EP0512236A1 - Procédé de récupération mécanique de sable de fonderie décoché - Google Patents
Procédé de récupération mécanique de sable de fonderie décochéInfo
- Publication number
- EP0512236A1 EP0512236A1 EP92105216A EP92105216A EP0512236A1 EP 0512236 A1 EP0512236 A1 EP 0512236A1 EP 92105216 A EP92105216 A EP 92105216A EP 92105216 A EP92105216 A EP 92105216A EP 0512236 A1 EP0512236 A1 EP 0512236A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- cleaning
- foundry sand
- sand
- mechanical
- container
- 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
- 239000004576 sand Substances 0.000 title claims abstract description 90
- 238000000034 method Methods 0.000 title claims abstract description 31
- 238000004140 cleaning Methods 0.000 claims abstract description 70
- 230000008929 regeneration Effects 0.000 claims abstract description 27
- 238000011069 regeneration method Methods 0.000 claims abstract description 27
- 239000010453 quartz Substances 0.000 claims abstract description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 8
- 238000001816 cooling Methods 0.000 claims abstract description 6
- 230000000930 thermomechanical effect Effects 0.000 claims abstract description 4
- 229910000278 bentonite Inorganic materials 0.000 claims description 10
- 239000000440 bentonite Substances 0.000 claims description 10
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 claims description 10
- 239000000428 dust Substances 0.000 claims description 7
- 230000001105 regulatory effect Effects 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 238000002485 combustion reaction Methods 0.000 claims description 2
- 239000000470 constituent Substances 0.000 claims description 2
- 238000012545 processing Methods 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- 238000011109 contamination Methods 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 238000001035 drying Methods 0.000 abstract description 4
- 230000006378 damage Effects 0.000 abstract description 3
- 239000002245 particle Substances 0.000 abstract 1
- 235000012216 bentonite Nutrition 0.000 description 12
- 230000000694 effects Effects 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000011230 binding agent Substances 0.000 description 4
- 239000000356 contaminant Substances 0.000 description 4
- 239000012530 fluid Substances 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000012216 screening Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 241000538562 Banjos Species 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
- 238000007669 thermal treatment Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22C—FOUNDRY MOULDING
- B22C5/00—Machines or devices specially designed for dressing or handling the mould material so far as specially adapted for that purpose
- B22C5/18—Plants for preparing mould materials
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S241/00—Solid material comminution or disintegration
- Y10S241/10—Foundry sand treatment
Definitions
- the invention relates to a method for the mechanical cleaning of foundry sand by means of thermo-mechanical regeneration, the foundry sand being blown pneumatically against a deflection hood.
- a process for the regeneration of foundry rubble sands, the old sand mixtures with organic and inorganic binders, the active and still burned bentonite and synthetic resins, optionally containing further sludge materials is known.
- This process involves dry pre-regeneration, subsequent thermal regeneration and post-cleaning. With dry pre-regeneration the grains of the foundry sand are preferably accelerated horizontally, radially and hurled against stationary baffle plates.
- the foundry sand is dried and preheated during the pre-regeneration by hot exhaust gas from the thermal regeneration flowing over it in countercurrent (EP 0 149 595).
- the object of the invention is to clean foundry sand thermally and mechanically so that it has a constant quality that comes close to that of new sand.
- this object is achieved in that the foundry sand is subjected to mechanical-pneumatic cleaning in batches in a separate apparatus before and / or after thermal regeneration.
- the foundry sand is sucked into the blower tube above a sheet with openings (preferably nozzle screws) at a distance from its bottom, with an air stream emerging from a blower nozzle at a distance from a vertical blower tube.
- the old sand accelerated by the air flow passes through the blow pipe to a deflection hood attached above the blow pipe and is flung against its inner surface.
- contaminants adhering to the foundry sand burst off and can form as dust by means of the air flow in the container through an opening located at the top thereof.
