Classifications

• • 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
  • C02F1/28—Treatment of water, waste water, or sewage by sorption
  • C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D41/00—Regeneration of the filtering material or filter elements outside the filter for liquid or gaseous fluids
  • B01D41/02—Regeneration of the filtering material or filter elements outside the filter for liquid or gaseous fluids of loose filtering material
• • 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
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
  • B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
• • 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
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
  • B01J20/28004—Sorbent size or size distribution, e.g. particle size
• • 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
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/30—Processes for preparing, regenerating, or reactivating
  • B01J20/34—Regenerating or reactivating
  • B01J20/3416—Regenerating or reactivating of sorbents or filter aids comprising free carbon, e.g. activated carbon
• • 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
  • B01J49/00—Regeneration or reactivation of ion-exchangers; Apparatus therefor
• • 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
• • 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
  • C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
• • 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
  • C02F1/008—Control or steering systems not provided for elsewhere in subclass C02F
• • 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
  • C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
  • C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2209/00—Controlling or monitoring parameters in water treatment
  • C02F2209/42—Liquid level
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2209/00—Controlling or monitoring parameters in water treatment
  • C02F2209/44—Time
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2303/00—Specific treatment goals
  • C02F2303/16—Regeneration of sorbents, filters

Definitions

• Process for the potabilization and / or purification of water comprising the elimination of a targeted compound and filtration within a filter drum
• the field of the invention is that of water treatment processes for their purification and / or their potabilization.
• the invention relates in particular to the purification of any type of water (urban waste water, industrial water) and / or the potabilisation of any type of water (surface or underground freshwater, treated urban wastewater, industrial water, water sea ”) containing any type of pollutant (organic matter of natural origin, organic micropollutants such as for example pesticides, non-organic micropollutants such as for example bromates, chemical pollutant ).
• pollutant organic matter of natural origin, organic micropollutants such as for example pesticides, non-organic micropollutants such as for example bromates, chemical pollutant .
• Water treatment processes are commonly used to produce, in particular, drinking water.
• These methods also known as potabilization processes, generally comprise an elimination step of contacting the water to be treated with an active particulate material in a stirred tank. This removal step is necessarily followed by a separation step in which the active particulate material is separated from the active water / particulate material mixture from the stirred tank, and treated water is collected. The active particulate material is then re-routed into the stirred tank. The collected treated water is optionally conveyed to downstream filtration units in order to reduce the residual turbidity.
• Such a potabilization technique is known in which the elimination stage uses CAP (activated carbon in powder).
• CAP activated carbon in powder
• the separation of the CAP and the treated water is obtained by decantation. This involves previously injecting a polymer in the mixture of CAP and water so as to drain the CAP and facilitate its decantation.
• Another potabilization technique is known which is described in the international patent application WO-A1 -96 / 077615, in which the elimination step uses magnetic ion exchange resins weighted with metal oxides. In this case, the separation of the resins, a part of the fines resulting from the attrition of the resins, and the treated water is obtained by decantation. The remainder of the fines not separated by settling is subsequently recovered by magnetization.
• Decantation implemented in these techniques is influenced by many parameters (temperature, hydraulic strokes %) complicating even more the control of this liquid / solid separation step.
• this separation technique has the drawbacks of not allowing such an absolute and rapid separation as a physical barrier, such as formed by a sieve. Consequently, the settling may possibly lead to a loss of active particulate material and reagents initially supplied.
• Japanese Patent Application JP-A-5 157333 discloses a technique for preventing leakage of particulate active material into the treated water. This technique involves introducing the water to be treated into a tank. A lower portion of a porous rotating cylinder containing ion exchange resins bullies in this vessel. The water to be treated enters the cylinder, comes into contact with the resins ion exchangers which are housed therein, then spring out of the cylinder and is collected, while the ion exchange resins remain inside the cylinder. The ion exchange resins are continuously withdrawn from the cylinder for regeneration before being continuously fed back into the cylinder.
