electrons (e ⁻ ) from the cathode,
2H ⁺ + 2e ⁻ → H ₂
Reacts with hydrogen molecules (H ₂ ).
When it is in the state of hydrogen molecules (H ₂ ), it is released from the cathode because it has no charge. At this time, since the molecular weight of the hydrogen molecule is very light, which is 2 as compared with the molecular weight 18 of water, it is easy to move upward. Utilizing this property, hydrogen molecules (H ₂ ) can be collected.

Next, for alkali metals such as lithium (Li), sodium (Na), and potassium (K), alkali metals tend to emit electrons or be deprived to become positive ions, that is, have a very strong ionization tendency. Therefore, when it exists in water, it becomes a positive ion. Even if the positive ions are attracted to the cathode, the positive ions tend to remain positive. Therefore, the positive ions remain attached to the cathode even after being attached. Of course, the positive ions of lithium (Li), sodium (Na), and potassium (K) are Li ⁺ , Na ⁺ , and K ⁺ , respectively.

And about other metal ions, when other metal ions are present in water, if they are in a positive ion state, they are attracted to the cathode, and electrons are obtained from the cathode, for example, copper ( Cu ²⁺ )
Cu ²⁺ + 2e ⁻ → Cu
Reacts with copper to be deposited on the cathode. In this way, other metals are deposited on the cathode and can be collected.

  Further, for alkaline earth metals such as magnesium (Mg) and calcium (Ca), if the alkaline earth metal has the same properties as the alkali metal, it can be treated in the same manner as the alkali metal, If it has the same properties as other metals, it can be treated in the same manner as other metals.

On the other hand, atoms attracted to the anode are halogens such as fluorine (F), chlorine (Cl), bromine (Br), and iodine (I), and these halogens exist in an anionic state in water. . For that purpose, it is attracted to the anode and attached to the anode to take away electrons. For example, if it is chlorine (Cl),
2Cl ⁻ → Cl ₂ + 2e ⁻
React with. At room temperature, chlorine (Cl ₂ ) becomes a gas and is released from the cathode because it has no charge. Chlorine molecules have a molecular weight of 71 and are easy to move downward. Chlorine can be collected using this property. Fluorine (F) can also be collected as a gas because the molecular weight of F ₂ is 38 as is the case with chlorine. Since bromine (Br) becomes a liquid, it can be collected as a liquid. Furthermore, since iodine (I) becomes an individual, it can be collected by being deposited on the anode.

  Furthermore, for substances that do not have an electric charge, substances that do not have an electric charge are non-polar substances that are not soluble in water but are soluble in organic substances (organic solvents), and are mixed with oil in the first stage of the process of treating sewage. As a result, the oil is charged in the process of being treated by the oil and the sewage is being processed, so that substances that do not have the charge are processed together in a form mixed with the oil. All uncharged material is not taken up and removed by the oil; if not taken up by the oil, the uncharged material goes straight without Lorentz forces and is centrifuged. It can be removed.

By the way, as described above, the water treatment system 10 will be described in detail based on the properties of various substances mixed in the sewage. The water treatment system 10 includes a reduced pressure vaporization type reciprocating pump 11, a separation device. 12, the separation and collection device 13, the centrifuge (not shown), etc. are assembled in order. And in this water treatment system 10, the pressure reduction vaporization type reciprocating pump 11 is assembled in an inverted type.
This vacuum vaporization type reciprocating pump 11 is fitted to an inverted cylinder 14, an inverted piston 15 which is fitted to a cylinder bore 19 of the cylinder 14 so as to be slidable back and forth, and forms a cylinder chamber 20 in the cylinder bore 19, A shaft (not shown), a connecting rod 16 and a piston pin (not shown) are connected to the piston 15 and geared to the crank shaft to connect the piston 15 to the cylinder bore of the cylinder 14. 19 is assembled by an electric motor (not shown) or the like that is slid back and forth in the interior.

The cylinder 14 has a water inlet 21 and an air outlet 22 on the cylinder side wall 17 on the cylinder head 18 side with an appropriate separation in the circumferential direction, and an electromagnetic water supply valve 23 is attached to the absorption port 21 to form a pipe. 25 is connected to a sewage tank (not shown) of the factory, while a check valve 24 is attached to the exhaust port 22 and connected to the intake opening 30 of the sorting device 12 by a divergent duct 32.
The electromagnetic water supply valve 23 is continuous with the reciprocating motion of the piston 15, and is opened and closed at the beginning of water supply in the reduced-pressure vaporization process to flow an appropriate amount of dirty water into the cylinder 14. On the other hand, the check valve 24 is a check valve that adopts a structure used for an air duct and enhances the sealing effect. Further, the water inlet 21 is preferably closer to the cylinder head 18 than the exhaust port 22.

  The piston 15 has a structure in which a plurality of ring grooves (not shown) are formed on the outer peripheral surface near the piston head 26 and a plurality of piston rings (not shown) are correspondingly fitted in the plurality of ring grooves. In addition, the electromagnetic water supply valve 23 is opened at the beginning of suction in the decompression vaporization step, and is closed at the beginning of decompression vaporization so that the sewage is sucked into the cylinder chamber 20 of the cylinder 14 by an appropriate amount. I have to.

  The separating apparatus 12 has a horizontal box cylinder 27 having an intake opening 30 at one end and a wide air supply opening 31 by opening the other end, and left and right sides of the box cylinder 27. A large number of electromagnetic coils (not shown) are arranged side by side on the side walls 28 and 29, and the large number of electromagnetic coils are energized, passed through the intake opening 30, and from the reduced pressure vaporization type reciprocating pump 11 to the inside 12. Apply a magnetic field in the upper and lower separation direction that gives force by the rule to the left hand regarding Lorentz force against metal ions, halogen ions, hydrogen ions, positive and negative charge organic compounds etc. mixed in the gas flow flowing into The gas flow is branched into a main straight flow, an anode side branch flow, and a cathode side branch flow. If it demonstrates in FIG. 1, the magnetic field penetrates perpendicularly | vertically toward the bottom from the paper surface.

The separation collection device 13 has a wide intake opening 33 at one end thereof that is aligned with the wide air supply opening 31 of the separation device 12, and the inside communicates with the intake opening 33 so as to be partitioned by partitions 34, 35, 36, and 37. The straight passage chamber 38, the anode built-in chamber 39, and the cathode built-in chamber 40 are divided. The straight passage chamber 38 is branched in the separation device 12 and corresponds to the main straight flow, anode side branch flow, and cathode side branch flow flowing from the separation device 12. In the middle, the anode built-in chamber 39 is divided under the straight passage chamber 38, and the cathode built-in chamber 40 is divided on the straight passage chamber 38, and the straight passage chamber 38 is divided. The other end is opened to form an outlet (air supply opening) 41, the anode built-in chamber 39 closes the other end, the outlet (discharge port) 42 opens downward, and the cathode built-in chamber 40 closes the other end. An outlet (exhaust port) 43 is opened upward.
Further, the straight passage chamber 38 is connected to the outlet (air supply opening) 41 of the centrifugal separator, the anode built-in chamber 39 has an anode plate 46 inside, and the cathode built-in chamber 40 has a cathode plate inside. 47 are arranged respectively.
The anode plate 46 and the cathode plate 47 are electrically connected to the battery 48.