- the relatively heavy foundry sand falls again on the sheet metal of the container provided with openings and reaches the deflection hood again with the aid of the air flow through the blow pipe, so that the cleaning process can be repeated until the desired cleaning effect is achieved.
- a valve located on the container can be opened and the now cleaned foundry sand can either be fed to a subsequent thermal regeneration or the mold or core production, depending on whether the mechanical-pneumatic cleaning is intended as a pre-cleaning or post-cleaning stage. This procedure ensures that the foundry sand leaving the container has a constant quality, that all the grains of the foundry sand have been subjected to an almost equal number of cleaning cycles in the container.
- the parallel connection of at least two such cleaning containers ensures quasi-continuous operation of a foundry sand cleaning system.
- Pneumatic-mechanical cleaning means that there is almost no mechanical wear if the nozzle, blowpipe and deflection hood are appropriately selected. Furthermore, the cleaning effect of the foundry sand can be easily regulated by varying the air delivery pressure, changing the distance at the end of the blowpipe and on the deflection hood, as well as adjusting the angle of impact of the foundry sand on the deflection hood and the duration of the cleaning process.
- the deflection hood attached to the upper part of the container can be fixed by simple mechanical means at different distances from the end of the blowpipe and possibly be pivoted through certain angles. This makes it possible to achieve greater cleaning effects at the beginning of the cleaning process and to achieve a gentler treatment of the grains towards the end of the cycle.
- hot air can advantageously be used to convey and fluidize the old sand.
- the air is advantageously heated using the waste heat from the thermal regeneration. At temperatures of the hot air above 350 ° C, it is possible to dry the inorganic contaminants quickly and safely.
- the mechanical pre-cleaning of bentonite-bound used sand is made more difficult by the residual moisture that is necessarily present.
- the still active bentonite absorbs a lot of water and acts like a "lubricant". This reduces the cleaning effect caused by Kornan-Korn friction.
- the hot conveying and fluidizing air flowing around the old sand on all sides dries and embrittles the bentonite layer adhering to it very quickly, so that it can be removed more easily mechanically.
- the valve on the container is opened and the now preheated and pre-cleaned old sand is fed to a thermal regeneration stage, such as a fluidized bed oven.
- the old sand is then cleaned from the organic binders adhering to it and the "dead burning" of the bentonites, which are also still adhering.
- a similar pneumatic-mechanical cleaning can follow the thermal regeneration stage. It proves to be advantageous to provide a heat exchanger in the interior of the container above the plate provided with holes, which cools the old sand falling down from the deflection hood.
- the thermally regenerated old sand reaches the container at a temperature of approx. 650 ° C.
- the fireclay shells of the quartz grains are softer in this state than after cooling to approx. 50 ° C. This results in a gentler cleaning of the fireclay casings than at comparatively low temperatures, so that less grain destruction can be expected. Due to the cooling to be carried out in the container, the bentonites become brittle and thermal stresses arise, which enables easier separation.
- the invention is to be explained below using two exemplary embodiments.
- the foundry sand arrives in a cleaning container 2 from a preliminary container 1.
- An air flow is generated by a fan 6, which flows through the heat exchanger 7 and is heated therein by the heat of the fluidized bed furnace 10.
- the air heats up in the heat exchanger 7 to values of 400-500 ° C (at least 350 ° C).
- the now hot air passes through the air duct 3 into the cleaning container 2 and conveys the old sand through the blow pipe 4.
- the old sand accelerated with the air flow impinges against the deflection hood 5 and contaminants adhering to it, particularly inorganic binders, burst off in the process. Due to the very hot medium air, which flows around the old sand on all sides, the bentonite dries very quickly. This embrittles and is therefore easier to remove from the old sand.
- the old sand falls onto a perforated plate 19 which is attached above the floor of the cleaning container.
- nozzle screws preferably cross-drilled hollow screws, through which the air flows into the cleaning container 2 and fluidizes the foundry sand.
