• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
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    • 专利摘要:
    Method and installation for water treatment using a contact tank (21) of water with an adsorbent granular material and a clarification, the adsorbent material consisting of agglomerates of activated carbon particles having a mean size of between 200 μm and 600 μm and a specific surface area of between 800 and 1000 m2 / g, a screen (9) being provided in the upper part of the contact tank (21) comprising a layer of porous material of 1 mm and 5 mm thick. thickness and a cutoff threshold of between 100 μm and 200 μm, said tank having a bottom portion (21a) hopper-shaped, purge means (21b) and stirring means (22) for stirring the contents of the upper part thereof without stirring the contents of the bottom hopper-shaped.
    公开号:FR3050200A1
    申请号:FR1653262
    申请日:2016-04-13
    公开日:2017-10-20
    发明作者:Philippe Sauvignet；Abdelkader Gaid
    申请人:Veolia Water Solutions and Technologies Support SAS；
    IPC主号:
    专利说明:

    Activated carbon adsorption water treatment process and clarification, and corresponding installation.
    TECHNICAL FIELD OF THE INVENTION The invention relates to the field of water treatment.
    More specifically, the invention relates to water treatment processes employing at least one treatment step during which the water is brought into contact with an inert carbonaceous adsorbent granular material in order to reduce the organic matter content. and pollutants (pesticides, micropollutants, endocrine disruptors, industrial residues, drug residues ...) followed by a clarification step.
    Prior art
    Powdered or granular inert carbonaceous materials have a highly developed intrinsic porosity which gives them a high surface area which gives them the property of adsorbing large quantities of organic molecules and catalyzing reactions. In practice, the adsorption capacity of a granular adsorbent material can be evaluated by measuring its iodine number. The adsorption capacity by measurement of the iodine number indicates the amount of iodine, expressed in milligrams, adsorbed per gram of activated carbon powder. This measurement of the iodine number can in particular be carried out according to the international standard ASTM No. D4607.
    The activated carbon powder (PAC) used in the context of water treatment processes have an average particle size of between 10 μm and 50 μm and a specific surface area corresponding to an iodine number of between 800 and 1000 mg / g of CAP. (index measured according to the standard indicated above).
    In such processes, the CAP can be implemented in different configurations.
    Thus, the CAP can be added to the water to be treated in a reactor at a sufficient contact time to allow the adsorption of the organic material they contain. The CAP, in charge of the substances which have been adsorbed there, must then be separated from the treated waters by clarification. This clarification step is generally carried out by decantation or by membrane separation.
    Coagulant reagents and / or flocculants are conventionally added to promote the aggregation of organic matter and CAP in the form of flocs and thus facilitate the clarification operation.
    Given the high cost of CAP, recycling of this material is planned. For this purpose, the sludge recovered at the end of the clarification step indicated above and containing adsorbent material, are treated so as to eliminate most of the aqueous phase. This step is generally carried out by hydrocycloning. At the end of this step, under the hydrocyclone, a phase is obtained containing adsorbent powder material which can be reintroduced into the water treatment process. In practice, this phase contains a high proportion of pulverulent material and still water and is in the form of a relatively fluid sludge, most of the aqueous phase of the sludges from the separation step indicated below. above having however been removed in overflow of the hydrocyclone.
    An example of such a method of the prior art is described in the French patent application FR-A-2868064.
    According to such prior art, the powder material recycled in situ is not freed by the hydrocycloning step of all the organic material adsorbed thereon but only a small part thereof. Although recycled in situ, the adsorbent material progressively sees its adsorbent capacity decrease. It is thus necessary to regularly replace part of the CAP implemented in the reactor with new CAP. Quantities of new CAP must therefore be regularly injected into the reactor to compensate for the loss of adsorption CAP used.
    Although this type of method allows the replacement of part of the CAP used by new CAP without having to shut down the facilities that implement it, it also has other disadvantages.