  The separate collection device 13 adopts such a branch chamber structure, and the main straight flow in the straight passage chamber 38, the anode side branch flow in the anode built-in chamber 39, and the cathode built-in chamber 40 in the cathode built-in chamber 40. In the straight passage passage 38, the main straight flow flows as it is to the air supply opening 41 in the straight passage passage 38, and in the anode built-in chamber 39, the halogen ions and negative charge organic compounds are fed to the anode plate 46. Then, in the cathode built-in chamber 40, metal ions, positively charged organic compounds, etc. are attached to the cathode plate 47.

  The centrifuge is operated by an electric motor (not shown) connected to the air inlet opening 41 of the straight passage chamber 38 of the fraction collector 13 by a duct 49 and passes through the straight passage chamber 38. Then, the gas flowing in is processed.

Next, the operation of the water treatment system 10 will be described. First, a start switch (not shown) is turned on. When the activation switch is turned on, a controller (not shown) works in the water treatment system 10, and the decompression vaporization type reciprocating pump 11, the separation device 12, the separation collection device 13, and the centrifugal separator are controlled by the controller. Is done.
In this reduced pressure vaporization type reciprocating pump 11, first, the electric motor is energized, the inverted piston 15 is reciprocated up and down in the cylinder bore 19 of the inverted cylinder 14 by the electric motor, and the electromagnetic The water supply valve 23 is opened / closed under continuous energization control of the reciprocating motion of the piston 15, and the electromagnetic water supply valve 23 is connected to the cylinder 14 during the decompression vaporization step of the decompression vaporization type reciprocating pump 11. The cylinder 14 is opened and closed at the beginning of water absorption when sliding up and down in the cylinder bore 19 so that an appropriate amount of dirty water is sucked into the cylinder bore 19 of the cylinder 14.
As the piston 15 slides further up and down into the cylinder bore 19 of the cylinder 14, the pressure is rapidly reduced and the sewage is instantly vaporized within the cylinder chamber 20.

When the piston 15 reaches bottom dead center, the electric motor then begins to slide downward into the cylinder bore 19 of the cylinder 14, and in this discharge process, the vaporized water molecule gas And oil, metal ions, halogen ions, hydrogen ions, and non-charged substances mixed in the gas are discharged from the exhaust port 22 by the piston 15, push the check valve 24 open, and It flows through the divergent duct 32 to the intake opening 30 of the sorting device 12 and then flows into the sorting device 12. Of course, the oil is charged to positive and negative charges in the course of the discharge process from the reduced pressure vaporization process of the reduced pressure vaporization type reciprocating pump 11.
During the operation of the water treatment system 10, the reduced pressure vaporization type reciprocating pump 11 continuously evaporates the sewage under reduced pressure and continuously flows the wastewater to the separation device 12.

  In this sorter 12, the many electromagnetic coils are energized, and the magnetic field gives a force to the metal ions, halogen ions, hydrogen ions, positive and negative charge organic compound oil, etc. according to the left-hand rule concerning Lorentz force. 1 and is placed in a state where the ions and oils of the positive and negative charge organic compounds are separated, and based on FIG. 1, the magnetic field is generated vertically from the top of the page to the bottom. The ion or oil is mixed with the gas flow of the vaporized water molecules, and the vaporized water is subjected to force from the magnetic field. The molecular gas flow is branched into a main straight flow, an anode-side branch flow, and a cathode-side branch flow, and flows from the air supply opening 31 to the wide intake opening 33 of the separate collection device 13. .

  In the sorting and collecting apparatus 13, voltage is applied to the anode plate 46 and the cathode plate 47 by the battery 48, the halogen ions and oil are applied to the anode plate 46, and the metal ions and hydrogen ions are applied to the cathode plate 47. The main straight flow flows from the wide intake opening 33 to the straight passage chamber 38, and the cathode side branch flow flows from the wide intake opening 33 to the separate collection. The cathode side branch flow flows to the anode internal chamber 39 and the cathode side branch flow from the wide intake opening 33 to the cathode internal chamber 40, and in the straight passage passage chamber 38, the main straight flow is straightened as it is to supply the air. The water molecules are flowed to the opening 41 and sent from the air supply opening 41 to the centrifugal separator through the duct 49, where the water molecules separated and collected are vaporized. Body, such as to release.

At the same time, in the anode built-in chamber 39, the halogen ions, oil, and the like are attracted to and attached to the anode plate 46 and collected. The anode built-in chamber 39 returns the gas of water molecules vaporized by the straight passage chamber return 44 to the air supply opening 41 side of the straight passage chamber 38.
On the other hand, at the same time, in the cathode built-in chamber 39, the metal ions, oil, and the like are attracted to the cathode plate 47 and attached to be collected. In the cathode built-in chamber 40, the hydrogen ions flow into the discharge port 42 as hydrogen molecules (H ₂ ) in the cathode plate 47. The cathode internal chamber 40 returns the gas of water molecules vaporized by the straight passage chamber return 45 to the air supply opening 41 side of the straight passage chamber 38.
In this way, in this water treatment system 10, mixed substances such as metal ions, halogen ions, hydrogen ions, non-charged substances, and organic compounds are embodied in a simple structure from the sewage discharged from the factory. Thus, the wastewater is purified by using a means that makes maintenance and maintenance simple and easy, and can be separated and collected efficiently, economically and safely with less energy consumption.
This water treatment system 10 can be easily adapted by changing the treatment capacity by increasing or decreasing the treatment capacity, number, etc. of the vacuum vaporization type reciprocating pump 11, the separation device 12, and the separation collection device 13 according to the scale of the factory or plant. In addition, the reduced pressure vaporization type reciprocating pump 11, the separating device 12, and the separating and collecting device 13 can be kept functional only by exchanging parts, and can be easily inspected and repaired. It will be easier, save money and be economical.
Further, the fractional collection rate of the metal ions, halogen ions, hydrogen ions, non-charged substances, organic compounds, and the like is classified into the fractionation device 12 and the fractionation collection device 13 in the straight passage chamber 38 of the fractionation collection device 13. It can be easily given by repeatedly connecting. When the sewage is further contaminated with radioactive substances, the water treatment system 10 can be used in the same manner to remove the radioactive substances from the sewage.
Further, even when the sewage is contaminated with bacteria or viruses, in the water treatment system 10, the bacteria and viruses are ruptured and killed by the reduced pressure during the reduced pressure vaporization process of the reduced pressure vaporization type reciprocating pump 11. .