- the foundry sand located on the bottom plate 19 of the cleaning container in turn reaches the blowpipe 4 and is sucked into it by means of the air flow.
- the used sand runs through this cycle until a certain drying and cleaning effect or a certain preheating temperature is reached, in order then to be removed from the cleaning container 2 via the line 17.
- a shut-off device not shown, which opens or closes the line 17. From the line 17, the pre-cleaned old sand reaches an intermediate container 8 and is fed via a vibration conveyor 9 to a fluidized bed furnace 10, in which the old sand is subjected to thermal regeneration.
- the residues and valuable materials removed in a cyclone have a high concentration of bentonite and whole carbon, which are immediately returned to the green sand processing.
- the proportion of undersize quartz in the dust increases, the dust separated in the cyclone is fed to the fluidized bed furnace 10 for combustion of the organic constituents and inerting of the residues.
- FIG. 2 shows the cleaning container 2, which is constructed in principle in the same way, following a thermal regeneration stage, in the form of a fluidized bed furnace 10.
- the hot used sand passes through an intermediate container 11 into the cleaning container 2, in which there is a heat exchanger 12 for cooling the hot used sand above the plate 19 provided with holes.
- the pneumatic-mechanical post-cleaning works like the corresponding pre-cleaning.
- cold air is conveyed into the cleaning container 2 by a fan 14 through the air duct 3. This, in cooperation with the heat exchanger 12, ensures rapid cooling of the old sand, which was hot up to that point.
- the favorable control options and the possibility of predetermining the cleaning time ensure that a lower proportion of grain destruction occurs.
- the foundry sand that has been cleaned in this way can at most be returned to the mold or core production, such as new sand.
- the combination of several operations in one part of the plant ensures economic operation of a foundry sand cleaning plant.
- the foundry sand can be dried, preheated, pre-cleaned at the same time in a pre-cleaning stage and cooled, post-cleaned and sifted at the same time in the pneumatic-mechanical post-cleaning. This eliminates the need for additional facilities such as Intermediate conveyor systems that are required for other types of systems.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Molds, Cores, And Manufacturing Methods Thereof (AREA)
- Mold Materials And Core Materials (AREA)
- Casting Devices For Molds (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE4111726 | 1991-04-10 | ||
| DE4111726A DE4111726C2 (de) | 1991-04-10 | 1991-04-10 | Verfahren zur mechanischen Reinigung von Gießereialtsand |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0512236A1 true EP0512236A1 (fr) | 1992-11-11 |
| EP0512236B1 EP0512236B1 (fr) | 1995-12-06 |
Family
ID=6429302
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP92105216A Expired - Lifetime EP0512236B1 (fr) | 1991-04-10 | 1992-03-26 | Procédé de récupération mécanique de sable de fonderie décoché |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US5291935A (fr) |
| EP (1) | EP0512236B1 (fr) |
| AT (1) | ATE131091T1 (fr) |
| DE (2) | DE4111726C2 (fr) |
