EP1542931A1 - Method and device for reducing production of wastewater treatment station sludge with fixed biological cultures - Google Patents
Method and device for reducing production of wastewater treatment station sludge with fixed biological culturesInfo
- Publication number
- EP1542931A1 EP1542931A1 EP03772377A EP03772377A EP1542931A1 EP 1542931 A1 EP1542931 A1 EP 1542931A1 EP 03772377 A EP03772377 A EP 03772377A EP 03772377 A EP03772377 A EP 03772377A EP 1542931 A1 EP1542931 A1 EP 1542931A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- sludge
- production
- rpb
- reduction
- biological treatment
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 239000010802 sludge Substances 0.000 title claims abstract description 52
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 31
- 238000000034 method Methods 0.000 title claims abstract description 22
- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 8
- 230000008569 process Effects 0.000 claims abstract description 10
- 239000000758 substrate Substances 0.000 claims abstract description 7
- 230000001580 bacterial effect Effects 0.000 claims abstract description 6
- 241000894006 Bacteria Species 0.000 claims abstract description 5
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000005416 organic matter Substances 0.000 claims abstract description 5
- 230000003647 oxidation Effects 0.000 claims abstract description 5
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 5
- 230000002255 enzymatic effect Effects 0.000 claims abstract description 4
- 238000009434 installation Methods 0.000 claims description 14
- 230000009467 reduction Effects 0.000 claims description 14
- 230000009089 cytolysis Effects 0.000 claims description 5
- 238000000746 purification Methods 0.000 claims description 4
- 230000008719 thickening Effects 0.000 claims description 4
- 238000013019 agitation Methods 0.000 claims description 3
- 239000002562 thickening agent Substances 0.000 claims description 2
- 239000010842 industrial wastewater Substances 0.000 abstract description 2
- 238000010907 mechanical stirring Methods 0.000 abstract description 2
- 239000002028 Biomass Substances 0.000 description 12
- 239000002351 wastewater Substances 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000005406 washing Methods 0.000 description 4
- 238000005273 aeration Methods 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000010169 landfilling Methods 0.000 description 2
- 239000011368 organic material Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007515 enzymatic degradation Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1205—Particular type of activated sludge processes
- C02F3/1221—Particular type of activated sludge processes comprising treatment of the recirculated sludge
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/06—Aerobic processes using submerged filters
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Definitions
- the present invention relates to a method and a device ensuring the reduction of the production of sludge from wastewater treatment plants, urban or industrial, by fixed biological cultures.
- RPB sludge
- FIG. 1 of the accompanying drawings there is shown schematically a known installation of this type, comprising, in a loop on an aeration tank, a device for reducing the production of sludge can be an aerobic thermophilic reactor or a partial ozone oxidation unit producing mechanical agitation.
- the reference 1 designates the introduction of the waste water to be treated, the latter passing respectively through an anaerobic zone R, an anoxic zone X, an aerobic zone A, before being treated in a clarifier C.
- the RPB reactor designated as a whole by the reference B, is mounted in parallel and in a loop on the activated sludge treatment installation (C / N / P treatment).
- volume of the station 15,000 m 3
- a fraction of the sludge present in the aeration tank is directed continuously and after any thickening to the device for reducing the production of sludge.
- the quantity of sludge sent daily to the RPB process is equivalent to 1 to 10 times the quantity of sludge produced by the water treatment installation under operating conditions conventional.
- the outlet effluent from the RPB loop is made up of both solubilized compounds in the RPB device and suspended solids. In the example illustrated in FIG. 1, the installation ensures the production of sludge in excess of 600 kg MES / d (ie 80% GWP).
- the present invention takes the opposite of the prior art recalled above, by dissociating the step to reduce sludge production, from step purification, by providing a step of biological treatment of the activated sludge type at low, medium or high load, associated with a step of RPB by thermophilic enzymatic way or by partial oxidation with ozone coupled with a mechanical agitation.
- the source of substrate for bacteria in biological treatment is no longer the organic matter of the wastewater, but the organic matter coming from the lysis of the bacterial cells induced during the RPB stage.