• This technique has the advantage of avoiding the leakage of ion exchange resins in the treated water and obviates the disadvantages that result (clogging downstream filtration units, additional operating cost related to employment of new or regenerated particulate material to compensate for losses ).
• the invention particularly aims to overcome these disadvantages of the prior art.
• an object of the present invention is to provide, in at least one embodiment, such a technique that allows to completely separate the active particulate material from the treated water.
• Another object of the invention is to implement, in at least one embodiment, such a technique that ensures a good stability of the water treatment process.
• the invention has the objective of maintaining a concentration of substantially constant active particulate material all along the treatment die.
• the invention also aims to provide, in at least one embodiment, such a technique that increases productivity.
• the invention aims to reduce downtime during which the production of treated water is stopped.
• the invention also aims at providing, in at least one embodiment, such a technique that makes it possible to limit the degradation of the active particulate material, for example into beads or grains.
• An object of the invention is also, in at least one embodiment, to provide such a technique which leads to reduce the operating costs inherent in the water purification, particularly by the absence of reagents use coagulant and / or flocculant.
• Yet another object of the invention is to provide, in at least one embodiment, such a technique which is reliable and effective and whose impact on the environment is relatively low, particularly because of the lack of use. coagulating and / or flocculating reagents.
• an extraction step consisting in continuously extracting said vessel from contacting a mixture of water and active particulate material
• Said step of continuous separation consists of:
• the method also includes washing steps of said rotary filtering drum, said washing steps comprising:
• washing steps being carried out according to a predetermined cycle.
• Said washing water and said residues recovered during said washing steps are stored momentarily in a stirred recirculation tank before being returned substantially in their entirety to said contact tank so as to maintain said predetermined concentration of active particulate material substantially constant in said contact tank.
• a filtering drum is a hollow element of generally cylindrical shape whose walls delimiting its outer surface are at least partially porous.
• Such a filter drum has a generally cylindrical shape means that it is cylindrical or capable of being inscribed in a cylinder.
• stirred tank in which the water to be treated is brought into direct contact with the active particulate material increases the contact between these two elements and improves the performance of the treatment while limiting its duration.
• the treated water collected at the outlet of the filter drum is thus totally free of active particulate material. This helps to prevent clogging of filtration units that could be placed downstream in order to eliminate the residual turbidity of the treated water produced.
• This technique thus makes it possible at the same time to improve the contact between the water to be treated and the active particulate material and to avoid losses in this material.
• the washing of the drum makes it possible to recover all of the active particulate material while continuing the filtration of the water through the drum. This implementation avoids downtime and increases productivity.
• the mixture of wash water and active particulate material is recirculated substantially in its entirety in the agitated contact tank so that the concentration of active particulate material within this vessel is kept constant. This makes it possible to guarantee the stability of the water treatment and to reduce the costs inherent in the consumption of particulate active material.
• cleaning the drum with pressurized water does not require the use of cleaning solution. This limits the impact on the environment of water purification.
• the washing of the drum is carried out according to a predetermined cycle.
• the washing steps may, for example, be carried out according to a predetermined frequency, or whenever the maximum level of water in the drum is reached, or each time the maximum threshold for clogging of the drum is reached or else in taking into account two or three of these information.
• Said particulate active material preferably has a particle size of between 20 micrometers and 500 micrometers and advantageously a coefficient of uniformity of between 1.0 and 1.5.
• the coefficient of uniformity will be between 1 and 1.2.
• said active particulate material has a particle size equal to 350 microns.
• the coefficient of uniformity is equal to the ratio between the mesh size of a sieve allowing the passage of 60% of particles of a given size and the mesh size of a sieve allowing the passage of 10% of said particles. .
• the greater the uniformity coefficient of an active particulate material is removed from 1 the more this material is heterodisperse, that is to say the greater the dispersion of the size of the particles that constitute it is important.
