EP0072837A1 - Procede, dispositif et moyen pour l'epuration des eaux usees - Google Patents

Procede, dispositif et moyen pour l'epuration des eaux usees

Info

Publication number
EP0072837A1
EP0072837A1 EP82900635A EP82900635A EP0072837A1 EP 0072837 A1 EP0072837 A1 EP 0072837A1 EP 82900635 A EP82900635 A EP 82900635A EP 82900635 A EP82900635 A EP 82900635A EP 0072837 A1 EP0072837 A1 EP 0072837A1
Authority
EP
European Patent Office
Prior art keywords
wastewater
activated sludge
tank
fouling
circulation
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Withdrawn
Application number
EP82900635A
Other languages
German (de)
English (en)
Inventor
Jürgen Zink
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Menzel and Co GmbH
Original Assignee
Menzel and Co GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Menzel and Co GmbH filed Critical Menzel and Co GmbH
Publication of EP0072837A1 publication Critical patent/EP0072837A1/fr
Withdrawn legal-status Critical Current

Links

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
    • C02F3/08—Aerobic processes using moving contact bodies
    • C02F3/085—Fluidized beds
    • 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
    • C02F3/10—Packings; Fillings; Grids
    • 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
    • C02F3/28—Anaerobic digestion processes
    • C02F3/2806—Anaerobic processes using solid supports for microorganisms
    • 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
    • C02F3/30—Aerobic and anaerobic processes
    • C02F3/301—Aerobic and anaerobic treatment in the same reactor
    • 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
    • C02F3/30—Aerobic and anaerobic processes
    • C02F3/302—Nitrification and denitrification treatment
    • 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 invention relates to a method for wastewater treatment according to the preamble of claim 1.
  • Nitrification of the wastewater is known for plants which are designed as so-called low-load plants. »In such low-load plants, a relatively high sludge age is reached due to only a low sludge load, so that a sufficient increase in nitrifying factors is possible with a longer retention time.
  • the rate of nitrification is also strongly dependent on the temperature of the wastewater. If the temperature is low, the nitrification process proceeds correspondingly slowly. Therefore, in particular due to the long-term low outside and waste water temperatures in order to achieve sufficient nitrification, it has been necessary to extend the dwell times accordingly, which means that to achieve sufficient waste water throughput, the waste water treatment plant must be designed with a correspondingly large volume st. This means that in practice both high investment costs for the construction of the plant and high operating costs for the implementation
  • the object of the invention is to carry out a method for wastewater purification according to the preamble of claim 1 so that a small-volume system design with high Ni ⁇ rification achievement is achieved and cost savings in the manufacture and during the operation of the cleaning system is possible.
  • this object is achieved in that in an activated sludge containing activated sludge with 3iomass fouling body. due to a flow of wastewater suspended and in. circulate essentially without fluidized bed.
  • the wastewater treatment in the aeration tank is practically carried out in the system of a multiphase reactor, two different sludges, namely. the activated sludge and the biomass-contaminated growth bodies are kept.
  • This provides the opportunity to increase the efficiency for the waste water hitification many times over, so that the aeration tank can be made inexpensively small, while at the same time reducing the operating costs.
  • Another advantage is there in the fact that the growth bodies introduced into the aeration tank as extremely inexpensive bulk material have a high level of stability, so that the nitrifying agents adhering to them have a long service life.
  • the biomass is essentially so-called sessile bacteria, which preferentially settle on the surface of the growth cells.