- the present invention also relates to a device for implementing the process specified above, which is in the form of an installation dedicated to the reduction of sludge production associating a device for reducing sludge production (RPB) and a low, medium or high charge biological treatment reactor, the source of substrate for the biological treatment bacteria consists of the organic material originating from the lysis of the bacterial cells induced in the RPB reactor.
- RPB reducing sludge production
- FIG. 2 schematically illustrates an installation implementing the method of the invention.
- this installation takes the form of a platform dedicated to the reduction of sludge production which is associated with an installation for treating waste water by a fixed biomass reactor ( biofilter, for example), designated as a whole by the reference 2.
- This dedicated platform consists of a RPB device, designated as a whole by the reference 3, coupled to a biological treatment, carried out in a reactor designated by the reference 8 and comprising a separation device - thickening 9.
- the organic material originating from the lysis of the bacterial cells induced during the RPB stage constitutes the source of substrate for the biological treatment in the reactor 8.
- the present invention has the advantage of allowing objective measurement of the reduced quantity of sludge.
- the reduction in sludge production is calculated by the difference between the quantity of sludge extracted from the water treatment line (in 6) and the quantity of residual sludge, extracted (in 7) from the dedicated RPB process.
- thermophilic enzymatic reactor 650 m
- Such a device makes it possible to respond to the drawbacks of applying, to biological treatment stations with fixed biomass, RPB methods directly integrated in a loop. It also provides the following advantages: - possibility of adjusting the sludge reduction according to needs (20 to 100% o reduction);
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
- Activated Sludge Processes (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
The invention concerns a method for reducing production of urban or industrial waste water treatment station sludge with fixed biological cultures. The invention is characterized in that it consists in: dissociating the step of reducing sludge production from the purifying step, by providing a step of activated sludge type biological treatment with low, medium or high load, associated with a sludge production reducing step by thermophilic enzymatic process, or by partial ozone oxidation combined, with mechanical stirring, the substrate source for the biological treatment bacteria consisting of the organic matter derived from lyzed bacterial cells induced during the sludge production reducing step.
Description
Procédé et dispositif de Réduction de la Production de Boues des stations de traitement d'eaux résiduaires par cultures biologiques fixées" Method and device for Reducing the Production of Sludge from wastewater treatment plants by fixed organic cultures "
La présente invention a pour objet un procédé et un dispositif assurant la réduction de la production de boues des stations de traitement d'eaux résiduaires, urbaines ou industrielles, par cultures biologiques fixées.The present invention relates to a method and a device ensuring the reduction of the production of sludge from wastewater treatment plants, urban or industrial, by fixed biological cultures.
On sait que l'épuration des eaux résiduaires par voie biologique consiste à utiliser la pollution organique et azotée comme substrat nutritif pour la biomasse épuratrice, ladite pollution carbonée et azotée se transformant en dioxyde de carbone et en azote, tandis que la biomasse prolifère proportionnellement à la quantité de pollution dégradée. L'excédent de biomasse formée constitue ce qu'on nomme couramment les boues biologiques en excès.It is known that the purification of waste water by biological means consists in using organic and nitrogen pollution as a nutritive substrate for the purifying biomass, said carbon and nitrogen pollution transforming into carbon dioxide and nitrogen, while the biomass proliferates in proportion to the amount of pollution degraded. The excess biomass formed constitutes what is commonly called excess biological sludge.
Le traitement et l'évacuation finale de ces boues est un enjeu environnemental et économique majeur. Avec une prévision de production annuelle, en 2002, dé plus de 1 200 000 tonnes de matières sèches par an pour le traitement des eaux usées urbaines en France, et de plus de 10 millions de tonnes pour la Communauté Européenne, on réalise que la gestion de la production et du traitement des boues produites par les stations d'épuration constitue une préoccupation grandissante, amplifiée par les nouvelles contraintes réglementaires, environnementales, sanitaires, économiques, voire politiques et psychologiques.The treatment and final disposal of this sludge is a major environmental and economic issue. With an annual production forecast in 2002 of more than 1,200,000 tonnes of dry matter per year for the treatment of urban wastewater in France, and more than 10 million tonnes for the European Community, we realize that the management of the production and treatment of sludge produced by wastewater treatment plants is a growing concern, amplified by new regulatory, environmental, health, economic, and even political and psychological constraints.