  Therefore, in this water treatment system 10, first, sewage containing at least metal ions, halogen ions, hydrogen ions, non-charged substances, and organic compounds is depressurized to vaporize the sewage by depressurization. In the gas stream of water molecules, the metal ions, halogen ions, hydrogen ions, non-charged substances, and organic compounds are mixed, and then the mixed substances are separated by a magnetic field, and then the electrodes are used to separate the mixed substances. Since the collected mixed substances are collected, the metal ions, halogen ions, hydrogen ions, non-charged substances, and organic compounds, which are difficult to remove with filters and filtration tanks, can be consumed from the sewage with low energy consumption. Efficiently separated and collected, the sewage is purified safely and economically, and the water treatment facility is realized in a simple structure Depending on the amount of sewage discharged, the processing capacity and number of units are increased or decreased to easily adapt to the scale of the factory or plant, and inspection and repair are easy and easy. It becomes simple and easy, and the cost of it is reduced, making it more economical, and even if the sewage is contaminated with radioactive material, the radioactive material is removed from the sewage and the sewage is Even if the sewage is purified and contaminated with bacteria and viruses, the bacteria and viruses are killed by the reduced pressure during vaporization under reduced pressure, and the sewage is purified. As such, the sewage is purified. It is useful for practical use.

FIG. 2 shows a water treatment system of the present invention which is improved so that various kinds of dirty water can be purified, and is used to continuously purify a large amount of waste water discharged from a factory. The water treatment system 50 is embodied by replacing the reduced pressure vaporization type reciprocating pump 11 of the water treatment system 10 described above with a reduced pressure vaporizer 51.
The water treatment system 50 continuously applies reduced-pressure vaporization, magnetic field separation, and electricity collection to the sewage, and metal ions, halogen ions, hydrogen ions, non-charged substances, organic compounds, etc. In order to remove water, the vacuum vaporizer 51, the separation device 12, the separation collection device 13, the centrifuge, and the like are assembled in order, and the sewage discharged from the factory is purified.
In this water treatment system 50, the decompression vaporization device 51 enlarges the long cylindrical decompression vaporization chamber 56, and the large long tubular decompression vaporization chamber 56 is composed of decompression vaporization pumps 62, 62, 62, 62, with electric motors, 62, 62, the pressure is reduced and the pressure is reduced, and sewage containing at least metal ions, halogen ions, hydrogen ions, non-charged substances, and organic compounds is guided and vaporized while slowly flowing into the room. The vaporized water molecule gas is mixed with its metal ions, halogen ions, hydrogen ions, non-charged substances, organic compounds, etc., and the reduced-pressure vaporization pumps 62, 62, 62, 62, 62 are mixed. , 62 serves to flow to the next separation device 12. Therefore, the water treatment system 50 makes it possible to purify the sewage continuously and in large quantities.

  The decompression vaporization apparatus 51 employs a structure in which a large long cylindrical casing 52 is closed at both ends by front and rear end walls 53, 54 and the inside is utilized as a large long cylindrical decompression vaporization chamber 56, and The cylindrical casing 52 is appropriately tilted forward and downward and placed on the ground 110 in a horizontal state so that sewage can flow slowly into the large long cylindrical decompression vaporization chamber 56.

In the vacuum vaporizer 51, the sewage inlet 57 is opened at the front end wall 53 of the cylindrical casing 52, and the sewage return port 58 is opened below the side wall 55 of the cylindrical casing 52 near the rear end wall 54. In addition, the connection ports 59, 59, 59, 59, 59, 59 are opened at predetermined intervals in the direction of flowing the connection ports 59, 59, 59, 59, 59, 59 above the side wall 55 of the cylindrical casing 52, and the sewage inlet 57 is electromagnetic A sewage pipe 61 having a water supply valve 60 is connected to a sewage tank (not shown) of the factory, while the connection ports 59, 59, 59, 59, 59, 59 are respectively decompressed vaporization pumps 62, 62 with electric motors. , 62, 62, 62, 62 are connected to the separation device 12 by connection pipes 63, 63, 63, 63, 63, 63 and connected to the sewage tank and the separation device 12. Of course, it is desirable to use a reciprocating pump with an electric motor for the decompression vaporization pumps 62, 62, 62, 62, 62, 62 with an electric motor. Then, in this water treatment system 50, bacteria and viruses contained in the sewage are ruptured and killed by the pressure reducing effect of the reciprocating pump as in the case of the water treatment system 10 described above.
Further, since the number of the decompression vaporization pumps 62, 62, 62, 62, 62, 62 is large, they may be combined and replaced with one multi-cylinder reciprocating pump with an electric motor.

In addition, the vacuum vaporizer 51 is connected to the sewage inlet 57 side by a sewage return pipe 67 having a sewage return port 58 having an electromagnetic return valve 64 and a sewage return pump 65 with an electric motor. The structure is set back to the sewage inlet 57 side.
Then, the sewage slowly flows into the long cylindrical decompression vaporization chamber 56 and is completely vaporized, but when the sewage is not completely vaporized and a part of it remains, the part of the sewage is the rear end. It flows to the wall 54 side, then flows through the sewage return pipe 67 from the sewage return port 58 to the sewage reservoir 66 and accumulates there.
When a certain amount of the unsteamed sewage accumulates in the sewage reservoir 66, a water level sensor (not shown) operates to open the electromagnetic return valve 64, and at the same time, the sewage return pump 65 is operated. The sewage that has not been vaporized is returned to the sewage inlet 57 side by the sewage return pump 65 through the sewage return pipe 67. Then, when the sewage that has not been vaporized is returned to the sewage inlet 57 side and the water level of the sewage falls to a certain value in the sewage reservoir 66, the water level sensor is activated and the sewage return pump 65 is activated. At the same time, the electromagnetic return valve 64 is closed.

Next, the operation of the water treatment system 50 will be described. First, a start switch (not shown) is turned on. When the activation switch is turned on, a controller (not shown) works in the water treatment system 50, and the decompression vaporization device 51, the separation device 12, the separation collection device 13, and the centrifuge device are controlled by the controller. The
In the decompression vaporization apparatus 51, the decompression vaporization pumps 62, 62, 62, 62, 62, 62 with electric motors are operated, and the pressure in the decompression vaporization chamber 56 is lowered.
When the depressurization vaporization chamber 56 is depressurized and reaches a predetermined depressurization value, the electromagnetic water supply valve 60 is opened, and the sewage flows from the sewage tank to the sewage inlet 57 via the sewage pipe 61 and further flows into the sewage inlet 57. Then, it flows into the decompression vaporization chamber 56 and is vaporized while slowly flowing into the decompression vaporization chamber 56.
Then, the flow of water molecules vaporized in the vacuum vaporization chamber 56 is mixed with the metal ions, halogen ions, hydrogen ions, non-charged substances, organic compounds, and the like. The reduced pressure vaporizing pumps 62, 62, 62, 62, 62, 62 are sent to the separation device 12.
As described above, the water treatment system 50 uses the reduced pressure vaporization device 51, so that a large amount of sewage is continuously purified.
When the sewage is contaminated with radioactive substances, the water treatment system 50 similarly removes the radioactive substances from the contaminated water and purifies the contaminated water.
In addition, when the sewage is contaminated with bacteria or viruses, the water treatment system 50 ruptures and dies due to the decompression effect in the water treatment system 50. It makes it possible to purify contaminated water contaminated with viruses and viruses.

