EP1100605A1 - Eindicker - Google Patents
EindickerInfo
- Publication number
- EP1100605A1 EP1100605A1 EP99914409A EP99914409A EP1100605A1 EP 1100605 A1 EP1100605 A1 EP 1100605A1 EP 99914409 A EP99914409 A EP 99914409A EP 99914409 A EP99914409 A EP 99914409A EP 1100605 A1 EP1100605 A1 EP 1100605A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- water
- belt
- pressure
- pressing
- cake
- 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
- 239000002562 thickening agent Substances 0.000 title description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 73
- 239000000725 suspension Substances 0.000 claims abstract description 54
- 238000000034 method Methods 0.000 claims abstract description 39
- 239000007787 solid Substances 0.000 claims abstract description 5
- 238000003825 pressing Methods 0.000 claims description 64
- 239000004744 fabric Substances 0.000 claims description 63
- 230000008719 thickening Effects 0.000 claims description 10
- 230000009747 swallowing Effects 0.000 claims description 7
- 239000010802 sludge Substances 0.000 claims description 6
- 238000010276 construction Methods 0.000 claims description 2
- 239000010801 sewage sludge Substances 0.000 claims 2
- 238000005452 bending Methods 0.000 claims 1
- 238000006073 displacement reaction Methods 0.000 claims 1
- 239000006194 liquid suspension Substances 0.000 claims 1
- 239000002184 metal Substances 0.000 claims 1
- 239000002994 raw material Substances 0.000 claims 1
- 230000000284 resting effect Effects 0.000 claims 1
- 238000007789 sealing Methods 0.000 claims 1
- 125000006850 spacer group Chemical group 0.000 claims 1
- 230000003068 static effect Effects 0.000 claims 1
- 239000003351 stiffener Substances 0.000 claims 1
- 239000010893 paper waste Substances 0.000 abstract description 3
- 230000010354 integration Effects 0.000 abstract description 2
- 230000006835 compression Effects 0.000 abstract 4
- 238000007906 compression Methods 0.000 abstract 4
- 239000007900 aqueous suspension Substances 0.000 abstract 1
- 239000002002 slurry Substances 0.000 abstract 1
- 239000000123 paper Substances 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 239000011111 cardboard Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011087 paperboard Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/18—De-watering; Elimination of cooking or pulp-treating liquors from the pulp
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/24—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using an endless pressing band
- B30B9/241—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using an endless pressing band co-operating with a drum or roller
Definitions
- the invention relates to methods and corresponding devices for the continuous mechanical dewatering of water-containing suspensions or sludges, in particular of waste paper suspensions or sewage sludges, between an endless screen belt and a closed, smooth surface which has an endless pressing surface which moves in the running direction.
- the suspension cake to be dewatered is pressed between the sieve belt and the pressing surface.
- the required pressing pressure arises from the fact that the sieve fabric belt wraps around the cylindrical pressing surface under longitudinal tension during the dewatering process, the squeezed water being removed from the suspension cake with the aid of the sieve fabric.
- This thickener is also used for integration into existing drainage processes in order to increase the consistency of solids, without significantly increasing the installation space or operating effort.
- the screen tensions are in the order of 10 N / mm, rarely up to 30 N / mm, which with a small roller diameter of e.g. B. 200 mm gives a pressure of about 1 bar, rarely 2 bar.
- CH 644414 "Variosplit”
- the advantage lies in the one-sided rewetting of the cake and the simpler design with only one belt.
- the disadvantage is that the cake only on this one roller, ie only once can be dewatered on one side, so that the final dry content is not optimal.
- the cake thickness to be dewatered is limited because the water on the roller side must also travel through the entire cake thickness to the sieve fabric This can be compensated for somewhat by slower press operation.
- the third method is the chamber filter press, which is not a continuous, but a batch operation; the cumbersome filling and emptying process stands in the way of the long exposure time and the high baling pressure. Centrifuges (decanters) are also used to separate water. However, these two processes have nothing to do with the patent idea.
- the uniform marking-free pressing is not necessary at all in the present invention; on the contrary, a marking, i.e. H. non-uniform pressing is desirable because it will have a certain kneading effect, which helps the water to flow out of the cake better.
- a marking i.e. H. non-uniform pressing
- the cake forms a stable web after thickening.
