EP0177838B1 - Dispositif d'introduction de floculants dans des boues à l'intérieur de la chambre de chargement d'une centrifugeuse - Google Patents
Dispositif d'introduction de floculants dans des boues à l'intérieur de la chambre de chargement d'une centrifugeuse Download PDFInfo
- Publication number
- EP0177838B1 EP0177838B1 EP85112142A EP85112142A EP0177838B1 EP 0177838 B1 EP0177838 B1 EP 0177838B1 EP 85112142 A EP85112142 A EP 85112142A EP 85112142 A EP85112142 A EP 85112142A EP 0177838 B1 EP0177838 B1 EP 0177838B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- sludge
- flocculant
- feed tube
- inlet chamber
- centrifuge
- 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
- 239000010802 sludge Substances 0.000 title claims description 63
- 239000008394 flocculating agent Substances 0.000 title claims description 10
- 239000013013 elastic material Substances 0.000 claims description 3
- 239000007787 solid Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 3
- 230000002093 peripheral effect Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 230000002996 emotional effect Effects 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/20—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B11/00—Feeding, charging, or discharging bowls
- B04B11/02—Continuous feeding or discharging; Control arrangements therefor
Definitions
- the invention relates to a device for introducing flocculants into the sludge inside the inlet chamber of a centrifuge, consisting of a flocculant feed pipe which is passed through the sludge feed pipe and projects into the inlet chamber of the centrifuge provided with sludge through-openings, wherein in the inlet chamber at a distance from the mouth of the sludge feed pipe is arranged a baffle perpendicular to the mouth of the sludge feed pipe.
- the object of the invention is therefore to provide a device for introducing flocculants into the sludge within the inlet chamber of a centrifuge, which enables the flocculant to be optimally mixed with the sludge while using as little flocculant as possible.
- the baffle is provided with a baffle cone centrally directed onto the mouth of the sludge feed pipe, and in that the flocculant feed pipe in the sludge feed pipe is axially adjustable and / or rotatably held so that its outlet opening onto the area is directed between the baffle and the sludge passage openings arranged at a distance therefrom in the inlet chamber.
- baffle wall according to the invention is provided with a baffle cone centrally directed onto the mouth of the sludge feed pipe, an all-round uniform distribution of the sludge is very advantageously achieved in the inlet chamber, into which the flocculants can be introduced and mixed with it also equally .
- the flocculant feed pipe in the sludge feed pipe is axially adjustable and / or rotatably held so that its outlet opening is directed to the area between the baffle and the sludge passage openings arranged at a distance therefrom in the inlet chamber very advantageously the flocculant jet emerging from the nozzle-shaped outlet opening of the flocculant feed pipe is directed or adjusted precisely to the sludge flow located in the peripheral region of the inlet chamber, in which the flocculant jet penetrates deeply into the sludge and thereby mixes intimately with the sludge.
- this area lies between the baffle wall of the inlet chamber and the sludge passage openings in the chamber, specifically where the sludge flow undergoes a strong deflection in the opposite direction to the inlet direction.
- the intimate mixing of the flocculant with the sludge that has already taken place in this area is intensified by the subsequent subsequent strong redirection and circulation of the sludge in the area of the passage openings.
- the flocculant addition can very advantageously be reduced to the minimum required in each case, as a result of which, in comparison with the previously known flocculant supply devices, savings in flocculants can be achieved in some cases of up to over 50%.
- the flocculant feed tube consists of several parts which are arranged to be pluggable or telescopically displaceable. This configuration of the flocculant feed tube makes it easy to remove and install the flocculant feed tube in a small space.
- the flocculant supply pipe consists of a flexible or elastic material, in particular rubber.
- a flocculant feed pipe is particularly characterized by the easy handling during installation and removal and by the self-sealing at the through opening in the sludge feed pipe.
- the centrifuge consists of a centrifuge drum 1, in which a screw conveyor 2 is arranged coaxially, the shaft of which is designed as a hollow shaft 3 and is externally surrounded by the screw spiral 4.
- the hollow shaft 3 is closed by an end wall 5, which is provided in the central region with an opening 6 through which a stationary arranged sludge feed pipe 7 is passed.
- a baffle 8 with baffle cone 9 is installed in the hollow shaft 3 at a distance from the end wall 5, which together with the end wall 5 and the hollow shaft 3 forms an inlet chamber 10 for the sludge.
- Provided in the hollow shaft 3 in the area of this inlet chamber 10 are a plurality of openings 11 evenly distributed over the circumference for the sludge to pass into the centrifuge drum 1.