| DK (1) | DK0512236T3 (fr) |
| ZA (1) | ZA922356B (fr) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2696367A1 (fr) * | 1992-10-07 | 1994-04-08 | Fm Ind | Procédé et installation de régénération de sables de fonderies hétérogènes. |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4237838A1 (de) * | 1992-11-10 | 1994-05-11 | Badische Maschf Gmbh | Verfahren und Vorrichtung zum Regenerieren von Gießereialtsand |
| DE4322947B4 (de) * | 1992-11-27 | 2006-02-02 | Förder- und Anlagentechnik GmbH | Anordnung zur Verbesserung der Verarbeitungsgeigenschaften von Sanden |
| DE4316610A1 (de) * | 1993-05-18 | 1994-11-24 | Gut Gieserei Umwelt Technik Gm | Öko-Sandregenerierung mech./pneum. im Chargenbetrieb |
| DE4434115C1 (de) * | 1994-09-23 | 1995-11-23 | Kgt Giessereitechnik Gmbh | Verfahren zur pneumatisch-mechanischen Reinigung von in Gießereien anfallenden Altsanden |
| JP3355325B2 (ja) * | 2000-05-18 | 2002-12-09 | 旭有機材工業株式会社 | 原料鋳物砂又はシェルモールド用レジンコーテッドサンドの温度調節ユニット及びこれを用いた温度調節装置 |
| DE10346062B4 (de) * | 2003-10-04 | 2006-03-23 | Daimlerchrysler Ag | Verfahren zur Herstellung eines Gussteils |
| CA2916810A1 (fr) * | 2015-01-12 | 2016-07-12 | Russell Wynn Driver | Raffinage de sable en vue de retirer les impuretes |
| JP6687400B2 (ja) * | 2016-01-26 | 2020-04-22 | リグナイト株式会社 | 鋳型製造装置 |
| JP6687399B2 (ja) * | 2016-01-26 | 2020-04-22 | 株式会社大阪シェル | 鋳物砂の加熱装置 |
| IT201800004618A1 (it) * | 2018-04-17 | 2019-10-17 | Procedimento per la rigenerazione di sabbie di fonderia. | |
| CN108705030B (zh) * | 2018-07-04 | 2024-03-29 | 柳晶(溧阳)环保科技有限公司 | 一种铸造废砂处理设备 |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1806842A1 (de) * | 1968-11-04 | 1970-05-27 | Wilhelm Schwiese | Verfahren und Vorrichtung,um Giesserei-Altsande zu regenerieren |
| US4144088A (en) * | 1977-01-19 | 1979-03-13 | Kenzler Engineering Company, Inc. | Process of reclaiming used foundry sand |
| EP0343272A1 (fr) * | 1988-05-26 | 1989-11-29 | Pohl Giessereitechnik | Procédé et dispositif pour la régénération de sable décoché de fonderie |
| EP0416238A1 (fr) * | 1989-09-02 | 1991-03-13 | Balcke-Dürr AG | Réacteur à lit fluidisé et son procédé de fonctionnement |
| EP0265707B1 (fr) * | 1986-10-27 | 1992-06-03 | Förder- und Anlagentechnik GmbH | Procédé et installation pour la régénération thermo-mécanique de matières en vrac notamment de sable décoché de fonderie |
Family Cites Families (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2478461A (en) * | 1946-03-16 | 1949-08-09 | Nichols Eng & Res Corp | Apparatus and method for treating foundry sand |
| US3230635A (en) * | 1962-07-09 | 1966-01-25 | Dietert Co Harry W | Dryer and heater for granular material |
| US3825190A (en) * | 1973-02-14 | 1974-07-23 | Nat Eng Co | Apparatus for treating granular material |
| SE7505070L (sv) * | 1974-05-02 | 1975-11-03 | Simpson Ag Maschinen | Reningsanleggning. |
| FR2278424A1 (fr) * | 1974-06-10 | 1976-02-13 | Sapic | Procede et appareil pour le nettoyage mecanique et pneumatique et le depoussierage d'une substance granuleuse et/ou pulverulente |
| CH631643A5 (de) * | 1978-04-14 | 1982-08-31 | Fischer Ag Georg | Verfahren zur regenerierung von giesserei-altsand sowie einrichtung zur durchfuehrung des verfahrens und erzeugnis des verfahrens. |