Les techniques classiques pour l'élimination de ces déchets comprennent notamment la mise en décharge, la valorisation agricole et l'incinération. Ces techniques connues présentent toutefois de sérieux inconvénients. C'est ainsi que l'interdiction de mise en décharge des déchets non ultimes, les contraintes sévères (notamment vis-à-vis des métaux lourds et de certains composés organiques suspects) pour la valorisation agricole, la maîtrise des coûts et des risques
de pollution atmosphérique de l'incinération vont peser lourdement sur l'élimination de ces déchets.Conventional techniques for the disposal of this waste include landfilling, agricultural recovery and incineration. These known techniques have serious drawbacks, however. This is how the ban on landfilling of non-ultimate waste, the severe constraints (particularly with regard to heavy metals and certain suspect organic compounds) for agricultural recovery, control of costs and risks of air pollution from incineration will weigh heavily on the elimination of this waste.
Dans ce contexte, on a envisagé des technologies nouvelles, ayant pour objectif une Réduction de la Production de Boues (RPB) des installations de traitement biologique des eaux résiduaires urbaines ou industrielles. Certaines de ces techniques de RPB reposent sur le couplage entre un procédé à boues activées conventionnel et un traitement des boues installé en boucle sur le bassin d'aération. Le traitement associé peut faire appel à des techniques mécanique, chimique, thermique ou biologique et repose souvent sur le couplage de plusieurs de ces techniques.In this context, new technologies have been considered, with the objective of reducing the production of sludge (RPB) from biological treatment facilities for urban or industrial wastewater. Some of these RPB techniques are based on the coupling between a conventional activated sludge process and a sludge treatment installed in a loop on the aeration tank. The associated treatment can call upon mechanical, chemical, thermal or biological techniques and often relies on the coupling of several of these techniques.
On a envisagé de mettre en œuvre une étape de traitement de RPB, par dégradation enzymatique (notamment décrite dans EP-A-924 168) ou par oxydation partielle à l'ozone couplée à une agitation mécanique (selon WO 99/06327), installée en parallèle et en boucle sur le bassin biologique. Ces deux techniques sont très performantes et elles conduisent, pour certains procédés, à des réductions de production de boue significatives dépassant 80%.It has been envisaged to implement a step for treating RPB, by enzymatic degradation (in particular described in EP-A-924 168) or by partial oxidation with ozone coupled with mechanical stirring (according to WO 99/06327), installed in parallel and in a loop on the biological basin. These two techniques are very effective and lead, for certain processes, to significant reductions in sludge production exceeding 80%.
Sur la figure 1 des dessins annexés, on a représenté de façon schématique une installation connue, de ce type, comportant, en boucle sur un bassin d'aération, un dispositif de réduction de la production de boue pouvant être un réacteur thermophile aérobie ou une unité d'oxydation partielle à l'ozone produisant une agitation mécanique. Sur cette figure, la référence 1 désigne l'introduction de l'eau résiduaire à traiter, celle-ci traversant respectivement une zone anaérobie R, une zone anoxie X, une zone aérobie A, avant d'être traitée dans un clarificateur C. Le réacteur de RPB, désigné dans son ensemble par la référence B, est monté en parallèle et en boucle sur l'installation de traitement à boues activées (traitement C/N/P).In Figure 1 of the accompanying drawings, there is shown schematically a known installation of this type, comprising, in a loop on an aeration tank, a device for reducing the production of sludge can be an aerobic thermophilic reactor or a partial ozone oxidation unit producing mechanical agitation. In this figure, the reference 1 designates the introduction of the waste water to be treated, the latter passing respectively through an anaerobic zone R, an anoxic zone X, an aerobic zone A, before being treated in a clarifier C. The RPB reactor, designated as a whole by the reference B, is mounted in parallel and in a loop on the activated sludge treatment installation (C / N / P treatment).