• an active particulate material whose uniformity coefficient is between 1 and 1.5 and preferably between 1 and 1.2 makes it possible to guarantee that the size of the particles which compose it varies very little. It is thus possible to use a filter drum having a cut-off point higher. This makes it possible to limit the clogging of the filter drum and to reduce the frequency of cleaning steps thereof.
• the use of an active particulate material having a particle size greater than or equal to 20 microns provides gravity filtration of the mixture of water and active particulate material through the filter drum. This makes it possible to avoid the use of a pump to force this mixture to pass through the pores of the filter drum.
• a process according to the invention comprises purges of saturated active particulate material from said recirculation tank with a view to their elimination or their regeneration and additional contributions of new and / or regenerated active particulate material. in said contact tank, the amounts of said purges being substantially identical to the amounts of new and / or regenerated particulate active material.
• the particulate particulate active material When the particulate particulate active material is saturated, it is no longer effective so that it must be replaced with a new and / or regenerated particulate active material.
• the saturated active particulate material is then removed from the recirculation vessel and then an equal amount of new and / or regenerated particulate active material is injected into the agitated contact vessel. This makes it possible to maintain a constant concentration of active particulate material inside the agitated contact vat and thus to guarantee the stability of the treatment.
• New active particulate material is material that has never been used.
• Regenerated active particulate material is material that has already been used to treat water after which it has been reactivated so as to recover, at least in large part, its original active properties.
• the purges in active particulate material consist in continuously extracting a small amount of active particulate material which may or may not be saturated with the recirculation tank. At the same time, an identical amount of material, new and / or regenerated, is introduced into the contact tank.
• the quantities put at stake depend on the operating conditions.
• a method according to the invention comprises a stage of regeneration in situ of said saturated active particulate material.
• Some saturated active particulate materials can be regenerated directly within the installation used for the implementation of the process. These are, for example, ion exchange resins.
• the method then comprises a corresponding regeneration step.
• the regeneration may for example consist of a co-current regeneration, or a countercurrent regeneration.
• the regeneration can be implemented ex-situ.
• said new and / or regenerated particulate active material provided in said contact tank during said supply step is from said in situ regeneration step of said saturated active particulate material.
• said discharged filtered water then undergoes a final filtration step to reduce its residual turbidity.
• Said final filtration is advantageously a conventional filtration on granular filter media such as sand.
• Said final filtration is advantageously a membrane filtration.
• said membrane filtration is preferably an ultrafiltration. Its implementation makes it possible to significantly reduce, if not total, the turbidity, the viruses, the bacteria and any fines resulting from the attrition of the balls or grains of active particulate material.
• FIG. 1 illustrates an installation for implementing a method according to the invention implementing a regenerable active particulate material in situ
• FIG. 2 illustrates an installation for implementing a method according to the invention implementing a non-regenerable active particulate material in situ
• FIGS 3 and 4 illustrate a variant of a filter drum implementing filter discs.
• the general principle of the invention consists, in a potabilization and / or purification technique including contacting a water to be treated with an active particulate material, to separate the active particulate material from the treated water by means of a rotating filter drum.
• a filter drum completely separates the active particulate material, which remains trapped inside the drum, the treated water flowing out of the drum through the pores that pass through it.
• the washing of the drum consists in injecting countercurrent of the filtered water under pressure forming washing water on the outer surface of an upper part of said filtering drum in order to loosen the residues accumulated inside thereof and to recover said wash water and said residues within said filter drum without bringing them into contact with said mixture introduced inside said filter drum.
• FIG. 1 an embodiment of a water treatment installation according to the invention is presented.
• Such an installation comprises a pipe 1 for supplying water to be treated.
• This pipe opens into a contact tank 2, housing a stirring means 3, for example a stirrer, inside which water to be treated is brought into contact with an active particulate material 19 regenerable in situ.
• the contact tank 2 has an outlet which is connected to a pipe 20 which opens inside a filtering drum 4.
