WO1993021114A1 - Apparatus and method for cleaning waste water and waste sludge by means of ion exchangers - Google Patents

Apparatus and method for cleaning waste water and waste sludge by means of ion exchangers Download PDF

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Publication number
WO1993021114A1
WO1993021114A1 PCT/NL1993/000082 NL9300082W WO9321114A1 WO 1993021114 A1 WO1993021114 A1 WO 1993021114A1 NL 9300082 W NL9300082 W NL 9300082W WO 9321114 A1 WO9321114 A1 WO 9321114A1
Authority
WO
WIPO (PCT)
Prior art keywords
carriers
container
waste water
ion exchangers
cleaning
Prior art date
Application number
PCT/NL1993/000082
Other languages
French (fr)
Inventor
Johannes Laurentius De Reuver
Aloysius Fredericus Maria Van Velsen
Jan Bart Kok
Leonardus Gerardus Catherina Mathias Urlings
Original Assignee
Envimag B.V.
Tauw Milieu B.V.
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 Envimag B.V., Tauw Milieu B.V. filed Critical Envimag B.V.
Priority to EP93908169A priority Critical patent/EP0636109A1/en
Publication of WO1993021114A1 publication Critical patent/WO1993021114A1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J47/00Ion-exchange processes in general; Apparatus therefor
    • B01J47/10Ion-exchange processes in general; Apparatus therefor with moving ion-exchange material; with ion-exchange material in suspension or in fluidised-bed form
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J47/00Ion-exchange processes in general; Apparatus therefor
    • B01J47/011Ion-exchange processes in general; Apparatus therefor using batch processes
    • 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
    • C02F1/42Treatment of water, waste water, or sewage by ion-exchange

