FR2859634A1 - Method of eliminating legionella bacteria from hot water systems using a cartridge partially filled with granules consisting of activated silica and iron and manganese oxide particles - Google Patents

Method of eliminating legionella bacteria from hot water systems using a cartridge partially filled with granules consisting of activated silica and iron and manganese oxide particles Download PDF

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FR2859634A1
FR2859634A1 FR0310841A FR0310841A FR2859634A1 FR 2859634 A1 FR2859634 A1 FR 2859634A1 FR 0310841 A FR0310841 A FR 0310841A FR 0310841 A FR0310841 A FR 0310841A FR 2859634 A1 FR2859634 A1 FR 2859634A1
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FR2859634B1 (en
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Du Laz Olivier Jegou
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WATER TREAT INTERNAT Ltd
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/16Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using chemical substances
    • A61L2/23Solid substances, e.g. granules, powders, blocks, tablets
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/281Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F5/00Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
    • C02F5/02Softening water by precipitation of the hardness
    • C02F5/025Hot-water softening devices
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F5/00Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
    • C02F5/08Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
    • C02F5/083Mineral agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/32Manganese, technetium or rhenium
    • B01J23/34Manganese
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/745Iron
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/06Halogens; Compounds thereof
    • B01J27/138Halogens; Compounds thereof with alkaline earth metals, magnesium, beryllium, zinc, cadmium or mercury
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/31Density
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/40Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/725Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/02Non-contaminated water, e.g. for industrial water supply
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/02Non-contaminated water, e.g. for industrial water supply
    • C02F2103/023Water in cooling circuits
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/42Nature of the water, waste water, sewage or sludge to be treated from bathing facilities, e.g. swimming pools
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • C02F2201/006Cartridges
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/04Disinfection

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Organic Chemistry (AREA)
  • Water Supply & Treatment (AREA)
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  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

A method of continuous elimination of aerobic bacteria, especially amoebae and legionella in a pH neutral medium in hot water circuits by passing the water through a cartridge containing a catalytic mass consisting of granules capable of rubbing against one another by the action of the water flow consisting of anionic activated silica compounds and metal particles especially of iron oxide and manganese oxide bearing opposing electromagnetic charges. The dipolarization leads to the contraction of the calcium and bicarbonates present in the flow of water in colloidal form and the formation of minute seeds of cationic calcium carbonate which attract small particles of silica detached from the granules by the rubbing action to form around them an anionic belt capable of absorbing in its turn the cations, especially calcium cations present in the water penetrating the bacterial cells by electromagnetic attraction.

Description

La présente invention concerne un procédé permettant l'élimination enThe present invention relates to a method for the elimination of

continu de bactéries aérobies notamment d'amibes et de légionelles en milieu pH neutre dans des circuits d'eau chaude sanitaire individuels ou collectifs et le détartrage simultané de ces circuits.  continuous aerobic bacteria including amoebae and legionella in neutral pH medium in individual or collective domestic hot water circuits and the simultaneous descaling of these circuits.

Dans de nombreuses régions les eaux brutes sont chargées en sels notamment de calcium et ont une teneur importante en ions bicarbonates HCO3- (eaux calcaires ou dures) qui, dans certaines conditions, notamment suite à une élévation de température, ont tendance à précipiter sous forme de carbonate de calcium très peu soluble, qui constitue le tartre.  In many regions the raw water is loaded with salts including calcium and have a high content of bicarbonate ions HCO3- (limestone or hard water) which, under certain conditions, especially following a rise in temperature, tend to precipitate in form calcium carbonate very little soluble, which is the scale.

Parallèlement à cet inconvénient, les circuits d'eau chaude sanitaire peuvent donner lieu à la prolifération de bactéries aérobies telles que les amibes et les légionelles pouvant être très dangereuses pour la santé.  In addition to this drawback, domestic hot water circuits can lead to the proliferation of aerobic bacteria such as amoebae and legionella that can be very dangerous for health.

En effet, les installations d'eau chaude sanitaire sont équipées de chaudières élevant la température de l'eau à des valeurs moyennes de 30 à 45 C.  Indeed, domestic hot water installations are equipped with boilers raising the temperature of the water to average values of 30 to 45 C.