    Thus, the CAP from purges of the system can not be regenerated in the sense that there is no known economically efficient treatment to restore the CAP its original adsorbent capacity or adsorbent power thereof. This results in the production of PAC sludge that must be removed from the factory. The treatment of these sludges is not without inconvenience. In particular, sludge must be dewatered before being transported, which increases the costs associated with landfilling or incineration or with agricultural land application.
    The CAP is an expensive material, its use in the context of water treatment therefore faces economic imperatives, the techniques implementing it has the disadvantage of involving, therefore, high operating costs.
    In addition, the treatment of water with CAP involves in practice the addition of large amounts of coagulants, such as FeCis, and / or flocculants, such as polymers, to form sufficiently dense flocs. This, in order to promote settling and also to avoid CAP leaks that would degrade downstream refining treatments, such as filtration. The addition of a microlest, such as microsand to accelerate settling is also common. The use of polymers can lead to an accelerated saturation of the CAP which forces the user to renew it more frequently. Above all, the use of these products leads to obtaining increased volumes of sludge to be treated in parallel channels. In practice, these sludges must be thickened, dehydrated and removed from the production site. The operating costs of such processes are therefore also increased. These sludges of CAP can not in any case not be treated so as to allow obtaining CAP regenerated.
    OBJECTIVES OF THE INVENTION The object of the present invention is to provide a method of treating water with a view to removing organic matter and pollutants in which the water is brought into contact with a contact tank. adsorbent material and clarified avoiding the problems of the prior art resulting from the presence of adsorbent material in the water during their clarification.
    An object of the present invention is to provide such a method which leads to minimizing the quantities of sludge resulting from the clarification.
    Another object of the present invention is to describe such a method which leads to minimizing the amounts of polymer when the clarification implements such a material.
    Yet another object of the present invention and to disclose such a method that the adsorbent material can be renewed without interrupting the treatment.
    An object of the present invention is also to disclose such a method that allows to maintain a water treatment level substantially constant over time.
    It is also an object of the present invention to provide such a method which, in at least one of its embodiments, leads to a used adsorbent material which can be directly regenerated, that is to say, whose adsorption capacity vis-à-vis organic matter can be easily restored.
    Thus, an object of the invention is to describe such a method which, in at least one of its embodiments, makes it possible to restore 50% of the adsorption capacity of the adsorbent material, that is to say to to obtain an at least partially regenerated adsorbent material whose adsorption capacity corresponds to at least 50% of that of the same new adsorbent material.
    Another object of the present invention is to describe such a method inducing lower processing costs than those of the prior art processes, with substantially equal treatment levels.
    Another object of the invention is to propose an installation for the implementation of such a method.
    Yet another object of the invention is to disclose such an installation that can result from the rehabilitation of existing old stations.
    Presentation of the invention
    These various objectives are achieved thanks to the invention which relates to a water treatment process with a view to cutting down the content of organic matter and pollutants, said process comprising: a step of contacting water to be treated with a granular adsorbent material in a contact tank provided with stirring means; followed by a step of clarifying water from said tank leading to obtaining clarified water and sludge; characterized in that said granular adsorbent material consists of agglomerates of activated carbon particles, said agglomerates having a mean size of between 200 μm and 600 μm and a specific surface area of between 800 and 1000 mVg, said granular adsorbent material being regenerable by thermal pathway; said water is screened out of said tank, before undergoing clarification, to retain said granular adsorbent material within said tank while not retaining the non-adsorbed organic material on said adsorbent material. and in that the content of said contact tank is only partially agitated so as to create a concentration gradient of said adsorbent material within it, the bottom of said contact tank constituting a non-agitated zone; spent adsorbent granular material being continuously or intermittently purged from said non-agitated zone of said contact tank for freshly regenerated thermally, and replaced with fresh adsorbent granular material.
    Thus, according to the invention, no in situ recycling of said granular adsorbent material is necessary.
    The adsorbent material used in the context of the process according to the invention is a commercially available material which is therefore not a CAP in the sense that is meant in the field of water treatment. It has indeed a higher specific surface than the CAP. It is also not a granular activated carbon (GAC) as it is understood in the field of water treatment. It has indeed a smaller particle size.
