EP0795359A2 - Séparateur pneumatique - Google Patents
Séparateur pneumatique Download PDFInfo
- Publication number
- EP0795359A2 EP0795359A2 EP97890007A EP97890007A EP0795359A2 EP 0795359 A2 EP0795359 A2 EP 0795359A2 EP 97890007 A EP97890007 A EP 97890007A EP 97890007 A EP97890007 A EP 97890007A EP 0795359 A2 EP0795359 A2 EP 0795359A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- air
- sifter
- classifier
- angle
- opening
- 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
- 229920002522 Wood fibre Polymers 0.000 claims abstract description 5
- 239000012535 impurity Substances 0.000 claims abstract description 3
- 239000000463 material Substances 0.000 claims description 49
- 239000000835 fiber Substances 0.000 claims description 14
- 238000009826 distribution Methods 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 238000000926 separation method Methods 0.000 claims description 6
- 239000002657 fibrous material Substances 0.000 claims description 5
- 238000007599 discharging Methods 0.000 claims description 4
- 239000002025 wood fiber Substances 0.000 claims description 4
- 230000001174 ascending effect Effects 0.000 claims description 2
- 239000002245 particle Substances 0.000 abstract description 6
- 239000002184 metal Substances 0.000 abstract description 2
- 229910052751 metal Inorganic materials 0.000 abstract description 2
- 230000000630 rising effect Effects 0.000 abstract description 2
- 150000002739 metals Chemical class 0.000 abstract 1
- 230000000007 visual effect Effects 0.000 description 4
- 238000010276 construction Methods 0.000 description 2
- 238000003892 spreading Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000035508 accumulation Effects 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 238000004026 adhesive bonding Methods 0.000 description 1
- 239000011093 chipboard Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000011094 fiberboard Substances 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
- B27N—MANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
- B27N1/00—Pretreatment of moulding material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
- B07B11/04—Control arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
- B07B11/06—Feeding or discharging arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B4/00—Separating solids from solids by subjecting their mixture to gas currents
- B07B4/02—Separating solids from solids by subjecting their mixture to gas currents while the mixtures fall
Definitions
- the invention relates to a classifier for separating coarse material and impurities in fiber processing in the course of the production of wood fiber boards according to the preamble of patent claim 1.
- MDF boards medium-density wood fiber boards
- the shredded wood is wet glued, dried and then pressed into boards.
- a certain proportion of coarse material e.g. Hanks and lumps. caused by gluing or moisture, as well as contamination. such as. Metal or rubber particles.
- These coarse fibers or foreign bodies interfere with the pressing into sheets and influence the homogeneity of the material. It is the task of a classifier to separate them from the material flow and thus improve the quality of MDF boards.
- the sifters used in the manufacture of wood fiber boards are generally wind sifters, the material to be sifted being fed into an air stream from the side or from above. The fibers are caught by an upward air flow.
- Particles with a higher sink rate than the speed of the air flow fall down and are discharged via a lock. Particles with a lower sink rate leave the classifier, carried by the air flow. up. With some classifiers, the separation is supported by centrifugal forces. The air with the fibers is fed into a cyclone by a fan, the material is separated from the air flow and then compressed. With most classifiers, a large part of the air required for classifying is drawn in directly below the classifier. Sometimes the air is heated and humidified to raise the temperature of the glued fibers. The amount of energy required for this is not insignificant.
- the amount of exhaust air from the pneumatic conveying system of the classifier can be reduced to a minimum, as a result of which only a small volume of air has to be dedusted.
- the supply air required according to the amount of exhaust air is supplied outside the classifier and can theoretically be reduced to zero except for a slight leak in the system. The amount of energy required to heat the air can thus be significantly reduced. If necessary, the humidity of the air can be regulated with the amount of exhaust air.
- DE 41 12 556 C1 describes a system for spreading the spreading material in the course of the production of fiberboard, chipboard, gypsum board reinforced with chips and / or fibers.
- a device for windsifting the flow of grit is connected.
- the sifter contains a material feed opening, at least one opening for the sight wind, an opening for removing all the air and the sifted fiber material and a lock for discharging the coarse material, the air being returned to the sifter in a circuit via a cyclone.
- the inlet openings for the classifying air are connected to each other outside the classifying chamber by a classifying wind distribution chamber, which is why it is essentially an air supply line, the flow of which can be directed through various openings in the separating wall of the classifier.
