Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J47/00—Ion-exchange processes in general; Apparatus therefor
  • B01J47/10—Ion-exchange processes in general; Apparatus therefor with moving ion-exchange material; with ion-exchange material in suspension or in fluidised-bed form
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J47/00—Ion-exchange processes in general; Apparatus therefor
  • B01J47/011—Ion-exchange processes in general; Apparatus therefor using batch processes
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/42—Treatment 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.

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• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Life Sciences & Earth Sciences (AREA)
• Hydrology & Water Resources (AREA)
• Engineering & Computer Science (AREA)
• Environmental & Geological Engineering (AREA)
• Water Supply & Treatment (AREA)
• Treatment Of Water By Ion Exchange (AREA)
• Water Treatment By Electricity Or Magnetism (AREA)

Applications Claiming Priority (3)

Publications (1)

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ID=19860708

Family Applications (1)

Country Status (3)

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Family Cites Families (4)

• 1992
  • 1992-04-16 NL NL9200707A patent/NL9200707A/nl not_active Application Discontinuation
• 1993
  • 1993-04-16 WO PCT/NL1993/000082 patent/WO1993021114A1/en not_active Application Discontinuation
  • 1993-04-16 EP EP93908169A patent/EP0636109A1/en not_active Ceased

Non-Patent Citations (1)

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