On a donné ci-après un exemple de caractéristiques techniques d'une telle installation connue :An example of the technical characteristics of such a known installation has been given below:
Nombre équivalent habitant : 50 000 eq-Hab Débit quotidien : 7 500 m3/j Production de boues : 3 000 kg-MES/jEquivalent inhabitant number: 50,000 eq-Hab Daily flow: 7,500 m 3 / d Sludge production: 3,000 kg-MES / d
Volume de la station : 15 000 m3
Dans ce procédé, une fraction de la boue présente dans le bassin d'aération est dirigée en continu et après épaississement éventuel vers le dispositif de réduction de la production de boues. En fonction du niveau de réduction de production de boue requis, la quantité de boue envoyée quotidiennement vers le procédé de RPB est équivalente à 1 à 10 fois la quantité de boues produite par l'installation de traitement de l'eau dans les conditions de fonctionnement conventionnelles. L'effluent de sortie de la boucle de RPB est constitué à la fois de composés solubilisés dans le dispositif de RPB et de matières en suspension. Dans l'exemple illustré par la figure 1, l'installation assure une production de boues en excès de 600 kg MES/j (soit 80% RPB).Volume of the station: 15,000 m 3 In this process, a fraction of the sludge present in the aeration tank is directed continuously and after any thickening to the device for reducing the production of sludge. Depending on the level of reduction in sludge production required, the quantity of sludge sent daily to the RPB process is equivalent to 1 to 10 times the quantity of sludge produced by the water treatment installation under operating conditions conventional. The outlet effluent from the RPB loop is made up of both solubilized compounds in the RPB device and suspended solids. In the example illustrated in FIG. 1, the installation ensures the production of sludge in excess of 600 kg MES / d (ie 80% GWP).
Dans le cas des filières de traitement biologique du type « biomasse fixée », encore dénommées « cultures fixées », les boues excédentaires sont extraites durant les phases de lavage et de décolmatage. La mise en œuvre d'un procédé de RPB en boucle sur la ligne de traitement de l'eau est donc difficilement réalisable, dans ce cas, notamment pour les raisons suivantes :In the case of biological treatment systems of the “fixed biomass” type, also called “fixed crops”, the excess sludge is extracted during the washing and unclogging phases. The implementation of a RPB loop process on the water treatment line is therefore difficult to achieve, in this case, in particular for the following reasons:
> La mise en place d'un procédé de RPB en boucle sur une installation de type biomasse fixée conduirait à réintroduire en tête de l'installation une quantité importante de biomasse lysée et de MES. Ce mode d'opération est difficilement compatible avec la charge en matières en suspension supportée par les installations à biomasse fixée qui est fortement limitée pour des problèmes de colmatage. L'extraction de la biomasse en excès sur les installations de traitement biologique à biomasse fixée est effectuée de manière discontinue lors des phases de lavage. Ce mode d'extraction n'est pas compatible avec le mode de fonctionnement de la boucle de RPB qui doit permettre le traitement d'une quantité équivalente à 1 à 10 fois la production de boue du système conventionnel.> The implementation of a RPB loop process on a fixed biomass type installation would lead to reintroducing at the head of the installation a large amount of lysed biomass and MES. This operating mode is hardly compatible with the load of suspended matter supported by fixed biomass installations which is greatly limited for clogging problems. Extraction of excess biomass on biological treatment plants with fixed biomass is carried out discontinuously during the washing phases. This extraction mode is not compatible with the operating mode of the RPB loop which must allow the treatment of an amount equivalent to 1 to 10 times the production of sludge from the conventional system.
Pour résoudre les problèmes ainsi posés par la réduction de production de boue des stations de traitement d'eaux résiduaires par cultures biologiques fixées, la présente invention prend le contre-pied de l'état antérieur de la technique rappelé ci- dessus, en dissociant l'étape de réduction de la production de boues, de l'étape
d'épuration, en prévoyant une étape de traitement biologique du type boues activées à faible, moyenne ou forte charge, associée à une étape de RPB par voie enzymatique thermophile ou par oxydation partielle à l'ozone couplée à une agitation mécanique. La source de substrat pour les bactéries du traitement biologique n'étant plus la matière organique des eaux usées, mais la matière organique provenant de la lyse des cellules bactériennes induite lors de l'étape de RPB.To solve the problems thus posed by the reduction of sludge production from wastewater treatment plants by fixed biological cultures, the present invention takes the opposite of the prior art recalled above, by dissociating the step to reduce sludge production, from step purification, by providing a step of biological treatment of the activated sludge type at low, medium or high load, associated with a step of RPB by thermophilic enzymatic way or by partial oxidation with ozone coupled with a mechanical agitation. The source of substrate for bacteria in biological treatment is no longer the organic matter of the wastewater, but the organic matter coming from the lysis of the bacterial cells induced during the RPB stage.