- the object of the invention is the production of a classifier with energetically more favorable properties and improved visibility.
- the object of the invention is achieved by the features specified in the characterizing part of claim 1.
- the separation of the air flows is essential for the visual effect.
- the lower air flow serves to hold the material column in the classifier, while the upper air flow or the upper air flows essentially takes on the task of classifying, that is to say the separation of the fine fiber material from the coarse material.
- the volume fractions of the air streams are adjustable, optimal flow conditions can be achieved within the classifier, regardless of the pressure conditions in the system.
- the distribution of the air flows takes place with the help of regulators outside the classifier. Throttle installations in the classifier itself, which are annoying during the classifying, are not required.
- the recirculated sight air is separated into upper air and lower air, and flows into the classifier via two lines through two inflow openings.
- the volume fraction of the upper air is 35% to 65%, preferably 50% and that of the lower air correspondingly 65% to 35%, preferably 50% of the recirculated visual air.
- the material is fed into the classifier by dosing devices above the material feed opening.
- the cross section of the dosing elements is smaller than that of the material feed opening.
- this problem is avoided by an appropriate arrangement of the opening rollers directly in the feed channel.
- the opening rollers extend over the entire depth of the classifier, which is varied in accordance with the desired material throughput.
- the opening rollers are arranged in increasing order in the feed channel. By correspondingly rotating all opening rollers in the direction of the rising rollers, material is transported upwards and at the same time is distributed over the depth of the classifier. After passing through the spaces between the opening rollers, the fibers sink with an even distribution into the classifier.
- the circulating classifying air is separated into two air streams, which flow laterally into the classifier 1 via two lines, the upper air line 2 and the lower air line 3 through two stacked inlet openings.
- the total air, which contains the fiber material to be sifted, is discharged via a line 4 on the top of the sifter 1 next to the material feed opening 5.
- the classifying air is led via fans 6 to a cyclone 7 for the separation of the fiber material. If necessary, the recirculated visual air in a mixer 8 supply air is supplied via a supply air line 10.
- the amount of the supply air supplied in the direction of arrow 10a via the supply air line 10 corresponds to the set amount of the exhaust air discharged via the exhaust air line 9 in the direction of arrow 9a. Since the mixture with the recycled classifying air takes place outside the classifier 1, a homogeneous air condition can be ensured within the classifier 1. With the help of control flaps 11 in the upper air line 2 and the lower air line 3, the air quantity ratio between upper air and lower air can be adjusted.
- FIG. 2 shows a section through the classifier 1 according to the invention.
- the material is fed to the classifier 1 via the material feed opening 5 in the direction of arrow 5a, with more material being accumulated on one side due to the material task.
- the fibers are caught by the opening rollers 12 arranged in increasing sequence.
- the direction of rotation of all opening rollers 12 is the same and in the direction of the ascending rollers, in the present view correspondingly counterclockwise.
- material is transported upwards and into the depth of the sifter 1 and the material sinks evenly distributed into the sifter 1.
- the upper air reaches the sifter 1 via a line 2 in the direction of the arrow 2a Particles are caught by the air flow in the upper air and whirled upwards.
- the distribution pipes 14 in the mouth of the upper air line 2 in the classifier 1 form an angle ⁇ with the vertical, which is preferably 30 °.
- material accumulations occur on the wall opposite the inflow opening of the upper air, which are no longer carried by the air flow.
- tear-off edge 15 on the rear wall of the classifier 1
- the material slides away from the wall and a separation of the strands of material and thereby allows the light fibers to be transported upwards. There must be enough space below the tear-off edge 15 in order to decelerate the material falling down and to accelerate it up again.
- the angle ⁇ of the tear-off edge 15 can be changed to adapt to the material density and is in the range from 90 ° to 180 °, preferably between 120 ° and 130 °. In the case of very light fibers, in which the setting of the tear-off edge 15 is not necessary, the angle ⁇ is increased to 180 °. Due to the incoming air flowing in from the side, very irregular flow conditions occur due to the necessary 90 ° deflection. By using baffles 16, the flow is deflected evenly and with the adjustable baffles 17, the flow of the lower air is directed against the direction of material strands.