  Therefore, in this water treatment system 50, wastewater containing at least metal ions, halogen ions, hydrogen ions, non-charged substances, and organic compounds is vaporized while slowly flowing into a large long vacuum vaporization chamber 56. The vaporized water molecules are mixed with metal ions, halogen ions, hydrogen ions, non-charged substances, and organic compounds, and then a magnetic field is applied to the water molecules and the mixed substances are mixed. Since the separated mixed substances are collected by the electrode, the metal ions, halogen ions, hydrogen ions, non-charged substances, and organic compounds are efficiently consumed from the wastewater with less energy consumption. The sewage is collected in a separate manner, and the sewage is continuously and safely purified economically. Easily adapts to the scale of the runt, makes repairs easier and easier, and makes parts maintenance longer and easier and easier to maintain, reducing costs and making it more economical In addition, in the case of contaminated water containing radioactive material, it can be used safely and economically, the radioactive material is removed from the wastewater, and the wastewater can be purified, and bacteria and viruses In the case of contaminated water that is contaminated with, etc., bacteria and viruses are ruptured and killed by the decompression effect, so there is a sterilization and virucidal effect. As a result, various water including the sewage and contaminated water can be used. It is practically useful for purifying a large amount continuously.

FIG. 3 shows a water treatment system according to the present invention which is improved so that various kinds of dirty water can be continuously purified in large quantities and is used to purify a large amount of waste water discharged from a factory. Further, another specific example 70 of the present invention is shown, and this water treatment system 70 is obtained by replacing the reduced pressure vaporization device 51 of the water treatment system 50 with a multistage cascade reduced pressure vaporization device (multistage cascade water pressure reduction vaporization device) 71. It becomes.
The water treatment system 70 continuously applies multi-stage cascade vacuum vaporization, magnetic field fractionation, and electricity collection to the sewage, and from the sewage, metal ions, halogen ions, hydrogen ions, non-charged substances, and organic In order to remove compounds and the like, the multistage cascade vacuum vaporizer 71, the fractionator 12, the fraction collector 13 and the centrifuge are assembled in order, and the sewage discharged from the factory is purified.
In this water treatment system 70, the multistage cascade depressurization vaporizer 71 has a multistage cascade depressurization vaporization chamber 81, 82, 83, 84, 85, 86 connected in a small waterfall shape in a direction in which the large long cylindrical casing 72 flows. The pressure is reduced and reduced by a vacuum vaporization pump 103, 103, 103, 103, 103, 103 with an electric motor, and at least metal ions, halogen ions, hydrogen ions, non-charged substances, and organic The sewage containing compound is introduced, and it is slowly flushed and vaporized while sequentially flushing into a number of rooms partitioned by the waterfall, and the metal ions, halogen ions, hydrogen are vaporized into the vaporized water molecules. Ions, non-charged substances, and organic compounds are mixed, and the reduced pressure vaporization pump 10 is used. , Eggplant and serves to flow to the next sorting apparatus 12 in 103,103,103,103,103. Therefore, since the multistage cascade vacuum vaporization apparatus 71 is enlarged in this water treatment system 70, the wastewater can be purified continuously and efficiently in large quantities.

  The multistage cascade vacuum vaporization apparatus 71 is a large long cylindrical casing 72 whose both ends are closed by end walls 73 and 74, and is arranged at a predetermined interval in the direction of flowing into the cylindrical casing 72. A large number of partition walls 76, 77, 78, 79, 80 for partitioning the inside of the casing 72 into multistage cascade decompression vaporization chambers 81, 82, 83, 84, 85, 86, a sewage inlet 93 on the front end wall 73 and the partition walls thereof The flash weirs 87 are disposed in the decompression vaporization chambers 81, 82, 83, 84, 85, and 86, appropriately adjacent to each of the communication ports 96, 97, 98, 99, and 100 of 76, 77, 78, 79, and 80. , 88, 89, 90, 91, 92, and the like, and the ground casing 110 is placed in a horizontal state with its cylindrical casing 72 tilted forward and downward as appropriate. It is placed.

Further, the multistage cascade vacuum vaporizer 71 has connection ports 95, 95, 95, 95 on the upper side of the side wall 75 of the cylindrical casing 72 corresponding to the vacuum vaporization chambers 81, 82, 83, 84, 85, 86. , 95, 95 are opened, and a sewage return port 94 is opened under the side wall 75 of the cylindrical casing 72 near the rear end wall 74 in the decompression vaporization chamber 86, and the sewage tank and the A structure that enables connection to the sorting device 12 is employed.
More specifically, the multistage cascade vacuum vaporizer 71 has a sewage inlet 93 connected to a sewage tank of the factory by a sewage pipe 102 having an electromagnetic water supply valve 101, while its connection ports 95, 95, 95, 95, 95, 95 are fluid circuits connected to the separation device 12 by connection pipes 104, 104, 104, 104, 104, 104 having decompression vaporization pumps 103, 103, 103, 103, 103, 103 with electric motors Then, it is connected to the sewage tank and the separation device 12. Of course, it is desirable to use a reciprocating pump with an electric motor for the decompression vaporization pump 103, 103, 103, 103, 103, 103 with an electric motor. Then, in this water treatment system 70, bacteria and viruses contained in the sewage are ruptured and killed by the pressure reduction effect of the reciprocating pump, as in the water treatment systems 10 and 50 described above.
Further, since the decompression vaporization pumps 103, 103, 103, 103, 103, 103 are numerous, they may be replaced by being combined into one multi-cylinder reciprocating pump with an electric motor.

Further, in this multistage cascade pressure reduction vaporizer 71, the wastewater return port 94 is connected to the wastewater inlet 93 side by a wastewater return pipe 108 having an electromagnetic return valve 105 and an electric motor-equipped wastewater return pump 106. Is taken back to the sewage inlet 93 side.
The sewage then slowly and slowly flows into the multistage cascade decompression vaporization chambers 81, 82, 83, 84, 85, 86, and the flash weirs in the multistage cascade decompression vaporization chambers 81, 82, 83, 84, 85, 86, respectively. 87, 88, 89, 90, 91, and 92, when flushed, the gas is flushed and promoted to vaporize while flowing from the first-stage decompression vaporization chamber 81 to the final-stage decompression vaporization chamber 86. Is not vaporized and a part of the sewage remains in the final-stage decompression vaporization chamber 86, the part of the sewage flows toward the rear end wall 71, and passes through the sewage return pipe and from the sewage return port 94. It flows into the sewage reservoir 107 and accumulates there.
When a certain amount of the sewage that has not been vaporized accumulates in the sewage reservoir 107, a water level sensor (not shown) operates to open the electromagnetic return valve 105, and at the same time, the sewage return pump 105 is operated. Then, the sewage that has not been vaporized is returned to the sewage inlet 93 side through the sewage return pipe 108, that is, from the final-stage decompression vaporization chamber 86 to the first-stage decompression vaporization chamber 81. Then, when the sewage that has not been vaporized is returned to the sewage inlet 93 side and the water level of the sewage falls to a certain value in the sewage reservoir 107, the water level sensor is activated and the sewage return pump 106 is activated. At the same time, the electromagnetic return valve 105 is closed.