    Such a specific adsorbent material has, among other advantages, the ability to be regenerated thermally unlike CAPs conventionally used in the field of water treatment that can not be.
    According to the invention, this material is retained in the contact tank by appropriate means, which prevents its propagation during the clarification step and avoids any risk of dissemination of this material in clarified water. These means make it possible to retain the adsorbent material in the contact tank while allowing water and organic matter and non-adsorbed pollutants to pass through. Thus, all the problems of the prior art resulting from the presence of adsorbent material in the clarification members, whatever they are, are avoided.
    In particular, the quantities of sludge resulting from the clarification are lower than in the prior art. These sludge does not contain adsorbent material, it is also useless to treat them to separate it. The implementation costs of the process according to the invention are therefore reduced with respect to the costs incurred by the processes of the prior art which imply the need to treat the sludge resulting from the clarification in order to recover the adsorbent material which 'they contain.
    According to the invention, the content of the contact tank is stirred only partially, a non-agitated area of the tank being formed in the lower part thereof. Thus, a concentration gradient of adsorbent material is created within the contact tank. The granular adsorbent material used, weighed down by the materials which have adsorbed it, increases its density. It thus accumulates in the lower part of the contact tank. This granular material used can be purged from this lower part and replaced by new material, without having to interrupt the process.
    The purged adsorbent material can be drained and stored in drums which, once filled, are conveyed to an external site for the purpose of regenerating the adsorbent material which they contain thermally. The specific adsorbent material used in the context of the present invention can indeed be regenerated thermally in the absence of any treatment, apart from a simple preliminary draining.
    The duration of the contacting of the adsorbent material with the water in the contact tank will be chosen by those skilled in the art so as to optimize the adsorption of the organic material and pollutants contained therein. In practice, this contact time will preferably be between 5 min and 20 min.
    The concentration of adsorbent material in the contact tank will be chosen by those skilled in the art as a function of the load of organic matter and pollutants of the water to be treated. In practice, preferably, the used adsorbent granular material is purged and replaced by new adsorbent granular material so as to maintain a mean concentration of said adsorbent material in said contact tank during said contacting step. This average concentration will vary depending on the waters to be treated.
    Preferably, the process comprises a preliminary step of pre-filtering the water to be treated before entering said reactor on a pre-filter having a cutoff threshold of between 1 mm and 5 mm. Such pre-filtration is intended to rid the water to be treated solids that could be trapped in subsequent steps of the process.
    Alternatively, the method comprises periodic steps of cleaning said screen by a cleaning method selected from the group consisting of a backwashing method and a method of cleaning by air blowing. Thus, clogging of the filter is avoided.
    The method according to the invention can be implemented with many clarification techniques. According to one advantageous variant, this clarification comprises a step of coagulation of said water to be treated producing coagulated waters, a step of flocculation of said coagulated water producing flocculated water, a step of decantation of said flocculated water producing clarified water and sludge. said coagulation, flocculation and settling steps being, by virtue of the invention, carried out in the absence of granular adsorbent material.
    According to such a variant, the method makes it possible to save the quantities of flocculant (polymer) to be used compared to the prior art in which the waters to be clarified contain adsorbent material. Indeed, this material aggregates with the polymer. In its absence there is therefore a need for less polymer.
    Also according to a variant, said step of clarifying by coagulation-flocculation-settling also comprises a step of injecting a ballast to ballast the formed flocs, a step of treating said sludge to extract most of the ballast they contain and a step of recycling it in said clarification step, said sludge not containing granular adsorbent material. The invention also relates to an installation for implementing the method according to the invention characterized in that it comprises: a contact tank provided with means for supplying water, means for discharging water by overflow and agitation means, said contact tank accommodating a mixture of water to be treated and adsorbent granular material; clarification means connected to said overflow means; characterized in that said adsorbent material consists of agglomerates of activated carbon particles, said agglomerates having an average size of between 200 μm and 600 μm and a specific surface area of between 800 and 1000 mVg; in that it includes a sieve installed in the upper part of said contact tank, said sieve comprising a layer of porous material having a thickness of between 1 and 5 mm, said material having a cutoff threshold of between 100 μm and 200 μm; pm; in that said tank has a bottom hopper-shaped portion, the end of said hopper being provided with purge means; in that said means for agitating said contact tank are designed to be able to stir the contents of the upper part of said contact tank without agitating the contents of the hopper-shaped lower part.