Or, à cette température, les bactéries présentes dans l'eau, notamment les amibes et les légionelles peuvent se développer très rapi- dement, faisant ainsi faire courir de réels dangers aux usagers.  However, at this temperature, the bacteria present in the water, in particular amoebae and legionellae, can develop very rapidly, thus making the users run a real risk.

Les spécialistes savent, en particulier qu'à partir du seuil de 106u.f.c. (unités de formation de colonies) par litre d'eau, les légionelles peuvent envahir les cellules humaines macrophages, c'est-à-dire les cellules sanguines destinées à détruire les intrus, et neutraliser celles- ci en se multipliant, ce qui provoque finalement leur destruction.  Specialists know, especially that from the threshold of 106u.f.c. (colony forming units) per liter of water, Legionella can invade human macrophage cells, ie blood cells intended to destroy intruders, and neutralize them by multiplying, causing finally their destruction.

Les amibes véhiculent les légionelles, dont le caractère nocif n'est plus à démontrer: en effet ces bactéries ont la faculté particulière de survivre à l'intérieur de certains unicellulaires eucaryotes en tant que parasites intracellulaires.  Amoebae carry legionella, the harmful nature of which is well established: in fact, these bacteria have the particular ability to survive within certain unicellular eukaryotes as intracellular parasites.

Les légionelles ont en outre la particularité d'avoir une nidification très rapide, de l'ordre de 4 heures in vivo.  Legionellae also have the particularity of having a very fast nesting, of the order of 4 hours in vivo.

Pour stopper ces proliférations bactériennes, on a proposé d'effectuer des injections de chlore, accompagnées de chocs thermiques réguliers à 70 .  To stop these bacterial proliferations, it has been proposed to perform chlorine injections, accompanied by regular thermal shocks to 70.

Toutefois, les légionelles, qui sont des saprophytes gram-négatives (c'est-à-dire disposant d'une paroi cellulaire complexe et d'une deuxième membrane phospholipidique extérieure) sont protégées contre les agressions du chlore par les amibes à l'intérieur desquelles elles vivent.  However, legionellae, which are gram-negative saprophytes (ie having a complex cell wall and a second outer phospholipid membrane) are protected against chlorine attack by amoebae inside. which they live.

Par suite, quand les injections de chlore sont arrêtées, des colonies de légionelles réapparaissent rapidement, vu que leur habitat protecteur n'a pas été touché par le chlore.  As a result, when chlorine injections are stopped, legionella colonies quickly reappear, as their protective habitat has not been affected by chlorine.

Il est par ailleurs à noter que de telles injections de chlore accompagnées de chocs thermiques sont dangereuses pour les canalisations ainsi que pour les usagers, et en outre coûteuses en thermies, sauf si l'on met en oeuvre des appareils de récupération de chaleur informatisés mais très onéreux et sophistiqués, donc susceptibles de tomber en panne.  It should also be noted that such injections of chlorine accompanied by thermal shocks are dangerous for the pipes as well as for the users, and moreover expensive in thermics, except if computerized heat recovery apparatuses are used but very expensive and sophisticated, so likely to fail.

Pour détruire les bactéries présentes dans les circuits d'eau io chaude, on a également déjà proposé, des procédés cuivre - argent qui présentent toujours un danger de surdosage supérieur aux normes européennes et sont en outre sans effet sur des circuits entartrés.  To destroy the bacteria present in the hot water circuits, it has also been proposed, copper-silver processes which always present a danger of overdose higher than European standards and also have no effect on scaled circuits.

La présente invention a pour objet de remédier à ces inconvénients en proposant un procédé permettant d'éliminer en continu des bactéries aérobies, notamment des amibes et des légionelles en milieu pH neutre dans des circuits d'eau chaude sanitaire, sans chlore ni choc thermique, et permettant d'obtenir simultanément un détartrage de ces circuits.  The object of the present invention is to remedy these drawbacks by proposing a method for the continuous elimination of aerobic bacteria, in particular amoebae and legionella in neutral pH medium, in domestic hot water circuits, without chlorine or thermal shock, and to simultaneously obtain a descaling of these circuits.

