WO2010043221A1 - Schüttgutreinigungsanlage - Google Patents
Schüttgutreinigungsanlage Download PDFInfo
- Publication number
- WO2010043221A1 WO2010043221A1 PCT/DE2009/075056 DE2009075056W WO2010043221A1 WO 2010043221 A1 WO2010043221 A1 WO 2010043221A1 DE 2009075056 W DE2009075056 W DE 2009075056W WO 2010043221 A1 WO2010043221 A1 WO 2010043221A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- bulk material
- arrangement
- water
- cleaning
- soiled
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
- B03B5/02—Washing granular, powdered or lumpy materials; Wet separating using shaken, pulsated or stirred beds as the principal means of separation
-
- 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
Definitions
- the invention relates to an arrangement for cleaning soiled bulk material.
- Bulk material in particular sand, granules or gravel, is frequently used as filter material, for example in sewage treatment plants. By filtering the bulk material is contaminated. Also in road construction or in the oil industry bulk material is used, which is polluted in various ways. Contaminated materials to which the present invention applies also include oil sludges. The dirt or the impurity are often very difficult to separate using chemicals from the bulk material. This causes high costs for cleaning. Alternatively, the contaminated bulk material is no longer used and only final storage.
- German Patent DE 40 34 227 C2 describes a method for treating deposits, in particular sediments, in particular of sediments in the drainage of water, of waste material or the like, in which the material to be treated is classified in successive stages and cleaned of pollutants.
- the collected sediments arrive on a screen with high-frequency vibration.
- the passed material is fed to a sword scrubber and then passes into a screening cyclone, which forms a first separation stage with a washing drum and a vibrating classifier.
- organic and inorganic components are fed to a cyclone plant, which controls the separation of the sand by a Schwergübsortierer over a
- German utility model DE 298 24 791 Ul also discloses an arrangement for sand separation by density gradients. Through the sand mixture fine bubble air is bubbled. This sand store can do the job of an upstream
- the object of the invention is therefore to avoid the above-mentioned and other existing disadvantages of the prior art and to provide an environmentally friendly device that allows the cleaning of very heavily polluted bulk material.
- the arrangement for the purification of soiled bulk material of the type mentioned includes the following components: a) a receiving and conveying device for receiving and conveying the soiled bulk material within the arrangement,
- a mechanical separation unit for the mechanical separation of the bulk material with a supply and mixing device for the supply and mixing of support grains and water to the polluted bulk material
- the invention is based on a principle which relies solely on mechanical cleaning stages, which are environmentally friendly in contrast to the use of chemicals. These mechanical components are arranged and combined in such a way that the result of the cleaning is optimal without unduly burdening the environment.
- the arrangement consists of several processing stages. about
- Conveyor belts the respective material is transported from processing level to processing level.
- support grains with water are added to the contaminated bulk material in the feed and mixing device.
- Support grain the impurities are crushed into small components, shot or dissolved.
- the bulk material, support grains and water mixture is conveyed onto a vibrating screen.
- the support grains are screened out of the mixture and returned to the feed and mixing device. Oversizes or larger contaminants can also be screened out here and, for example, discharged via a conveyor belt and thus removed from the further washing process.
- a centrifuge In a third processing stage, the now present mixture from the second processing stage is fed to a centrifuge.
- the centrifuge separates a large part of the bulk material from water and impurities due to their different
- the separated water with the dissolved impurities is passed for example in an intermediate container.
- the bulk material falls into an upflow classifier placed under the centrifuge.
- the Aufströmklassierer separates by its functional principle bulk of suspended matter. The suspended matter is thereby rinsed out by water and also passed into the between container.
- the rinsed bulk material from the Aufströmklassierer is placed in a fifth processing stage on a Schwingentskysserer. This drains that
- Arrangement for cleaning soiled bulk material having a first high-pressure water generator.
- This high-pressure generator leads the water at high pressure into the feeding and mixing device.
- This sludge dewatering apparatus may be added to the arrangement as the sixth processing stage.
- the contaminants, suspended matter and process water fed into the intermediate container are pumped off via a pumping station and fed to a sludge press. In this mud press is water from the rest
- the cleaned water will be returned to the bulk material washing.