Definitions

  • the present invention relates to a device for cleaning waste water by means of ion exchangers held on carriers. Such devices are generally known.
  • the ion exchangers are held on carriers, which carriers are placed together into a con ⁇ tainer, and wherein the waste water for cleaning is guided through the container.
  • the waste water for cleaning herein flows into the pores which are formed by the spaces between the carriers, so that the waste water for cleaning comes into intensive contact with the walls of the carriers.
  • the object of the present invention is to provide a de ⁇ vice which also operates well in the case of turbid waste water and remains operative.
  • the device comprises: a container; feed means for feeding the waste water for cle ⁇ aning to the container; carrier feed means for feeding carriers provided with ion exchangers to the container; an agitation device arranged in the container; and a separa ⁇ ting device connected to the container by means of a pipe for separating the carriers from the waste water.
  • the separating device prevents the ion exchangers from being discharged together with the waste water that has meanwhile been cle ⁇ aned.
  • This separating device can be formed by a filter, for example a mechanical or an electro-static filter, but is
  • SUBSTI preferably formed by a magnetic separating device.
  • the carriers must then of course be magnetic.
  • the device for cleaning waste water is formed by at least two devices connected in series as claimed in claim 1 or 2, wherein the carrier feed means are adapted for feeding the carriers provided with ion exchangers to the second con ⁇ tainer in the flow direction, wherein the second sepa ⁇ rating device in downstream direction is adapted for feeding the separated carriers provided with partially used up ion exchangers to the first container in the flow direction, and wherein the first separating means in the flow direction is adapted for discharging the carriers provided with used up ion exchangers.
  • This device is particularly suitable for removing metals from waste water.
  • the invention offers a solution for this problem in that the carriers can be magnetized and the separating device is a magnetic separating device. This offers the possibility of adapting the amount of supplied carriers to the flow rate of waste water for cleaning and the degree of contamination.
  • this device can of course likewise be applied in a multi-stage embodiment.
  • SUBSTITUTE SHEET fig. 1 shows a schematic perspective view of a first embodiment of the present invention
  • fig. 2 is a schematic perspective view of a second embo ⁇ diment of the invention
  • fig. 3 is a schematic perspective view of a third embo ⁇ diment of the invention.
  • a feed pipe 2 with which the waste water for cleaning is fed debouches into the container 1.
  • a feed pipe 3 for feeding carriers provided with ion exchangers further de- foundeds into the container 1.
  • an agitation device 4 Arranged in container 1 is an agitation device 4 formed by a motor 5 which is fixed onto a connecting beam 6 arranged in container 1 and which drives an agitation blade 8 by means of a shaft 7.
  • a discharge pipe 9 leads from container 1 to a magnetic separating device 10. From the magnetic separating device 10 a discharge pipe 11 leads to a pump 12 with which the cleaned waste water is drained.
  • the separating device 10 is of the type as described in the Dutch patent applica- tion 8801463.
  • a discharge pipe 13 for separated carriers is connected to the separating device 10, which pipe 13 leads to a schematically depicted regeneration device 14. From the regeneration device 14 a pipe 15 leads to a storage con- tainer 16 in which the regenerated carriers 17 are stored. From the storage container the feed pipe already indicated leads to container 1. A closing valve 18 is otherwise arranged in the pipe 3.
  • this device is such that the waste water for cleaning, which can be turbid, is fed to the container 1.
  • the device according to the invention will otherwise also operate well with clear, that is non-turbid, waste water.
  • the carriers 17 provided with ion exchangers by means of the pipe 3 and closing valve 18 are also supplied to the container 1. Once there the waste water for cleaning is agitated by the agitation device 4 so that an intensive contact is created between the carriers and the supplied waste water.
  • the waste water together with the carriers moving therein - flows through the pipe 9 to the magnetic separating device 10. Separation of the magnetic carriers takes place there and the waste water with the magnetic carriers removed is drained by means of the discharge pipe 11 and the pump 12. This waste water is of course divested not only of the carriers but of the substances for removal taken up by the ion exchangers present on the carriers.