Next, the operation of this water treatment system 70 will be described. First, a start switch (not shown) is turned on. When the activation switch is turned on, a controller (not shown) works in the water treatment system 70, and the multistage cascade vacuum vaporizer 71, the fractionator 12, the fraction collector 13 and the centrifuge are operated by the controller. Be controlled.
In the multistage cascade depressurization vaporizer 71, the decompression vaporization pumps 103, 103, 103, 103, 103, 103 with electric motors are operated, and the multistage cascade depressurization vaporization chambers 81, 82, 83, 84, 85, 86 are operated. When the pressure is reduced and the decompression vaporization chamber 81, 82, 83, 84, 85, 86 reaches a predetermined decompression value, the electromagnetic water supply valve 101 is opened, and sewage passes through the sewage pipe 102 and the sewage tank. From the sewage inlet 73 and flows into the first-stage decompression vaporization chamber 81 from the sewage inlet 73.
The sewage that has flowed in is vaporized while slowly flowing into the first-stage decompression vaporization chamber 81, and a part of the sewage that has flowed in is flushed and vaporized when the flash dam 87 is crossed. The sewage that has not been flowed and vaporized slowly while being sequentially flushed in the decompression vaporization chambers 82, 83, 84, 85, 86. The metal ions, halogen ions, hydrogen ions, non-charged substances, and organic compounds are mixed in the flow of water molecules vaporized in the vacuum vaporization chambers 82, 83, 84, 85, 86, and The gas flow of water molecules is sent to the separation device 12 by the decompression vaporization pump 103, 103, 103, 103, 103, 103 with the electric motor.
As such, the water treatment system 70 uses the multistage cascade vacuum vaporization apparatus 71, so that the vaporization of sewage is promoted, and the sewage is continuously and efficiently purified in large quantities.
When the sewage is contaminated with radioactive substances, the water treatment system 70 similarly removes the radioactive substances from the contaminated water and purifies the contaminated water.
Further, when the sewage is contaminated with bacteria or viruses, the water treatment system 70 ruptures and dies due to the decompression effect in the water treatment system 70. It also makes it possible to purify contaminated water that is contaminated with viruses and viruses.

  In this multistage cascade decompression vaporization apparatus 71, the pressure of the multistage cascade decompression vaporization chamber 81, 82, 83, 84, 85, 86 is set to a predetermined decompression value, but the multistage cascade decompression vaporization chamber 81, 82, 83 , 84, 85, 86 may be set so that the reduced pressure value is gradually increased from the first-stage decompression vaporization chamber 81 to the final-stage decompression vaporization chamber 86, for example.

  Therefore, in this water treatment system 70, wastewater containing at least metal ions, halogen ions, hydrogen ions, non-charged substances, organic compounds, and the like is treated as a large-scale multistage cascade decompression vaporization chamber (multistage cascade waterfall decompression vaporization chamber) 81. , 82, 83, 84, 85, and 86, the gas is slowly flushed and vaporized in sequence, and the metal ions, halogen ions, hydrogen ions, non-charged substance, and organic matter in the flow of the vaporized water molecules A compound is mixed, then a magnetic field is applied to the water flow of the water molecules to separate the mixed substances, and then the separated mixed substances are collected by the electrode, so that the metal ions, halogen ions, Efficient separation from wastewater with less energy consumption, such as hydrogen ions, non-charged substances, and organic compounds The sewage is collected continuously, efficiently and in large quantities, safely and economically purified, easily adapted to the scale of the factory or plant as a sewage treatment facility, and easy to repair and repair, and In addition to the function being maintained by replacing parts, the maintenance is simple and easy, the cost to be reduced is further economical, and in the case of contaminated water containing radioactive materials, it is equally safe and economical. The radioactive material can be removed from the contaminated water, and the contaminated water can be purified. In the case of contaminated water contaminated with bacteria and viruses, the bacteria and viruses Because it is ruptured and killed by the decompression effect, it has a sterilizing and virucidal effect. As a result, various waters including the sewage and contaminated water are continuously and efficiently purified in large quantities and safely. It is useful is in practical use.

4 and 5 show another reduced pressure vaporization type reciprocating pump 120 that is utilized in the water treatment system 10 described above.
In this reduced pressure vaporization type reciprocating pump 120, a large number of cylinder bores 133, 133, 133, 133 are communicated with each other in the radial direction perpendicular to the body central axis, opened to the body outer peripheral surface 130, and radially drilled. The suction port 134 communicates with the multiple cylinder bores 133, 133, 133, 133 on the body center axis, and the discharge port 135 is disposed on the body center axis. A cylinder body 121 communicated with a number of cylinder bores 133, 133, 133, 133 and released to the other body end surface 132, respectively, and the number of cylinder bores 133, 133, 133 of the cylinder body 121; A large number of pistons 122, 1 fitted in a reciprocating manner corresponding to 133 2, 122, 122, a pump casing 123 covering the cylinder body 121 with an appropriate piston protruding space 138 around the outer peripheral surface 130 of the body, and a large number of pistons 122, 122, 122, 122, respectively. A fixed electromagnetic coil 124 correspondingly fixedly mounted on the pump casing 123 and a movable electromagnetic coil 126 fixedly mounted on the piston skirt 137 of each of the plurality of pistons 122, 122, 122, 122; The electromagnetic water supply valve 126 disposed on the suction port 134 side and communicated with the suction port 134 of the cylinder body 121 and the discharge port 135 of the cylinder body 121 and communicated with the discharge port Discharge check valve 12 arranged on the side of the inlet 135 It assembled including the door. Of course, the water treatment system 10 has a start switch (not shown) turned on, and when the start switch is turned on, the controller works and the operation is controlled by the controller, so the discharge check valve 127 is electromagnetic. It may be replaced with a discharge valve.

Next, the operation in which the reduced pressure vaporization type reciprocating pump 120 vaporizes the sewage under reduced pressure during the operation of the water treatment system 10 and discharges the vaporized substance to the sorting device 12 will be described.
The water treatment system 10 first turns on the start switch. When the activation switch is turned on, in this water treatment system 10, a controller (not shown) works, and the decompression vaporization type reciprocating pump 120, the separation device 12, the separation collection device 13, and the centrifugal separator are controlled by the controller. Is done.

In this reduced pressure vaporization type reciprocating pump 120, first, the fixed side and movable side electromagnetic coils 124, 125 are energized in the same direction, and the pistons 122, 122, 122, 122 slide from the top dead center to the bottom dead center. Start to move. At that time, the electromagnetic water supply valve 126 is opened and closed by being energized and controlled in a short period of time at the beginning of the decompression and vaporization process, and a plurality of cylinder bores 133, 133, 133 that communicate an appropriate amount of sewage accordingly. Inhale to 133.
As the multiple pistons 122, 122, 122, 122 are slid further into the multiple cylinder bores 133, 133, 133, 133 in communication with each other, they are depressurized instantaneously and rapidly. The sucked sewage is instantly and strongly vaporized in the cylinder bores 133, 133, 133, 133.

