WO1997017297A1 - An apparatus for cleaning water - Google Patents

An apparatus for cleaning water Download PDF

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Publication number
WO1997017297A1
WO1997017297A1 PCT/FI1996/000591 FI9600591W WO9717297A1 WO 1997017297 A1 WO1997017297 A1 WO 1997017297A1 FI 9600591 W FI9600591 W FI 9600591W WO 9717297 A1 WO9717297 A1 WO 9717297A1
Authority
WO
WIPO (PCT)
Prior art keywords
water
chamber
electrodes
purified
reaction chamber
Prior art date
Application number
PCT/FI1996/000591
Other languages
French (fr)
Inventor
Juhani Ilves
Original Assignee
Juhani Ilves
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Juhani Ilves filed Critical Juhani Ilves
Priority to AU74978/96A priority Critical patent/AU7497896A/en
Publication of WO1997017297A1 publication Critical patent/WO1997017297A1/en
Priority to FI972842A priority patent/FI972842A/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/283Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/34Treatment of water, waste water, or sewage with mechanical oscillations
    • C02F1/36Treatment of water, waste water, or sewage with mechanical oscillations ultrasonic vibrations
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/38Treatment of water, waste water, or sewage by centrifugal separation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4672Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/78Treatment of water, waste water, or sewage by oxidation with ozone
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46133Electrodes characterised by the material
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/08Seawater, e.g. for desalination
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/4611Fluid flow
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/04Disinfection
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis

Definitions

  • the present invention relates to an apparatus for electrical purification of water as defined in the preamble of claim 1. Moreover, the invention relates to a procedure for electrical purification of water.
  • Pa ⁇ tent specification US 5 227 052 presents a water puri ⁇ fication apparatus based on an electrochemical reacti- on, comprising a reaction chamber with a partition di ⁇ viding the reaction chamber into two compartments. In each compartment of the reaction chamber there is one plate-shaped electrode, in which the water purificati ⁇ on reaction takes place.
  • a reaction producing hydrogen, ozone and pure water ta ⁇ kes place at the positive plate electrode, OH " ions are separated, producing water and oxygen and then ozone, while on the negative electrode H 3 0 + ions are separated, producing water and hydrogen.
  • the partition prevents the gas bubbles formed in the reaction from combining, and the hydrogen produced can be passed out of the reaction chamber.
  • the water inlet is in the bottom wall of the reaction chamber and the water is passed via it into both chambers simultaneously.
  • the water can flow from one chamber to the other under the partition and through holes provided in the partition.
  • the outlet for the purified water is placed in a side wall of the chamber on the same side with the inlet, and the gas outlet is in the top wall of the reaction chamber.
  • a problem with this apparatus is that the wa ⁇ ter cannot flow freely in the reaction chamber, with the result that dirt is heavily accumulated on the electrodes, requiring cleansing of the apparatus at short intervals, thus reducing its purification effect and increasing down time.
  • the object of the invention is to eliminate the drawbacks mentioned above.
  • a specific object of the invention is to pre ⁇ sent an apparatus that does not require much clean- sing.
  • Another object of the invention is to present a small-sized apparatus that has a good purification effect.
  • a further object of the invention is to pre- sent an apparatus that produces water having a low de ⁇ gree of hardness.
  • a further object of the invention is to pre ⁇ sent an apparatus that allows water purification wit ⁇ hout chemicals, using a purification reaction that ta- kes place at the molecule level and leaves no detri ⁇ mental residue in the water. Therefore, no smells or tastes detrimental to water quality are developed in the purified water.
  • the apparatus of the invention comprises a reaction chamber having side walls, a bottom wall, a top wall and a partition wall which divides the reac ⁇ tion chamber into a first chamber and a second cham- ber.
  • Each one of the two chambers is provided with a mainly vertical plate electrode, and the partition wall and the plate electrodes are disposed at a dis ⁇ tance from the bottom wall.
  • the apparatus comprises an inlet for the water to be purified, an outlet for the purified water, a power source and a gas outlet. The water inlet is placed in a wall of the first chamber, so that the water to be purified can flow freely from the first chamber into the second chamber, washing the electrodes and the reaction cha - ber.
  • the inlet for the water to be purified may be lo ⁇ cated in the top, bottom or side wall of the first chamber of the reaction chamber, and, correspondingly, the outlet for the purified water may be located in the top, bottom or side wall of the second chamber, preferably in the opposite wall, so that the water to be purified will wash the entire reaction chamber as fully as possible.
  • the gas outlet is placed in a dif ⁇ ferent chamber than the outlet for purified water to ensure that the gases produced in the electrochemical reaction will not be discharged via the outlet for pu ⁇ rified water but can be recovered and utilized if de- sired.