Selon l'invention, ce procédé est caractérisé en ce que l'on fait passer en continu le flux d'eau circulant dans le circuit à traiter au travers d'au moins une cartouche contenant une masse catalytique constituée par des granulés susceptibles de frotter les uns contre les autres sous l'action du flux d'eau en circulation.  According to the invention, this process is characterized in that the flow of water circulating in the circuit to be treated is continuously passed through at least one cartridge containing a catalytic mass constituted by granules capable of rubbing the against each other under the action of the flow of water in circulation.

Selon l'invention, il est possible de prévoir, soit une cartou- che unique, soit, en particulier pour des installations de plus fort débit plusieurs cartouches montées en série de manière à augmenter l'efficacité du procédé.  According to the invention, it is possible to provide either a single cartridge or, particularly for higher throughput installations, several cartridges mounted in series so as to increase the efficiency of the process.

Les granulés constituant la masse catalytique sont d'une part essentiellement composés de silice activée anionique Si3O12 et renferment d'autre part des particules métalliques, de préférence des particules d'oxyde de fer et des particules d'oxyde de manganèse polarisées portant des charges électromagnétiques de signe contraire.  The granules constituting the catalytic mass are on the one hand essentially composed of anionic Si 3 O 12 activated silica and on the other hand contain metal particles, preferably iron oxide particles and polarized manganese oxide particles carrying electromagnetic charges. of opposite sign.

La présence de ces particules métalliques crée, au sein de la masse catalytique une dipolarisation de nature à provoquer la contraction du calcium et des bicarbonates présents dans le flux d'eau en circulation, essentiellement sous forme colloïdale, et par suite la formation de minuscules germes de carbonate de calcium cationiques.  The presence of these metal particles creates, within the catalytic mass, a dipolarization likely to cause the contraction of calcium and bicarbonates present in the flow of circulating water, mainly in colloidal form, and consequently the formation of tiny seeds. cationic calcium carbonate.

Lors de leur formation et de leur passage à travers la masse catalytique, ces germes attirent des petites particules de silice qui se détachent des granulés sous l'action de leur frottement les uns contre les autres pour former une ceinture anionique autour de ces germes.  During their formation and passage through the catalytic mass, these seeds attract small silica particles which are detached from the granules under the action of their friction against each other to form an anionic belt around these germs.

Cette ceinture anionique est à son tour susceptible d'absorber les cations rencontrés, et en particulier les cations, notamment les ions calcium renfermés dans l'eau pénétrant dans les cellules bactériennes présentes dans le flux d'eau circulant dans le circuit à traiter, ce par attraction électromagnétique.  This anionic belt is in turn capable of absorbing the cations encountered, and in particular the cations, in particular the calcium ions contained in the water penetrating into the bacterial cells present in the flow of water flowing in the circuit to be treated. by electromagnetic attraction.

Les germes ainsi revêtus d'une ceinture de silice ont en effet un pouvoir séquestrant très fort vis-à-vis des cations rencontrés.  The seeds thus coated with a silica belt have in fact a very strong sequestering power vis-à-vis the cations encountered.

Par suite on observe au sein du flux d'eau en circulation une croissance rapide de cristaux expansés très légers consécutive à l'incorporation continue de cations dans leur structure cristalline.  As a result, there is observed within the circulating water flow a rapid growth of very light expanded crystals resulting from the continuous incorporation of cations into their crystalline structure.

Ces cristaux qui ont à l'origine une structure hexagonale de type grenat à six pans s'allongent au cours de leur développement pour devenir orthorhombiques.  These crystals, which originally have a six-sided garnet-like hexagonal structure, lengthen during their development to become orthorhombic.

Il est ainsi possible d'éliminer rapidement le tartre suite au développement rapide de cristaux expansés et légers non incrustants du fait de l'incorporation continue d'ions calcium dans la structure cristalline de ces cristaux.  It is thus possible to quickly eliminate scale because of the rapid development of non-incrusting expanded and light crystals due to the continuous incorporation of calcium ions into the crystal structure of these crystals.