Subsequently, when the multiple pistons 122, 122, 122, 122 reach bottom dead center, the stationary and movable electromagnetic coils 124, 125 are energized in a reverse direction, and the multiple pistons 122, 122, 122, 122 and 122 begin to slide from the bottom dead center to the top dead center correspondingly in the multiple cylinder bores 133, 133, 133, and 133 that are energized to each other. Gases of water molecules, oils mixed in the gas, metal ions, halogen ions, hydrogen ions, and non-charged substances are discharged from the discharge port 135 by a large number of pistons 122, 122, 122, 122. Then, the discharge check valve 127 is pushed open, and then flows through the divergent duct 32 to the intake opening 30 of the separation device 12 and correspondingly. It flows into the interior of the device 12. Of course, the oil is charged to positive and negative charges in the course of the discharge step from the reduced pressure vaporization step of the reduced pressure vaporization type reciprocating pump 120.
During the operation of the water treatment system 10, the reduced pressure vaporization type reciprocating pump 120 repeats the operation of causing the sewage to vaporize under reduced pressure and flowing it to the separation device 12.

  Therefore, the reduced pressure vaporization type reciprocating pump 120 has a plurality of cylinder bores 133, 133, 133, 133 communicated with the cylinder body 121 in a radial manner, and the plurality of pistons 122, 122. , 122, 122 are reciprocally fitted to the multiple cylinder bores 133, 133, 133, 133 so that the multiple fixed and movable electromagnetic coils 124, 125 can Since the bores 133, 133, 133, and 133 are reciprocated simultaneously, the reduced-pressure vaporization is more instantaneous and more rapid and powerful than the above-described reduced-pressure vaporization type reciprocating pump 11, and the sewage is effective. In addition to being able to handle a large amount efficiently and efficiently, the rotating mechanism is omitted, the structure is simplified, and the weight is reduced.

6 and 7 show still another multistage vacuum vaporization type reciprocating pump 140 which is utilized in the water treatment system 10 described above.
In this multi-stage vacuum evaporation type reciprocating pump 140, a large number of cylinder bores (cylinder chambers) 163, 164, 165, 166, 167 are respectively provided from the first stage to the last stage (fifth stage) at predetermined intervals in the direction of the body center axis. And is communicated with each other in the radial direction perpendicular to the body center axis and between the first stage and the last stage in the direction of the body center axis, and is open to the outer peripheral surface 160 of the body. The suction port 168 communicates with a number of cylinder bores (cylinder chambers) 163 at the first stage, and the discharge port 169 has a number of discharge ports 169 at the end of the first stage. Cylinder body 141 communicated with the cylinder bore (cylinder chamber) 167 and released to the end surface 162 of the last stage side, and its series A plurality of pistons 142, 143, 144, 145 which are reciprocally fitted to the cylinder bores 163, 164, 165, 166, 167 respectively from the first stage to the last stage of the dar body 141; 146, a pump casing 147 covering the cylinder body 141 with an appropriate piston projecting space 172 around the outer peripheral surface 160 of the body, and a number of pistons 142, 143, 144 in the first stage to the last stage, respectively. , 145, 146 and fixed-side electromagnetic coils 148, 149, 150, 151, 152 that are fixedly assembled to the pump casing 147, and the pistons 142, 143 in the first stage to the last stage, respectively. 144, 145, 146 The movable side electromagnetic coils 153, 154, 155, 156, and 157 fixedly assembled to the piston skirts 171, 171, 171, 171, and 171 and the suction port 168 of the cylinder body 141 can be communicated therewith. An electromagnetic water supply valve 158 disposed on the suction port 168 side, and a discharge check valve 159 disposed on the discharge port 169 side that can communicate with the discharge port 169 of the cylinder body 141. Assembled in. Of course, the water treatment system 10 has a start switch (not shown) turned on, and when the start switch is turned on, the controller works and the operation is controlled by the controller, so the discharge check valve 159 is electromagnetic It may be replaced with a discharge valve.

Next, the operation of the multistage reduced pressure vaporization type reciprocating pump 140 for evaporating the sewage under reduced pressure during the operation of the water treatment system 10, and discharging the vaporized substance to send it to the separation device 12 will be described. .
The water treatment system 10 first turns on the start switch. When the activation switch is turned on, in this water treatment system 10, a controller works, and the multistage vacuum vaporization type reciprocating pump 140, the separation device 12, the separation collection device 13, and the centrifugal separator are controlled by the controller.

  In this multi-stage vacuum evaporation type reciprocating pump 140, first, in the first stage, the fixed and movable side electromagnetic coils 148, 148, 148, 148 and 153, 153, 153, 153 are energized in the same direction. The pistons 142, 142, 142, 142 begin to slide from the top dead center to the bottom dead center. At that time, the electromagnetic water supply valve 158 is opened and closed by being energized and controlled in a short time from the beginning of the decompression vaporization step to the middle, and a plurality of cylinder bores 163 communicated with a predetermined amount of waste water. 163, 163, and 163 are sucked. Of course, the amount of sewage sucked into the large number of cylinder bores 163, 163, 163, 163 in this reduced pressure vaporization step is larger than that of the aforementioned reduced pressure vaporization reciprocating pump 120. For this purpose, the electromagnetic water supply valve 158 is controlled to be energized for a longer time by the controller than the electromagnetic water supply valve 126 described above, and is set to be opened and closed longer.

When the electromagnetic water supply valve 158 is closed by being energized and controlled by the controller, the fixed and movable electromagnetic coils 149 and 150 corresponding to each other from the second stage to the final stage (five stages) are used. , 151, 152 and 154, 155, 156, 157 are energized in the same direction, and the plurality of pistons 143, 144, 145, 146 from the second stage to the last stage are dead from the first stage. The time is adjusted in accordance with the sliding to the point, and the sliding is made from the top dead center to the bottom dead center at a speed higher than that of the plurality of first-stage pistons 122.
As such, the multiple pistons 143, 144, 145, 145 from the second stage to the final stage are slid at a faster speed than the first plurality of pistons 142, and accordingly, from the first stage to the final stage. Its multiple cylinder bores 163, 164, 165, 166, 167, i.e., the pressure in the cylinder chamber is depressurized more instantaneously, more drastically and more strongly, and the sucked sewage Vaporization is more effective and more efficient in the cylinder chambers 163, 164, 165, 166, 167.

