DE29812751U1 - Multi-stage small sewage treatment plant for domestic wastewater - Google Patents
Multi-stage small sewage treatment plant for domestic wastewaterInfo
- Publication number
- DE29812751U1 DE29812751U1 DE29812751U DE29812751U DE29812751U1 DE 29812751 U1 DE29812751 U1 DE 29812751U1 DE 29812751 U DE29812751 U DE 29812751U DE 29812751 U DE29812751 U DE 29812751U DE 29812751 U1 DE29812751 U1 DE 29812751U1
- Authority
- DE
- Germany
- Prior art keywords
- sewage treatment
- treatment plant
- small sewage
- clarification
- tank
- 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.)
- Expired - Lifetime
Links
- 239000010865 sewage Substances 0.000 title claims description 20
- 239000010840 domestic wastewater Substances 0.000 title claims description 4
- 238000005352 clarification Methods 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 8
- 239000010802 sludge Substances 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 4
- 238000011144 upstream manufacturing Methods 0.000 claims 1
- 238000005273 aeration Methods 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 3
- 239000008213 purified water Substances 0.000 description 2
- 238000011086 high cleaning Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000009423 ventilation Methods 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
- C02F3/1236—Particular type of activated sludge installations
- C02F3/1242—Small compact installations for use in homes, apartment blocks, hotels or the like
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
- B01D17/0214—Separation of non-miscible liquids by sedimentation with removal of one of the phases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/12—Auxiliary equipment particularly adapted for use with liquid-separating apparatus, e.g. control circuits
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0018—Separation of suspended solid particles from liquids by sedimentation provided with a pump mounted in or on a settling tank
- B01D21/0021—Separation of suspended solid particles from liquids by sedimentation provided with a pump mounted in or on a settling tank provided with a jet pump
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2405—Feed mechanisms for settling tanks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2444—Discharge mechanisms for the classified liquid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/30—Control equipment
- B01D21/34—Controlling the feed distribution; Controlling the liquid level ; Control of process parameters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/30—Control equipment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2221/00—Applications of separation devices
- B01D2221/02—Small separation devices for domestic application, e.g. for canteens, industrial kitchen, washing machines
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Water Supply & Treatment (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Microbiology (AREA)
- Biodiversity & Conservation Biology (AREA)
- Treatment Of Biological Wastes In General (AREA)
- Activated Sludge Processes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Description
Christian Weise 14.7.1998Christian Weise 14.7.1998
90475 Nürnberg90475 Nuremberg
Mehrstufige Kleinkläranlage für häusliche AbwässerMulti-stage small sewage treatment plant for domestic wastewater
Die Erfindung betriflt eine mehrstufige Kleinkläranlage tür häusliche Abwässer, bestehend aus mechanischer Grobentschlammung und nachgeschalteten Klärbehältern. Bekannte Kleinkläranlagen neigen bei stark schwankenden Zuflüssen und bei plötzlichen Betriebsunterbrechungen zu kritischen Betriebszuständen. Tritt nach einer Betriebsunterbrechung oder nach einer Phase sehr geringer Belastung stossartig eine sehr hohe Belastung auf, kann auch eine relativ betriebssicher arbeitende Kleinkläranlage gemäss DE 195 34 657 Al sehr schnell in kritische Betriebszustände kommen. Eine eventuelle, ursprünglich nicht geplante Erhöhung der Belastung durch Anschluss zusätzlicher Einwohner kann die genannte Kleinkläranlage ebenfalls sehr schnell überfordern.The invention relates to a multi-stage small sewage treatment plant for domestic wastewater, consisting of mechanical coarse sludge removal and downstream treatment tanks. Known small sewage treatment plants tend to reach critical operating conditions when there are strong fluctuations in inflows and when there are sudden interruptions in operation. If a very high load suddenly occurs after an interruption in operation or after a phase of very low load, even a relatively reliable small sewage treatment plant according to DE 195 34 657 Al can very quickly reach critical operating conditions. A possible, originally unplanned increase in load due to the connection of additional residents can also very quickly overwhelm the small sewage treatment plant mentioned.
