摘要:
Method for treating a fluid aqueous waste stream comprising a biodegradable organic substance, comprising - feeding said stream into a bioreactor containing a fluid which contains biomass; - reacting the biodegradable organic substance with the biomass in the bioreactor under essentially anaerobic conditions; - taking a first flow from the bioreactor and using the first flow as a feed to a membrane filtration unit, in which said feed is subjected to filtration, thereby forming a permeate stream and a retentate stream; - returning the retentate stream to the bioreactor; - taking a second flow from the bioreactor as feed to a sludge treatment unit, in which sludge treatment unit the second flow is separated into a third flow, having an increased organic substance content compared to the second flow, and a fourth flow, having a decreased organic substance content compared to the second flow.
摘要:
The invention relates to a method and an apparatus for treating and/or pre- treating liquid manure or biogas plant reject for eliminating harmful substances, particularly nitrogen, phosphorus, and odor molecules. Process tanks (5), which include inlet means (4) for supplying a process tank (5) with a substance to be treated, outlet means for passing a post-treatment matter out of the tank, and air inlet means (2) for supplying the process tank with air required by a biological process, are used for conducting a biological treatment on the matter to be treated. The process tanks (5) are first provided with a microbe population adapted for treating the matter to be treated. The matter to be treated is supplied gradually into the first process tank and thence further into a subsequent process tank, such that the microbe population initially provided in the process tanks displaces in a step- by-step manner the original microbe population present in the matter to be treated. The matter, which is substantially free of the original microbes and has been expelled from the final process tank, is returned into the first process tank for diluting the matter to be treated. Downstream of the process tanks is conducted a nitrogen removal treatment by feeding the matter to be treated from the process tank (5) of a stripping tower (22A), in which the pH of a matter to be treated has been raised by means of a biological treatment to a level sufficient from the standpoint of nitrogen removal.
摘要:
L'invention concerne un système de traitement des eaux usées comprenant : - un réacteur principal (1) contenant la matière d'un lit filtrant (2) granulaire, ladite matière étant fixe et reposant sur un bac de récupération (3) des eaux traitées, - un dispositif (4) pour injecter les eaux usées disposé dans le réacteur principal (1), au-dessus du lit filtrant (2), - un dispositif (7) pour injecter du gaz oxygéné ou de l'air dans le lit filtrant, se caractérisant par le fait que : - ledit système comprend un réacteur primaire (5) configuré pour assurer le stockage préalable temporaire des eaux usées à traiter avant leur injection régulière dans le lit filtrant (2), ledit réacteur primaire contenant un lit enzymatique (50), les eaux usées transitant par ledit réacteur primaire avant d'être injectées dans le réacteur principal (1), - le dispositif (4) pour injecter les eaux usées comprend des buses (40) aménagées au-dessus du lit filtrant (2) et disposées de manière à assurer une répartition uniforme des eaux usées dans ledit lit filtrant, ledit dispositif d'injection étant configuré pour injecter les eaux usées de manière discontinue dans ledit lit filtrant, - le dispositif (7) pour injecter le gaz oxygéné ou l'air est disposé dans la partie inférieure du lit filtrant (2), au coeur de celui-ci, ledit dispositif d'injection étant configuré pour injecter le gaz oxygéné ou l'air de manière discontinue.
摘要:
Sequential biological reactor (R), comprising: a tank (1) delimited by a base and peripheral walls (3); an inlet (11) equipped with a selector (S) that determines a baffled route with contacting of the effluent to be treated and a portion (5) of the recirculated sludges; a means (6) for discharging the treated water in the top part of the water surface of the tank, and an outlet (7) for discharging the excess sludges in the bottom of the tank. The selector (S) comprises a vessel (8) placed in the tank (1) at a distance from the peripheral walls (3); the vessel is compartmentalized into several sectors (8.1, 8.2, 8.3, 8.4), the outlet from one sector, which is also the inlet of the following sector, being alternately low and high, or vice versa, and a last step is defined by a chamber (13) formed by two partitions (14, 15) that extend between the wall of the vessel (8) and the peripheral walls (3) of the tank and that surround the top outlet (12) of the last sector of the vessel, the lower edge of the partitions being at a distance from the base and determining two low openings for passage of the effluent into the tank.