  • the carriers thus provided with these substances are fed by means of the pipe 13 to the regeneration device 14 where they are regenerated.
  • the regenerated carriers are fed to the storage container 16 by means of the pipe 15.
  • the device described here can be modified in various ways; for example instead of a mag- netic separating device it is possible to apply another separating device, for example a mechanical filter, which must be regularly divested of carriers to prevent blockage, or for example an electro-static filter. It is important for this purpose that the carriers all have a similar electrical charge.
  • the waste water for cleaning is also fed by means of a feed pipe 2 which debouches in a first container 19.
  • a pipe 20 leads to a separating device designated in its entirety by 21.
  • the water coming from the first separating device is fed via a pipe 22, in which a pump 23 is arranged, to a second con ⁇ tainer 24.
  • a discharge pipe 25 leads to a second separating device 26.
  • a discharge pipe 27 leads away the cleaned waste water.
  • a pump 28 is received in this pipe.
  • Carriers with regenerated ion exchangers are supplied from a storage container 16 to the container 24 by means of a pipe 3 in which a closing valve 18 is incorporated.
  • SUBSTITUTE SHEET are supplied to the first container 19 by means of a pipe 29, in which for example may be arranged a pump (not shown in the drawing) .
  • Carriers coming from the first separating device 21 are supplied by means of a pipe 30 to a regeneration device 14 from which a pipe 15 leads to the container 16.
  • the first and the second separation device are each pro ⁇ vided with a housing 31 in which is situated a horizontal shaft 32 driven in rotation, whereon in the present embo- diment three discs 33 provided with magnets are fixed.
  • a motor 34 fixed on the shaft the discs are driven in rotation.
  • the mixture consisting of waste water and the carriers taken up therein is fed to the interior of the housing by means of the pipe 20.
  • the magnetic carriers are attracted by the magnets present in discs 33, whereafter they are then scraped off by the scraping devices through rotation of the discs and by means of the ducts connected thereto fall into a collection space 37 and are then discharged through pipe 30.
  • Such a device otherwise forms the subject of the non-prepublished Dutch patent application 9101872.
  • fig. 3 shows a third embodiment which is par ⁇ ticularly suitable for processing waste water with greatly varying flow rate.
  • This third embodiment differs from the second embodiment in that an extra storage container 40 is arranged in which a store of carriers with ion exchangers can be stored. This relates to carriers coming from the second separating device 26 which are supplied via the pipe 29 and which have thus already been “used up” to a certain degree.
  • This third embodiment further differs in that above the regeneration device 14 is arranged a storage container 41 fulfilling the same function; with a large feed of the waste water for cleaning the separating device will sepa-
  • the device also provides for the possibility that the quality of the supplied waste water is relatively good, that is, that it is lightly contaminated. In such a situation it is possible to bypass the first stage, that is, to stop feed of carriers provided with ion exchangers from storage container 40 and to lead the waste water via the bypass pipe 42 to the container 24. It is also possible in such a situation to switch off the first sepa ⁇ rating device 21.
  • the above described embodiment further relates to cleaning of contaminated waste water; not only domestic, industrial or other waste water must be considered as waste water, but also other liquids from which can be re ⁇ moved materials removable by means of ion exchangers.
  • the invention is, partly because of the fact that blockage is prevented, particularly suitable for cleaning liquids with particles suspended therein, even so many particles that it may be described as a slurry.
  • the invention offers the possibility of removing the waste products from the waste water in a manner such that neither the remaining liquid medium nor the separated pro ⁇ duct is regarded as chemical waste and can even be used as raw material.
  • Waste water coming from the nickel washing baths of an enamelling plant comprising ⁇ 90 mg Hi/1, ⁇ 45 mg Fe/1 and 920 mg Na/1, was treated in a two-stage counterflow system as described in figure 2.
  • the capture of the mag- ' netic resin took place with electromagnets.
  • the ion exchanger used consisted of a weak acid resin with Fe 2 0 3 as magnetic component. The resin is selective for the transition elements.

