DE1816932B2 - Process for the purification of waste water with a flotation stage - Google Patents
Process for the purification of waste water with a flotation stageInfo
- Publication number
- DE1816932B2 DE1816932B2 DE1816932A DE1816932A DE1816932B2 DE 1816932 B2 DE1816932 B2 DE 1816932B2 DE 1816932 A DE1816932 A DE 1816932A DE 1816932 A DE1816932 A DE 1816932A DE 1816932 B2 DE1816932 B2 DE 1816932B2
- Authority
- DE
- Germany
- Prior art keywords
- flotation
- added
- wastewater
- stage
- purification
- 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.)
- Granted
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
- C02F3/12—Activated sludge processes
- C02F3/1205—Particular type of activated sludge processes
- C02F3/1215—Combinations of activated sludge treatment with precipitation, flocculation, coagulation and separation of phosphates
-
- 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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- 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)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Engineering & Computer Science (AREA)
- Hydrology & Water Resources (AREA)
- Analytical Chemistry (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Physical Water Treatments (AREA)
- Paper (AREA)
Description
Die Erfindung bezieht sich auf ein Verfahren zur Reinigung von Abwasser mit einer Flotationsstufe für das Rohabwasser und/oder das von Grobstoff befreite Rohabwasser.The invention relates to a method for cleaning waste water with a flotation stage for the raw sewage and / or the raw sewage freed from coarse material.
Es ist schon bekannt, Eisen- oder Aluminiumhydroxydflocken als flotierbare Substanz zur Reinigung von Abwasser zu benutzen.It is already known to use iron or aluminum hydroxide flakes as a floatable substance for cleaning To use sewage.
Die Flotation von Abwasser ist grundsätzlich insbesondere aus der Papierabwasserreinigung bekannt. Der Erfindung liegt dabei die Aufgabe zugrunde, den Flotationseffekt erheblich zu erhöhen, indem die praktisch nicht flotierbaren gelösten und kolloidalen Verschmutzungsanteile der organischen Verschmutzung mitausflotiert werden, insgesamt also ein höherer Anteil der gesamten organischen Verschmutzung durch die Flotation von dem Abwasser abgetrennt wird.The flotation of wastewater is known in particular from paper wastewater treatment. The invention is based on the object of significantly increasing the flotation effect by the practically non-floatable dissolved and colloidal pollution fractions of organic pollution are also floated out, so overall a higher proportion of the total organic pollution by the flotation is separated from the wastewater.
Die Lösung dieser Aufgabe besteht darin, daß dem Abwasser als flotierbare Substanzen mit der Fähigkeit,
gelöste bzw. im anschließenden kolloidalen Bereich vorliegende organische Stoffe adsorptiv zu binden,
erfindungsgemäß biologisch aktiver organischer Schlamm zugesetzt wird. Dieser Schlamm zeichnet sich
einerseits durch seine hohe Fähigkeit aus, gelöste bzw. kolloidal vorliegende organische Schmutzungen adsorptiv
zu binden, und zum anderen ist er flotierbar.
Der gegenüber der SW-PS 211366, die die
Verwendung von Aluminiumsulfat und Eisenchlorid vorsieht, erreichte technische Fortschritt ist im wesentlichen
darin zu sehen, daß der in der Abwasserreinigung anfallende biologisch aktive organische SchlammThe solution to this problem is that according to the invention biologically active organic sludge is added to the wastewater as flotable substances with the ability to adsorptively bind dissolved organic substances or organic substances present in the subsequent colloidal area. This sludge is characterized on the one hand by its high ability to adsorptively bind dissolved or colloidal organic dirt, and on the other hand it is floatable.