• the filter drum 4 has the shape of a hollow cylinder whose outer surface is porous.
• the outer surface of the filter drum is a sieve.
• the pore diameter of the sieve are chosen in such a way as to retain the active particulate material with which the water to be treated is brought into contact.
• the filtering drum 4 is rotatably mounted inside a chamber 5.
• a motor 6 is able to rotate the filtering drum 4.
• a chute 9 is housed inside the filter drum 4 in an upper part thereof.
• a water injection manifold 7 comprising nozzles is housed outside the filter drum 4 near its outer surface. It is approximately facing chute 9.
• the injection manifold 7 is connected to the bottom of the enclosure 5 containing treated water 21 by a pipe on which a pump 8 is mounted.
• Control means (not shown) make it possible to activate according to a predetermined frequency that can be adjusted. activation of the pump 8. In this case, a washing cycle of the drum may be implemented at a predetermined frequency.
• an installation according to the invention may comprise an on-off sensor comprising two electrodes placed at the entrance of the drum. The resistance between these two electrodes can be measured to determine if the maximum water level in the drum, defined by the height of the sensor, has been reached. In this case, a drum wash cycle can be triggered whenever the maximum water level in the drum is reached.
• an installation according to the invention may comprise an analog piezoelectric type sensor for determining the level of clogging of the drum.
• a drum washing cycle can be triggered each time a maximum drum clogging threshold is reached.
• the chute 9 is connected by means of a pipe to a recirculation tank 10 housing a stirring means 11, for example a stirrer.
• a recirculation pipe 12 links the recirculation tank 10 to the contact tank 2.
• a saturated active particulate material extraction line 13 links the recirculation tank 10 to a regeneration unit 15.
• the regeneration unit 15 is connected to the contact tank 2 by means of a channel of regenerated active particulate material 14.
• the bottom of the enclosure 5 has a treated water discharge outlet which is connected via a pipe 17 to a filtration unit 16.
• the filtration unit 16 has an outlet connected to a pipe for discharging treated and filtered water 18.
• FIG. 2 illustrates an alternative of a treatment plant according to the invention intended to be implemented when the active particulate material injected inside the tank of contact 2 is not regenerable in situ.
• the saturated active particulate material extraction line 13 then opens into an ex-situ disposal or treatment zone.
• the installation then comprises a pipe 14 'of new or regenerated particulate active material which opens into the contact tank 2.
• FIGS 3 and 4 illustrate a variant of a filter drum according to the invention.
• the filtering drum comprises a tube 31 whose surface is traversed by perforations 32 distributed in such a way that they form rings spaced from each other around the periphery of the tube 31.
• Disc portions 35 are attached all around some of the rings to form filter discs 36 which are secured to the tube 31.
• Each of the disc portions 35 constitutes a frame housing filter elements 37. In this way, water introduced in the tube 31 flows through the perforations 32 into the disc portions 35 and leaves while the impurities it contained remain trapped in the filter elements 37 they carry.
• Water injection ramps 38 are placed near the outer surface of the disks 35, in an upper part of the filter drum.
• the filter discs 36 have an outer contour of polygonal type.
• the injection ramps are rotatably mounted along an axis parallel to the axis of rotation of the drum. They can thus be animated by a synchronized pendulum movement with the rotation of the discs 36 to cover the total surface of each disc portion 35.
• a chute 9 is housed inside the filter drum below the injection ramps 38.
• a given volume of water to be treated for the purpose of its potabilization, previously decanted, is introduced continuously inside the contact tank 2 by means of the pipe 1.
• the water is mixed therewith by means of stirring 3 with active particulate material regenerable in situ at a given concentration.
• concentration of active particulate material in the contact tank 2 is essentially constant makes it possible to ensure better stability and better control of the water treatment.
• the water to be treated then undergoes an elimination step during which the elimination of the targeted pollutant (s) takes place.