Ces cristaux, très légers et très expansés ne peuvent en effet pas se déposer sur les parois des canalisations et au fond des chauffe-eau et des chaudières, et peuvent être éliminés par simple rinçage.  These crystals, very light and very expanded can not indeed be deposited on the walls of the pipes and the bottom of the water heaters and boilers, and can be eliminated by simple rinsing.

L'avantage essentiel du procédé, conforme à l'invention, est toutefois lié au fait qu'il permet d'éliminer en continu les bactéries aérobies et notamment les amibes et les légionelles présentes dans le flux d'eau en circulation dans le circuit à traiter.  The essential advantage of the process according to the invention is, however, linked to the fact that it makes it possible to continuously eliminate aerobic bacteria, and in particular amoebae and legionella present in the flow of water circulating in the circulating circuit. treat.

Les amibes sont en effet des bactéries de structure protéini- que constituées de cellules déformables extrêmement élastiques.  Amoebae are in fact proteinaceous structure bacteria consisting of extremely elastic deformable cells.

Tout durcissement des parois et tout blocage des membranes de ces cellules leur enlève la possibilité de se mouvoir et de se nourrir par phagocytage.  Any hardening of the walls and any blockage of the membranes of these cells removes the ability to move and feed by phagocytion.

Or, l'eau entrant dans l'amibe avec des éléments en décom- position (algues et particules végétales de toute sorte) véhicule des cris- taux constitués par des germes cationiques entourés d'une ceinture de silice S13O12 anionique qui absorbent le calcium présent dans ces résidus et font obstacle au mécanisme de fonctionnement de l'amibe suite à l'accumulation d'amas calcaires dans son corps interne.  However, the water entering the amoeba with decomposing elements (algae and plant particles of all kinds) carries crystals consisting of cationic seeds surrounded by an anionic S13O12 silica belt which absorb the calcium present. in these residues and hinder the mechanism of operation of the amoeba following the accumulation of limestone clusters in its internal body.

En conséquence, celle-ci éclate par manque d'élasticité.  As a result, it bursts for lack of elasticity.

En effet, la salinité de l'amibe augmentant par rapport à celle du milieu aquatique environnant, celle-ci ne peut plus compenser les différences de pression et se fend en multiples morceaux d'où sa destruction.  Indeed, the salinity of the amoeba increases compared to that of the surrounding aquatic environment, it can no longer compensate for differences in pressure and splits into multiple pieces from where its destruction.

Les légionelles, qui comme il a déjà été indiqué vivent sans dommage à l'intérieur de la plupart des espèces d'amibes, utilisent quant o à elles dans leur métabolisme des acides aminés tels que la cystéine, en combinaison avec certains oligo-éléments dont le calcium mêlé à du fer et à du magnésium, c'est-à-dire des cations attirés par les silices anioniques ceinturant les germes se formant dans le flux d'eau circulant dans le circuit à traiter.  Legionellae, which, as already mentioned, live harmlessly in most amoeba species, use in their metabolism amino acids such as cysteine, in combination with certain trace elements of which calcium mixed with iron and magnesium, that is to say cations attracted by the anionic silicas surrounding the germs forming in the flow of water circulating in the circuit to be treated.

Par suite, les cations tels que le calcium et le magnésium dont se' nourrissent les légionelles, par le biais de l'eau pénétrant dans les amibes se trouvent incorporés dans des structures stables.  As a result, cations such as calcium and magnesium which are fed legionella, through the water entering the amoeba are incorporated into stable structures.

La croissance des légionelles est donc ainsi stoppée et les colonies sont rapidement anéanties par manque des conditions nécessai-20 res à leur reproduction.  The growth of Legionella is thus halted and the colonies are quickly destroyed by lack of the necessary conditions for their reproduction.