In this way, the pistons 142, 143, 144, 145, and 146 in the final stage are simultaneously slid to the bottom dead center from the first stage. The stationary and movable electromagnetic coils 148, 149, 150, 151, 152 and 153, 154, 155, 156, 157 in the final stage are rapidly energized in the opposite direction, and the multiple pistons 142, 143, 144, 145 and 146 are slid from the bottom dead center to the top dead center correspondingly in a number of cylinder bores 163, 164, 165, 166 and 167 communicated with each other. Gases of water molecules, oils mixed in the gas, metal ions, halogen ions, hydrogen ions, and non-charged substances, etc. 2,143,144,145,146 that is discharged from the discharge and the mouth 169, the check valve 159 and the discharge pushes open, and flows into the inside of the separation device 12 through the diverging duct 32. Of course, the oil is charged to positive and negative charges during the process from the reduced pressure vaporization step of the reduced pressure vaporization type reciprocating pump 140 to the discharge step. Then, during the operation of the water treatment system 10, the multistage reduced pressure vaporization type reciprocating pump 140 repeats the operation of vaporizing the sewage under reduced pressure and flowing it to the separation device 12.
In the multi-stage reduced pressure vaporization type reciprocating pump 140, in the reduced pressure vaporization process, the pistons 143, 144, 145, and 146 from the second stage to the final stage are slid with a slight time difference for each stage. In the discharging process, the pistons 142, 143, 144, 145, and 146 from the initial stage to the final stage may be slid with a slight time difference for each stage.

  Therefore, this multi-stage reduced pressure vaporization type reciprocating pump 140 has a more instantaneous pressure in the cylinder chambers 163, 164, 165, 166, and 167 in the reduced pressure vaporization process than the reduced pressure vaporization type reciprocating pumps 11 and 120 described above. Abrupt, more powerful and rapid pressure reduction, sewage is more effectively and efficiently vaporized in the cylinder chambers 163, 164, 165, 166, 167, so that a large amount of sewage can be treated. In addition, the rotating mechanism is omitted, the structure is simplified, and the weight can be reduced.

  As will be apparent from the specific embodiments of the present invention described above with reference to the drawings, for those of ordinary skill in the art to which the present invention pertains, It is easily embodied in another embodiment that derives from the nature and the nature of the invention and is objectively recognized as having them inherent. Of course, the contents of the present invention correspond to the problem of the invention and are essential for the establishment of the invention.

  As can be understood from the above, the water treatment system of the present invention sucks dirty water containing at least metal ions, halogen ions, hydrogen ions, non-charged substances, and organic compounds, and vaporizes them by decompression. And a decompression vaporization type reciprocating pump to be discharged and flown next, and an intake opening at one end and a wide air supply opening at the other end, respectively, and flow into the inside from the decompression vaporization type reciprocating pump through the intake opening A magnetic field is applied to the ions in the gas flow, positive and negative charge organic compounds, etc. in the separation direction that gives force according to the left-hand rule regarding the Lorentz force, and the gas flow is divided into the main straight flow, anode side branch flow, and cathode side branch flow A separation device that branches to the next through the air supply opening, and has a wide intake opening at one end, and the inside is connected to the intake opening, and the straight passage chamber and the anode Partitioning into a chamber and a built-in cathode chamber, flowing the main straight flow into the straight passage chamber, the anode branch flow into the anode built-in chamber, the cathode branch flow into the cathode built-in chamber, and In the straight passage chamber, the main straight flow flows directly to the outlet thereof, in the anode built-in chamber, the halogen ions, negatively charged organic compounds, etc. are attached to the anode, and in the cathode built-in chamber, And a separate collection device for adhering the metal ions, positively charged organic compounds, etc. to the cathode. In the water treatment system of the present invention, the metal ions, halogen ions, Low energy consumption due to hydrogen ions, non-charged substances, and organic compounds The dirty water is separated and collected efficiently, the dirty water is purified safely and economically, the water treatment facility is embodied in a simple structure, the treatment capacity and The number of units can be increased or decreased to easily adapt to the scale of the factory or plant, inspection and repair are easy and easy, maintenance of parts can be maintained for a long time by replacing parts, and maintenance costs are simple and easy. In the purification process of contaminated water, bacteria and viruses are killed and removed in the process of vaporization under reduced pressure, and radioactive substances are removed and contaminated in the same way. It can be used safely and economically for the purification of dirty water, and as a result, it is practically useful for the purification of dirty water.

DESCRIPTION OF SYMBOLS 10 Water treatment system 11 Pressure reduction vaporization reciprocating pump 12 Separation device 13 Separation collection device 14 Inverted cylinder 15 Inverted piston 16 Connecting rod 17 Cylinder side wall 18 Cylinder head 19 Cylinder bore 20 Cylinder chamber 21 Water supply port 22 Exhaust port 23 Electromagnetic water supply Valve 24 Check valve 25 Pipe 26 Piston head 27 Box-shaped cylinder 28 Left side wall 29 Right side wall 30 Intake opening 31 Wide air supply opening 32 End wide duct 33 Wide intake opening 34 Partition wall 35 Partition wall 36 Partition wall 37 Partition wall 38 Straight passage chamber 39 Built-in anode chamber 40 Built-in cathode chamber 41 Exit / air supply opening 42 Outlet / discharge port 43 Outlet / discharge port 44 Straight passage chamber return 45 Straight passage chamber return 46 Anode plate 47 Yin Plate 48 Battery 49 Duct 50 Water treatment system 51 Depressurization vaporizer 52 Large long cylindrical casing 56 Large long tubular depressurization vaporization chamber 62 Decompression vaporization pump with electric motor 70 Water treatment system 71 Multistage cascade depressurization vaporizer 72 Large long Cylindrical casing 76 Partition wall 77 Partition wall 78 Partition wall 79 Partition wall 80 Partition wall 81 Multistage cascade decompression vaporization chamber 82 Multistage cascade decompression vaporization chamber 83 Multistage cascade decompression vaporization chamber 84 Multistage cascade decompression vaporization chamber 85 Multistage cascade decompression vaporization chamber 86 Multistage Cascade decompression vaporization chamber 87 Flash weir 88 Flash weir 89 Flash weir 90 Flash weir 91 Flash weir 92 Flash weir 95 Connection port 96 Communication port 97 Communication port 98 Communication port 99 Communication port 100 Communication port 103 Communication port 1 Decompression vaporization type reciprocating pump 121 Cylinder body 122 Piston 123 Pump casing 124 Fixed side electromagnetic coil 125 Movable side electromagnetic coil 126 Electromagnetic water supply valve 127 Discharge check valve 133 Cylinder bore / cylinder chamber 136 Piston head 137 Piston head Skirt 138 Piston protrusion space 139 Reinforcement plate / Reinforcement rib 140 Multistage decompression vaporization type reciprocating pump 141 Cylinder body 142 Piston 143 Piston 144 Piston 145 Piston 146 Piston 147 Pump casing 148 Fixed side electromagnetic coil 149 Fixed side electromagnetic coil 150 Fixed side electromagnetic Coil 151 Fixed side electromagnetic coil 152 Fixed side electromagnetic coil 153 Movable side electromagnetic coil 154 Movable side electromagnetic coil 155 Movable side electromagnetic coil 156 Movable side electromagnetic coil 15 7 Movable side electromagnetic coil 158 Electromagnetic water supply valve 159 Discharge check valve 163 Cylinder bore / cylinder chamber 164 Cylinder bore / cylinder chamber 165 Cylinder bore / cylinder chamber 166 Cylinder bore / cylinder chamber 167 Cylinder bore / cylinder chamber 167 170 Piston head 171 Piston skirt 172 Piston protrusion space 173 Reinforcement plate / Reinforcement rib 174 Mounting base