  • the construction of the apparatus of the in- vention makes it possible to achieve a good purifica ⁇ tion effect in relation to the size of the apparatus. As the apparatus accumulates less dirt than prior-art devices, no prolonged down time is incurred and the operating costs of the apparatus are low. The inventi- on also allows long-time continuous operation of the apparatus.
  • the apparatus of the invention is economic and easy to maintain.
  • electrochemical purification occurs via a prior-art process. Electric power is supplied to the electrodes in the reaction chamber and the resulting electroche ⁇ mical reaction is utilized, discharging the ionic charges of the impurities; at the same time, the reac ⁇ tion produces ozone, hydrogen and even ultraviolet ra ⁇ diation.
  • This reaction is so effective that it has a substantially more effective ability to kill bacteria, viruses and microbes than do most chemical purifying agents, such as chlorine compounds, e.g. chlorine.
  • the electrochemical reaction covers a consi ⁇ derably wider range than chemical purifying agents, which do not necessarily have any effect on all bacte ⁇ ria, viruses and microbes.
  • the ozone produced in the reaction dissolves quickly and the purified water con ⁇ tains no ozone.
  • the inlet opening for the water to be purified is of a rectangu ⁇ lar shape and is placed in a side wall of the first chamber of the reaction chamber, and the water outlet opening is located in that side wall of the second chamber of the reaction chamber which lies opposite to the inlet, so the water can circulate freely from the first chamber into the second chamber and the electrochemical purifying reaction occurs as effecti ⁇ vely as possible on the surface of all electrodes.
  • the chambers in the reaction chamber are provided with several plate electrodes, preferably at least two plate electrodes in each chamber.
  • the electrodes may be placed in a mainly parallel arrangement in each chamber.
  • the plate electrodes can be mounted at right angles relative to the walls of the apparatus, preferably at a sharp angle relative to the walls of the apparatus, so the number of electrodes and the surface area on which the electrochemical purification reaction takes place are maximized in relation to the size of the apparatus and the water can circulate effectively in the reaction chamber, washing the electrodes and the reaction cham ⁇ ber.
  • the plate electrodes may be placed parallel to each other at a suitable angle relative to the reaction chamber wall, e.g.
  • the electrodes may be of a plate ⁇ like shape or they may be composed of rod-shaped ele- ments or the like.
  • the electrodes are of a rod-like shape, placed in rows, preferably parallel rows, the rows being arran- ged at an angle to the walls of the reaction chamber, preferably at a sharp angle to the walls of the reac ⁇ tion chamber.
  • the electrodes are made of electrically con- ductive material, preferably e.g. zinc, copper, car ⁇ bon, silver, graphite, titan, or the like.
  • all the electrodes are made of the same mate ⁇ rial. It is also possible for the apparatus of the in- vention to have electrodes made of two or more diffe ⁇ rent materials; in this case, the purification effect can be adjusted by considering the impurities, the de ⁇ sired purification effect and/or the desired degree of purification.
  • the electrodes may be attached to the top wall of the apparatus, e.g. to a detachable cover part, in which case they can be lifted up together with the cover for cleansing if required. This allows easier and faster cleansing of the apparatus.
  • the bottom wall of the ap ⁇ paratus consists of an electrically conductive bottom plate, which allows a homogeneous electric field to be set up over the whole liquid flow through the appara ⁇ tus, so that no bypass flow occurs. This enhances the effect of the electrochemical purification.
  • the bottom plate may be made of metal, preferably copper, stain ⁇ less steel or the like.
  • the apparatus further com ⁇ prises a filter for further purification of the water.
  • the apparatus may be provided e.g. with a reverse os ⁇ mosis filter, in which case detrimental foreign matter of even the smallest molecular size can be removed from the water.
  • the diffusion shell of the reverse os ⁇ mosis filter can be so selected that it will only pass substances of a given molecular size through it.
  • the apparatus may comprise an active car ⁇ bon filter, which can be used to filter e.g. the water filtered through the reverse osmosis filter or in ge ⁇ neral the purified water.
  • the appa ⁇ ratus comprises a centrifugal crystallizing/separating cyclone, into which any water not filtered by the fil ⁇ ter is passed and in which foreign matter is crystal ⁇ lized for possible recovery.
  • the water purification ap ⁇ paratus is mainly of the shape of a parallelopiped and placed at an oblique angle, preferably a sharp angle, e.g. 45°, relative to the horizontal plane.
  • the water inlet is below while the outlet for purified water and the gas outlet are above.
  • water is supplied into the water purification apparatus, where the water is purified electrically.
  • the water circulates freely in the reaction chamber and, as a result of an electrochemical reaction, ozone and possibly even ult- raviolet radiation are produced, while at the same ti ⁇ me the ionic charges of the impurities are discharged, bacteria, viruses and micro-organisms present in the water are destroyed and, depending on the electroche ⁇ mical reaction, metal ions are dissolved.
  • the reaction produces pure water and, as a by ⁇ product, hydrogen gas.