The technical progress achieved in relation to SW-PS 211366, which provides for the use of aluminum sulfate and ferric chloride, is essentially to be seen in the fact that the biologically active organic sludge obtained in wastewater treatment
to praktisch kostenlos als Flotationsmittel zur Verfugung stehtto be available practically free of charge as a flotation agent stands
Da bei der Flotation als Trennprozeß einerseits eine Verarmung des Abwassers an Feststoffen und somit an Adsorptionsflächen stattfindet, andererseits jedoch die Adsorption in Abhängigkeit von der Zeit und den Kontaktmöglichkeiten steht, kann es erforderlich sein, den aktiven Schlamm nicht nur zu Verfahrensbeginn dem Rohabwasser zuzusetzen. Aus diesem Grunde kann es in Abweichung der in der Abwassertechnik üblichen Flotationspraxis notwendig werden, das Abwasser mehrstufig in hintereinandergeschalteten Flotationskammern zu flotieren, wobei jeder Flotationskammer erneut biologisch aktiver organischer Schlamm zugesetzt wird. Gegebenenfalls kann dabei wenigstens ein Teil des Feststoffaustrages einer nachfolgenden Flotationskammer der vorhergehenden Flotationskammer wieder zugeleitet werden. Diese mehrstufige Flotation ist sinnvoll, um eine Verarmung des Abwassers an Feststoffen und somit an Adsorptionsflächen zu vermeiden.Since the flotation as a separation process on the one hand Depletion of the wastewater in solids and thus on adsorption surfaces takes place, on the other hand, however, the Adsorption depends on the time and the contact possibilities, it may be necessary not only to add the active sludge to the raw sewage at the start of the process. Because of this, can it becomes necessary, in deviation from the flotation practice customary in wastewater technology, to remove the wastewater to float in multiple stages in series-connected flotation chambers, each flotation chamber biologically active organic sludge is added again. If necessary, at least one Part of the solids discharge of a subsequent flotation chamber of the preceding flotation chamber be fed back. This multi-stage flotation is useful in order to prevent the wastewater from becoming impoverished Avoid solids and thus on adsorption surfaces.
Die Erfindung sieht ferner vor, daß dem Abwasser zusätzlich an sich bekannte organische und/oder anorganische Flockungshilfsmittel, insbesondere organische Polymere, zugegeben werden. Zweckmäßig werden die Flockungshilfsmittel dabei in der letzten Kammer zugegeben, in der das Abwasser schon den weitestgehenden Reinigungsgrad erhalten hat, damit durch die Flockungshilfsmittel ein guter Restaustrag ermöglicht wird.The invention also provides that the waste water also known per se organic and / or inorganic flocculants, in particular organic polymers, are added. Appropriate the flocculants are added in the last chamber, in which the wastewater is already the Has obtained the greatest possible degree of purification, so that the flocculants ensure a good residual discharge is made possible.
Es ist auch möglich, zwischen den einzelnen Flotationskammern besondere Reaktionsräume vorzusehen,
in denen die Flockungshilfsmittel zugesetzt werden.
Der biologisch aktive organische Schlamm einer der Flotationsstufe kann einer biologischen Stufe als
Überschußschlamm entnommen werden. Bei einem solchen Verfahren mit nachgeschalteter biologischer
Stufe kann es auch sinnvoll sein, die in den letzten Flotationskammern zugesetzten Schlammengen nicht
restlos auszuflotieren, sondern an die biologische Stufe weiterzugeben.It is also possible to provide special reaction spaces between the individual flotation chambers, in which the flocculants are added.
The biologically active organic sludge of one of the flotation stages can be removed from a biological stage as excess sludge. In such a process with a downstream biological stage, it can also be useful not to completely float the sludge quantities added in the last flotation chambers, but to pass them on to the biological stage.
Sofern keine hinreichende Menge Überschußschlamm vorhanden ist oder aber keine nachbiologische Stufe existiert, der aktiver organischer Schlamm entnommen werden kann, ist nach einem weiteren Merkmal der Erfindung vorgesehen, daß ein Teil des Feststoffaustrages durch Sauerstoffzufuhr in einem oder mehreren Reaktionsräumen aktiviert und dem Flotationskreislauf wieder zugesetzt wird.Unless there is a sufficient amount of excess sludge or no post-biological sludge Stage exists from which active organic sludge can be removed is after another Feature of the invention provided that part of the solids discharge by oxygen supply in one or activated several reaction chambers and added to the flotation circuit again.