  • the nitrificants can thus grow and multiply on the surface of the fouling elements, which are prevented from being discharged from the activation tank by suitable precautions.
  • the sludge age necessary for the growth of the nitrificants is thus achieved by the growth bodies with the nitrificants adhering to them remaining in the activation tank, while the normal activated sludge, as is customary in a high-load system, is discharged as excess sludge with a relatively low sludge age.
  • the wastewater to be cleaned can be raked by a rake before it is fed into the aeration tank.
  • a so-called fine rake or a sieve device drum sieve, curved sieve or the like
  • the wastewater can then pass through a sand trap, whereby it can be advantageous to prevent the sand from entering the activation tank by taking appropriate measures, since otherwise the sand carried into the activation tank from time to time is remove.
  • the wastewater can advantageously be gassed with a gassing device using atmospheric oxygen or pure oxygen, the aeration preferably being carried out from below, but also being carried out by other aeration systems such as surface aerators and the like.
  • the circulation of the wastewater-sludge-fouling body mixture can advantageously be carried out with a separately arranged, mechanical water displacer such as a propeller with minimal energy expenditure.
  • the oxygen input can be precisely metered and coordinated, for example by an oxygen electrode, can be optimally adjusted, so that extremely economical high-performance operation is achieved.
  • the wastewater then reaches a secondary clarifier via a fouling device. From the secondary clarifier, the sludge can be returned to the aeration tank as return sludge, or can be removed from the system as excess sludge.
  • the cutting device can consist of a sisk covering with a corresponding hole diameter.
  • the sieve covering can be cleaned automatically by means of an arrangement in the waste water, any solids being carried away from the sieve covering by the flow causing the fouling bodies to circulate.
  • the cleaning can also be supported in that, for example, a spray device is arranged on the back of the screen covering, which is switched on at certain time intervals and gently removes particles adhering to the screen covering.
  • the circulation of the growth bodies can advantageously run in a ring-like linear manner in the horizontal direction.
  • the floating suspension can be supported by additional fumigation from below, which are expediently arranged at certain distances from one another in the aeration tank, so that it is practically impossible to settle the bottom of the aeration tank.
  • the method according to the invention it is also possible to carry out a denitrification of the wastewater in the activation tank with continued circulation of the fouling bodies, regardless of whether the oxygen supply in the activation tank is reduced or completely switched off.
  • a clearing bar equipped with a fouling body buoyancy shield over the floor of the activated sludge tank, wherein an aerator candle or the like can be arranged above the fouling body buoyancy shield of the beam so that the fouling bodies can be arranged through the fine air bubbles emerging here receive a further boost.
  • the vegetation bodies according to the invention can advantageously be made of plastic.
  • the weight can be measured so that it is slightly larger than the specific weight of the wastewater, so that a buoyancy and accumulation on the surface of the water does not occur, but essentially a largely constant floating circulation is achieved.
  • the vegetation bodies themselves' can be designed in different ways. Thus, it may be expedient to form the growth bodies from two growth plates, which have slots and are joined together in a cross shape, as a result of which a relatively large overall surface is achieved. It is also possible to design the growth bodies as hollow spheres and to provide the wall with holes.
  • the outer wall of the growth bodies with depressions in which the biomass is largely protected, which can be achieved in particular by designing the growth bodies in a spherical shape and having a large number of striving support parts.
