WO1993017773A1 - Apparatus for separation - Google Patents
Apparatus for separation Download PDFInfo
- Publication number
- WO1993017773A1 WO1993017773A1 PCT/SE1993/000198 SE9300198W WO9317773A1 WO 1993017773 A1 WO1993017773 A1 WO 1993017773A1 SE 9300198 W SE9300198 W SE 9300198W WO 9317773 A1 WO9317773 A1 WO 9317773A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- inner cylinder
- water
- waste water
- depth
- cylinder
- Prior art date
Links
Classifications
-
- 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
- B01D21/02—Settling tanks with single outlets for the separated liquid
- B01D21/08—Settling tanks with single outlets for the separated liquid provided with flocculating compartments
-
- 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
- B01D21/2411—Feed mechanisms for settling tanks having a tangential inlet
-
- 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
- B01D21/26—Separation of sediment aided by centrifugal force or centripetal force
-
- 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
- B01D21/26—Separation of sediment aided by centrifugal force or centripetal force
- B01D21/267—Separation of sediment aided by centrifugal force or centripetal force by using a cyclone
Definitions
- the present invention relates to a device for increased separa- tion efficiency at waste water purification or purification of other water with large sedimentation amounts and comprising two concentric cylinders, where the waste water is arranged to be introduced in the outer cylinder and is arranged to pass into the inner cylinder.
- the object of the present invention is to obtain a possibility of increasing the amount of sludge in a plant for sewage water purification and to lower the amount of COD (oxygen consuming) substances in the water (sludge water) which is fed further in the purification process and/or to a recipient.
- the water is introduced , after a coarse filtration, into large aeration basins through which the water is allowed to pass during a simultaneous, vigorous aeration by means of air introduced via nozzles in the bottom of the basins before the water (sludge water) is led to a sedimentation basin for precipitation of what is called, in daily language, the bi- ological sludge.
- the water from the sedimentation basin is then led further on to process steps for chemical precipitation and/or direct to a recipient.
- Another process at waste water purification is pre- precipitation where an ingoing waste water is pre-precipitated using a coagulating agent in order to rapidly reduce the amount of settable material in order to reduce the volumes of the waste water plant.
- WO 89/09193 discloses a device at sedimentation of sludge, which comprises two concentric cylinders , whereby the outer cylinder is provided with an inlet opening for the waste water, the inner cylinder, at its bottom is provided with an inlet and the two cylinders are provided with a common spillway from the inner cylinder over the outer cylinder.
- the device is. intended to create an increased dwell time in order to improve contact, and thereby formation of floes by the rotational movement which is created by forcing the water into the outer jacket forming cylinder and further up through the inner cylinder.
- the device provides a certain improvement, whereby, however, it has been realized that the dwell time and the effect in the inner cylin ⁇ der are not the expected ones .
- the outer cylinder is provided with an inlet
- the inner cylinder is provided with a spillway
- the inner cylinder is provided with a substantially conical insert arranged with its tapering end downwardly directed.
- the amount of suspended material of a water of a subsequent set- tling step is reduced with up to 70%.
- the amount of oxygen con ⁇ suming material, particularly in heavy loaded plants, has also been reduced with up to 50%.
- FIG 1 schematically shows a plant in accordance with the pre ⁇ sent invention.
- Two concentric cylinders are denoted 1 and 2, whereby the outer cylinder 1 reaches over about half of depth of the inner cylin ⁇ der 2.
- the cylinders 1 and 2 have, in the embodiment shown, a common upper plane.
- the inner cylinder 2 is completely open upwardly and downwardly, while the outer cylinder 1 is closed downwardly.
- an inlet 3 is arranged and in the upper edge of the inner cylinder 2 an in ⁇ let spillway 4 is arranged.
- the area of the inlet 3 is about one third of the area of the inlet spillway 4.
- the conical insert 5 is arranged with its tapering end pointing downwardly, and is further movably arranged in vertical position along its longi ⁇ tudinal axis.
- the diameter of the insert 5 is about half the diameter of the diameter of the inner cylinder 2.
- the insert 5 extends to about two thirds of the depth of the inner cylinder 5 2, as well, preferably to 50 to 80% of the depth of the inner cylinder 2.
- the height position of the insert 5 can be adjusted in several ways, whereby in the accompanying figure, a scaffold 6 is placed over the inner cylinder and is provided with a mo ⁇ tor 7, which lifts, and lowers, respectively, a wire/chain 8 1-0 connected to the conical insert 5.
- the device of the present invention In using the device of the present invention in a sewage water plant, the device preferably being placed over a settling pocket, the sewage water is fed in through the inlet 3 of the ⁇ - 5 outer cylinder 1, and will, by means of the jacket effect to be rotated upwardly, and falls into the inner cylinder 2, where it, by means of the conical insert 5 will be rotated downwardly in order to exit the device through the open bottom of the in ⁇ ner cylinder 2.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The present invention relates to a device for increased separation efficiency at waste water purification or purification of other water with large sedimentation amounts and comprising two concentric cylinders, where the waste water is arranged to be introduced in the outer cylinder and is arranged to pass into the inner cylinder, whereby the outer cylinder (1) is provided with an inlet (3), the inner cylinder (2) is provided with an inlet spillway (4), the inner cylinder (2) is provided with a substantially conical insert (5) arranged with its tapering end downwardly directed.