  • the ozone produced in the reac ⁇ tion is a transient physical state of oxygen and di ⁇ sappears quickly.
  • the water can be passed further into a filter, preferably a reverse osmosis filter.
  • the water can be passed further through an active carbon filter and then taken into use.
  • any water not filtered by the reverse osmosis filter (substances having a large molecular size) is passed into a centrifugal crystalli- zing/separating cyclone and then back to the purifica ⁇ tion process.
  • the filtered water is circulated again several times in the purification apparatus, so that any foreign matter will crystallize and can be recove- red.
  • drinking water is purified from sea water, produ ⁇ cing table salt, among other things, as a by-product.
  • Fig. 1 presents a cross-sectional lateral view of an apparatus according to an embodiment of the invention
  • Fig. 2 presents the apparatus of Fig. 1 as sectioned along line II-II,
  • Fig. 3 presents a flow chart representing an apparatus according to the embodiment in Fig. 1, used for the purification of drinking water
  • Fig. 4 presents an embodiment of the appara- tus of the invention, in which the water purification apparatus is placed at an angle of 45° relative to the horizontal plane.
  • Fig. 1 shows the reaction chamber 1 of the water purification apparatus.
  • the reaction chamber has side walls 2, a bottom wall 3, a top wall 4 and a par ⁇ tition wall 5 dividing the reaction chamber into a first chamber 6 and a second chamber 7, each of which contains mainly vertical plate electrodes 8.
  • the par ⁇ tition and the plate electrodes are placed at a dis- tance from the bottom wall.
  • the apparatus comprises an inlet 9 for the water to be purified, an outlet 10 for the purified water, a power source 11 and a gas outlet 12 placed in the upper part of the reaction chamber 1 in the wall opposite to the water inlet, the inlet 9 for water to be purified being pla ⁇ ced in wall 2 of the first chamber 6 and the outlet 10 for purified water in the opposite wall of the second chamber 7, so that the water to be purified is caused to circulate freely from the first chamber 6 into the second chamber 7, washing the electrodes and the reac ⁇ tion chamber 1.
  • Fig. 2 shows the reaction chamber 1, the side walls 2, the first chamber 6 and the second chamber 7, the electrodes 8 and the bottom wall 3, which is pro ⁇ vided with a bottom plate 13.
  • the first 6 and second 7 chambers of the purification apparatus contain a num- ber of plate-shaped electrodes 8 placed parallel to each other at a sharp angle to the reaction chamber walls, which are also mainly parallel to each other.
  • the plate-shaped electrodes are so arran ⁇ ged that the second chamber is a mirror image of the first chamber.
  • the electrodes may also be of a rod ⁇ like shape and placed in rows, which are at a sharp angle to the walls of the apparatus.
  • Fig. 2 further shows the water inlet 9, which is located in a side wall of the first chamber, and the outlet 10 for puri- fied water, located in the opposite side wall of the second chamber.
  • the water is passed in via the inlet 9 into the first chamber 6 of the reaction chamber 1, which contains a large number of plate-shaped electro ⁇ des 8. From the first chamber, the water flows freely, circulating under the partition into the second cham ⁇ ber 7, from where the purified water is removed via the outlet 10 and the hydrogen gas is removed via the gas outlet 12.
  • the water comes into contact with the electrodes, it undergoes an electrochemical reac ⁇ tion, during which the ionic charges of the impurities are discharged, bacteria, viruses and micro-organisms present in the water are destroyed and, depending on the electrochemical reaction, metal ions are dissol ⁇ ved.
  • Fig. 3 shows an embodiment of the apparatus of the invention for the purification of drinking wa ⁇ ter from sea water.
  • the figure shows a water purifica ⁇ tion apparatus with a power source 11.
  • the water to be purified is supplied into the purification apparatus via the inlet 9, further into the reaction chamber 1, first into the first chamber 5 and then into the se ⁇ cond chamber 7, where the water circulates freely un ⁇ der the partition and between the plate-shaped electrodes.
  • the water is removed from the purification apparatus via the outlet 10 into a reverse osmosis filter 14, which is provided with an ultrasonic device (17) to prevent undesirable crystallization.
  • the dif ⁇ fusion shells of the reverse osmosis filter are so chosen that only molecules smaller than a given size can pass through the diffusion shell.
  • the water filte ⁇ red through the reverse osmosis filter 14 is passed further out into an active carbon filter 15, from which pure drinking water is obtained.
  • Substances and liquid having a larger molecular size are passed from the reverse osmosis filter 14 into a centrifugal crys ⁇ tallizing/separating cyclone 16 and back into circula ⁇ tion into the water purifier and into the reverse os ⁇ mosis filter 14.