    In such an installation, the physical characteristics of the layer of porous material used to form the sieve allow it to fulfill its function of retaining the granular adsorbent material within the contact tank while not retaining the material. organic non-adsorbed on it. This sieve therefore passes the turbidity of the water while preventing the granular material to gain the means of clarification.
    The small thickness of this layer, namely between 1 mm and 5 mm, allows in particular to avoid a filtration in its mass.
    The hopper shape of the lower part of the contact tank makes it possible to promote the migration of the granular material used in this part and its extraction by the purge means provided at its end.
    Preferably, the porous material used to form the sieve is a high density polyethylene (HDPE). Such a material has the advantage of being approved for food applications and also of very well to withstand chemical reagents in the exceptional case where they should be used to clean the sieve.
    According to an advantageous variant, the layer of porous material which forms the screen is organized into a structure in the form of a tube or box, the filtration being effected from the outside towards the inside of the tube or the box, the said means being evacuation of said contact tank being connected to the inside of the tube or the box. Such tubes or boxes have the advantage of being commercially available and can easily be replaced.
    Also, according to a variant of the invention said stirring means of said contact tank include a blade rotor mounted vertically movable therein and means for varying the rotational speed of said rotor and means for making vary the vertical position of the rotor in said contact tank. Such means are preferential means so that, according to the method of the invention, the contents of said contact tank are only partially agitated so as to create a concentration gradient of said adsorbent material within it, the bottom said contact tank constituting a non-agitated zone.
    Although the installation according to the present invention may include various means of clarification, said installation preferably comprises coagulant injection means in a coagulation zone and flocculant injection means in a flocculation zone for coagulation clarification. -floculation-settling.
    Preferably, it also comprises means for injecting a ballast into said flocculation zone and advantageously means for extracting the sludges from said clarification means connected to means for treating said sludge so as to extract most of the ballast they contain and means of distribution of the ballast extracted in said flocculation zone.
    List of Figures The invention, as well as the various advantages that it presents, will be better understood thanks to the following description of a nonlimiting embodiment thereof, with reference to the drawings in which: FIG. 1 is a schematic view of an installation according to the invention; FIG. 2 represents a graph indicating the NTU turbidity of a water before and after treatment according to the method of the invention in the installation represented in FIG. 1; FIG. 3 represents a graph indicating the UV absorbance at 254 nm of a water before and after treatment according to the process of the invention in the installation represented in FIG.
    Embodiment of an installation according to the invention
    In relation with FIG. 1, an embodiment of an installation according to the invention is presented.
    Such a water treatment plant comprises a raw water supply line to be treated 1 which arrives in a zone 2 for bringing this water into contact with an adsorbent material.
    On the water supply pipe 1, a pre-filter 13 consisting of metal mesh is provided. This pre-filter has, in the present embodiment, a cut-off threshold of 1 mm.
    The adsorbent granular material consists of agglomerates of activated carbon particles and is marketed by CHEMVIRON under the name Microsorb® 400 R. These agglomerates have an average size of between 200 .mu.m and 600 .mu.m, and a d iodine greater than 800 mg / g. Their specific surface (N 2, BET method) is 900 mVg. This granular adsorbent material is regenerable thermally. This material can be brought into the contact tank 21 by means such as a distributor 23.
    The pre-contact zone 2 is delimited by the walls of a contact tank 21 having a hopper-shaped bottom portion 21a whose lower end is equipped with purge means 21b. This contact tank 21 houses stirring means comprising a stirrer with blades 22 whose rotational speed can be adapted by means of a motor 22a. Means 22b also make it possible to adjust the height of the stirrer in the contact tank 21.