摘要:
In a single-tank activated sludge process or a multistage activated-sludge process using predation action of animalcules, an improvement in treatment efficiency and a decrease in the amount of excess sludge generation are achieved, while maintaining stable treated water qualities. In a biological treatment wherein organic wastewater is introduced to a first biological treatment tank 1A and is biologically treated with bacteria, the treatment liquid containing the bacteria in the first biological treatment tank 1A is introduced to a second biological treatment tank 1B and is activated-sludge treated, and the treatment liquid from the second biological treatment tank 1B is separated into sludge and treated water, a portion of the sludge in the second biological treatment tank 1B and/or at least a portion of the separated sludge is introduced into a sludge treatment tank 3 having a submerged filter element 4 with a pore diameter of 5 to 100 µm in the tank and is subjected to aerobic biological treatment, and the liquid permeated through the submerged filter element 4 is returned to the first biological treatment tank 1A and/or the second biological treatment tank 1B. Both high effect of reduction in the amount of sludge and satisfactory treated water qualities can be simultaneously achieved by reducing the amount of sludge with animalcules in the sludge treatment tank 3, allowing residual fine components to permeate through the submerged filter element 4, and, again, returning the fine components to the filter predation animalcule tank 1B for predation.
摘要:
The invention relates to a filtration device for separating particles from a liquid using hollow-fibre membranes, which are combined to form a fibre bundle. The hollow-fibre membranes are traversed by the liquid from the exterior to the interior and the liquid that has been cleaned of the particles is withdrawn at at least one of the ends of the hollow-fibre membrane. The hollow-fibre membrane bundle is wound onto a support, whose external peripheral surface can be traversed by a gas at least partially from the interior to the exterior. The winding of the hollow-fibre bundle onto the support permits a space-saving arrangement and allows deposited materials to be reliably cleaned from the hollow-fibre membranes. The filtration device can be used on its own or in the form of a module containing several devices for purifying waste water. The invention also relates to a method for purifying waste water using the filtration module and a membrane bioreactor.
摘要:
The method of producing aerobic biogranules for the treatment of waste water comprising the steps of: a) introducing waste water into a reactor; b) seeding the reactor with a active biomass material; c) supplying the oxygen-containing gas to the reactor to provide a mixing action to the suspension of biomass material in said waste water, the supply of oxygen-containing gas providing a superficial upflow gas velocity greater than 0.25 cm/s; d) initiating a period of nutrient starvation of the biomass material while continuing to supply oxygen-containing gas; e) allowing formed aerobic granules to settle in a settling zone in said reactor; f) discharging at least a portion of the waste water; g) repeating steps (a) to (f) until at least a portion of the biogranules in said settling zone are within a predetermined properties; and h) recovering said biomass granules within those predetermined properties.
摘要:
The invention relates to a method for biological purification of wastewater wherein the wastewater is purified in a biofilm process (1) followed by an activated sludge process (2). The biological degradation in the biofilm process is performed under limitation of one of the nutrient salts nitrogen or phosphorous, and the surplus sludge from the biofilm process is allowed to pass to the activated sludge process.
摘要:
A method and a system for selecting and retaining solids with superior settling characteristics, the method comprising feeding wastewater to an input of a processor that carries out a treatment process on the wastewater, outputting processed wastewater at an output of the processor, feeding the processed wastewater to an input of a gravimetric selector that selects solids with superior settling characteristics, and outputting a recycle stream at a first output of the gravimetric selector back to the processor.
摘要:
High levels of microbial storage compound (MSC) such as polyhydroxyalkanotaes (PHA) can be produced from wastewater comprising Readily Biodegradable COD (RBCOD) using activated sludge comprising microorganisms capable of accumulating MSC by contacting the wastewater with the activated sludge in the presence of dissolved oxygen during a first period of time, to obtain MSC-loaded activated sludge comprising MSC at a level of at least 60 wt.% based on dry weight of the organic part of the sludge, and then supplying elements essential for growth such as nitrogen and phosphorus and allowing up-take of these elements and limited growth during a second period of time, the supplied amount of at least of one of said essential elements compared to the amount of RBCOD supplied in step a) limiting the growth to an extent that not all MSC is used for growth, to obtain grown activated sludge comprising residual MSC at a level of at least 20 wt.% based on dry weight of the organic part of the sludge; and removing or harvesting part of the MSC-loaded activated sludge and/or part of the grown activated sludge, so that the total average retention time of the sludge is less than 72 h.