Description
APPARATUS FOR SEPARATION DESCRIPTION Technical field
The present invention relates to a device for increased separa- tion efficiency at waste water purification or purification of other water with large sedimentation amounts and comprising two concentric cylinders, where the waste water is arranged to be introduced in the outer cylinder and is arranged to pass into the inner cylinder.
The object of the present invention is to obtain a possibility of increasing the amount of sludge in a plant for sewage water purification and to lower the amount of COD (oxygen consuming) substances in the water (sludge water) which is fed further in the purification process and/or to a recipient.
Background of the invention
At so called biological purification in a plant for the purifi¬ cation of waste water the water is introduced , after a coarse filtration, into large aeration basins through which the water is allowed to pass during a simultaneous, vigorous aeration by means of air introduced via nozzles in the bottom of the basins before the water (sludge water) is led to a sedimentation basin for precipitation of what is called, in daily language, the bi- ological sludge. The water from the sedimentation basin is then led further on to process steps for chemical precipitation and/or direct to a recipient.
Outgoing water from the precipitation basin contains, however, too large amounts of suspended material and particularly at heavy loaded plants, the outgoing water will also contain large amounts of oxygen consuming material. The more pollutants, which are brought forward to the chemical precipitation step, the more chemicals are needed to reduce the amounts of pollut- ants to an acceptable level. However, there is a desire to re¬ duce the amount o chemicals which are used in a waste water pu¬ rification plant for several reasons, partly economical, as the
chemicals is a great cost in the operation of the plant, partly for the risk of dissolving undesired side products, or at very acidic waters, release of dissociated aluminium or iron, which ions can damage biological life. Normally such a risk will not appear but the metal salts used will be precipitated with the so called chemical sludge.
Another process at waste water purification is pre- precipitation where an ingoing waste water is pre-precipitated using a coagulating agent in order to rapidly reduce the amount of settable material in order to reduce the volumes of the waste water plant. The larger the amounts of COD and BOD mate¬ rials, which are present, the larger is the load, and thereby a larger plant is needed for a certain amount of waste water.
Other processes are simultaneous precipitation and post- precipitation, whereby precipitation is carried out using a chemical flocculating agent in different steps of the waste wa¬ ter purification process.
WO 89/09193 discloses a device at sedimentation of sludge, which comprises two concentric cylinders , whereby the outer cylinder is provided with an inlet opening for the waste water, the inner cylinder, at its bottom is provided with an inlet and the two cylinders are provided with a common spillway from the inner cylinder over the outer cylinder. The device is. intended to create an increased dwell time in order to improve contact, and thereby formation of floes by the rotational movement which is created by forcing the water into the outer jacket forming cylinder and further up through the inner cylinder. The device provides a certain improvement, whereby, however, it has been realized that the dwell time and the effect in the inner cylin¬ der are not the expected ones .
Thus demands have been raised for an increased settling effi¬ ciency in the different precipitation steps and thereby a low¬ ered amount of outgoing suspended material to a subsequent pre-
cipitation or recipient.
Description of the present invention
It has now surprisingly been shown possible to be able to re- duce the amount of outgoing suspended material by means of the present invention, which is characterized in that the outer cylinder is provided with an inlet, that the inner cylinder is provided with a spillway, that the inner cylinder is provided with a substantially conical insert arranged with its tapering end downwardly directed.
Further characteristics are evident from the accompanying claims .
By means of the present invention it is achieved that the amount of suspended material of a water of a subsequent set- tling step is reduced with up to 70%. The amount of oxygen con¬ suming material, particularly in heavy loaded plants, has also been reduced with up to 50%.
The invention will be described in the following with reference to the accompanying drawings, wherein
FIG 1 schematically shows a plant in accordance with the pre¬ sent invention.
Two concentric cylinders are denoted 1 and 2, whereby the outer cylinder 1 reaches over about half of depth of the inner cylin¬ der 2. The cylinders 1 and 2 have, in the embodiment shown, a common upper plane. The inner cylinder 2 is completely open upwardly and downwardly, while the outer cylinder 1 is closed downwardly. In the lower part of the cylinder 1 an inlet 3 is arranged and in the upper edge of the inner cylinder 2 an in¬ let spillway 4 is arranged. The area of the inlet 3 is about one third of the area of the inlet spillway 4. Further, there is a conical insert 5 in the inner cylinder 2 concentrically arranged with the other cylinders 1 and 2. The conical insert 5 is arranged with its tapering end pointing downwardly, and is
further movably arranged in vertical position along its longi¬ tudinal axis. The diameter of the insert 5 is about half the diameter of the diameter of the inner cylinder 2. The insert 5 extends to about two thirds of the depth of the inner cylinder 5 2, as well, preferably to 50 to 80% of the depth of the inner cylinder 2. The height position of the insert 5 can be adjusted in several ways, whereby in the accompanying figure, a scaffold 6 is placed over the inner cylinder and is provided with a mo¬ tor 7, which lifts, and lowers, respectively, a wire/chain 8 1-0 connected to the conical insert 5.