- the squeezed mud cake can be disposed of.
- the arrangement according to the invention is designed to be mobile for the purpose of cleaning soiled bulk material.
- Wastewater treatment plants do not require continuous cleaning of bulk material.
- the cost of such a cleaning arrangement are not worthwhile, especially for small sewage treatment plants. Therefore, this mobility of the arrangements serves to be able to always provide the arrangement for the cleaning of soiled bulk material at its place of use. For example, the cost of such a facility may be shared by smaller communities.
- the arrangement for cleaning soiled bulk material is formed as a unit. This measure makes it compact and can therefore be used practically anywhere.
- a second high-pressure water generator for the screening device is provided, which the dirty bulk material on the
- Vibrating screen irradiated with water under high pressure for example, the contaminated bulk material is irradiated via water nozzles.
- One or more water nozzles can be swiveled.
- the water jet accelerates the sieving process.
- the Grains of bulk material that pass through the openings of the sieve are rinsed through faster.
- the openings of the vibrating screen variable in size.
- the grain size can still be selected, which should pass through the sieve.
- the arrangement is formed mobile with a transport unit.
- the transport unit may, for example, be designed as a low loader, whereupon the arrangement according to the invention is largely permanently installed. In this way, the arrangement can be moved quickly everywhere.
- Fig. 1 shows a three-dimensional representation of an inventive arrangement for the purification of contaminated bulk material as a schematic schematic diagram.
- Fig. 2 shows a three-dimensional representation of a schematic diagram of the principles
- FIG. 3 shows in a three-dimensional representation a schematic outline sketch of the Aufströmklassierers the arrangement according to the invention.
- Fig. 1 is denoted by 10 an erf ⁇ ndungshiele arrangement for cleaning soiled bulk material.
- the assembly is located as a unit on a semi-trailer 11 for a semitrailer, not shown, whereby the arrangement becomes mobile. Wheels 13 of the trailer 11 are to be seen beginning.
- the contaminated bulk material is introduced into a funnel 12 designed as a receptacle.
- the contaminated bulk material falls through the hopper 12 on a conveyor belt 14, 16, 22, 29, 34.
- the conveyor belt 14, 16, 22, 29, 34 consists of several components and transports the contaminated and later cleaned bulk material, as well as the contamination between the individual processing stages.
- About the conveyor belts 16 support grains are fed to the conveyor belt 14 the polluted bulk material.
- This mixture enters a mixing device 18 of a mechanical separation unit
- a first high-pressure water generator 20 irradiated with its water jet, the mixture of supporting grains and contaminated bulk material. Due to the added supporting grain, the impurities are broken down into small components, shot up or dissolved.
- the conveyor belt 22 below the mixing device 18 transports the dissolved mixture of soiled bulk material, support grains and water on a vibrating screen 24 a screening device 25.
- a second, not visible in this figure, high pressure generator generates one or more water jets, with which the soiled bulk material on the Vibrating screen 24 is irradiated to speed up the screening process.
- Openings 26 of the vibrating screen 24 are kept variable in size to be able to separate different particle sizes. The size of the openings 26 is chosen in particular so that the support grains are separated and fall from the vibrating screen 24 on the conveyor belts 16. From there, they are returned to the process, ie to the conveyor belt 14, the polluted bulk material for mixing.
- the contaminated bulk material is now supplied to a centrifuge 28 with a pump station, not shown.
- a centrifuge 28 In the centrifuge 28, a large part of the bulk material is separated from water and impurities. Another part of the screened material is deposited on conveyor belt 29 at a location 31. L-shaped bricks 33 serve to delimit and prevent impurities from getting under the machine.
- the separated water with proportions of impurities is passed in an intermediate container, not shown.
- the bulk material with the residues of impurities falls into an upstream classifier placed under the centrifuge 28
- the Aufströmklassierer 30 separates by its principle of operation, the bulk of suspended matter.
- the suspended matter is thereby rinsed out by water and also passed into the intermediate container.
- the thus cleaned bulk material is rinsed out of the Aufströmklassierer 30 and placed on a trained as Schwingentskysserer dehydrating agent 32.