La présente invention vise également un dispositif pour la mise en œuvre du procédé spécifié ci-dessus, qui se présente sous la forme d'une installation dédiée à la réduction de production de boues associant un dispositif de réduction de la production de boues (RPB) et un réacteur de traitement biologique à faible, moyenne ou forte charge dont la source de substrat pour les bactéries du traitement biologique est constituée par la matière organique provenant de la lyse des cellules bactériennes induite dans le réacteur RPB.The present invention also relates to a device for implementing the process specified above, which is in the form of an installation dedicated to the reduction of sludge production associating a device for reducing sludge production (RPB) and a low, medium or high charge biological treatment reactor, the source of substrate for the biological treatment bacteria consists of the organic material originating from the lysis of the bacterial cells induced in the RPB reactor.
D'autres caractéristiques et avantages de la présente invention ressortiront de la description faite ci-après, en référence aux dessins annexés qui en illustrent un exemple de réalisation dépourvu de tout caractère limitatif. Sur le dessin :Other characteristics and advantages of the present invention will emerge from the description given below, with reference to the appended drawings which illustrate an embodiment thereof devoid of any limiting character. On the drawing :
- la figure 1 illustre l'état antérieur de la technique mentionné ci-dessus et- Figure 1 illustrates the prior art mentioned above and
- la figure 2 illustre de façon schématique une installation mettant en œuvre le procédé de l'invention. En se référant à cette figure 2, on voit que cette installation se présente sous la forme d'une plate-forme dédiée à la réduction de production de boues qui est associée à une installation de traitement d'eaux résiduaires par réacteur à biomasse fixée (biofiltre, par exemple), désignée dans son ensemble par la référence 2. Cette plate-forme dédiée consiste en un dispositif de RPB, désigné dans son ensemble par la référence 3, couplé à un traitement biologique, effectué dans un réacteur désigné par la référence 8 et comportant un dispositif de séparation - épaississement 9. Comme on le voit sur cette figure 2, la matière organique provenant de la lyse des cellules bactériennes induite lors de l'étape de RPB constitue la source de substrat pour le traitement biologique dans le réacteur 8. Grâce à l'invention, il est possible de concevoir une filière biologique de réduction de production de boue dédiée, de manière très différente de la filière de
traitement des eaux usées, ce qui permet de gagner en compacité, en efficacité, sans devoir satisfaire strictement les contraintes de traitement requises pour l'épuration des eaux usées (retour de Peffiuent en tête de la ligne de traitement de l'eau, flèche 4- Figure 2 schematically illustrates an installation implementing the method of the invention. Referring to this FIG. 2, it can be seen that this installation takes the form of a platform dedicated to the reduction of sludge production which is associated with an installation for treating waste water by a fixed biomass reactor ( biofilter, for example), designated as a whole by the reference 2. This dedicated platform consists of a RPB device, designated as a whole by the reference 3, coupled to a biological treatment, carried out in a reactor designated by the reference 8 and comprising a separation device - thickening 9. As can be seen in this FIG. 2, the organic material originating from the lysis of the bacterial cells induced during the RPB stage constitutes the source of substrate for the biological treatment in the reactor 8. Thanks to the invention, it is possible to design a biological sector for reducing the production of dedicated sludge, very differently from the sector. re from wastewater treatment, which makes it possible to gain in compactness, in efficiency, without having to strictly satisfy the treatment constraints required for the purification of wastewater (return of Peffiuent at the head of the water treatment line, arrow 4
)• Le caractère cyclique des extractions ne pose pas de problème pour la conduite du dispositif de RPB qui peut être alimenté en continu en prélevant les boues, après épaississement éventuel, dans le séparateur-épaississeur 9 de la filière dédiée (en 5), le réacteur 8 recueillant les eaux de lavage provenant du réacteur 2.) • The cyclic nature of the extractions does not pose any problem for the operation of the RPB device which can be fed continuously by removing the sludge, after any thickening, in the separator-thickener 9 of the dedicated die (in 5), the reactor 8 collecting the washing water from reactor 2.