- a flocculant feed pipe 12 is guided through the sludge feed pipe 7, which opens into the inlet chamber 10 and is provided in the end region with a nozzle-shaped outlet opening 13.
- This flocculant feed pipe 12 is held in the sludge feed pipe 7 according to the invention both axially adjustable and rotatable.
- a tubular extension piece 14 with a locking screw 15 arranged at the outer end of the sludge feed pipe 7 serves as a holder. By loosening the adjusting screw 15, the flocculant feed pipe 12 can be moved both in the axial direction and rotated about the axis.
- the flocculant supply pipe 12 with the nozzle-shaped outlet opening 13 can be adjusted very advantageously in such a way that the flocculant jet 16 emerging from the nozzle-shaped outlet opening 13 under pressure strikes the rotating sludge layer located in the peripheral area within the sludge inlet chamber 10 and at least partially penetrates, with an intimate mixing of sludge and flocculant.
- this area lies between the baffle 8 and the sludge passage openings 11, specifically at the point where the sludge in the peripheral region of the inlet chamber 10 is away from the baffle wall 8, approximately in the axial direction towards the sludge passage openings 11 emotional.
- the amount of flocculant supplied to the sludge in the inlet chamber 10 via line 12, for example under a pressure of approximately 0.5 to 10 bar, can be optimally adjusted in this way, i.e. be adjusted to the amount of flocculant that is necessary to capture and flocculate all solid particles present in the sludge. In this way, the flocculant consumption can be reduced considerably in comparison to the previously known devices and the separation effect can be significantly improved.
- the flocculant supply pipe 12 can consist of several parts 17 which are arranged to be pluggable or telescopically displaceable.
- the flocculant feed pipe 12 can also be attached in the sludge feed pipe 7 centrally, laterally at the top in the axial direction, or also at an angle to it.
- the flocculant feed pipe 12 can optionally also be introduced into the inlet chamber 10 outside the sludge feed pipe 12.
- the flocculant supply pipe 12 according to the invention can also be very advantageously provided with a plurality of nozzle-shaped outlet openings.
Landscapes
- Centrifugal Separators (AREA)
Claims (3)
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3437157 | 1984-10-10 | ||
DE3437157 | 1984-10-10 | ||
DE3444349 | 1984-12-05 | ||
DE19843444349 DE3444349A1 (de) | 1984-10-10 | 1984-12-05 | Vorrichtung zum einbringen von flockungsmitteln in den schlamm innerhalb der einlaufkammer einer zentrifuge |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0177838A2 EP0177838A2 (fr) | 1986-04-16 |
EP0177838A3 EP0177838A3 (en) | 1987-10-28 |
EP0177838B1 true EP0177838B1 (fr) | 1990-05-09 |
Family
ID=25825520
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP85112142A Expired - Lifetime EP0177838B1 (fr) | 1984-10-10 | 1985-09-25 | Dispositif d'introduction de floculants dans des boues à l'intérieur de la chambre de chargement d'une centrifugeuse |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0177838B1 (fr) |
DE (2) | DE3444349A1 (fr) |
FI (1) | FI853805L (fr) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5374234A (en) * | 1990-03-13 | 1994-12-20 | Alfa-Laval Separation A/S | Decanter centrifuge with energy dissipating inlet |
DK170967B1 (da) * | 1990-03-13 | 1996-04-09 | Alfa Laval Separation As | Dekantercentrifuge |
US6561965B1 (en) | 2000-10-20 | 2003-05-13 | Alfa Laval Inc. | Mist pump for a decanter centrifuge feed chamber |
DE102004057861A1 (de) * | 2004-11-30 | 2006-06-01 | Siebtechnik Gmbh | Einlaufrohr einer Zentrifuge |
CN110550712B (zh) * | 2019-08-27 | 2022-03-22 | 济南林源环保工程有限公司 | 一种污水处理絮凝剂快速混合设备 |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1101301B (de) * | 1957-08-23 | 1961-03-02 | Krauss Maffei Ag | Verfahren und Vorrichtung zum Eindicken von Schlamm, insbesondere Abwasserschlamm, der schwer sedimentierbare Bestandteile enthaelt, durch Zentrifugieren unter Verwendung eines Flockungsmittels |
DE1215606B (de) * | 1963-01-31 | 1966-04-28 | Beteiligungs & Patentverw Gmbh | Vorrichtung zum Vermischen von Flockungsmitteln mit Schlaemmen in Absetzzentrifugen |
US3471081A (en) * | 1967-12-21 | 1969-10-07 | Ametek Inc | Acid feed pipe |