Claims (6)
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1816932A DE1816932C3 (en) | 1968-12-24 | 1968-12-24 | Process for the purification of waste water with a flotation stage |
NL6919007A NL6919007A (en) | 1968-12-24 | 1969-12-18 | |
ES374847A ES374847A1 (en) | 1968-12-24 | 1969-12-23 | Procedure for wastewater purification. (Machine-translation by Google Translate, not legally binding) |
CH1922869A CH500140A (en) | 1968-12-24 | 1969-12-24 | Process for the purification of waste water with a flotation stage |
FR6944880A FR2027060A1 (en) | 1968-12-24 | 1969-12-24 | Purification of effluent by treatment with - a flotation agent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1816932A DE1816932C3 (en) | 1968-12-24 | 1968-12-24 | Process for the purification of waste water with a flotation stage |
Publications (3)
Publication Number | Publication Date |
---|---|
DE1816932A1 DE1816932A1 (en) | 1970-07-02 |
DE1816932B2 true DE1816932B2 (en) | 1978-06-01 |
DE1816932C3 DE1816932C3 (en) | 1979-02-08 |
Family
ID=5717358
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE1816932A Expired DE1816932C3 (en) | 1968-12-24 | 1968-12-24 | Process for the purification of waste water with a flotation stage |
Country Status (5)
Country | Link |
---|---|
CH (1) | CH500140A (en) |
DE (1) | DE1816932C3 (en) |
ES (1) | ES374847A1 (en) |
FR (1) | FR2027060A1 (en) |
NL (1) | NL6919007A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3014678A1 (en) * | 1979-04-16 | 1980-11-06 | Mobil Oil Corp | WATER TREATMENT REFINING SYSTEM AND INDUSTRIAL WASTE TREATMENT METHOD |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL7701608A (en) * | 1977-02-16 | 1978-08-18 | Pielkenrood Vinitex Bv | METHOD AND SYSTEM FOR THE TREATMENT OF LIQUIDS, IN PARTICULAR WASTE WATER |
CH656374A5 (en) * | 1981-12-18 | 1986-06-30 | Benno Perren | METHOD FOR CONTINUOUSLY SEPARATING SUBSTANCES CONTAINED IN A POLLUTED LIQUID, AND DEVICE FOR CARRYING OUT THE METHOD. |
DE3712032C1 (en) * | 1987-04-09 | 1988-11-24 | Franz Dipl-Ing Koeppl | Process and plant for the treatment of dissolved and undissolved substances containing recycled industrial waste water |
-
1968
- 1968-12-24 DE DE1816932A patent/DE1816932C3/en not_active Expired
-
1969
- 1969-12-18 NL NL6919007A patent/NL6919007A/xx unknown
- 1969-12-23 ES ES374847A patent/ES374847A1/en not_active Expired
- 1969-12-24 CH CH1922869A patent/CH500140A/en not_active IP Right Cessation
- 1969-12-24 FR FR6944880A patent/FR2027060A1/en not_active Withdrawn
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3014678A1 (en) * | 1979-04-16 | 1980-11-06 | Mobil Oil Corp | WATER TREATMENT REFINING SYSTEM AND INDUSTRIAL WASTE TREATMENT METHOD |
Also Published As
Publication number | Publication date |
---|---|
DE1816932A1 (en) | 1970-07-02 |
FR2027060A1 (en) | 1970-09-25 |
ES374847A1 (en) | 1972-01-16 |
CH500140A (en) | 1970-12-15 |
NL6919007A (en) | 1970-06-26 |
DE1816932C3 (en) | 1979-02-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE2908134C2 (en) | Plant for the purification of wastewater | |
DE2218180B2 (en) | ||
DE69416698T2 (en) | METHOD AND DEVICE FOR A WASTEWATER PURIFICATION PLANT | |
DE2640875B2 (en) | Two-stage activated sludge process for cleaning wastewater | |
DE3014678C2 (en) | ||
DE112016001462T5 (en) | Method for biological wastewater treatment with phosphorus removal | |
DE1816932C3 (en) | Process for the purification of waste water with a flotation stage | |
DE2756171B1 (en) | Process for the rehabilitation of wastewater treatment plants that are overloaded during continuous operation and for the implementation of such a process | |
DE4036548C2 (en) | Process for the purification of wastewater with the help of a wastewater treatment plant which has two activation stages | |
DE2341415A1 (en) | Chemical waste water processing - using purifier contg. calcium carbonate, acid and or metal sulphate, oil adsorbent and flocculant | |
DE2239406A1 (en) | METHOD FOR TREATMENT OF BIODEGRADABLE WASTEWATER AND EQUIPMENT FOR CARRYING OUT THIS PROCESS | |
DE2447501C3 (en) | Process and device for wastewater purification | |
DE3602944C1 (en) | Process and plant for the purification of waste water containing poorly degradable substances | |
DE3602736A1 (en) | Process and device for the biological degradation of phosphorus from waste water | |
DE3117805A1 (en) | Plant for purifying waste water | |
DE2829537A1 (en) | METHODS FOR TREATMENT OF WATER AND SLURRY | |
DE1172614B (en) | Process for the two-stage treatment of waste water | |
DE504993C (en) | Process for the chemical-biological cleaning of waste water | |
DE2536628A1 (en) | Industrial wastes treatment after iron hydroxide flocculation - by anodic oxidation and aluminium hydroxide flocculation | |
DE2641718A1 (en) | METHODS FOR WASTE WATER PURIFICATION | |
DE2627781C2 (en) | Biological-chemical process for wastewater treatment with dephosphating | |
DE112016001925T5 (en) | Method for biological wastewater treatment | |
DE3508299C2 (en) | ||
EP0087092B1 (en) | Process and device for the biological purification of waste water containing phosphate | |
CH622227A5 (en) |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C3 | Grant after two publication steps (3rd publication) | ||
8339 | Ceased/non-payment of the annual fee |