En outre la présente invention présente l'avantage de permettre la mesure objective de la quantité de boues réduite. La réduction de production de boue est calculée par différence entre la quantité de boues extraites de la ligne de traitement de l'eau (en 6) et la quantité de boues résiduelle, extraite (en 7) de la filière de RPB dédiée.Furthermore, the present invention has the advantage of allowing objective measurement of the reduced quantity of sludge. The reduction in sludge production is calculated by the difference between the quantity of sludge extracted from the water treatment line (in 6) and the quantity of residual sludge, extracted (in 7) from the dedicated RPB process.
A titre d'exemple, on a indiqué ci-après les données caractéristiques d'un exemple de réalisation d'une installation selon la figure 2. Réacteur à biomasse fixée 2By way of example, the following are the characteristic data of an embodiment of an installation according to FIG. 2. Fixed biomass reactor 2
Nombre équivalent habitant : 200 000 eq-HabInhabitant equivalent number: 200,000 eq-Hab
Débit quotidien moyen : 30 000 m /jAverage daily flow: 30,000 m / d
Production de boues de l'étage de traitement biologique : 3 500 kg MES/jProduction of sludge from the biological treatment stage: 3,500 kg MES / day
Filière RPB dédiée Débit quotidien : 3500 m3/jDedicated RPB stream Daily flow: 3500 m 3 / d
Volume du traitement biologique : 1 200 mBiological treatment volume: 1,200 m
Volume du réacteur thermophile enzymatique : 650 mVolume of the thermophilic enzymatic reactor: 650 m
Production de boues : 350 kg MES/j (90% de RPB)Sludge production: 350 kg MES / d (90% RPB)
Un tel dispositif permet de répondre aux inconvénients de l'application, aux stations de traitement biologique à biomasse fixée, des procédés de RPB directement intégrés en boucle. Il apporte par ailleurs les avantages ci-après :
- possibilité d'ajuster la réduction des boues en fonction des besoins (20 à 100%o de réduction) ;Such a device makes it possible to respond to the drawbacks of applying, to biological treatment stations with fixed biomass, RPB methods directly integrated in a loop. It also provides the following advantages: - possibility of adjusting the sludge reduction according to needs (20 to 100% o reduction);
- possibilité de traiter les eaux de lavage de biofîltres ;- possibility of treating biofilters washing water;
- possibilité de concevoir un dispositif de réduction des boues biologiques pour un niveau d'épuration très inférieur au niveau d'épuration requis pour le traitement des eaux usées proprement dites ;- possibility of designing a device for reducing biological sludge for a level of treatment much lower than the level of treatment required for the treatment of wastewater proper;
- dimensionnement du dispositif de RPB pour un débit hydraulique de 5 à 50 fois inférieur au débit de la station d'épuration ayant généré les boues et- dimensioning of the RPB device for a hydraulic flow rate of 5 to 50 times lower than the flow rate of the treatment plant that generated the sludge and
- possibilité d'adapter la capacité d'oxygénation et le mode de diffusion d'air ou d'oxygène indépendamment de celui de la station ayant généré la boue.- possibility of adapting the oxygenation capacity and the air or oxygen diffusion mode independently of that of the station that generated the sludge.
Il demeure bien entendu que la présente invention n'est pas limitée à l'exemple de réalisation décrit et représenté ici, mais qu'elle en englobe toutes les variantes.
It remains to be understood that the present invention is not limited to the embodiment described and shown here, but that it encompasses all variants thereof.