• the active particulate material is ion exchange resins 19 having a particle size of 350 microns and a uniformity coefficient of 1.2.
• the mixture of water and ion exchange resins contained in the contact tank 2 is introduced inside the filtering drum 4, essentially below its axis of rotation, by means of the pipe 20.
• the screen pore size of the filter drum 4 is chosen such that it retains all of the active particulate material.
• the drum filter 4, driven by a rotational movement by means of the motor 6, thus allows to filter this mixture and to separate the water and the ion exchange resins.
• the ion exchange resins are trapped by the screen of the filter drum 4 and remain therein, whereas the treated water 21, free of active particulate material, flows through the pores of the screen into the bottom of the enclosure 5.
• the treated water 21 is conveyed via line 17 into a filtration unit 16 so as to reduce the residual turbidity.
• the filtered and filtered water is then discharged via line 18.
• the filtration unit 16 is a membrane filtration unit, for example of the ultrafiltration type. Its implementation makes it possible to significantly reduce, if not total, turbidity, viruses, bacteria and any fines resulting from the attrition of ion exchange resins.
• the filtration unit may be a media filtration unit, such as sand. Its implementation will significantly reduce turbidity and any fines resulting from the attrition of ion exchange resins.
• a washing step is implemented.
• a treatment cycle starts as soon as a given volume of water to be treated is introduced into the contact tank 2, and ends as soon as the given volume of water to be treated has been eliminated. in the contact tank 2 and then a filtration in the filter drum 4.
• the washing steps are triggered at a predetermined frequency corresponding approximately to the duration of a cycle. Alternatively, they can be triggered whenever the maximum level of water that can be present in the filter drum is reached or a predetermined threshold of maximum clogging of the drum is reached.
• Such a washing step consists in injecting under pressure a constant volume of treated water 21 against the current on the outer surface of the filtering drum 4.
• the pump 8 is implemented so as to draw treated water 21 in the bottom of the chamber 5 and to inject it via the ramp 7 to the outer surface of the filter drum 4.
• the ion exchange resins accumulated on the inner surface of the filter drum 4 detach from it. A mixture of washing water and ion exchange resins flows into the trough 9. It is therefore not brought into contact with the mixture of water and active particulate material introduced inside the filtering drum 4 via line 20.
• the mixture of washing water and ion exchange resins flows from the trough 9 into the recirculation tank 10.
• the concentration of ion exchange resins in the contact tank 2 is constant.
• a new washing step is initiated after each treatment cycle, i.e. after a constant given volume of water has been processed.
• the amount of water used during each wash step is constant. Washing enables the ion exchange resins trapped in the filter drum 4 to be completely recovered during a treatment cycle.
• the concentration of ion exchange resins in the recirculation tank 10 is therefore constant.
• the mixture of washing water and ion exchange resins contained in the recirculation tank 10 at the end of washing is essentially in its entirety reinjected into the contact tank 2 throughout the next treatment cycle.
• the saturated ion exchange resins contained in the recirculation tank 10 are extracted by the implementation of purges by means of the pipe 13. These saturated ion exchange resins are conveyed in the regeneration unit 15 in order to to be regenerated.
• the ion exchange resins may for example be regenerated within the regeneration unit 15 as follows.
• the regeneration unit 15 comprises an accumulation vessel (not shown) in which the saturated ion exchange resins are conveyed from the recirculation vessel 10.
• This accumulation vessel comprises, at its base, a filter screen.
• the ion exchange resins are stored, concentrated and accumulated over time (filtering the interstitial water through the filter screen to concentrate the exchange resins).
• the concentrated water-resin mixture is directed to a reaction vessel, also equipped with a sieve. filtering in its lower part.
• the volume (or bed) of accumulated ion exchange resins is firstly measured.
• a regeneration solution is then introduced into the reaction vessel.
• the volume of regeneration solution injected is generally a function of the volume of ion exchange resins to be regenerated.