- the intended difference in speed between the screen fabric and the pressing surface on both sides of the cake and / or the coarser structure of the additional water-permeable belts intended to destroy the web structure in order to clear the water during the squeezing process for easier drainage and to achieve crumbling after thickening.
- the suspension is not brought on the same screen belt from a liquid phase to a consistency of about 25%, which is achieved with the invention.
- the aim of the invention is to avoid the disadvantages of the techniques used to date or to combine the advantages of the known devices, ie to increase the pressing pressures acting on the suspension cake significantly and long enough with minimal rewetting, in continuous operation.
- the object is achieved according to the invention in that devices are provided which both increase the exposure time of the pressing pressure (dewatering pressure) of the existing sieve fabric belt to the suspension cake and at the same time increase the pressing pressure significantly without blocking the water which is squeezed out.
- the method according to the invention increases the pressure from previously about 1 bar to pressures of z. B. up to 100 bar.
- the invention can the washing process,.
- H Separation of fine materials from the recyclable fiber material by means of dewatering a thin-layer, low-consistency suspension ( ⁇ 2%) at a higher working speed (> 200 m / min.), Using the screen mesh belt with the appropriate belt guide rollers for both steps. There is also no need to transport the partially dewatered suspension from the scrubber to the thickener.
- Claims 2 and 8 state that the pressing pressure is increased in that several endless belts run on one another. The pressure is increased accordingly, but the belt tension remains within the usual range.
- Claims 3 - 7 deal with different band constructions which allow the water to pass through.
- a belt is claimed in claim 7, which does not hold any water in its cavities and consequently cannot rewet this water either.
- the claims 5 and 9 deal with the high rigidity of the tape to bridge unevenness in the cake or leveling by pressing, which at the same time rolls the cake and thus promotes the outflow of squeezed water.
- the claims 15-17 show alternatives to where the squeezed water can flow or how it is transported out of the press zone so that the squeezing process is not hindered by a lack of swallowing volume.
- Claim 17 discloses that the still unstable filter cake is gradually put under increasing pressure by adding several bands in succession and only as - 6 -
- Claims 18-20 are concerned with preventing the free flow of free water from the tapes into the cakes when separating them from one another after the maximum pressing, because this would again deteriorate the consistency achieved in the cake.
- Claim 18 assumes that if all water-carrying tapes are completely separated quickly, this water will have little time to be sucked back (use especially at higher operating speeds).
- Claim 19 mainly intended for slow operation, assumes that the first screen fabric tape remains on the cake for a little longer and can release its water to the cake, but other water-carrying tapes take their water away and do not rewet it.
- a sieve fabric with a small swallowing volume is selected for the press water, or this sieve can be compressed under the press pressure, so that only a small amount of water adheres to it when it leaves the press zone.
- the water is removed from the sieve mesh after leaving the press zone before the sieve is lifted off the suspension cake.
- This can be done by applying a flat water jet tangentially to the screen fabric, the higher jet speed with its kinetic energy tearing the water out of the screen mesh. The same can be done by inflating an air jet.
- these two methods are not very handy because the water that has to be removed has to be collected again. It is therefore more sensible to use a pipe suction device that forms a gap to the sieve with a longitudinal bar through which the suction air flows. This is the water torn out of the sieve and immediately removed with the suction air through the pipe suction device.
- Claims 21 to 27 show variants of how the pressing surface against which the first screen fabric belt presses the suspension cake can be designed.
- Claim 24 shows a shoe roller with a progressively narrowing radius of curvature, which is possible without differential speed and friction between the roller shell and the fabric belt.
- the claims 25 to 27 have a modified principle to the content, in that the pressing surface takes on a concave shape in the pressing zone (shoe roller) and presses against a round roller.
- the belts should be moved away after pressing with a decreasing incline so that no white water can run back to the cake.
- Claim 32 deals with the possibility of operating the first screen fabric belt at different speeds relative to the pressing surface, as a result of which the suspension cake is shifted and torn open, which increases the overall surface and improves the outflow of the water. - 8th -
- Fig. 1 shows the representation of a dewatering device using several belts and a roller as a pressing surface (claims 2, 6, 8, 21).