  • the size of the growth bodies can be very different and, for example, be in the range between 0.2 mm to 50 mm in diameter, so that a selection of growth bodies corresponding to the different requirements can be used optimally, it being possible not only to have growth bodies of a size or size To use design form, but to mix differently sized and differently designed growth bodies and to circulate them in a single aeration tank in a floating manner.
  • FIG. 2 is a plan view of the wastewater treatment plant of FIG. 1, 3 is a partial sectional side view of the wastewater treatment plant of FIG. 2 in the direction of arrow III,
  • FIG. 4 is an exploded view of a two-plate vegetation body according to the invention.
  • FIG. 5 is an exploded view of the two-plate vegetation body according to FIG. 4, but rotated through 90 °,
  • FIG. 6 is a sectional view of a hollow spherical growth body
  • Fig. 7 is an illustration of a growth body provided with outer recesses and
  • FIG. 8 is an illustration of a vegetation-shaped body with strut-shaped support parts
  • the wastewater treatment plant 1 shown in the drawing has an aeration basin 2 designed as a circular horizontal ring and a secondary clarification basin 5, which is delimited by the aeration basin 2 by a hanging wall 4.
  • a bridge 6 rotatable about a central vertical axis 5 spans the aeration basin 2 and the secondary clarification basin 3.
  • the wastewater 7 to be cleaned is introduced into the activation tank 2 via an inlet 8.
  • a flow 10 is generated by a propeller 9 arranged in the activation tank 2, through which the waste water 7 with the activated sludge circulates in the activation tank 2 in the manner of a horizontal ring.
  • 2 flow bodies 11 circulate with this flow 10 in the aeration tank in a floating and wide manner walking spine free.
  • the vegetation bodies 11 are contaminated with a biomass, the accelerated nitrification of the
  • Waste water 7 causes. Due to the floating, fluidized bed-free circulation of the growth bodies 11, mechanical abrasion of the biomass is practically avoided, which ensures a long service life, because the growth bodies 11 are moved almost linearly in the same direction and can therefore hardly be lined up.
  • aerators 12 which are arranged at intervals. Oxygen can be blown into the wastewater 7 via the aerators 12, whereby the floating circulation of the fouling bodies 11 can also be supported.
  • FIG. 3 shows that on a beam 14 of the rotatable bridge 6, which is led over the bottom 13 of the activation tank 2, a fouling element buoyancy shield 15 is fastened and runs somewhat inclined; a further aerating core 16 is arranged above the fouling body buoyancy shield 15. Any deposited growth bodies 11 are carried up by the growth body lift shield 15. Through that at. of the aerator 1 ⁇ emerging air bubbles, the fouling body 11 receives a further buoyancy pulse, so that there is essentially a largely uniform floating circulation of the fouling body 11 in the waste water 7.
  • fouling bodies 11 ', 11'',11''', 11 ''' are made of plastic and have a weight that is somewhat greater than the specific weight of the waste water 7, so that the fouling bodies contaminated with biomass 11 essentially remain in suspension and possibly only very slowly downwards sink, but do not chill on the water surface.
  • the fouling body 1 1 consist of two Bewuchsplat th 17, 13, which are identical and have a Schli ⁇ s 19.
  • the vegetation plates 17, 13 are plugged together in a cross shape in the area of the slots 19.
  • the vegetation body 11 ′′ is designed as a hollow ball 20.
  • the wall 21 of the hollow sphere 20 has through holes 22 so that the waste water 7 can penetrate into the hollow sphere 20 and nitricants can also grow on the inner surface of the wall 21.
  • the vegetation body 11 '''of FIG. 7 has a corrugation 23 which is Mulder on the outer surface. 24 has, in which the biomass can stick abrasion protected.
  • Fig. 8 shows a vegetation body 11 '''', which is designed in the form of a hedgehog ball and, for this purpose, has a large number of striving support parts 25 for the adhesion of the biomass.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