Claims
REVENDICATIONS
1 - Procédé assurant la réduction de la production de boues de stations de traitement d'eaux résiduaires, urbaines ou industrielles, par cultures biologiques fixées, caractérisé en ce qu'il consiste à dissocier l'étape de réduction de la production de boues, de l'étape d'épuration, en prévoyant une étape de traitement biologique du type boues activées à faible, moyenne ou forte charge, associée à une étape de RPB par voie enzymatique thermophile, ou par oxydation partielle à l'ozone couplée à une agitation mécanique, la source de substrat pour les bactéries du traitement biologique étant constituée par la matière organique provenant de la lyse des cellules bactériennes induite lors de l'étape de réduction de production de boues (RPB).1 - Process ensuring the reduction of sludge production from wastewater treatment plants, urban or industrial, by fixed biological cultures, characterized in that it consists in dissociating the step of reduction of sludge production, from the purification step, by providing a step of biological treatment of the activated sludge type at low, medium or high charge, associated with a step of RPB by thermophilic enzymatic way, or by partial oxidation with ozone coupled with mechanical agitation , the source of substrate for the bacteria of the biological treatment being constituted by the organic matter originating from the lysis of the bacterial cells induced during the step of reduction of production of sludge (RPB).
2 - Dispositif pour la mise en œuvre du procédé selon la revendication 1 , caractérisé en ce qu'il se présente sous la forme d'une installation dédiée à la réduction de production de boues associant un dispositif de RPB (3), et un réacteur de traitement biologique à faible, moyenne ou forte charge (8) dont la source de substrat pour les bactéries est constituée par la matière organique provenant de la lyse des cellules bactériennes induite dans le dispositif de réduction de production de boues (3).2 - Device for implementing the method according to claim 1, characterized in that it is in the form of an installation dedicated to the reduction of sludge production associating a RPB device (3), and a reactor low, medium or high load biological treatment (8) whose source of substrate for bacteria consists of organic matter originating from the lysis of bacterial cells induced in the sludge production reduction device (3).
3 - Dispositif selon la revendication 2, caractérisé en ce que le dispositif de RPB (3) est alimenté en continu en prélevant les boues après épaississement éventuel dans le séparateur- épaississeur (9) recueillant les boues activées issues du réacteur de traitement biologique (8).
3 - Device according to claim 2, characterized in that the RPB device (3) is continuously supplied by removing the sludge after any thickening in the separator-thickener (9) collecting the activated sludge from the biological treatment reactor (8 ).
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0211860 | 2002-09-25 | ||
| FR0211860A FR2844786B1 (en) | 2002-09-25 | 2002-09-25 | METHOD AND DEVICE FOR REDUCING SLUDGE PRODUCTION OF WASTEWATER TREATMENT STATIONS BY FIXED BIOLOGICAL CROPS |
| FR0215384A FR2844785B1 (en) | 2002-09-25 | 2002-12-05 | METHOD AND DEVICE FOR REDUCING SLUDGE PRODUCTION OF WASTEWATER TREATMENT STATIONS BY FIXED BIOLOGICAL CROPS |
| FR0215384 | 2002-12-05 | ||
| PCT/FR2003/002806 WO2004028979A1 (en) | 2002-09-25 | 2003-09-24 | Method and device for reducing production of wastewater treatment station sludge with fixed biological cultures |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP1542931A1 true EP1542931A1 (en) | 2005-06-22 |
Family
ID=31979943
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP03772377A Withdrawn EP1542931A1 (en) | 2002-09-25 | 2003-09-24 | Method and device for reducing production of wastewater treatment station sludge with fixed biological cultures |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US7357870B2 (en) |