  • the amount of filtered water obtained via the reverse osmosis filter reaches about six times the total volume of the apparatus, the quan ⁇ tity of salt contained in the sea water in circulation has increased so much that its volume as a weight per ⁇ centage exceeds the supersaturation salt content (25%), resulting in crystallization and sedimentation of the salt.
  • salt Since salt has a higher specific weight than water, it sinks to the bottom of the cyclone, from where it can be recovered as a secondary product. If premature crystallization occurs, it is possible to provide the water purifier with an ultrasonic device, mounted on a suitable point, e.g. on the reverse osmo ⁇ sis filter, to prevent the crystallization of salt.
  • the apparatus of the invention can be opera- ted with alternating current, direct current or pulsa ⁇ ting direct current.
  • the voltage used may vary from a low voltage to high voltages. Preferably a voltage of about 1 - 36 V or even 40 V is used, in which case the voltage involves no danger and the apparatus need not be insulated.
  • the apparatus of the invention is applicable for use for a variety of water purification purposes. It can be used for the purification of the water in swimming pools, swirl pools etc., reducing the need for purifying agents. Thus, the invention also reduces waste water problems.
  • the low hardness of the water can also be utilized in thin-film evaporators, redu ⁇ cing the amount of energy needed.
  • An apparatus as provided by the invention was used for the purification of the water in a swimming pool.
  • the swimming pool was continuously used in the normal way and the water purifier of the invention was occasionally in operation.
  • Sample 1 was taken when the swimming pool had been in normal use and the purifica ⁇ tion apparatus had been in operation.
  • Sample 2 was ta ⁇ ken five weeks after sample 1.
  • the purification appa- ratus was in operation between the samples, yet not during the last week before sample 2 was taken.
  • Sample 3 was taken four weeks after sample 2. Between samples 2 and 3, the purification apparatus was not in opera ⁇ tion at all. Table 1 presents the results of analysis of the water samples.

Abstract

The invention relates to an apparatus for electrical purification of water, said apparatus comprising a reaction chamber (1) provided with side walls (2), a bottom wall (3), a top wall (4) and a partition wall (5) dividing the reaction chamber into a first chamber (6) and a second chamber (7), each provided with a mainly vertical electrode (8), the partition wall and the electrodes being disposed at a distance from the bottom wall; an inlet (9) for the water to be purified; an outlet (10) for the purified water; a power source (11) and a gas outlet. According to the invention, the inlet for the water to be purified is located in a wall (2, 3, 4) of the first chamber (6) and the outlet (10) for the purified water in a wall (2, 3, 4) of the second chamber (7), so that the water to be purified can circulate freely from the first chamber (6) into the second chamber (7), washing the electrodes (8) and the reaction chamber (1).

Description

AN APPARATUS FOR CLEANING WATER
The present invention relates to an apparatus for electrical purification of water as defined in the preamble of claim 1. Moreover, the invention relates to a procedure for electrical purification of water.
In prior art, many types of electrochemical water purification devices and filters are known. Pa¬ tent specification US 5 227 052 presents a water puri¬ fication apparatus based on an electrochemical reacti- on, comprising a reaction chamber with a partition di¬ viding the reaction chamber into two compartments. In each compartment of the reaction chamber there is one plate-shaped electrode, in which the water purificati¬ on reaction takes place. When electric power to the electrodes in the reaction chamber is switched on, a reaction producing hydrogen, ozone and pure water ta¬ kes place; at the positive plate electrode, OH" ions are separated, producing water and oxygen and then ozone, while on the negative electrode H30+ ions are separated, producing water and hydrogen. The partition prevents the gas bubbles formed in the reaction from combining, and the hydrogen produced can be passed out of the reaction chamber. The water inlet is in the bottom wall of the reaction chamber and the water is passed via it into both chambers simultaneously. The water can flow from one chamber to the other under the partition and through holes provided in the partition. The outlet for the purified water is placed in a side wall of the chamber on the same side with the inlet, and the gas outlet is in the top wall of the reaction chamber.
A problem with this apparatus is that the wa¬ ter cannot flow freely in the reaction chamber, with the result that dirt is heavily accumulated on the electrodes, requiring cleansing of the apparatus at short intervals, thus reducing its purification effect and increasing down time. The object of the invention is to eliminate the drawbacks mentioned above.
A specific object of the invention is to pre¬ sent an apparatus that does not require much clean- sing.
Another object of the invention is to present a small-sized apparatus that has a good purification effect.
A further object of the invention is to pre- sent an apparatus that produces water having a low de¬ gree of hardness.
A further object of the invention is to pre¬ sent an apparatus that allows water purification wit¬ hout chemicals, using a purification reaction that ta- kes place at the molecule level and leaves no detri¬ mental residue in the water. Therefore, no smells or tastes detrimental to water quality are developed in the purified water.
The apparatus of the invention is characteri- zed by what is presented in the claims.