Claims (5)

  A vacuum vaporization type reciprocating pump that sucks dirty water containing at least metal ions, halogen ions, hydrogen ions, non-charged substances, organic compounds, and the like, vaporizes them by vacuum, discharges them, and then flows them; Lorenz has an intake opening at one end and a wide air supply opening at the other end for the ions, positive and negative charge organic compounds, etc. in the gas flow flowing through the intake opening from the vacuum vaporization type reciprocating pump. A separation device that applies a magnetic field in a separation direction that applies force according to the rule of the left hand with respect to force, branches the gas flow into a main straight flow, an anode side branch flow, and a cathode side branch flow, and then flows from the air supply opening; It has a wide intake opening at one end, and the inside is divided into a straight passage chamber, an anode built-in chamber, and a cathode built-in chamber through the intake opening. The main straight flow is passed through the straight passage chamber, the anode side branch flow through the anode internal chamber, the cathode side branch flow through the cathode internal chamber, and the main straight flow through the straight passage chamber. In the chamber with a built-in anode, the halogen ion, a negatively charged organic compound, etc. are attached to the anode, and in the chamber with a built-in cathode, the metal ion, a positively charged organic compound, etc. A water treatment system comprising a separate collection device for adhering.   A long vacuum vaporization chamber is depressurized and reduced in pressure by a vacuum vaporization pump, and leads to dirty water containing at least metal ions, halogen ions, hydrogen ions, uncharged substances, and organic compounds, etc. The gas is vaporized while slowly flowing into the room, and the vaporized water molecule gas is mixed with its metal ions, halogen ions, hydrogen ions, non-charged substances, and organic compounds. A vacuum vaporizer for flowing into the gas, an intake opening at one end, and a wide air supply opening at the other end, and the ions and positive and negative charge organic compounds in the gas stream flowing into the interior from the vacuum vaporizer through the intake opening For example, a magnetic field is applied in the direction of separation that gives the force according to the left-hand rule for Lorentz force, and the gas flow is main straight flow, anode branch flow, and A separation device for branching into the pole-side branch flow and flowing from the air supply opening to the next, and a wide intake opening at one end, and the inside is connected to the intake opening to the straight passage chamber, the anode internal chamber, and the cathode internal chamber Partitioning and dividing, flowing the main straight flow into the straight passage chamber, the anode branch flow into the anode built-in chamber, the cathode side branch flow into the cathode built-in chamber, and in the straight passage chamber, The main straight flow is allowed to flow directly to the outlet thereof, and in the anode internal chamber, the halogen ions, negatively charged organic compounds, etc. are attached to the anode, and in the cathode internal chamber, the metal ions are applied to the cathode, A water treatment system including a separate collection device for adhering positively charged organic compounds and the like. The multistage cascade vacuum vaporization chamber is partitioned into a small waterfall in the direction of flowing into the long cylindrical casing, the pressure is reduced by the vacuum vaporization pump, and at least metal ions, halogen ions, hydrogen ions, charges Dirty water containing substances without organic substances and organic compounds etc. is guided, and it is gradually flushed and vaporized while sequentially flushing into a number of chambers partitioned by the waterfall, and the vaporized water molecule gas is A multistage cascade vacuum vaporizer that mixes metal ions, halogen ions, hydrogen ions, non-charged substances, and organic compounds, etc., and then flows them through the vacuum vaporizer pump, and an intake opening at one end and an intake opening at the other Each has a wide air supply opening and passes through the intake opening through the multistage cascade vacuum vaporizer to the interior of the gas flow. A magnetic field is applied in the direction of separation that gives force to the ions and positive and negative charge organic compounds according to the left-hand rule regarding the Lorentz force, and the gas flow is branched into a main straight flow, an anode side branch flow, and a cathode side branch flow. A separation device that flows next from the air supply opening and a wide intake opening at one end, and the inside is divided into a straight passage chamber, an anode built-in chamber, and a cathode built-in chamber through the intake opening, and the straight passage chamber is divided. And the anode side branch flow into the anode built-in chamber and the cathode side branch flow into the cathode built-in chamber, respectively. In the chamber with a built-in anode, the halogen ions, negatively charged organic compounds, etc. are attached to the anode, and then In the cathode internal organs chamber, a water treatment system that includes the metal ions to the cathode, and a separate collection device for attaching and positively charged organic compound.   A plurality of cylinder bores communicate with each other in the radial direction perpendicular to the body center axis, open to the outer peripheral surface of the body and drilled, and a suction port is connected to the plurality of cylinder bores on the body center axis A cylinder body that is communicated with one of the body end faces, and a discharge port is communicated with the cylinder bores on the center axis of the body and opened to the other body end face, and the cylinder body A plurality of pistons that can be slidably fitted to a plurality of cylinder bores, a pump casing that covers the cylinder body with an appropriate piston protruding space around the outer peripheral surface of the piston, Fixed-side electromagnetic coil that is fixedly assembled to the pump casing corresponding to each piston , A movable electromagnetic coil fixedly assembled to the skirts of each of the plurality of pistons, an electromagnetic water supply valve arranged on the suction port side of the cylinder body so as to communicate with the suction port, and the cylinder A reduced-pressure vaporization type reciprocating pump including a discharge check valve or an electromagnetic discharge valve which is communicated with the discharge port of the body and disposed on the discharge port side.   A plurality of cylinder bores are arranged at predetermined intervals in the direction of the body center axis at respective positions from the first stage to the last stage, and also in the radial direction perpendicular to the body center axis and in the direction of the body center axis The first stage to the last stage communicate with each other, open to the outer peripheral surface of the body and drilled, and the suction port communicates with the first stage cylinder bores to the first stage body end face. A cylinder body that is connected to a plurality of cylinder bores in the final stage and is opened to the end surface of the final stage side body, and a plurality of the cylinder body from the first stage to the final stage. A plurality of pistons that can be slidably reciprocated corresponding to the cylinder and bore, and an appropriate piston protruding space around the outer peripheral surface of the body. A pump casing that covers the cylinder body, a fixed electromagnetic coil that is fixedly assembled to the pump casing corresponding to each of the plurality of pistons from the first stage to the final stage, and from the first stage to the final stage. A movable side electromagnetic coil fixedly assembled to each skirt of each of the plurality of pistons in each stage, an electromagnetic water supply valve arranged on the side of the suction port so as to communicate with the suction port of the cylinder body, and A multistage depressurization vaporization type reciprocating pump including a discharge check valve or an electromagnetic discharge valve which is arranged to be connected to the discharge port of the cylinder body and arranged on the discharge port side.

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