Le procédé conforme à l'invention, permet par suite d'éliminer efficacement en continu deux variétés de bactéries aérobies à savoir d'une part les légionelles, qui sont très dangereuse pour l'homme, et d'autre part, les amibes qui sont moins nocives, mais véhiculent les lé- gionelles tout en les protégeant.  The process according to the invention thus makes it possible to effectively and efficiently remove two varieties of aerobic bacteria, namely legionella, which is very dangerous for humans, and amoebae which are less harmful, but convey the legions while protecting them.

L'efficacité toute particulière du procédé conforme à l'invention est essentiellement liée à la proportion très importante de silice dans la masse catalytique.  The very particular efficiency of the process according to the invention is essentially related to the very large proportion of silica in the catalytic mass.

Cette proportion permet en effet, grâce à l'action conjuguée de métaux de signe contraire, la formation quasi instantanée, autour de germes cationiques, d'éléments anioniques ayant un très fort pouvoir séquestrant vis-à-vis de tous les cations rencontrés.  This proportion makes it possible, thanks to the combined action of metals of opposite sign, almost instantaneous formation, around cationic seeds, of anionic elements having a very high sequestering power with respect to all the cations encountered.

Selon l'invention, les granulés constituant la masse catalytique peuvent avantageusement renfermer entre 80 et 95 %, de préférence 35 environ 90 % de silice activée en proportion volumétrique.  According to the invention, the granules constituting the catalytic mass may advantageously contain between 80 and 95%, preferably approximately 90% of activated silica in volumetric proportion.

Conformément à l'invention, on a pu obtenir des résultats particulièrement satisfaisants en mettant en oeuvre une masse catalytique ayant une densité apparente d'environ 1,00 correspondant à une masse d'environ 1000 kg/m3 et se présentant sous forme de billes dures et homogènes régulièrement calibrées de 1,5 à 2 mm de diamètre.  According to the invention, it has been possible to obtain particularly satisfactory results by using a catalytic mass having a bulk density of about 1.00 corresponding to a mass of about 1000 kg / m 3 and being in the form of hard balls. and homogeneous regularly calibrated 1.5 to 2 mm in diameter.

A titre d'exemple, on peut utiliser à cet effet des billes catalytiques qui sont actuellement proposées sur le marché pour le traitement s d'eaux ferrugineuses exemptes de calcaire et renferment essentiellement les composés suivants: Fe2O3, CaC12 et Ca3Mn2Si3O12.  By way of example, it is possible to use for this purpose catalytic beads which are currently on the market for the treatment of ferruginous waters free of limestone and essentially contain the following compounds: Fe2O3, CaCl2 and Ca3Mn2Si3O12.

Selon une autre caractéristique de l'invention, on fait circuler le flux d'eau à traiter de haut en bas dans la cartouche contenant la masse catalytique.  According to another characteristic of the invention, the flow of water to be treated from top to bottom is circulated in the cartridge containing the catalytic mass.

Ce flux d'eau peut également sans pour cela sortir du cadre de l'invention circuler de bas en haut dans la cartouche, en particulier si celle-ci est installée dans un corps de filtre à entrée d'eau centrale et à sortie par diffusion latérale.  This flow of water can also, without departing from the scope of the invention, circulate upwardly in the cartridge, in particular if it is installed in a filter body having a central water inlet and a diffusion outlet. lateral.

Selon une autre caractéristique de l'invention, la cartouche 15 n'est que partiellement remplie de granulés, ce de préférence environ aux 2/3 de sa hauteur.  According to another characteristic of the invention, the cartridge 15 is only partially filled with granules, preferably about 2/3 of its height.

Cette cartouche peut avantageusement avoir une configuration essentiellement similaire à celle de la première cartouche de l'installation décrite dans le document FR-2 700 324, c'est-à-dire être constituée par un cylindre notamment en un matériau synthétique ayant environ 20 cm de hauteur et 7 cm de diamètre monté à la partie médiane d'un récipient notamment en matière synthétique équipé d'une ouverture latérale supérieure d'entrée de façon à définir à sa périphérie un manchon recevant l'eau à traiter.  This cartridge may advantageously have a configuration substantially similar to that of the first cartridge of the installation described in the document FR-2 700 324, that is to say be constituted by a cylinder, in particular a synthetic material having about 20 cm height and 7 cm in diameter mounted at the middle portion of a container including synthetic material equipped with an upper inlet opening side so as to define at its periphery a sleeve receiving the water to be treated.