The apparatus of the invention comprises a reaction chamber having side walls, a bottom wall, a top wall and a partition wall which divides the reac¬ tion chamber into a first chamber and a second cham- ber. Each one of the two chambers is provided with a mainly vertical plate electrode, and the partition wall and the plate electrodes are disposed at a dis¬ tance from the bottom wall. Furthermore, the apparatus comprises an inlet for the water to be purified, an outlet for the purified water, a power source and a gas outlet. The water inlet is placed in a wall of the first chamber, so that the water to be purified can flow freely from the first chamber into the second chamber, washing the electrodes and the reaction cha - ber. The inlet for the water to be purified may be lo¬ cated in the top, bottom or side wall of the first chamber of the reaction chamber, and, correspondingly, the outlet for the purified water may be located in the top, bottom or side wall of the second chamber, preferably in the opposite wall, so that the water to be purified will wash the entire reaction chamber as fully as possible. The gas outlet is placed in a dif¬ ferent chamber than the outlet for purified water to ensure that the gases produced in the electrochemical reaction will not be discharged via the outlet for pu¬ rified water but can be recovered and utilized if de- sired.
Due to the continuous washing, less dirt is accumulated in the apparatus of the invention than in prior-art electrochemical water purification devices. Moreover, the construction of the apparatus of the in- vention makes it possible to achieve a good purifica¬ tion effect in relation to the size of the apparatus. As the apparatus accumulates less dirt than prior-art devices, no prolonged down time is incurred and the operating costs of the apparatus are low. The inventi- on also allows long-time continuous operation of the apparatus.
Furthermore, due to its simple construction, the apparatus of the invention is economic and easy to maintain. In the apparatus of the invention, electrochemical purification occurs via a prior-art process. Electric power is supplied to the electrodes in the reaction chamber and the resulting electroche¬ mical reaction is utilized, discharging the ionic charges of the impurities; at the same time, the reac¬ tion produces ozone, hydrogen and even ultraviolet ra¬ diation. This reaction is so effective that it has a substantially more effective ability to kill bacteria, viruses and microbes than do most chemical purifying agents, such as chlorine compounds, e.g. chlorine. Moreover, the electrochemical reaction covers a consi¬ derably wider range than chemical purifying agents, which do not necessarily have any effect on all bacte¬ ria, viruses and microbes. The ozone produced in the reaction dissolves quickly and the purified water con¬ tains no ozone. In an embodiment of the invention, the inlet opening for the water to be purified is of a rectangu¬ lar shape and is placed in a side wall of the first chamber of the reaction chamber, and the water outlet opening is located in that side wall of the second chamber of the reaction chamber which lies opposite to the inlet, so the water can circulate freely from the first chamber into the second chamber and the electrochemical purifying reaction occurs as effecti¬ vely as possible on the surface of all electrodes. In another embodiment, the chambers in the reaction chamber are provided with several plate electrodes, preferably at least two plate electrodes in each chamber. The electrodes may be placed in a mainly parallel arrangement in each chamber. As the reaction chamber is of a rectangular shape, the plate electrodes can be mounted at right angles relative to the walls of the apparatus, preferably at a sharp angle relative to the walls of the apparatus, so the number of electrodes and the surface area on which the electrochemical purification reaction takes place are maximized in relation to the size of the apparatus and the water can circulate effectively in the reaction chamber, washing the electrodes and the reaction cham¬ ber. Further, in each chamber separately, the plate electrodes may be placed parallel to each other at a suitable angle relative to the reaction chamber wall, e.g. so that the second chamber is a mirror image of the first chamber. The electrodes may be of a plate¬ like shape or they may be composed of rod-shaped ele- ments or the like. In an embodiment of the apparatus, the electrodes are of a rod-like shape, placed in rows, preferably parallel rows, the rows being arran- ged at an angle to the walls of the reaction chamber, preferably at a sharp angle to the walls of the reac¬ tion chamber.
The electrodes are made of electrically con- ductive material, preferably e.g. zinc, copper, car¬ bon, silver, graphite, titan, or the like.
In an embodiment of the apparatus of the in¬ vention, all the electrodes are made of the same mate¬ rial. It is also possible for the apparatus of the in- vention to have electrodes made of two or more diffe¬ rent materials; in this case, the purification effect can be adjusted by considering the impurities, the de¬ sired purification effect and/or the desired degree of purification. The electrodes may be attached to the top wall of the apparatus, e.g. to a detachable cover part, in which case they can be lifted up together with the cover for cleansing if required. This allows easier and faster cleansing of the apparatus. In an embodiment, the bottom wall of the ap¬ paratus consists of an electrically conductive bottom plate, which allows a homogeneous electric field to be set up over the whole liquid flow through the appara¬ tus, so that no bypass flow occurs. This enhances the effect of the electrochemical purification. The bottom plate may be made of metal, preferably copper, stain¬ less steel or the like.