Der Erfindung liegt daher die Aufgabe zugrunde, eine auch bei extrem wechselnden Belastungszuständen und unvorhergesehenem Belastungszuwachs hochwirksame und äusserst betriebssicher arbeitende Kleinkläranlage zu schaffen. Diese Aufgabe wird nach der Erfindung gelöst durch eine mehrstufige Kleinkläranlage, bestehend aus der mechanischen Grobentschlammung und mindestens zwei nachgeschalteten, gleichartig aufgebauten Klärbehältern.The invention is therefore based on the object of creating a small sewage treatment plant that is highly effective and extremely reliable even under extremely changing load conditions and unforeseen load increases. This object is achieved according to the invention by a multi-stage small sewage treatment plant, consisting of the mechanical coarse sludge removal and at least two downstream, similarly constructed sewage tanks.
Die mechanische Grobentschlammung hält groben Schlamm und sperrige Gegenstände zurück. Die der mechanischen Grobentschlammung nachgeschalteten Klärbehälter sind in sich völlig gleichartig aufgebaut und arbeiten nach dem bekannten Aufstaubelebungsverfahren. Jeder Klärbehälter stellt eine Kombination aus Vorspeicherbehälter und Bioreaktor dar und ist also zugleich Vorspeicher für den nachfolgenden Klärbehälter. Steuerung, Belüftung, Umwälzung, Einlass, Überleitung und Auslass des Wassers erfolgen durch bekannte Vorrichtungen. Durch die Kombination von Bioreaktor und Vorspeicher in einem Behälter und die Zusammenschaltung der einzelnen Reinigungsstufen in Form einer mehrstufige Kleinkläranlage wird ein sehr sicherer Betrieb und eine sehr hohe Reinigungsleistung auch bei extremen Belstungen und Belastungsschwankungen der Kleinkläranlage sichergestellt. Die hohen Leistungsreserven dieser mehrstufigen Kleinkläranlage ermöglichen es, das Gesamtarbeitsvolumen der Anlage zu verkleinern oder aber im umgekehrten Fall wesentlich mehr Einwohner an ein bestimmtes Arbeitsvolumen anzuschliessen.The mechanical coarse sludge removal holds back coarse sludge and bulky objects. The sewage treatment tanks downstream of the mechanical coarse sludge removal are constructed in a completely identical manner and work according to the well-known aeration process. Each sewage treatment tank is a combination of a pre-storage tank and a bioreactor and is therefore also a pre-storage tank for the subsequent sewage treatment tank. Control, ventilation, circulation, inlet, transfer and outlet of the water are carried out by well-known devices. The combination of bioreactor and pre-storage tank in one tank and the interconnection of the individual cleaning stages in the form of a multi-stage small sewage treatment plant ensures very safe operation and a very high cleaning performance even under extreme loads and load fluctuations in the small sewage treatment plant. The high performance reserves of this multi-stage small sewage treatment plant make it possible to reduce the total working volume of the plant or, conversely, to connect significantly more residents to a certain working volume.
In der Zeichnung ist ein Ausführungsbeispiel der Erfindung dargestellt. Es zeigt:An embodiment of the invention is shown in the drawing. It shows:
Fig. 1 einen Schnitt durch eine zweistufige Kleinkläranlage . 35Fig. 1 a section through a two-stage small sewage treatment plant . 35
Bei der in der Zeichnung gezeigten zweistufigen Kleinkläranlage fliesst das Abwasser
durch die Zulaufleitung 1 in die Grobentschlammung 2. Durch die tauchrohrgesicherte
Überlaufleitung 3 fliesst das vorgereinigte Abwasser in den Klärbehälter 4 der ersten Reinigungsstufe.
Der Klärbehälter 4 arbeitet nach dem Aufstaubelebungsverfahren und stellt eine Kombination von Bioreaktor und Vorspeicherbehälter dar, ist also Vorspeicher für
den Klärbehälter 8 der zweiten Reinigungsstufe.In the two-stage small sewage treatment plant shown in the drawing, the wastewater flows through the inlet line 1 into the coarse sludge removal system 2. The pre-treated wastewater flows through the dip-pipe-protected overflow line 3 into the treatment tank 4 of the first treatment stage.