Abstract

The invention relates to a device for cleaning waste water or waste slurry by means of ion exchangers held on carriers, comprising: a container; feed means for feeding the waste water for cleaning to the container; carrier feed means for feeding carriers provided with ion exchangers to the container; an agitation device arranged in the container; and a separating device connected to the container by means of a pipe for separating the carriers from the waste water. As a result of these steps the carriers of the ion exchangers are carried suspended or floating into the water, so that the danger of blockage is avoided. The separating device prevents the ion exchangers being discharged together with the waste water that has meanwhile been cleaned. This separating device can be formed by a filter, for example, a mechanical or an electrostatic filter, but can likewise be formed by a magnetic separating device. The carriers must then of course be magnetic.

Description

APPARATUS AND METHOD FOR CLEANING WASTE WATER AND WASTE SLUDGE BY MEANS OF ION EXCHANGERS
The present invention relates to a device for cleaning waste water by means of ion exchangers held on carriers. Such devices are generally known.
With such known devices the ion exchangers are held on carriers, which carriers are placed together into a con¬ tainer, and wherein the waste water for cleaning is guided through the container. The waste water for cleaning herein flows into the pores which are formed by the spaces between the carriers, so that the waste water for cleaning comes into intensive contact with the walls of the carriers.
Although such carriers operate well in removing the was¬ te products from the water, such devices operate badly with turbid waste water; due to solid substances present in suspension or otherwise floating or formed in the waste water, this device becomes blocked so that it becomes in¬ operative.
The object of the present invention is to provide a de¬ vice which also operates well in the case of turbid waste water and remains operative.
This object is achieved in that the device comprises: a container; feed means for feeding the waste water for cle¬ aning to the container; carrier feed means for feeding carriers provided with ion exchangers to the container; an agitation device arranged in the container; and a separa¬ ting device connected to the container by means of a pipe for separating the carriers from the waste water.
As a result of these steps the carriers of the ion ex¬ changers are placed suspended or floating in the water, so that the danger of blockage is avoided. The separating device prevents the ion exchangers from being discharged together with the waste water that has meanwhile been cle¬ aned.
This separating device can be formed by a filter, for example a mechanical or an electro-static filter, but is
SUBSTI preferably formed by a magnetic separating device. The carriers must then of course be magnetic.
According to a preferred embodiment the device for cleaning waste water is formed by at least two devices connected in series as claimed in claim 1 or 2, wherein the carrier feed means are adapted for feeding the carriers provided with ion exchangers to the second con¬ tainer in the flow direction, wherein the second sepa¬ rating device in downstream direction is adapted for feeding the separated carriers provided with partially used up ion exchangers to the first container in the flow direction, and wherein the first separating means in the flow direction is adapted for discharging the carriers provided with used up ion exchangers. In this preferred embodiment of the invention particu¬ larly effective use is made of the ion exchangers; the already used ion exchangers come into contact with the most contaminated water, while the water already somewhat cleaned water comes into contact with fresh ion ex- changers, so that these can remove the last remnants of the substances for removing from the water.
This device is particularly suitable for removing metals from waste water.
A problem which is typical for the treatment of waste water, whether of an industrial or domestic nature, is the greatly varying and often unpredictable flow rate and the greatly varying and likewise poorly predictable degree of contamination. The invention offers a solution for this problem in that the carriers can be magnetized and the separating device is a magnetic separating device. This offers the possibility of adapting the amount of supplied carriers to the flow rate of waste water for cleaning and the degree of contamination.
In addition to the described two-stage embodiment this device can of course likewise be applied in a multi-stage embodiment.
The present invention will subsequently be elucidated with reference to the annexed drawings, in which:
SUBSTITUTE SHEET fig. 1 shows a schematic perspective view of a first embodiment of the present invention; fig. 2 is a schematic perspective view of a second embo¬ diment of the invention; and fig. 3 is a schematic perspective view of a third embo¬ diment of the invention.
A feed pipe 2 with which the waste water for cleaning is fed debouches into the container 1. A feed pipe 3 for feeding carriers provided with ion exchangers further de- bouches into the container 1.
Arranged in container 1 is an agitation device 4 formed by a motor 5 which is fixed onto a connecting beam 6 arranged in container 1 and which drives an agitation blade 8 by means of a shaft 7. A discharge pipe 9 leads from container 1 to a magnetic separating device 10. From the magnetic separating device 10 a discharge pipe 11 leads to a pump 12 with which the cleaned waste water is drained. The separating device 10 is of the type as described in the Dutch patent applica- tion 8801463.
A discharge pipe 13 for separated carriers is connected to the separating device 10, which pipe 13 leads to a schematically depicted regeneration device 14. From the regeneration device 14 a pipe 15 leads to a storage con- tainer 16 in which the regenerated carriers 17 are stored. From the storage container the feed pipe already indicated leads to container 1. A closing valve 18 is otherwise arranged in the pipe 3.