DE2260461C3 (de) * | 1972-12-11 | 1980-06-04 | Krauss-Maffei Ag, 8000 Muenchen | Filterzentrifuge |
GB1602601A (en) * | 1977-05-24 | 1981-11-11 | Broadbent & Sons Ltd Thomas | Solid bowl decanter centrifuges |
-
1984
- 1984-12-05 DE DE19843444349 patent/DE3444349A1/de not_active Withdrawn
-
1985
- 1985-09-25 DE DE8585112142T patent/DE3577515D1/de not_active Expired - Lifetime
- 1985-09-25 EP EP85112142A patent/EP0177838B1/fr not_active Expired - Lifetime
- 1985-10-02 FI FI853805A patent/FI853805L/fi not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
FI853805A0 (fi) | 1985-10-02 |
DE3444349A1 (de) | 1986-04-10 |
DE3577515D1 (de) | 1990-06-13 |
EP0177838A2 (fr) | 1986-04-16 |
FI853805L (fi) | 1986-04-11 |
EP0177838A3 (en) | 1987-10-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0550510B1 (fr) | Buse d'aeration de liquides contenant des substances organiques | |
DE3216393C2 (fr) | ||
DE2417355A1 (de) | Zentrifugaldruckduese | |
EP0177838B1 (fr) | Dispositif d'introduction de floculants dans des boues à l'intérieur de la chambre de chargement d'une centrifugeuse | |
DE3640315C2 (fr) | ||
EP0082268B1 (fr) | Dispositif pour l'électroplacage des rouleaux d'impression | |
DE4402516A1 (de) | Vorrichtung und Verfahren zur verstopfungsfreien Drosselung einer fluiden Suspensionsströmung | |
EP0023899B1 (fr) | Installation pour la déshydratation de suspensions aqueuses et de boues | |
DE3230977A1 (de) | Zweistoff-zerstaeubungsduese | |
DE2918768C2 (de) | Verfahren zum Entnehmen von Stoffproben aus einem Behälter und Vorrichtung zur Durchführung des Verfahrens | |
DE10053296C2 (de) | Hochrotationszerstäuber zur Aufbringung von Pulverlack | |
DE3741843A1 (de) | Verfahren und vorrichtung zur innigen vermischung von fluessigkeiten mit gasen | |
DE3120260A1 (de) | Vorrichtung zum befeuchten von schuettguetern | |
DE2942647A1 (de) | Zentrifuge zum trenne von feststoff- fluessigkeitsgemischen | |
EP0075258A2 (fr) | Appareil pour le revêtement d'objets par un liquide | |
DE2822533A1 (de) | Festkoerper-vollmanteldekantierzentrifuge | |
EP0781168A1 (fr) | Panier centrifuge autodechargeur | |
DE19724882A1 (de) | Adapter für Offenend-Rotorspinnvorrichtungen | |
DE4431369C2 (de) | Vorrichtung für die Klärung von Abwasser | |
WO1996014129A1 (fr) | Dispositif a filtres en forme de bougie utilise pour la filtration de biere | |
DE7535504U (de) | Flockulator fuer wasserreinigungsanlagen | |
DE4422277C1 (de) | Verfahren zum Beschicken von Kammerfilterpressen, Membranfilterpressen, Siebbandpressen und Zentrifugen mit Schlamm zur Entwässerung desselben sowie Düse zur Durchführung des Verfahrens | |
DE4329716C2 (de) | Vorrichtung zum Beschichten einer optischen Faser | |
DE1482723A1 (de) | Vorrichtung zum Eindicken von Trueben | |
DE3428103A1 (de) | Auslassduese fuer zentrifugentrommeln |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A2 Designated state(s): DE FR GB IT SE |
|
PUAL | Search report despatched |
Free format text: ORIGINAL CODE: 0009013 |
|
AK | Designated contracting states |
Kind code of ref document: A3 Designated state(s): DE FR GB IT SE |
|
17P | Request for examination filed |
Effective date: 19871218 |
|
17Q | First examination report despatched |
Effective date: 19880610 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): DE FR GB IT SE |
|
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) | ||
REF | Corresponds to: |
Ref document number: 3577515 Country of ref document: DE Date of ref document: 19900613 |
|
ITF | It: translation for a ep patent filed | ||
ET | Fr: translation filed | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19900829 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 19900913 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: SE Payment date: 19900918 Year of fee payment: 6 |
|
ITTA | It: last paid annual fee | ||
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Effective date: 19910925 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Effective date: 19910926 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Effective date: 19920529 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
EUG | Se: european patent has lapsed |
Ref document number: 85112142.6 Effective date: 19920408 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20031031 Year of fee payment: 19 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20050401 |