- an adjustment flap 18 is arranged in the center of the classifier 1 with an adjustable angle ⁇ , with which the geometry of the classifying space can be changed and the material fed in is separated from the classed material.
- the angle ⁇ of the adjusting flap 18 against the vertical is preferably in the range of ⁇ 20 °.
- the outlet cross section of the classifier 1 can be varied. This allows the flow conditions to be optimized depending on the material.
- the rear wall 19 forms an angle ⁇ with the vertical, which is preferably in the range between 0 ° and 20 °.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Wood Science & Technology (AREA)
- Forests & Forestry (AREA)
- Combined Means For Separation Of Solids (AREA)
- Preliminary Treatment Of Fibers (AREA)
- Cyclones (AREA)
- Lubricants (AREA)
- Medicines Containing Plant Substances (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Paper (AREA)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT486/96 | 1996-03-14 | ||
AT48696 | 1996-03-14 | ||
AT0048696A AT403133B (de) | 1996-03-14 | 1996-03-14 | Sichter |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0795359A2 true EP0795359A2 (fr) | 1997-09-17 |
EP0795359A3 EP0795359A3 (fr) | 1998-03-11 |
EP0795359B1 EP0795359B1 (fr) | 2001-07-18 |
Family
ID=3491881
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP97890007A Expired - Lifetime EP0795359B1 (fr) | 1996-03-14 | 1997-01-15 | Séparateur pneumatique |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP0795359B1 (fr) |
AT (2) | AT403133B (fr) |
DE (1) | DE59704052D1 (fr) |
ES (1) | ES2161434T3 (fr) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0982082A1 (fr) * | 1998-08-21 | 2000-03-01 | Beloit Technologies, Inc. | Procédé de séparation d' un mélange de particules |
DE10352119A1 (de) * | 2003-11-04 | 2005-06-09 | Focke & Co.(Gmbh & Co. Kg) | Verfahren und Einrichtung zum Sichten von Tabak |
EP1782893A3 (fr) * | 2005-11-02 | 2008-07-16 | Manfred Dr. Ottow | Triage de copeaux de bois |
WO2014037237A1 (fr) * | 2012-09-06 | 2014-03-13 | Thyssenkrupp Resource Technologies Gmbh | Dispositif et procédé de traitement de combustibles de substitution |
CN106892284A (zh) * | 2017-04-11 | 2017-06-27 | 苏州尚梵斯科技有限公司 | 粮食谷物筛分农机设备及其工作方法 |
CN107824450A (zh) * | 2016-09-15 | 2018-03-23 | 辛北尔康普机器及成套设备有限责任公司 | 筛分机 |
CN107824449A (zh) * | 2016-09-15 | 2018-03-23 | 辛北尔康普机械设备制造有限责任公司 | 筛分机 |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE202006014455U1 (de) | 2006-09-18 | 2006-11-16 | Lhs Clean Air Systems Gmbh | Vorrichtung zum Trennen von Grob- und Feinmaterial |
DE102017110600B4 (de) | 2017-05-16 | 2023-09-07 | Siempelkamp Maschinen- Und Anlagenbau Gmbh | Sichter |
CN115283254B (zh) * | 2022-07-29 | 2023-08-25 | 中触媒新材料股份有限公司 | 一种用于制氧吸附剂颗粒气流快速筛分活化系统及方法 |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0491278A2 (fr) | 1990-12-19 | 1992-06-24 | Holger Lübke | Procédé et dispositif pour le dépoussiérage et/ou le tri de matières granuleuses ou fibreuses dans un courant d'air |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE583680C (de) * | 1927-01-11 | 1933-09-07 | Rudolf Lessing | Verfahren und Vorrichtung zur Abtrennung der groeberen Bestandteile von den mittelfeinen und staubfoermigen Teilen aus Kohlen o. dgl. durch einen in einem Rohre aufsteigenden Gasstrom |
DE2313614C3 (de) * | 1973-03-19 | 1978-07-13 | Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler, 6000 Frankfurt | Vorrichtung zum Abtrennen von Grit aus einem feindisperse Feststoffe enthaltenden, zur pneumatischen Förderung dieser Stoffe dienenden Gasstrom |