In an embodiment, the apparatus further com¬ prises a filter for further purification of the water. The apparatus may be provided e.g. with a reverse os¬ mosis filter, in which case detrimental foreign matter of even the smallest molecular size can be removed from the water. The diffusion shell of the reverse os¬ mosis filter can be so selected that it will only pass substances of a given molecular size through it. In an embodiment, the apparatus may comprise an active car¬ bon filter, which can be used to filter e.g. the water filtered through the reverse osmosis filter or in ge¬ neral the purified water.
In an embodiment of the invention, the appa¬ ratus comprises a centrifugal crystallizing/separating cyclone, into which any water not filtered by the fil¬ ter is passed and in which foreign matter is crystal¬ lized for possible recovery.
In an embodiment, the water purification ap¬ paratus is mainly of the shape of a parallelopiped and placed at an oblique angle, preferably a sharp angle, e.g. 45°, relative to the horizontal plane. In this case, the water inlet is below while the outlet for purified water and the gas outlet are above.
In the procedure of the invention for the pu- rification of water, water is supplied into the water purification apparatus, where the water is purified electrically. In the procedure, the water circulates freely in the reaction chamber and, as a result of an electrochemical reaction, ozone and possibly even ult- raviolet radiation are produced, while at the same ti¬ me the ionic charges of the impurities are discharged, bacteria, viruses and micro-organisms present in the water are destroyed and, depending on the electroche¬ mical reaction, metal ions are dissolved. On the who- le, the reaction produces pure water and, as a by¬ product, hydrogen gas. The ozone produced in the reac¬ tion is a transient physical state of oxygen and di¬ sappears quickly.
From the electric purification apparatus, the water can be passed further into a filter, preferably a reverse osmosis filter. The water can be passed further through an active carbon filter and then taken into use.
In an embodiment for the purification of drinking water, any water not filtered by the reverse osmosis filter (substances having a large molecular size) is passed into a centrifugal crystalli- zing/separating cyclone and then back to the purifica¬ tion process. The filtered water is circulated again several times in the purification apparatus, so that any foreign matter will crystallize and can be recove- red. In an embodiment of the procedure of the inventi¬ on, drinking water is purified from sea water, produ¬ cing table salt, among other things, as a by-product.
In the following, the invention is described in detail by the aid of examples of its embodiments by referring to the attached drawing, in which
Fig. 1 presents a cross-sectional lateral view of an apparatus according to an embodiment of the invention,
Fig. 2 presents the apparatus of Fig. 1 as sectioned along line II-II,
Fig. 3 presents a flow chart representing an apparatus according to the embodiment in Fig. 1, used for the purification of drinking water,
Fig. 4 presents an embodiment of the appara- tus of the invention, in which the water purification apparatus is placed at an angle of 45° relative to the horizontal plane.
Fig. 1 shows the reaction chamber 1 of the water purification apparatus. The reaction chamber has side walls 2, a bottom wall 3, a top wall 4 and a par¬ tition wall 5 dividing the reaction chamber into a first chamber 6 and a second chamber 7, each of which contains mainly vertical plate electrodes 8. The par¬ tition and the plate electrodes are placed at a dis- tance from the bottom wall. Moreover, the apparatus comprises an inlet 9 for the water to be purified, an outlet 10 for the purified water, a power source 11 and a gas outlet 12 placed in the upper part of the reaction chamber 1 in the wall opposite to the water inlet, the inlet 9 for water to be purified being pla¬ ced in wall 2 of the first chamber 6 and the outlet 10 for purified water in the opposite wall of the second chamber 7, so that the water to be purified is caused to circulate freely from the first chamber 6 into the second chamber 7, washing the electrodes and the reac¬ tion chamber 1. Fig. 2 shows the reaction chamber 1, the side walls 2, the first chamber 6 and the second chamber 7, the electrodes 8 and the bottom wall 3, which is pro¬ vided with a bottom plate 13. The first 6 and second 7 chambers of the purification apparatus contain a num- ber of plate-shaped electrodes 8 placed parallel to each other at a sharp angle to the reaction chamber walls, which are also mainly parallel to each other. In addition, the plate-shaped electrodes are so arran¬ ged that the second chamber is a mirror image of the first chamber. The electrodes may also be of a rod¬ like shape and placed in rows, which are at a sharp angle to the walls of the apparatus. Fig. 2 further shows the water inlet 9, which is located in a side wall of the first chamber, and the outlet 10 for puri- fied water, located in the opposite side wall of the second chamber.
To purify water by means of the apparatus of the invention, the water is passed in via the inlet 9 into the first chamber 6 of the reaction chamber 1, which contains a large number of plate-shaped electro¬ des 8. From the first chamber, the water flows freely, circulating under the partition into the second cham¬ ber 7, from where the purified water is removed via the outlet 10 and the hydrogen gas is removed via the gas outlet 12. When the water comes into contact with the electrodes, it undergoes an electrochemical reac¬ tion, during which the ionic charges of the impurities are discharged, bacteria, viruses and micro-organisms present in the water are destroyed and, depending on the electrochemical reaction, metal ions are dissol¬ ved.