• the regeneration solution is prepared prior to the regeneration step in a preparation tank (preparation for the desired concentration from the network water and a concentrated regeneration solution).
• Percolation of the regeneration solution through the ion exchange resin bed then takes place at a fixed rate. Used brine is then withdrawn from the reaction vessel and discharged to the sewers or stored for reuse.
• the ion exchange resins are then rinsed with water from the network by percolating this water through the bed of resins at a fixed rate.
• the rinsing water is withdrawn and discharged to a suitable subsequent treatment.
• the regenerated ion exchange resins are then recovered. They are mixed with water from the network to form a slurry. A certain amount of new ion exchange resins can be integrated into the slip.
• the regenerated ion exchange resins in the form of slip from the regeneration unit 15 are injected into the contact tank 2 via line 14.
• the concentration of ion exchange resins inside the contact tank 2 is kept constant.
• the washing of the drum is effected efficiently without the addition of any washing chemical. Moreover, the treatment of water does not require the use of coagulant. In addition, the fact of implementing a filter drum prevents the implementation of a settling step that most often requires injecting polymer into the mixture of water and active particulate material to facilitate its settling. The technique according to the invention therefore has a limited impact on the environment.
• Prior art separation techniques most often require concentrating the active particulate material in an accumulation vessel after it has been separated from the treated water, before returning it to the contact tank.
• the use of the filtering drum makes it possible to directly obtain a mixture of washing water and active particulate material which is very concentrated in active particulate material (approximately between 200 ml and 500 ml of active particulate material per liter of mixture ).
• the invention thus prevents the setting implementation of a concentration step, which reduces the duration of treatment and increases productivity.
• the active particulate material used is not regenerable in situ. It consists of granular activated carbon (GAC).
• the saturated GAC contained in the recirculation tank 10 is extracted by the implementation of purges by means of the line 13.
• This saturated GAC is conveyed to an ex-situ treatment zone, that is to say ie located outside the installation used for the implementation of the process.
• Fresh CAG is injected into contact tank 2 via line 14.
• the amount of saturated GAC extracted from recirculation vessel 10 is substantially equal to the amount of new GAC introduced into contact tank 2 via line 14.
• the concentration of AGC inside the contact tank 2 is kept constant.
• particulate adsorbent materials regenerable or non-in situ
• ion exchange resins such as, for example, ion exchange resins, CAG, CAP (activated carbon powder), composite particles, etc.
• FIGS. 1 and 2 may be implemented in an installation in which the filtering drum comprising a screen may be replaced by a filtering drum such as that described above with reference to FIGS. and 4.
• the washing of the drum consists in injecting treated water against the current against the outer surface of the discs 36 by means of the ramps 38.
• the mixture of washing water and active particulate material is then collected in the chute.

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• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Engineering & Computer Science (AREA)
• Analytical Chemistry (AREA)
• Hydrology & Water Resources (AREA)
• Life Sciences & Earth Sciences (AREA)
• Environmental & Geological Engineering (AREA)
• Water Supply & Treatment (AREA)
• Inorganic Chemistry (AREA)
• Materials Engineering (AREA)
• Water Treatment By Sorption (AREA)
• Treatment Of Water By Ion Exchange (AREA)
• Separation Using Semi-Permeable Membranes (AREA)

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• 2009
  • 2009-12-17 FR FR0959091A patent/FR2954174B1/fr active Active
• 2010
  • 2010-12-16 AU AU2010332807A patent/AU2010332807B2/en not_active Ceased
  • 2010-12-16 WO PCT/EP2010/069952 patent/WO2011073335A2/fr active Application Filing
  • 2010-12-16 EP EP10798303A patent/EP2512616A2/de not_active Withdrawn
  • 2010-12-16 CA CA2780861A patent/CA2780861C/en not_active Expired - Fee Related
  • 2010-12-16 US US13/516,041 patent/US9422170B2/en active Active

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