The action of this device is such that the waste water for cleaning, which can be turbid, is fed to the container 1. The device according to the invention will otherwise also operate well with clear, that is non-turbid, waste water. The carriers 17 provided with ion exchangers by means of the pipe 3 and closing valve 18 are also supplied to the container 1. Once there the waste water for cleaning is agitated by the agitation device 4 so that an intensive contact is created between the carriers and the supplied waste water. Once the mixture of waste water and carriers has remained long enough in the container 1, the waste water together with the carriers moving therein - flows through the pipe 9 to the magnetic separating device 10. Separation of the magnetic carriers takes place there and the waste water with the magnetic carriers removed is drained by means of the discharge pipe 11 and the pump 12. This waste water is of course divested not only of the carriers but of the substances for removal taken up by the ion exchangers present on the carriers.
The carriers thus provided with these substances are fed by means of the pipe 13 to the regeneration device 14 where they are regenerated. The regenerated carriers are fed to the storage container 16 by means of the pipe 15. It will be apparent that the device described here can be modified in various ways; for example instead of a mag- netic separating device it is possible to apply another separating device, for example a mechanical filter, which must be regularly divested of carriers to prevent blockage, or for example an electro-static filter. It is important for this purpose that the carriers all have a similar electrical charge.
It is of course likewise possible to make use of other types of magnetic separating devices.
Another embodiment of the invention is now shown in fig. 2, wherein corresponding components are designated with corresponding reference numerals.
In this situation the waste water for cleaning is also fed by means of a feed pipe 2 which debouches in a first container 19. From the container 19 a pipe 20 leads to a separating device designated in its entirety by 21. The water coming from the first separating device is fed via a pipe 22, in which a pump 23 is arranged, to a second con¬ tainer 24. From the second container 24 a discharge pipe 25 leads to a second separating device 26. From the second separating device 26 a discharge pipe 27 leads away the cleaned waste water. A pump 28 is received in this pipe. Carriers with regenerated ion exchangers are supplied from a storage container 16 to the container 24 by means of a pipe 3 in which a closing valve 18 is incorporated. The carriers separated in the second separating device 26
SUBSTITUTE SHEET are supplied to the first container 19 by means of a pipe 29, in which for example may be arranged a pump (not shown in the drawing) .
Carriers coming from the first separating device 21 are supplied by means of a pipe 30 to a regeneration device 14 from which a pipe 15 leads to the container 16.
The first and the second separation device are each pro¬ vided with a housing 31 in which is situated a horizontal shaft 32 driven in rotation, whereon in the present embo- diment three discs 33 provided with magnets are fixed. By means of a motor 34 fixed on the shaft the discs are driven in rotation. The mixture consisting of waste water and the carriers taken up therein is fed to the interior of the housing by means of the pipe 20. The magnetic carriers are attracted by the magnets present in discs 33, whereafter they are then scraped off by the scraping devices through rotation of the discs and by means of the ducts connected thereto fall into a collection space 37 and are then discharged through pipe 30. Such a device otherwise forms the subject of the non-prepublished Dutch patent application 9101872.
It will likewise be apparent that various modifications can also be made to the device shown here; it is possible for example instead of the two-stage device applied here to apply a three-stage device or even a device with a num¬ ber of stages larger than three.
Finally, fig. 3 shows a third embodiment which is par¬ ticularly suitable for processing waste water with greatly varying flow rate. This third embodiment differs from the second embodiment in that an extra storage container 40 is arranged in which a store of carriers with ion exchangers can be stored. This relates to carriers coming from the second separating device 26 which are supplied via the pipe 29 and which have thus already been "used up" to a certain degree.
This third embodiment further differs in that above the regeneration device 14 is arranged a storage container 41 fulfilling the same function; with a large feed of the waste water for cleaning the separating device will sepa-
SUBSTI rate a large amount of completely used up ion exchangers which must be regenerated in the regeneration device 14. With an excess of waste water for cleaning the amount fed will exceed the capacity of the regeneration device 14 so that this excess can be stored in the storage container 41. This offers the possibility of selecting a smaller capacity for the regeneration unit 14.
The device also provides for the possibility that the quality of the supplied waste water is relatively good, that is, that it is lightly contaminated. In such a situation it is possible to bypass the first stage, that is, to stop feed of carriers provided with ion exchangers from storage container 40 and to lead the waste water via the bypass pipe 42 to the container 24. It is also possible in such a situation to switch off the first sepa¬ rating device 21.
The above described embodiment further relates to cleaning of contaminated waste water; not only domestic, industrial or other waste water must be considered as waste water, but also other liquids from which can be re¬ moved materials removable by means of ion exchangers. The invention is, partly because of the fact that blockage is prevented, particularly suitable for cleaning liquids with particles suspended therein, even so many particles that it may be described as a slurry.
The invention offers the possibility of removing the waste products from the waste water in a manner such that neither the remaining liquid medium nor the separated pro¬ duct is regarded as chemical waste and can even be used as raw material.
In general ion exchangers are used for removing metals, but it would likewise be possible when suitable adsorbents become available, to apply these for removing other sub¬ stances, such as organic pollutants. Finally, an example follows of the application of a de¬ vice and method according to the invention.
Waste water coming from the nickel washing baths of an enamelling plant, comprising ± 90 mg Hi/1, ± 45 mg Fe/1 and 920 mg Na/1, was treated in a two-stage counterflow system as described in figure 2. The capture of the mag- ' netic resin took place with electromagnets. The ion exchanger used consisted of a weak acid resin with Fe203 as magnetic component. The resin is selective for the transition elements.
At an average treatment time of 15 minutes in the total system an effluent concentration of <0.5 mg/1 could be achieved.
SUBSTITUTE SHEET