Fig. 3 shows an embodiment of the apparatus of the invention for the purification of drinking wa¬ ter from sea water. The figure shows a water purifica¬ tion apparatus with a power source 11. The water to be purified is supplied into the purification apparatus via the inlet 9, further into the reaction chamber 1, first into the first chamber 5 and then into the se¬ cond chamber 7, where the water circulates freely un¬ der the partition and between the plate-shaped electrodes. The water is removed from the purification apparatus via the outlet 10 into a reverse osmosis filter 14, which is provided with an ultrasonic device (17) to prevent undesirable crystallization. The dif¬ fusion shells of the reverse osmosis filter are so chosen that only molecules smaller than a given size can pass through the diffusion shell. The water filte¬ red through the reverse osmosis filter 14 is passed further out into an active carbon filter 15, from which pure drinking water is obtained. Substances and liquid having a larger molecular size are passed from the reverse osmosis filter 14 into a centrifugal crys¬ tallizing/separating cyclone 16 and back into circula¬ tion into the water purifier and into the reverse os¬ mosis filter 14. When the amount of filtered water obtained via the reverse osmosis filter reaches about six times the total volume of the apparatus, the quan¬ tity of salt contained in the sea water in circulation has increased so much that its volume as a weight per¬ centage exceeds the supersaturation salt content (25%), resulting in crystallization and sedimentation of the salt. Since salt has a higher specific weight than water, it sinks to the bottom of the cyclone, from where it can be recovered as a secondary product. If premature crystallization occurs, it is possible to provide the water purifier with an ultrasonic device, mounted on a suitable point, e.g. on the reverse osmo¬ sis filter, to prevent the crystallization of salt.
The apparatus of the invention can be opera- ted with alternating current, direct current or pulsa¬ ting direct current. The voltage used may vary from a low voltage to high voltages. Preferably a voltage of about 1 - 36 V or even 40 V is used, in which case the voltage involves no danger and the apparatus need not be insulated.
The apparatus of the invention is applicable for use for a variety of water purification purposes. It can be used for the purification of the water in swimming pools, swirl pools etc., reducing the need for purifying agents. Thus, the invention also reduces waste water problems. The low hardness of the water can also be utilized in thin-film evaporators, redu¬ cing the amount of energy needed.
EXAMPLE 1
An apparatus as provided by the invention was used for the purification of the water in a swimming pool. The swimming pool was continuously used in the normal way and the water purifier of the invention was occasionally in operation. Sample 1 was taken when the swimming pool had been in normal use and the purifica¬ tion apparatus had been in operation. Sample 2 was ta¬ ken five weeks after sample 1. The purification appa- ratus was in operation between the samples, yet not during the last week before sample 2 was taken. Sample 3 was taken four weeks after sample 2. Between samples 2 and 3, the purification apparatus was not in opera¬ tion at all. Table 1 presents the results of analysis of the water samples.
As can be seen from Table 1, no bacterial growth took place in the swimming pool although the apparatus was not in operation at all for a week befo¬ re the taking of sample 2, nor even after five weeks (sample 3) without operating the apparatus. Thus, af¬ ter a certain level of ionisation with certain metals had been reached, it was not necessary to operate the water purifier at all except to maintain the level of ionization of the water. The ions present in the water obviously prevented bacterial growth. The water could be kept clean for weeks by using only mechanical fil- tering with a sand filter.
Table 1. Analysis of swimming pool water.
Sample 1 Sample 2 Sample 3
Amount of dissolved solids mg/ml 214 182 166
Hardness in CaC03 mg/ml 100 62 104
Iron, Fe mg/ml 0.01 0.001 0.01
Chloride, Cl mg/ml 54 47 43
PH 7.1 7.1 7.0 Copper, Cu mg/ml 0.661 0.673 0.325
Manganese, Mn mg/ml 0.011 0.007 0.007
Sodium, Na mg/ml 18.0 11.9 14.6
Turbidity, NTU 1.9 0.57 0.43
Zinc, Zn mg/ml 1.92 3.31 1.74 Bacteria; coliform
Bacteria; non-coliform
The invention is not restricted to any one of the examples presented above, but many variations are possible within the inventive idea defined by the claims.