    The contact tank 21 communicates, in an upper part, with a coagulation zone 3. At this level, there is provided a screen 9 constituted by a tube structure made of a layer of thickness equal to 1 mm of a porous material made of high density polyethylene (HDPE) having a porosity of 150 μm. This sieve makes it possible to filter the water passing from the contact zone 2 to the coagulation zone 3. It is equipped with an air supply ramp 9a passing through the tubular structure allowing, when necessary, to send water air on the porous material to clean it effectively.
    The coagulation zone 3 is delimited by the contours of a coagulation tank 31 which houses an agitator 32 controlled by a motor 32a. Injection means, such as an injector 33, allow the injection of a coagulating reagent, in this case ferric chloride, into the coagulation zone 3, in the present embodiment at a rate of 20 ppm. This coagulation zone 3 communicates in a lower part with a weighted flocculation zone 4.
    This weighted flocculation zone 4 is delimited by the contours of a flocculation tank 41 which houses an agitator 42 controlled by a motor 42a. Injection means, such as an injector 43, allow the injection of at least one flocculating reagent, in this case an anionic polymer, into the weighted flocculation zone, in the present embodiment at a rate of 0. , 2 ppm. Injection means 45 also make it possible to introduce into the flocculation tank 41 a ballast consisting of an insoluble granular material denser than water, in this case microsand, in the present embodiment at the rate of 4.9 g / m 2. This weighted flocculation zone 4 also houses a flow guide element which comprises a substantially tubular element 44 inside which the stirrer 42 is rotated. The weighted flocculation zone 4 thus constitutes a maturation zone. It communicates in an upper part with a settling zone 5.
    The settling zone 5 is defined by a decanter 51 provided with inclined slats 52 facilitating and accelerating the settling and a scraper 53 actuated by a motor 54. This settler 51 has an underflow 6 which is connected to an extraction pipe 7 of sludge containing ballast. It also has an overflow 8 for the evacuation of treated water.
    A pipe 19 and withdrawal means, including a pump 10, allow the delivery of this mixture to the inlet of a hydrocyclone 11. The hydrocyclone 11 has an underflow which allows the delivery of a mixture of ballast and a small amount of sludge to the injection means 45. This underflow is connected to service water injection means 18. This allows the injection of a mixture of ballast and diluted sludge in the zone 4. It also has an overflow which is connected to a pipe 12 which allows the evacuation of sludge removed from their ballast for treatment to dehydrate and hygienize.
    According to the invention, the installation has no means of recycling in situ said granular adsorbent material, which is confined in the contact tank 21.
    Example of a water treatment process according to the invention
    A water treatment method according to the invention will now be described in connection with the installation shown in FIG.
    Such a method consists in channeling water to be treated in line 1 through line 1, after having filtered through the pre-filter 13, in which it is brought into contact with the granular adsorbent material indicated below. above, at the rate of 75 mg of material per liter of water. This concentration will vary depending on the load of water to be treated organic matter and pollutants. Such a concentration makes it possible to adsorb some of the organic matter and pollutants contained in the water.
    According to the invention, the content of the contact tank 21 is agitated only in its middle and upper part by the agitator 22. For this purpose, the motor 22a and the means 22b for adjusting the height of the agitator in the tank are actuated so as to create a concentration gradient of said adsorbent material within the contact tank 21, the bottom of said tank constituting a non-agitated zone to which migrates, due to its increasing density, the granular material adsorbent as it is loaded with organic matter and pollutants.
    After a sufficient contact time, the mixture of water and adsorbent granular material is introduced into the coagulation tank 31 by passing through the screen 9 in order to retain the adsorbent granular material in the contact tank 21 while allowing its turbidity to pass .
    In the coagulation tank 31, the coagulating reagent is mixed with water. After a sufficient contact time, the mixture of water and coagulating reagent passes into the weighted flocculation zone 4 delimited by the flocculation tank 41. This mixture meets therein the flocculating reagent introduced by the implementation of the injection means. 43, and micro-sand introduced through the injection means 45.
    The implementation of flow guide 44 allows the creation of dynamic phenomena that generate water movements represented by arrows A. After maturation, the mixture from the weighted flocculation zone 4 passes into the settling zone 5 delimited by the Decanter 51. The sludge containing ballast is extracted in underflow 6 of the settling tank 51 by means of the pipe 7. The treated water is collected in overflow 8 thereof.