- the Schwingentskysserer 32 the bulk material is withdrawn more water. Subsequently, the clean bulk material is transported via the conveyor belt 34 and accumulated at a location 36 for further use.
- FIG. 2 compared to FIG. 1, the mixing device 18 is shown enlarged as a detailed drawing with the first high-pressure water generator 20.
- Mixing device 18 has in this embodiment, a cuboid frame 38, in which on the upper side designed as a funnel 40 supply is provided.
- the mixture of soiled bulk material with the support grains is ground by the water jet of the high-pressure water generator 20.
- the mixture is thus dissolved and falls onto the conveyor belt 22, which finally conveys the mixture to the vibrating screen 24.
- Below the conveyor belt 22 is a collecting container 42.
- the collecting container 42 traps material and water, which does not reach the conveyor belt 22.
- the Aufströmklassierer 30 is seen as an enlarged detail view.
- the contaminated bulk material is introduced in those Aufströmklassierer 30, which is also located in a cuboid frame 44.
- 46 denotes the edge and 48 denotes the interior of the inflow classifier 30.
- Water gets in from below Interior 48 of Aufströmklassierers 30 has flowed, so that the lighter compared to the bulk of dirt particles flow upward and are flushed away with the water over the upper edge 46.
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
- Optical Fibers, Optical Fiber Cores, And Optical Fiber Bundles (AREA)
- Filters For Electric Vacuum Cleaners (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL09768492T PL2334437T3 (pl) | 2008-10-17 | 2009-10-02 | Urządzenie do oczyszczania materiału sypkiego |
DE112009003239T DE112009003239A5 (de) | 2008-10-17 | 2009-10-02 | Schüttgutreinigungsanlage |
ES09768492.2T ES2539659T3 (es) | 2008-10-17 | 2009-10-02 | Instalación de purificación de producto a granel |
EP09768492.2A EP2334437B1 (de) | 2008-10-17 | 2009-10-02 | Schüttgutreinigungsanlage |
HRP20150651TT HRP20150651T1 (hr) | 2008-10-17 | 2015-06-16 | Sustav za äśišä†enje rasutih proizvoda |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE202008013646.6 | 2008-10-17 | ||
DE202008013646U DE202008013646U1 (de) | 2008-10-17 | 2008-10-17 | Sandreinigungsanlage |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2010043221A1 true WO2010043221A1 (de) | 2010-04-22 |
Family
ID=40299449
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/DE2009/075056 WO2010043221A1 (de) | 2008-10-17 | 2009-10-02 | Schüttgutreinigungsanlage |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP2334437B1 (de) |
DE (2) | DE202008013646U1 (de) |
ES (1) | ES2539659T3 (de) |
HR (1) | HRP20150651T1 (de) |
PL (1) | PL2334437T3 (de) |
PT (1) | PT2334437E (de) |
WO (1) | WO2010043221A1 (de) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012025071A1 (de) * | 2010-08-27 | 2012-03-01 | Ferdinand Doppstadt | Schüttgutreinigungsanlage |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4140845A1 (de) | 1990-12-11 | 1992-06-17 | Kloeckner Oecotec | Verfahren und vorrichtung zum entfernen von verunreinigungen aus kontaminierten boeden |
DE4034227C2 (de) | 1990-10-27 | 1993-03-18 | Heiner Dipl.-Ing. 4030 Ratingen De Kreyenberg | |
EP0613722A1 (de) | 1993-03-05 | 1994-09-07 | ROMPF KLÄRWERKEINRICHTUNGEN GmbH & Co. | Verfahren und Vorrichtung zur Trennung von Wasser und Feststoffen, insbesondere zur Gewinnung von wiederverwendbarem Sand |