Claims

1. Device for cleaning waste water or waste slurry by means of ion exchangers held on carriers, characterized by:
- a container; - feed means for feeding the waste water for cleaning to the container;
- carrier feed means for feeding to the container carriers provided with ion exchangers;
- an "agitation device arranged in the container; and - a separating device connected to the container by means of a pipe for separating the carriers from the waste water.
2. Device as claimed in claim 1, characterized in that the carrier feed means comprise a buffer storage con- tainer.
3. Device as claimed in claim 1 or 2, characterized in that the carriers can be magnetized, and that the separa¬ ting device is a magnetic separating device.
4. Device as claimed in claim 1, 2 or 3, characterized in. that a regeneration device for regenerating the ion exchangers is connected to the separating device.
5. Device as claimed in claim 4, characterized in that the regeneration device is coupled to a buffer storage container.
6. Device for cleaning waste water, characterized by at least two devices connected in series as claimed in any of the claims 1-5, wherein the carrier feed means are adapted for feeding the carriers provided with ion exchangers to the second container in the flow direction; wherein the second separating device in downstream direction is adapted for feeding the separated carriers provided with partially used up ion exchangers to the first container in the flow direction, and wherein the first separating means in the flow direction is adapted for discharging the carriers provided with used up ion exchangers.
7. Device as claimed in claim 6, characterized in that the carriers discharged by the first separating device in flow direction are supplied to a regeneration device, and that the carriers coming from the regeneration device are supplied to the second feed means in flow direction.
8. Device as claimed in any of the foregoing claims, characterized in that an agitation device is arranged in one of the containers.
9. Device as claimed in any of the claims 6-8, charac- terized in that the device comprises means switching off the first cleaning device depending on the degree of con¬ tamination of the waste water for cleaning.
SUBSTITUTE SHEET
PCT/NL1993/000082 1992-04-16 1993-04-16 Apparatus and method for cleaning waste water and waste sludge by means of ion exchangers WO1993021114A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP93908169A EP0636109A1 (en) 1992-04-16 1993-04-16 Apparatus for cleaning waste water and waste sludge by means of ion exchangers

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NL9200707A NL9200707A (en) 1992-04-16 1992-04-16 APPARATUS AND METHOD FOR CLEANING WASTE WATER AND WASTE SLURRIES BY MEANS OF ION EXCHANGERS.
NL9200707 1992-04-16

Publications (1)

Publication Number Publication Date
WO1993021114A1 true WO1993021114A1 (en) 1993-10-28

Family

ID=19860708

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/NL1993/000082 WO1993021114A1 (en) 1992-04-16 1993-04-16 Apparatus and method for cleaning waste water and waste sludge by means of ion exchangers

Country Status (3)

Country Link
EP (1) EP0636109A1 (en)
NL (1) NL9200707A (en)
WO (1) WO1993021114A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996007615A1 (en) * 1994-09-09 1996-03-14 South Australian Water Corporation Water treatment process
AU749656B2 (en) * 1994-09-09 2002-06-27 Orica Australia Pty Ltd Water treatment process
WO2006063404A1 (en) * 2004-12-15 2006-06-22 Orica Australia Pty. Ltd. Magnetic resin separator

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE668584A (en) * 1965-08-20 1966-02-21
DE1417619A1 (en) * 1961-02-11 1969-01-02 Asahi Chemical Ind Process for the recovery of metal ions from a slurry containing them
NL7307704A (en) * 1972-06-02 1973-12-04
NL7702147A (en) * 1976-02-28 1977-08-30 Clarke Chapman Ltd METHOD AND ARRANGEMENT FOR ION EXCHANGE.

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1417619A1 (en) * 1961-02-11 1969-01-02 Asahi Chemical Ind Process for the recovery of metal ions from a slurry containing them
BE668584A (en) * 1965-08-20 1966-02-21
NL7307704A (en) * 1972-06-02 1973-12-04
NL7702147A (en) * 1976-02-28 1977-08-30 Clarke Chapman Ltd METHOD AND ARRANGEMENT FOR ION EXCHANGE.

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
PATENT ABSTRACTS OF JAPAN vol. 12, no. 450 (C-547) *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996007615A1 (en) * 1994-09-09 1996-03-14 South Australian Water Corporation Water treatment process
AU749656B2 (en) * 1994-09-09 2002-06-27 Orica Australia Pty Ltd Water treatment process
US6669849B1 (en) 1994-09-09 2003-12-30 Orica Australia Pty Ltd Water treatment process
WO2006063404A1 (en) * 2004-12-15 2006-06-22 Orica Australia Pty. Ltd. Magnetic resin separator
WO2006063406A1 (en) * 2004-12-15 2006-06-22 Orica Australia Pty. Ltd. Water polishing process
AU2005316207B2 (en) * 2004-12-15 2011-09-01 Ixom Operations Pty Ltd Magnetic resin separator
US9011693B2 (en) 2004-12-15 2015-04-21 Orica Australia Pty Ltd Water polishing process

Also Published As

Publication number Publication date
EP0636109A1 (en) 1995-02-01
NL9200707A (en) 1993-11-16

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