    The sludge is recirculated to the inlet of the hydrocyclone 11 by means of the pipe 19 and the pump 10.
    The ballast is separated inside the hydrocyclone 11 from the rest of the sludge. It is extracted underflow and poured into the weighted flocculation zone 4. The rest of the sludge extracted overflow of the hydrocyclone 11 is evacuated.
    According to the invention, used adsorbent granular material is withdrawn from the contact tank 21 by the purge means 21b. This used material is drained and packaged in barrel which once filled can be routed to a thermal regeneration unit of the adsorbent material. A renewal rate of 20 g / m 2 is thus implemented.
    Thanks to the screen 9, the granular adsorbent material is retained in the contact tank 21 and does not migrate in the equipment located downstream thereof or, a fortiori, in the treated water. The operation of these equipment is thus facilitated and the risk of finding granular material in the treated water almost non-existent. Moreover, the quantity of sludge produced at the outlet of the settling tank is decreased and the action of the flocculant optimized. The energy required for recycling and treating these sludges from the decanter is also reduced. The quantities of sludge extracted from the hydrocyclone and to be treated are also less. The invention makes it possible to effectively and stably reduce the NTLI turbidity of the treated water as can be seen in FIG. 2. In practice, during the tests, the results of which are given in this figure, an average reduction of 92% of the turbidity. The invention also makes it possible to effectively cut down the organic matter contained in the treated water as can be seen in FIG. 3. In practice, during the tests, the results of which are given in this figure, an abatement was observed. average of 86% of the UV absorbance at 254 nm of the treated water, representative of its content of organic matter.
    权利要求:
    Claims (15)
    [1" id="c-fr-0001]
    A method of treating water with a view to reducing the content of organic matter and pollutants, said method comprising: a step of contacting water to be treated with a granular adsorbent material in a contact tank provided with stirring means; followed by a step of clarifying water from said tank leading to obtaining clarified water and sludge; characterized in that said granular adsorbent material consists of agglomerates of activated carbon particles, said agglomerates having a mean size of between 200 μm and 600 μm and a specific surface area of between 800 and 1000 mVg, said granular adsorbent material being regenerable by thermal pathway; said waters are screened out of said tank, before being subjected to clarification, in order to retain said adsorbent granular material within said tank while not retaining the non-adsorbed organic material on said adsorbent material, and in that the content of said contact tank is only partially agitated so as to create a concentration gradient of said adsorbent material within it, the bottom of said contact tank constituting a non-agitated zone; spent adsorbent granular material being continuously or intermittently purged from said non-agitated zone of said contact tank for freshly regenerated thermally, and replaced with fresh adsorbent granular material.
    [2" id="c-fr-0002]
    2. Method according to claim 1 characterized in that the contact time of the adsorbent material with the water in said contact tank is between 5 min and 20 min.
    [3" id="c-fr-0003]
    3. Method according to claim 1 or 2 characterized in that the used adsorbent granular material is purged and replaced by new adsorbent granular material so as to maintain a mean concentration of said adsorbent material in said contact tank.
    [4" id="c-fr-0004]
    4. Method according to any one of claims 1 to 3 characterized in that it comprises a preliminary step of pre-filtering the water to be treated before entering said reactor on a pre-filter having a cutoff threshold between 1 and 5 mm.
    [5" id="c-fr-0005]
    5. Method according to any one of claims 1 to 4 characterized in that it comprises periodic steps of cleaning said sieve by a cleaning process selected from the group consisting of a backwashing process and a cleaning method by air insufflation.
    [6" id="c-fr-0006]
    6. Method according to any one of claims 1 to 5 characterized in that said clarification step comprises a step of coagulation of said water to be treated producing coagulated water, a flocculation step of said coagulated water producing flocculated water, a decanting step of said flocculated water producing clarified water and sludge; said coagulation, flocculation and decantation steps being conducted in the absence of granular adsorbent material.