| EP (1) | EP1542931A1 (en) |
| AU (1) | AU2003279431A1 (en) |
| DE (1) | DE03772377T1 (en) |
| ES (1) | ES2239932T1 (en) |
| FR (1) | FR2844785B1 (en) |
| TR (1) | TR200502227T3 (en) |
| WO (1) | WO2004028979A1 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006052014A2 (en) * | 2004-11-11 | 2006-05-18 | Ebara Corporation | Organic waste water treatment method and apparatus for reducing amount of generated excess sludge |
| WO2008024445A2 (en) * | 2006-08-23 | 2008-02-28 | Siemens Water Technologies Corp. | Sequencing batch reactor with continuous membrane filtration and solids reduction |
| US9145315B2 (en) | 2013-03-01 | 2015-09-29 | Paradigm Environmental Technologies Inc. | Wastewater treatment process and system |
| CN106745796B (en) * | 2015-07-31 | 2019-12-17 | 盐池县荣桂昌食品科技有限公司 | Preparation of biological purification carrier for wastewater purification treatment |
| CN110510753A (en) * | 2019-08-20 | 2019-11-29 | 深圳市科世纪环保科技有限公司 | A kind of technique that organic enzymes are used for mud decrement |
Family Cites Families (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3718582A (en) * | 1971-03-23 | 1973-02-27 | E Smith | Microbial biolysis process |
| US3718528A (en) * | 1971-08-09 | 1973-02-27 | A Bergstrom | Heat reflecting laminate |
| JPS558835A (en) * | 1978-07-04 | 1980-01-22 | Shinryo Air Conditioning Co Ltd | Treatment of surplus sludge |
| EP0384162B1 (en) * | 1989-02-21 | 1993-04-14 | Leonhard Dipl.-Ing. Fuchs | Process for the disinfection and aerobic stabilisation of sewage sludge |
| US5013429A (en) * | 1989-03-08 | 1991-05-07 | Lenox Institute For Research, Inc. | Apparatus for stabilizing sludge |
| US5141646A (en) | 1991-03-12 | 1992-08-25 | Environmental Resources Management, Inc. | Process for sludge and/or organic waste reduction |
| JPH1052697A (en) * | 1996-08-09 | 1998-02-24 | Ebara Corp | Method for reduction of organic sludge |
| JP3449868B2 (en) * | 1996-08-22 | 2003-09-22 | 株式会社荏原製作所 | How to reduce organic sludge |
| JP3326080B2 (en) * | 1996-11-11 | 2002-09-17 | 株式会社荏原製作所 | How to reduce organic sludge |
| US6224769B1 (en) * | 1997-06-05 | 2001-05-01 | Shinko Pantec Co., Ltd. | Method and apparatus for treating organic waste water |
| FR2766813B1 (en) * | 1997-08-01 | 1999-10-01 | Degremont | PROCESS AND DEVICE FOR WASTEWATER TREATMENT INCLUDING ADDITIONAL TREATMENT OF SLUDGE BY OZONATION |
| FR2781785B1 (en) * | 1998-02-16 | 2000-09-29 | Omnium Traitement Valorisa | METHOD FOR THE BIOLOGICAL TREATMENT OF NON-OR LITTLE OR EXCESSIVE SLUDGE EFFLUENTS INCLUDING A FIXED BIOMASS TREATMENT STAGE |
| EP1254865A1 (en) * | 2001-04-27 | 2002-11-06 | VA TECH WABAG GmbH | Disintegration of Anaerobically digested sewage sludge |
-
2002
- 2002-12-05 FR FR0215384A patent/FR2844785B1/en not_active Expired - Fee Related
-
2003
- 2003-09-24 EP EP03772377A patent/EP1542931A1/en not_active Withdrawn
- 2003-09-24 DE DE2003772377 patent/DE03772377T1/en active Pending
- 2003-09-24 TR TR200502227T patent/TR200502227T3/en unknown
- 2003-09-24 AU AU2003279431A patent/AU2003279431A1/en not_active Abandoned
- 2003-09-24 US US10/528,692 patent/US7357870B2/en not_active Expired - Fee Related
- 2003-09-24 WO PCT/FR2003/002806 patent/WO2004028979A1/en not_active Application Discontinuation
- 2003-09-24 ES ES03772377T patent/ES2239932T1/en active Pending
Non-Patent Citations (1)
| Title |
|---|
| See references of WO2004028979A1 * |
Also Published As
| Publication number | Publication date |
|---|---|
| FR2844785B1 (en) | 2005-07-08 |
| US7357870B2 (en) | 2008-04-15 |
| US20060000770A1 (en) | 2006-01-05 |
| DE03772377T1 (en) | 2005-09-29 |
| TR200502227T3 (en) | 2005-08-22 |
| AU2003279431A1 (en) | 2004-04-19 |
| ES2239932T1 (en) | 2005-10-16 |
| FR2844785A1 (en) | 2004-03-26 |
| WO2004028979A1 (en) | 2004-04-08 |
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