- Fig. 2 shows the use of an impermeable tape with a pressure shoe
- Fig. 4 shows Fig. 3, but with the first screen belt on
- Fig. 5 shows the representation of a drainage device for slow
- Fig. 6 shows the progressive drainage through one or more tapes below
- FIG. 7 shows the pressure on a perforated roller tube (claim 23, 25).
- FIG. 8 shows, similar to FIG. 7, the pressure on a roller with circumferential grooving
- (Claim 27). 1 shows a dewatering device in which the fiber suspension (12) is injected with a distribution device (16) between a roller as a pressing surface (7) and a sieve fabric belt (1).
- the suspension (12) is subjected to a first dewatering under the pressure of the sieve fabric belt (1) and the centrifugal force, with fine substances in the suspension also being washed out intentionally.
- the corresponding press water (14) becomes less and less with increasing thickening.
- the pressing pressure is increased by a second looping permeable belt (2), so that further pressing water (14) is squeezed out.
- a third band (3) in this case an impermeable band, is also applied to the preceding bands by means of longitudinal tension and the pressing pressure is increased again.
- Fig. 2 the same drainage device is shown as in Fig. 1, but instead of with two other bands, here with an additional impermeable band (3) which is pressed by means of a sliding surface (5) of a pressure shoe (6).
- This band (3) has a swallowing volume on the surface and therefore throws off the water (14) it contains after leaving the pressing zone.
- Fig. 3 it is also the same device as in Fig. 1 and 2. But the thickening is achieved by a combination of Fig. 1 and 2, i. H. a second permeable (2) and a third impermeable band (4) are provided, but the third band (4) is pressed by a sliding surface (5). In this case, this third belt (4) has no swallowing volume, which is why no press water is thrown off by it.
- the three belts (1, 2, 4) are in turn led away from the cake (13) at the same time, but each in a different direction.
- Fig. 4 corresponds essentially to Fig. 3, but with the following differences: the third belt (4) again has swallowing volume and throws off water (14).
- the first sieve fabric belt is not led away from the cake at the same time as the other two belts (2, 4), but remains under longitudinal tension on the cake. During this stretch, the fabric is sucked dry with a pipe suction device (17) positioned on one side at a distance from the screen.
- Fig. 5 shows a very slow (under 10 m / min.) Running sludge dewatering device, which itself is provided with two fabric belts (1, 2) and a number of belt guide rollers (11) to alternate the sludge with each loop to drain each side.
- the device according to the invention is advantageously integrated immediately afterwards using one of the two sieve cloth belts (1).
- a smooth roller as a pressing surface (7), which is partially wrapped around by the existing fabric belt (1).
- the second band is no longer used, since according to the invention only one band is necessary.
- a third impermeable band (4) and a pressure shoe (6) with a sliding surface (5) now serve as the pressing device, the band (4) having circumferential grooves. - 11 -
- FIGS. 1 and 5 shows a combination of FIGS. 1 and 5:
- this sliding surface is provided with a progressively narrowing contour (R1 - R4) in the direction of travel, as a result of which the pressure on the suspension cake increases steadily.
- Fig. 7 also refers to the device according to Fig. 5 and leaves the guide shown there of the 1st screen belt.
- the two “rollers” (4, 7) are interchanged, whereby the impermeable belt with the pressure shoe becomes a smooth pressing surface (as in FIG. 6), but with a concave sliding surface (5), around the roller tube (8) provided here as a counter surface
- the press water can flow radially through the bores in the roller tube (8).
- This roller is also conceivable as a solid roller with blind holes on the surface (10). - 12 -
- Another band is also shown here in dashed lines if the band pressure before the shoe pressing (6) is to be increased.