Claims

1. Apparatus for electrical purification of water, said apparatus comprising a reaction chamber
(I) provided with side walls (2), a bottom wall (3), a top wall (4) and a partition wall (5) dividing the reaction chamber into a first chamber (6) and a second chamber (7), each provided with a mainly vertical pla¬ te-shaped electrode (8), the partition wall and the electrodes being disposed at a distance from the bot- torn wall; an inlet (9) for the water to be purified; an outlet (10) for the purified water; a power source
(II) and a gas outlet (12) , c h a r a c t e r i z e d in that the inlet (9) for the water to be purified is lo¬ cated in a wall (2, 3, 4) of the first chamber (6) and the outlet (10) for the purified water is located in a wall (2, 3, 4) of the second chamber (7), so that the water to be purified can circulate freely from the first chamber (6) into the second chamber (7), washing the electrodes (8) and the reaction chamber (1) .
2. Apparatus as defined in claim 1, c h a ¬ r a c t e r i z e d in that each one of the chambers (6, 7) contains at least two mainly plate-shaped electro¬ des (8) .
3. Apparatus as defined in claim 1 or 2, c h a r a c t e r i z e d in that the reaction chamber
(1) comprises two opposite, mainly parallel side walls
(2) and that the electrodes (8) are placed at a sharp angle relative to these walls.
4. Apparatus as defined in any one of claims 1 - 3, c h a r a c t e r i z e d in that the electrodes
(8) are mainly parallel to each other.
5. Apparatus as defined in any one of claims 1 - 4, c h a r a c t e r i z e d in that the electrodes (8) are composed of rod-shaped elements.
6. Apparatus as defined in any one of claims
1 - 5, c h a r a c t e r i z e d in that the electrodes (8) are made of zinc, copper, carbon, silver, graphi- te, titan or the like.
7. Apparatus as defined in any one of claims 1 - 6, ch a r a c t e r i z e d in that all the electro¬ des (8) are made of the same material.
8. Apparatus as defined in any one of claims
1 - 6, ch a r a c t e r i z ed in that the electrodes (8) are made of different materials.
9. Apparatus as defined in any one of claims 1 - 8, c ha r a c t e r i z e d in that the electrodes (8) are attached to the top wall (4) so that they can be lifted up for cleansing.
10. Apparatus as defined in any one of claims 1 - 9, cha r a c t e r i z ed in that the bottom wall (3) is provided with an electrically conductive bottom plate (13) serving to set up a homogeneous electric field.
11. Apparatus as defined in any one of claims 1 - 11, ch a r a c t e r i z e d in that the bottom pla¬ te is made of metal, preferably copper, stainless steel or the like.
12. Apparatus as defined in any one of claims 1 - 11, c ha ra c t e r i z ed in that the apparatus comprises a reverse osmosis filter (14) .
13. Apparatus as defined in any one of claims 1 - 12, c ha r a c t e r i z ed in that the apparatus comprises an active carbon filter (15) .
14. Apparatus as defined in any one of claims 1 - 13, c ha r a c t e r i z ed in that the apparatus comprises a centrifugal crystallizing/separating cyclone (16) .
15. Apparatus as defined in any one of claims 1 - 14, ch a r a c t e r i z e d in that it is mainly of the shape of a parallelopiped and placed at an oblique angle, preferably a sharp angle, e.g. 45°, relative to the horizontal plane.
16. Apparatus as defined in any one of claims 1 - 15, ch a ra c t e r i z ed in that it is provided with an ultrasonic device (17) to prevent undesirable crystallization of salt.
17. Procedure for electrical purification of water, in which the water to be purified is supplied via a water inlet into the reaction chamber of an electrical water purification apparatus, ch a r a c ¬ t e r i z e d in that the water is first passed into a first chamber of the reaction chamber and then into a second chamber, so that the water circulates freely, washing the reaction chamber and electrodes placed in the reaction chamber.
18. Procedure as defined in claim 17, c ha ¬ r a c t e r i z e d in that the purified water is passed out from the reaction chamber of the electrical water purification apparatus via an outlet and further into a reverse osmosis filter.
19. Procedure as defined in claim 17 or 18, cha r a c t e r i z e d in that the purified water is passed out into an active carbon filter.
20. Procedure as defined in any one of claims
17 - 19, cha ra c t e r i z e d iri that any water not filtered by the reverse osmosis filter is passed into a centrifugal crystallizing/separating cyclone and then back into the purification process.
21. Procedure as defined in any one of claims
17 - 20, ch a r a c t e r i z e d in that the water to be purified is sea water.
22. Procedure as defined in any one of claims 17 - 21, cha r a c t e r i z ed in that undesirable crystallization is prevented by means of an ultrasonic device.
PCT/FI1996/000591 1995-11-06 1996-11-04 An apparatus for cleaning water WO1997017297A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
AU74978/96A AU7497896A (en) 1995-11-06 1996-11-04 An apparatus for cleaning water
FI972842A FI972842A (en) 1995-11-06 1997-07-02 Device for purifying water

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI955333 1995-11-06
FI955333A FI955333A0 (en) 1995-11-06 1995-11-06 Anordning Foer rening av vatten

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WO (1) WO1997017297A1 (en)

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Also Published As

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