Une telle cartouche peut ainsi être munie à sa partie inférieure d'un orifice d'entrée du flux d'eau en circulation et à sa partie supérieure d'un orifice de sortie central.  Such a cartridge can thus be provided at its lower part with an inlet for the circulating water flow and at its upper part with a central outlet orifice.

En remontant pour sortir par l'orifice supérieur central de la cartouche, le flux d'eau en circulation passe au travers des granulés qui peuvent avantageusement être enveloppés dans un filet à mailles très souples non serrées permettant la libre circulation des granulés et leur frottement les uns contre les autres sous l'action du flux d'eau.  Going upwards to exit through the central upper orifice of the cartridge, the flow of circulating water passes through the granules which can advantageously be wrapped in a mesh with very flexible loosely mesh allowing the free circulation of the granules and their friction. against each other under the action of the flow of water.

Il est à cet effet indispensable que la cartouche ne soit pas totalement remplie de granulés.  It is essential for this purpose that the cartridge is not completely filled with pellets.

Claims (8)

REVENDICATIONS 1 ) Procédé d'élimination en continu de bactéries aérobies notamment d'amibes et de légionelles en milieu pH neutre dans des circuits d'eau chaude sanitaire, caractérisé en ce que l'on fait passer en continu le flux d'eau circulant dans le circuit à traiter au travers d'au moins une cartouche contenant une masse catalytique constituée par des granulés susceptibles de frotter les uns contre les autres sous l'action du flux d'eau en circulation, ces granulés étant d'une io part essentiellement composés de silice activée anionique Si3O12 et renfermant d'autre part des particules métalliques, de préférence des parti-cules d'oxyde de fer et des particules d'oxyde de manganèse polarisées portant des charges électromagnétiques de signe contraire, de façon à provoquer, sous l'action de cette dipolarisation, la contraction du calcium et des bicarbonates présents dans le flux d'eau en circulation essentielle-ment sous forme colloïdale, et la formation de minuscules germes de carbonate de calcium cationiques de nature à attirer des petites particules de silice se détachant des granulés sous l'action de leur frottement les uns contre les autres pour former autour de ces germes une ceinture anioni- que susceptible d'absorber à son tour les cations notamment les ions calcium présents dans l'eau pénétrant dans les cellules bactériennes, par attraction électromagnétique.  1) A method for the continuous elimination of aerobic bacteria including amoebae and legionella in a neutral pH medium in domestic hot water circuits, characterized in that the stream of circulating water is continuously passed through the circuit to be treated through at least one cartridge containing a catalytic mass constituted by granules capable of rubbing against each other under the action of the flow of water in circulation, these granules being essentially composed of Si3O12 anionic activated silica and furthermore containing metal particles, preferably iron oxide particles and polarized manganese oxide particles carrying electromagnetic charges of opposite sign, so as to cause, under the action of this dipolarization, the contraction of calcium and bicarbonates present in the flow of circulating water essentially in colloidal form, and the formation of tiny germs They are of cationic calcium carbonate, attracting small particles of silica which become detached from the granules under the action of their friction against each other in order to form around these seeds an anionic belt capable of absorbing, in its turn, the cations including calcium ions present in the water penetrating the bacterial cells, by electromagnetic attraction. 2 ) Procédé selon la revendication 1, caractérisé en ce que les granulés constituant la masse catalytique renferment entre 80 et 95 %, de préférence environ 90 % de silice activée en proportion volumétrique.  2) Process according to claim 1, characterized in that the granules constituting the catalytic mass contain between 80 and 95%, preferably about 90% of activated silica in volumetric proportion. 3 ) Procédé selon l'une quelconque des revendications 1 et 2, caractérisé en ce que les granulés constituant la masse catalytique se présentent sous la forme de billes dures et homogènes régulièrement calibrées de 1,5 à 2 mm de diamètre.  3) Process according to any one of claims 1 and 2, characterized in that the granules constituting the catalytic mass are in the form of hard and homogeneous balls regularly calibrated from 1.5 to 2 mm in diameter. 4 ) Procédé selon l'une quelconque des revendications 1 à 3, caractérisé en ce que la masse catalytique a une densité apparente d'environ 1,00 correspondant à une masse d'environ 1000 kg/m3.  4) Process according to any one of claims 1 to 3, characterized in that the catalytic mass has a bulk density of about 1.00 corresponding to a mass of about 1000 kg / m3. 5 ) Procédé selon l'une quelconque des revendications 1 à 4, caractérisé en ce que les granulés constituant la masse catalytique renferment essentiellement les composés suivants: Fe203, CaCl2 et Ca3Mn2Si3O12.  5) Process according to any one of claims 1 to 4, characterized in that the granules constituting the catalytic mass essentially contain the following compounds: Fe203, CaCl2 and Ca3Mn2Si3O12. 6 ) Procédé selon l'une quelconque des revendications 1 à 5, caractérisé en ce que l'on fait circuler le flux d'eau de haut en bas dans la cartouche contenant la masse catalytique. to  6) Process according to any one of claims 1 to 5, characterized in that it circulates the flow of water from top to bottom in the cartridge containing the catalytic mass. to 7 ) Procédé selon l'une quelconque des revendications 1 à 5, caractérisé en ce que l'on fait circuler le flux d'eau de bas en haut dans la cartouche contenant la masse catalytique.  7) Process according to any one of claims 1 to 5, characterized in that it circulates the flow of water from bottom to top in the cartridge containing the catalytic mass. 8 ) Procédé selon l'une quelconque des revendications 1 à 7, caractérisé en ce que l'on ne remplit que partiellement la cartouche de granulés, de préférence environ aux 2/3 de sa hauteur.  8) Process according to any one of claims 1 to 7, characterized in that it fills only partially the granule cartridge, preferably about 2/3 of its height.
FR0310841A 2003-09-16 2003-09-16 PROCESS FOR THE CONTINUOUS REMOVAL OF AEROBIC BACTERIA, IN PARTICULAR AMIBES AND LEGIONELLES IN PH NEUTRAL MEDIA IN HOT WATER CIRCUITS Expired - Lifetime FR2859634B1 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2168677A1 (en) * 2007-07-13 2010-03-31 Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences Ferrimanganic composite oxide absorbent, method for preparing the same, and method for utilizing the same
EP3847890A4 (en) * 2018-08-29 2022-05-11 HIYOSHI Corporation Disinfectant for legionella bacteria, water treatment method, bathwater additive, and additive for air-conditioning cooling tower water