US3883423A (en) * | 1973-08-01 | 1975-05-13 | Aerofall Mills Ltd | Vertical classifier |
IT1124576B (it) * | 1978-10-26 | 1986-05-07 | Hartmann Wibau Maschf | Disposizione e conformazione di un setaccio in un impianto in convogliamento ad aria di aspirazione funzionante sostanzalmente ad una pressione compresa fra 0,6 e 0,8 |
DE3131836C2 (de) * | 1981-08-12 | 1985-12-05 | Günter 4300 Essen Lübke | Vorrichtung zur Entstaubung und/oder Klassierung von Stoffen im Luftstrom |
DD203237A1 (de) * | 1982-02-08 | 1983-10-19 | Dietmar Kummer | Vorrichtung und verfahren zum entstauben von schuettguetern, insbesondere granulaten aus synthetischen hochpolymeren |
US4465194A (en) * | 1982-12-23 | 1984-08-14 | Universal Leaf Tobacco Co. | Threshed tobacco lead separator |
DE3409814A1 (de) * | 1984-03-16 | 1985-09-19 | Waeschle Maschinenfabrik Gmbh, 7980 Ravensburg | Gegenstromsichter |
DE3878072D1 (de) * | 1987-07-29 | 1993-03-18 | Bat Cigarettenfab Gmbh | Abscheider zur trennung von tabak-teilchen aus einem tabak/gas-gemisch. |
SE467044B (sv) * | 1990-09-28 | 1992-05-18 | Flaekt Ab | Saett och anordning foer avskiljning av tyngre partiklar fraan ett partikelformigt material |
DE4112556C1 (en) * | 1991-04-17 | 1992-06-17 | G. Siempelkamp Gmbh & Co, 4150 Krefeld, De | Spreading installation for chips, fibres etc. - has wind sifter for spreading flow coupled to spread material outlet shaft |
-
1996
- 1996-03-14 AT AT0048696A patent/AT403133B/de not_active IP Right Cessation
-
1997
- 1997-01-15 AT AT97890007T patent/ATE203191T1/de active
- 1997-01-15 DE DE59704052T patent/DE59704052D1/de not_active Expired - Lifetime
- 1997-01-15 ES ES97890007T patent/ES2161434T3/es not_active Expired - Lifetime
- 1997-01-15 EP EP97890007A patent/EP0795359B1/fr not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0491278A2 (fr) | 1990-12-19 | 1992-06-24 | Holger Lübke | Procédé et dispositif pour le dépoussiérage et/ou le tri de matières granuleuses ou fibreuses dans un courant d'air |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0982082A1 (fr) * | 1998-08-21 | 2000-03-01 | Beloit Technologies, Inc. | Procédé de séparation d' un mélange de particules |
DE10352119A1 (de) * | 2003-11-04 | 2005-06-09 | Focke & Co.(Gmbh & Co. Kg) | Verfahren und Einrichtung zum Sichten von Tabak |
EP1782893A3 (fr) * | 2005-11-02 | 2008-07-16 | Manfred Dr. Ottow | Triage de copeaux de bois |
WO2014037237A1 (fr) * | 2012-09-06 | 2014-03-13 | Thyssenkrupp Resource Technologies Gmbh | Dispositif et procédé de traitement de combustibles de substitution |
CN107824450A (zh) * | 2016-09-15 | 2018-03-23 | 辛北尔康普机器及成套设备有限责任公司 | 筛分机 |
CN107824449A (zh) * | 2016-09-15 | 2018-03-23 | 辛北尔康普机械设备制造有限责任公司 | 筛分机 |
US10195646B2 (en) | 2016-09-15 | 2019-02-05 | Siempelkamp Masclinen-Und Anlagenbau Gmbh | Sifter |
CN106892284A (zh) * | 2017-04-11 | 2017-06-27 | 苏州尚梵斯科技有限公司 | 粮食谷物筛分农机设备及其工作方法 |
CN106892284B (zh) * | 2017-04-11 | 2023-06-09 | 沅陵县辰州荞韵食品有限公司 | 粮食谷物筛分农机设备及其工作方法 |
Also Published As
Publication number | Publication date |
---|---|
EP0795359A3 (fr) | 1998-03-11 |
EP0795359B1 (fr) | 2001-07-18 |
ATA48696A (de) | 1997-04-15 |
ATE203191T1 (de) | 2001-08-15 |
DE59704052D1 (de) | 2001-08-23 |
ES2161434T3 (es) | 2001-12-01 |
AT403133B (de) | 1997-11-25 |
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