DE19621892A1 (de) | 1996-05-31 | 1997-12-04 | Ulrich Dipl Ing Franze | Verfahren und Vorrichtung zur In-Situ-Reinigung von Spiel- und Strandsanden |
DE19810866A1 (de) | 1998-03-13 | 1999-09-16 | Kupczik Kornelius | Anlage zur Aufbereitung eines Feinststoffgemisches |
DE19907513C1 (de) | 1999-02-22 | 2000-08-10 | Akw Apparate Verfahren | Verfahren zur Reinigung verunreinigter körniger Stoffe durch Attrition |
DE29824791U1 (de) | 1998-09-25 | 2002-10-10 | STRATE Technologie für Abwasser GmbH, 31157 Sarstedt | Sandwäsche |
US20040082828A1 (en) | 2002-05-27 | 2004-04-29 | Mario Bergeron | Method of decontaminating soil |
-
2008
- 2008-10-17 DE DE202008013646U patent/DE202008013646U1/de not_active Expired - Lifetime
-
2009
- 2009-10-02 PT PT97684922T patent/PT2334437E/pt unknown
- 2009-10-02 PL PL09768492T patent/PL2334437T3/pl unknown
- 2009-10-02 WO PCT/DE2009/075056 patent/WO2010043221A1/de active Application Filing
- 2009-10-02 ES ES09768492.2T patent/ES2539659T3/es active Active
- 2009-10-02 DE DE112009003239T patent/DE112009003239A5/de not_active Withdrawn
- 2009-10-02 EP EP09768492.2A patent/EP2334437B1/de not_active Not-in-force
-
2015
- 2015-06-16 HR HRP20150651TT patent/HRP20150651T1/hr unknown
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4034227C2 (de) | 1990-10-27 | 1993-03-18 | Heiner Dipl.-Ing. 4030 Ratingen De Kreyenberg | |
DE4140845A1 (de) | 1990-12-11 | 1992-06-17 | Kloeckner Oecotec | Verfahren und vorrichtung zum entfernen von verunreinigungen aus kontaminierten boeden |
EP0613722A1 (de) | 1993-03-05 | 1994-09-07 | ROMPF KLÄRWERKEINRICHTUNGEN GmbH & Co. | Verfahren und Vorrichtung zur Trennung von Wasser und Feststoffen, insbesondere zur Gewinnung von wiederverwendbarem Sand |
DE19621892A1 (de) | 1996-05-31 | 1997-12-04 | Ulrich Dipl Ing Franze | Verfahren und Vorrichtung zur In-Situ-Reinigung von Spiel- und Strandsanden |
DE19810866A1 (de) | 1998-03-13 | 1999-09-16 | Kupczik Kornelius | Anlage zur Aufbereitung eines Feinststoffgemisches |
DE29824791U1 (de) | 1998-09-25 | 2002-10-10 | STRATE Technologie für Abwasser GmbH, 31157 Sarstedt | Sandwäsche |
DE19907513C1 (de) | 1999-02-22 | 2000-08-10 | Akw Apparate Verfahren | Verfahren zur Reinigung verunreinigter körniger Stoffe durch Attrition |
US20040082828A1 (en) | 2002-05-27 | 2004-04-29 | Mario Bergeron | Method of decontaminating soil |
Non-Patent Citations (1)
Title |
---|
DETZNER D ET AL: "METHA - ERSTE GROSSANLAGE ZUR AUFBEREITUNG VON HAFENSEDIMENTEN", AUFBEREITUNGS TECHNIK, VERLAG FUER AUFBEREITUNG, WIESBADEN, DE, vol. 34, no. 5, 1 May 1993 (1993-05-01), pages 235 - 242, XP000351982, ISSN: 0004-783X * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012025071A1 (de) * | 2010-08-27 | 2012-03-01 | Ferdinand Doppstadt | Schüttgutreinigungsanlage |
RU2571112C2 (ru) * | 2010-08-27 | 2015-12-20 | Доппштадт, Фердинанд | Мобильная установка для очистки сыпучего материала |
Also Published As
Publication number | Publication date |
---|---|
DE202008013646U1 (de) | 2009-01-29 |
DE112009003239A5 (de) | 2012-07-05 |
HRP20150651T1 (hr) | 2015-07-31 |
EP2334437A1 (de) | 2011-06-22 |
PL2334437T3 (pl) | 2015-08-31 |
EP2334437B1 (de) | 2015-03-18 |
PT2334437E (pt) | 2015-07-20 |
ES2539659T3 (es) | 2015-07-02 |
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