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GB1063669A (en) * 1963-12-23 1967-03-30 Pall Corp Filter assembly for sterilizing water
US6395172B1 (en) * 1998-08-07 2002-05-28 Calfa Chemical Co., Ltd. Water purifying apparatus

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Publication number Priority date Publication date Assignee Title
GB1063669A (en) * 1963-12-23 1967-03-30 Pall Corp Filter assembly for sterilizing water
US6395172B1 (en) * 1998-08-07 2002-05-28 Calfa Chemical Co., Ltd. Water purifying apparatus

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2168677A1 (en) * 2007-07-13 2010-03-31 Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences Ferrimanganic composite oxide absorbent, method for preparing the same, and method for utilizing the same
EP2168677A4 (en) * 2007-07-13 2011-05-04 Res Ct Eco Environmental Scien Ferrimanganic composite oxide absorbent, method for preparing the same, and method for utilizing the same
US8207087B2 (en) 2007-07-13 2012-06-26 Research Center For Eco-Environmental Sciences, Chinese Academy Of Sciences Method for making ferric and manganese binary oxide based adsorbent
EP3847890A4 (en) * 2018-08-29 2022-05-11 HIYOSHI Corporation Disinfectant for legionella bacteria, water treatment method, bathwater additive, and additive for air-conditioning cooling tower water
US11753318B2 (en) 2018-08-29 2023-09-12 Hiyoshi Corporation Disinfectant against Legionella, method for treating water, additive for bathtub water, and additive for air-conditioning cooling tower water

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