    [7" id="c-fr-0007]
    7. Method according to claim 6 characterized in that said clarification step comprises a step of injecting a ballast, a step of treating said sludge to extract most of the ballast they contain and a step of recycling it in said clarification step, said sludge not containing granular adsorbent material.
    [8" id="c-fr-0008]
    8. Installation for carrying out the method according to any one of claims 1 to 7 characterized in that it comprises: a contact tank (21) provided with means for supplying (1) water, means overflow water evacuation and stirring means (22), said contact tank (21) receiving a mixture of water to be treated and adsorbent granular material; clarification means connected to said overflow means; characterized in that said adsorbent material consists of agglomerates of activated carbon particles, said agglomerates having an average size of between 200 μm and 600 μm and a specific surface area of between 800 and 1000 mVg; in that it includes a screen (9) installed in the upper part of said tank, said screen comprising a layer of porous material having a thickness of between 1 and 5 mm, said material having a cut-off threshold of between 100 μm and 200 pm; in that said contact tank (21) has a hopper-shaped lower portion (21a), the end of said hopper being provided with bleed means (21b); in that said stirring means (22) of said contact tank (21) are designed to be able to stir the contents of the upper part of said contact tank (21) without shaking the contents of the lower part ( 21a) in the shape of a hopper.
    [9" id="c-fr-0009]
    9. Installation according to claim 8 characterized in that said porous material is a HDPE.
    [10" id="c-fr-0010]
    10. Installation according to claim 8 or 9 characterized in that the layer of porous material forming said screen (9) is organized into a structure in the form of tube or box, the filtration being exerted from the outside to the inside tube or box, said means for discharging said tank being connected to the inside of the tube or the box.
    [11" id="c-fr-0011]
    11. Installation according to one of claims 8 to 10 characterized in that said stirring means (22) of said contact tank (21) include a blade rotor mounted vertically movable therein, means (22a). for varying the rotational speed of said rotor and means (22b) for varying the vertical position of the rotor in said vessel.
    [12" id="c-fr-0012]
    12. Installation according to one of claims 8 to 11 characterized in that it comprises a filter (13) for filtering the water to be treated, provided upstream of said contact tank (21) and having a cutoff threshold between 1 mm and 5 mm.
    [13" id="c-fr-0013]
    13. Installation according to one of claims 8 to 12 characterized in that said installation comprises coagulant injection means (33) in a coagulation zone (3) and flocculant injection means (43) in a zone flocculation (4).
    [14" id="c-fr-0014]
    14. Installation according to claim 13 characterized in that it comprises ballast injection means (45) in said flocculation zone (4).
    [15" id="c-fr-0015]
    15. Installation according to claim 14 characterized in that it includes extraction means (7) of sludge from said clarification means connected to means for treating said sludge to extract the bulk of the ballast they contain and distribution means of the ballast extracted in said flocculation zone (4).
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    同族专利:
    公开号 | 公开日
    EP3231771A1|2017-10-18|
    US20170297940A1|2017-10-19|
    ES2741284T3|2020-02-10|
    DK3231771T3|2019-08-12|
    EP3231771B1|2019-06-12|
    CA2963127A1|2017-10-13|
    FR3050200B1|2018-04-13|
    CN107285419A|2017-10-24|
    引用文献:
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    FR2973794A1|2011-04-11|2012-10-12|Veolia Water Solutions & Tech|CLARIFICATION-TREATED WATER TREATMENT PROCESS COMPRISING AN ADSORPTION OF A CLARIFIED WATER PORTION AND CLARIFICATION OF ADSORBED CLARIFIED WATER MIXTURE AND WATER TO BE PROCESSED|