Dans un bassin d'activation (2) contenant les eaux usees (7) et des boues activees, on maintient en equilibre dans un courant (10) d'eaux usees (7) des corps d'adherence (11) de facon que les corps (11) circulent sans creer des tourbillons. La biomasse servant a la nitrification des eaux usees adhere aux corps (11).
EP82900635A 1981-02-21 1982-02-19 Procede, dispositif et moyen pour l'epuration des eaux usees Withdrawn EP0072837A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3106465 1981-02-21
DE19813106465 DE3106465A1 (de) 1981-02-21 1981-02-21 Verfahren, vorrichtung und mittel zur abwasserreinigung

Publications (1)

Publication Number Publication Date
EP0072837A1 true EP0072837A1 (fr) 1983-03-02

Family

ID=6125404

Family Applications (2)

Application Number Title Priority Date Filing Date
EP82101307A Pending EP0058974A1 (fr) 1981-02-21 1982-02-19 Procédé, dispositif et moyen pour l'épuration d'eau usée
EP82900635A Withdrawn EP0072837A1 (fr) 1981-02-21 1982-02-19 Procede, dispositif et moyen pour l'epuration des eaux usees

Family Applications Before (1)

Application Number Title Priority Date Filing Date
EP82101307A Pending EP0058974A1 (fr) 1981-02-21 1982-02-19 Procédé, dispositif et moyen pour l'épuration d'eau usée

Country Status (4)

Country Link
EP (2) EP0058974A1 (fr)
JP (1) JPS58500156A (fr)
DE (1) DE3106465A1 (fr)
WO (1) WO1982002874A1 (fr)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3504037A1 (de) * 1985-02-06 1986-08-07 Dr.-Ing. Werner Weber Ingenieur-Gesellschaft mbH, 7530 Pforzheim Verfahren und einrichtung zur biologischen abwasserreinigung
US5192441A (en) * 1989-02-14 1993-03-09 Omnium De Traitements Et De Valorisation (Otv) Process and installation for biological treatment, e.g. by nitrification and/or denitrification, of an effluent including nitrated pollution
FR2643065B1 (fr) * 1989-02-14 1991-06-14 Omnium Traitement Valorisa Procede et installation de traitement biologique, y compris nitrification et denitratation, d'une eau residuaire a traiter
ES2064083T4 (es) † 1990-01-23 2007-04-01 Anoxkaldnes As Metodo y reactor para la purificacion de aguas.
DE4112377C2 (de) * 1991-04-16 2002-10-24 Leonhard Jagusch Kompaktreaktor für die aerobe biologische Abwasserreinigung
SE521148C2 (sv) 2002-02-18 2003-10-07 Kaldnes Miljoeteknologi As Förfarande för biologisk rening av vatten i en reaktor innehållande bärare för biofilmspåväxt
NO3077102T3 (fr) 2013-12-02 2018-02-24
CN105174477B (zh) * 2015-09-25 2018-03-30 哈尔滨工业大学 一种环形推流式微型动物生物床及利用其处理污水污泥的方法

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2071591A (en) * 1935-12-02 1937-02-23 Albert L Tholin Sewage treatment
FR1534812A (fr) * 1967-06-19 1968-08-02 Exxon Standard Sa Procédé de destruction par oxydation biologique des composés phénoliques contenus dans les eaux polluées ou les soudes usées
AT282495B (de) * 1968-05-21 1970-06-25 Passavant Werke Becken zum aeroben Stabilisieren von Schlamm
US3543937A (en) * 1968-08-02 1970-12-01 Joseph M Choun Filter media
DE2427550A1 (de) * 1974-06-07 1975-12-18 Menzel & Co Verfahren zur begasung von fluessigkeiten, insbesondere zur klaerung von abwaessern, und vorrichtung zur durchfuehrung des verfahrens
IT1098434B (it) * 1978-09-01 1985-09-07 Hydro System Srl Apparecchiatura per la produzione di elementi di riempimento a grande superficie di scambio in materia plastica a parete sottile,marigida,per impianti di depurazione biologica a letti filtranti,ed elementi di riempimento cosi' ottenuti
DE2936826A1 (de) * 1979-09-12 1981-04-16 Maschinenfabrik Hellmut Geiger Gmbh & Co Kg, 7500 Karlsruhe Verfahren und vorrichtung zur biologischen reinigung von abwasser
DE3017439A1 (de) * 1980-05-07 1981-11-12 Friedrich Wilhelm Dipl.-Ing. 6100 Darmstadt Siepmann Verfahren zur biologischen reinigung von abwasser

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO8202874A1 *

Also Published As

Publication number Publication date
EP0058974A1 (fr) 1982-09-01
DE3106465A1 (de) 1982-09-09
JPS58500156A (ja) 1983-02-03
WO1982002874A1 (fr) 1982-09-02

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XX Miscellaneous

Free format text: VERBUNDEN MIT 82101307.5 (EUROPAEISCHE ANMELDENUMMER) DURCH ENTSCHEIDUNG VOM 19.05.83.

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Effective date: 19840526

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Inventor name: ZINK, JUERGEN