The clarification tank 4 operates according to the aeration process and represents a combination of bioreactor and pre-storage tank, i.e. it is a pre-storage tank for the clarification tank 8 of the second purification stage.
-2--2-
Im Klärbehälter 4 wird das Abwasser zulaufbedingt aufgestaut und durch die Belüftervorrichtung 5 umgewälzt und belüftet. Hat der Wasserspiegel das obere Niveau 2 erreicht, leitet eine Steuerautomatik den Absetzvorgang und die Überleitung des gereinigten Wassers durch die Pumpe 6 und die Überlaufleitung 7 in den Klärbehälter der zweiten Reinigungs-stufe ein. Hat die Pumpe 6 im Klärbehälter 4 den Wasserspiegel wieder bis zum unteren Niveau 1 abgesenkt, unterbricht die Steuerautomatik den Abpumpvorgang. Die Arbeitsvorgänge beginnen von vorn. Im Klärbehälter 8 , welcher in sich völlig dem Klärbehälter 4 entspricht und welcher ebenfalls nach dem Aufstaubelebungsverfahren arbeitet, verlaufen alle Arbeitsvorgänge identisch zu denen im Klärbehälter 4. Das endgereinigte Wasser wird durch die Pumpe 6 des Klärbehälters 8 mittels der Ablaufleitung 9 nach aussen abgeleitet.In the clarification tank 4, the wastewater is dammed up due to the inflow and circulated and aerated by the aeration device 5. When the water level has reached the upper level 2 , an automatic control system initiates the settling process and the transfer of the purified water through the pump 6 and the overflow line 7 into the clarification tank of the second cleaning stage. When the pump 6 in the clarification tank 4 has lowered the water level back to the lower level 1 , the automatic control system interrupts the pumping process. The work processes start again from the beginning. In the clarification tank 8, which is completely identical to the clarification tank 4 and which also works according to the damming aeration process, all work processes are identical to those in the clarification tank 4. The finally purified water is drained outside by the pump 6 of the clarification tank 8 via the drain line 9.
-3--3-
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE29812751U DE29812751U1 (en) | 1998-07-17 | 1998-07-17 | Multi-stage small sewage treatment plant for domestic wastewater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE29812751U DE29812751U1 (en) | 1998-07-17 | 1998-07-17 | Multi-stage small sewage treatment plant for domestic wastewater |
Publications (1)
Publication Number | Publication Date |
---|---|
DE29812751U1 true DE29812751U1 (en) | 1998-12-03 |
Family
ID=8060011
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE29812751U Expired - Lifetime DE29812751U1 (en) | 1998-07-17 | 1998-07-17 | Multi-stage small sewage treatment plant for domestic wastewater |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE29812751U1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102006025393A1 (en) * | 2006-05-31 | 2007-12-06 | Aco Severin Ahlmann Gmbh & Co. Kg | Small-scale wastewater clarification plant comprises structurally identical biological containers with inlet, outlet and sludge recirculation pipeline, and sludge collection tank with pump, which is connected with sludge recirculation line |
DE102016224229A1 (en) | 2016-12-06 | 2018-06-07 | FWS GmbH | Process and apparatus for the purification of wastewater |
-
1998
- 1998-07-17 DE DE29812751U patent/DE29812751U1/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102006025393A1 (en) * | 2006-05-31 | 2007-12-06 | Aco Severin Ahlmann Gmbh & Co. Kg | Small-scale wastewater clarification plant comprises structurally identical biological containers with inlet, outlet and sludge recirculation pipeline, and sludge collection tank with pump, which is connected with sludge recirculation line |
DE102006025393B4 (en) * | 2006-05-31 | 2012-06-06 | Aco Severin Ahlmann Gmbh & Co. Kg | wastewater treatment plant |
DE102016224229A1 (en) | 2016-12-06 | 2018-06-07 | FWS GmbH | Process and apparatus for the purification of wastewater |
WO2018104255A1 (en) | 2016-12-06 | 2018-06-14 | FWS GmbH | Method and device for purifying wastewater |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
R207 | Utility model specification |
Effective date: 19990121 |
|
R156 | Lapse of ip right after 3 years |
Effective date: 20020501 |