| DE3110578A1 (de) * | 1981-03-18 | 1982-09-30 | Hermann 2105 Seevetal Jacob | Vorrichtung zur reinigung von giessereialtsand |
| DE3561928D1 (en) * | 1984-01-11 | 1988-04-28 | Gsr Sandregenerierungsgesellsc | Process and machine for regenerating used foundry sand |
| DE3400648A1 (de) * | 1984-01-11 | 1985-07-18 | Delta Engineering Beratung und Vermittlung Gesellschaft mbH, Irdning | Vorrichtung und verfahren zur regeneration von giesserei-schuttsand |
| EP0149876A1 (fr) * | 1984-01-20 | 1985-07-31 | Wheelabrator-Frye Inc. | Procédé et appareil pour la récupération de sable de fonderie |
| US4636168A (en) * | 1984-08-10 | 1987-01-13 | Institute Of Gas Technology | Apparatus for thermal and pneumatic treatment of granular solids |
| DE3825361A1 (de) * | 1988-07-26 | 1990-02-08 | Hermann Jacob | Verfahren und anlage zur regenerierung von giessereialtsandgemischen |
| CH680498A5 (fr) * | 1989-11-28 | 1992-09-15 | Fischer Ag Georg | |
| CH682641A5 (de) * | 1990-11-23 | 1993-10-29 | Fischer Ag Georg | Verfahren zum Trennen der Bentonit- und Kohlenstoffträgerpartikel von dem bei der Altsandregenerierung auf mechanischem Wege gewonnenen Staub. |
-
1991
- 1991-04-10 DE DE4111726A patent/DE4111726C2/de not_active Expired - Fee Related
-
1992
- 1992-03-26 DE DE59204541T patent/DE59204541D1/de not_active Expired - Fee Related
- 1992-03-26 DK DK92105216.3T patent/DK0512236T3/da active
- 1992-03-26 EP EP92105216A patent/EP0512236B1/fr not_active Expired - Lifetime
- 1992-03-26 AT AT92105216T patent/ATE131091T1/de active
- 1992-03-31 ZA ZA922356A patent/ZA922356B/xx unknown
- 1992-04-10 US US07/866,558 patent/US5291935A/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1806842A1 (de) * | 1968-11-04 | 1970-05-27 | Wilhelm Schwiese | Verfahren und Vorrichtung,um Giesserei-Altsande zu regenerieren |
| US4144088A (en) * | 1977-01-19 | 1979-03-13 | Kenzler Engineering Company, Inc. | Process of reclaiming used foundry sand |
| EP0265707B1 (fr) * | 1986-10-27 | 1992-06-03 | Förder- und Anlagentechnik GmbH | Procédé et installation pour la régénération thermo-mécanique de matières en vrac notamment de sable décoché de fonderie |
| EP0343272A1 (fr) * | 1988-05-26 | 1989-11-29 | Pohl Giessereitechnik | Procédé et dispositif pour la régénération de sable décoché de fonderie |
| EP0416238A1 (fr) * | 1989-09-02 | 1991-03-13 | Balcke-Dürr AG | Réacteur à lit fluidisé et son procédé de fonctionnement |
Non-Patent Citations (2)
| Title |
|---|
| GIESSEREI Bd. 59, Nr. 20, 5. Oktober 1972, DÜSSELDORF, DE Seiten 599 - 607; JANSEN: 'Die Regenerierung von Formstoffen, besonders von kunstharzgebundenen Altsanden' * |
| GIESSEREI Bd. 76, Nr. 10, 15. Mai 1989, DÜSSELDORF, DE Seiten 350 - 358; WELLER: 'Möglichkeiten und Grenzen bei der Regenierung von Giessereialtsanden' * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2696367A1 (fr) * | 1992-10-07 | 1994-04-08 | Fm Ind | Procédé et installation de régénération de sables de fonderies hétérogènes. |
Also Published As
| Publication number | Publication date |
|---|---|
| DE4111726A1 (de) | 1992-10-15 |
| ATE131091T1 (de) | 1995-12-15 |
| EP0512236B1 (fr) | 1995-12-06 |
| DE4111726C2 (de) | 1994-02-24 |
| DK0512236T3 (da) | 1996-01-22 |
| ZA922356B (en) | 1992-11-25 |
| DE59204541D1 (de) | 1996-01-18 |
| US5291935A (en) | 1994-03-08 |
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