    FR3022537A1|2014-06-18|2015-12-25|Veolia Water Solutions & Tech|METHOD FOR WATER TREATMENT BY ADSORPTION AND BED FILTRATION OF GRANULAR MATERIAL|
    US3658697A|1970-07-31|1972-04-25|Westvaco Corp|Chemical coagulation of carbon treated waste water|
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    GB1522268A|1975-11-03|1978-08-23|Takeda Chemical Industries Ltd|Liquid purification apparatus|
    DK165090D0|1990-07-09|1990-07-09|Kem En Tec As|CONLOMERATED PARTICLES|
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    FR2868064B1|2004-03-26|2007-01-26|Otv Sa|WATER TREATMENT PLANT COMPRISING A TANK FOR CONTACTING WATER WITH A PULVERULENT REAGENT AND A FLOCCULATING OR COAGULATING REAGENT, AND CORRESPONDING PROCESS|
    WO2006133139A1|2005-06-07|2006-12-14|Baird William E|A filter assembly, bioreactor catch basin and method of using the same|
    JP2007021347A|2005-07-14|2007-02-01|Idemitsu Kosan Co Ltd|Hardly decomposable substance-containing water treatment method|
    US9174865B2|2013-08-28|2015-11-03|Nicola T. Bleggi|Leachate treating system having settling spheres and method for same|
    CN103466768B|2013-09-18|2014-12-10|北京大学|Floc reflux coagulation process for treating biochemical printing and dyeing effluent|
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    CN104445691A|2014-11-28|2015-03-25|北京赛诺水务科技有限公司|Circulating powdered activated carbon and ultrafiltration combined water treatment system and application thereof|
    CN105417615A|2015-11-26|2016-03-23|中国矿业大学|Powdered activated carbon adsorption device achieving intermittent operation|CN108083491A|2017-11-23|2018-05-29|湖南望隆企业管理咨询有限公司|A kind for the treatment of of domestic sewage advanced device|
    CN108383280B|2018-03-19|2020-11-03|新沂市新南环保产业技术研究院有限公司|River sewage treatment process|
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    CN109317126A|2018-12-10|2019-02-12|上海活性炭厂有限公司|A kind of Regenevating Waste Activated Carbon system|
    CN110743198A|2019-11-05|2020-02-04|邳州富通生物制品有限公司|Plant extract product decoloration device|
    CN111804090A|2020-07-14|2020-10-23|芜湖良仕机械科技有限公司|Spray type dust removal device|
    法律状态:
    2017-03-21| PLFP| Fee payment|Year of fee payment: 2 |
    2017-10-20| PLSC| Publication of the preliminary search report|Effective date: 20171020 |
    2018-03-16| PLFP| Fee payment|Year of fee payment: 3 |
    2019-04-30| PLFP| Fee payment|Year of fee payment: 4 |
    2020-04-29| PLFP| Fee payment|Year of fee payment: 5 |
    2022-01-07| ST| Notification of lapse|Effective date: 20211205 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1653262A|FR3050200B1|2016-04-13|2016-04-13|PROCESS FOR WATER TREATMENT BY ADSORPTION ON ACTIVE CHARCOAL AND CLARIFICATION, AND CORRESPONDING INSTALLATION.|
    FR1653262|2016-04-13|FR1653262A| FR3050200B1|2016-04-13|2016-04-13|PROCESS FOR WATER TREATMENT BY ADSORPTION ON ACTIVE CHARCOAL AND CLARIFICATION, AND CORRESPONDING INSTALLATION.|
    DK17164456.0T| DK3231771T3|2016-04-13|2017-04-03|PROCEDURE FOR TREATING WATER BY ADSORPTION ON ACTIVE COAL AND CLEANING AND SIMILAR PLANT|
    CA2963127A| CA2963127A1|2016-04-13|2017-04-03|Method for a treatment of water by adsorption on active carbon and clarification, and corresponding plant|
    ES17164456T| ES2741284T3|2016-04-13|2017-04-03|Water treatment procedure by adsorption on activated carbon and clarification, and corresponding installation|
    EP17164456.0A| EP3231771B1|2016-04-13|2017-04-03|Water treatment process by adsorption in activated carbon and clarification, and corresponding installation|
    US15/486,366| US20170297940A1|2016-04-13|2017-04-13|Method for a treatment of water by adsorption on active carbon and clarification, and corresponding plant|
    CN201710237902.0A| CN107285419A|2016-04-13|2017-04-13|Pass through the method for treating water and corresponding factory of active carbon adsorption and purification|
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