In using the device of the present invention in a sewage water plant, the device preferably being placed over a settling pocket, the sewage water is fed in through the inlet 3 of the ■-5 outer cylinder 1, and will, by means of the jacket effect to be rotated upwardly, and falls into the inner cylinder 2, where it, by means of the conical insert 5 will be rotated downwardly in order to exit the device through the open bottom of the in¬ ner cylinder 2.
20
By means of the rotation both in the outer and in the inner cylinder the water will obtain a considerable dwell time, which influences the formation of floes positively. By means of the present invention the sludge yield can be considerably improved 5 and an increase with up to 25% has been determined in tests made visavi the cylindrical device shown in WO 89/09193.
At higher flow rates through the device the conical insert is raised in order not o counteract the flow too much, while at
30 low flow rates the insert 5 is lowered in order to provide the correct rotation in the device.
5
Claims
1. Device for increased separation efficiency at waste water purification or purification of other water with large sedimen¬ tation amounts and comprising two concentric cylinders, where the waste water is arranged to be introduced in the outer cyl¬ inder and is arranged to pass into the inner cylinder, charac¬ terized in that the outer cylinder (1) is provided with an in¬ let (3), that the inner cylinder (2) is provided with an inlet spillway (4), that the inner cylinder (2) is provided with a substantially conical insert (5) arranged with its tapering end downwardly directed.
2. Device according to claim 1, characterized in that the coni¬ cal insert (5) is movably arranged along its vertical axis.
3. Device according to claims 1-2, characterized in that the conical insert (5) extends over a depth which is 50 to 80 % of the depth of the inner cylinder (2).
4. Device according to claim 3, characterized in that the depth is two thirds of the depth of the inner cylinder (2).
5. Device according to one or more of claims 1 to 4 , character¬ ized in that the diameter of the base of the conical insert (5) is half the diameter of inner cylinder (2).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NO943290A NO304680B1 (en) | 1992-03-06 | 1994-09-06 | separation device |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE9200695-6 | 1992-03-06 | ||
SE9200695A SE9200695D0 (en) | 1992-03-06 | 1992-03-06 | DEVICE FOR SEPARATION |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1993017773A1 true WO1993017773A1 (en) | 1993-09-16 |
Family
ID=20385539
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/SE1993/000198 WO1993017773A1 (en) | 1992-03-06 | 1993-03-05 | Apparatus for separation |
Country Status (3)
Country | Link |
---|---|
NO (1) | NO304680B1 (en) |
SE (1) | SE9200695D0 (en) |
WO (1) | WO1993017773A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999051530A1 (en) * | 1996-10-18 | 1999-10-14 | Kvaerner Technology & Research Ltd. | Flocculator apparatus |
GB2340114A (en) * | 1998-04-07 | 2000-02-16 | Kvaerner Tech & Res Ltd | Flocculator apparatus |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE90855C1 (en) * | ||||
DE2708019A1 (en) * | 1976-02-27 | 1977-09-01 | Filtrator Ab | SEPARATOR WITH DISPOSABLE CONTAINER |
GB2152401A (en) * | 1983-11-30 | 1985-08-07 | Blue Circle Ind Plc | Clarifier |
EP0363050A1 (en) * | 1988-10-07 | 1990-04-11 | Hydro International Limited | Separator |
-
1992
- 1992-03-06 SE SE9200695A patent/SE9200695D0/en unknown
-
1993
- 1993-03-05 WO PCT/SE1993/000198 patent/WO1993017773A1/en active Application Filing
-
1994
- 1994-09-06 NO NO943290A patent/NO304680B1/en not_active IP Right Cessation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE90855C1 (en) * | ||||
DE2708019A1 (en) * | 1976-02-27 | 1977-09-01 | Filtrator Ab | SEPARATOR WITH DISPOSABLE CONTAINER |
GB2152401A (en) * | 1983-11-30 | 1985-08-07 | Blue Circle Ind Plc | Clarifier |
EP0363050A1 (en) * | 1988-10-07 | 1990-04-11 | Hydro International Limited | Separator |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999051530A1 (en) * | 1996-10-18 | 1999-10-14 | Kvaerner Technology & Research Ltd. | Flocculator apparatus |
GB2340114A (en) * | 1998-04-07 | 2000-02-16 | Kvaerner Tech & Res Ltd | Flocculator apparatus |
GB2340114B (en) * | 1998-04-07 | 2002-09-11 | Kvaerner Technology & Res Ltd | Flocculator apparatus |
Also Published As
Publication number | Publication date |
---|---|
NO943290D0 (en) | 1994-09-06 |
SE9200695D0 (en) | 1992-03-06 |
NO304680B1 (en) | 1999-02-01 |
NO943290L (en) | 1994-11-03 |
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