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Filtration Of Liquid (AREA)
- Paper (AREA)
- Confectionery (AREA)
Description
Claims
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19805593A DE19805593A1 (de) | 1998-02-12 | 1998-02-12 | Eindicker |
DE19805593 | 1998-02-12 | ||
PCT/DE1999/000359 WO1999040994A1 (de) | 1998-02-12 | 1999-02-10 | Eindicker |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1100605A1 true EP1100605A1 (de) | 2001-05-23 |
EP1100605B1 EP1100605B1 (de) | 2005-04-20 |
Family
ID=7857406
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP99914409A Expired - Lifetime EP1100605B1 (de) | 1998-02-12 | 1999-02-10 | Eindicker |
Country Status (7)
Country | Link |
---|---|
US (1) | US6514381B1 (de) |
EP (1) | EP1100605B1 (de) |
AT (1) | ATE293487T1 (de) |
CA (1) | CA2320997A1 (de) |
DE (2) | DE19805593A1 (de) |
ES (1) | ES2242390T3 (de) |
WO (1) | WO1999040994A1 (de) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4318856B2 (ja) * | 1998-03-05 | 2009-08-26 | ジョンソン・アンド・ジョンソン・リサーチ・ピー・ティー・ワイ・リミテッド | チモーゲン性核酸検出方法、および関連分子およびキット |
US7651619B2 (en) * | 2001-12-28 | 2010-01-26 | Danmarks Tekniske Universitet (Dtu) | Filtration method and apparatus |
EP1734855A2 (de) * | 2004-04-16 | 2006-12-27 | Kadant Black Clawson Inc. | Drahtlose zweizonen-zellstoff-waschanlage |
SE539535C2 (sv) * | 2013-11-07 | 2017-10-10 | Stora Enso Oyj | Förfarande för avvattning av en suspension innefattande mikrofibrillerad cellulosa |
Family Cites Families (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE308011C (de) * | ||||
JPS5232137B2 (de) * | 1971-12-29 | 1977-08-19 | ||
SE363056B (de) * | 1972-05-05 | 1974-01-07 | Nordstjernan Rederi Ab | |
CH563867A5 (de) * | 1973-03-01 | 1975-07-15 | Escher Wyss Gmbh | |
US4172416A (en) * | 1978-03-09 | 1979-10-30 | Rederiaktiebolaget Nordstjernen | Apparatus for dewatering a suspension |
CH644414A5 (de) * | 1980-02-06 | 1984-07-31 | Escher Wyss Gmbh | Siebmaschine, insbesondere zur behandlung von aus altpapier gewonnenen waesserigen faserstoffsuspensionen. |
US4686005B1 (en) * | 1980-02-06 | 1995-10-17 | Escher Wyss Gmbh | Method of washing stock suspensions by removing undesired material through an endless revolving wire |
NL8003667A (nl) * | 1980-06-25 | 1982-01-18 | Pannevis Bv Machf | Werkwijze en inrichting voor het verwijderen van vloei- stof uit een mengsel van vloeistof en vaste stof. |
AT380907B (de) * | 1981-01-27 | 1986-07-25 | Escher Wyss Gmbh | Nasspresse mit verlaengertem pressspalt fuer papiermaschinen |
DE3142657C2 (de) * | 1981-09-29 | 1985-06-20 | Sulzer-Escher Wyss GmbH, 7980 Ravensburg | Entwässerungsvorrichtung |
DE3410745A1 (de) * | 1984-03-23 | 1985-09-26 | Alb. Klein Gmbh & Co Kg, 5241 Niederfischbach | Doppelbandpresse |
DE3414879A1 (de) * | 1984-04-19 | 1985-10-31 | Gebr. Bellmer GmbH + Co KG Maschinenfabrik, 7532 Niefern | Verfahren und vorrichtung zum fluessigkeitsentzug aus suspensionen mit hohem fluessigkeitsgehalt, zur getraenkeherstellung oder -gewinnung aus rueckstaenden |
US4738752A (en) * | 1986-08-12 | 1988-04-19 | Beloit Corporation | Heated extended nip press apparatus |
AT386544B (de) * | 1986-08-18 | 1988-09-12 | Andritz Ag Maschf | Maschine zum pressen und entwaessern bzw. filtrieren |
DE3734974A1 (de) * | 1986-10-21 | 1989-04-20 | Baehr Albert | Vorrichtung zum entwaessern von schlamm und aehnlichen substanzen |
DE3709329A1 (de) * | 1987-03-21 | 1988-09-29 | Dorr Oliver Inc | Verfahren zum entwaessern von filterkuchen und vorrichtung zur durchfuehrung des verfahrens |
EP0289477A3 (de) * | 1987-04-28 | 1989-03-08 | Valmet Paper Machinery Inc. | Verfahren zur Heisspressung von Papierbahnen und Trocknungsanlage zur Durchführung des Verfahrens |
DE9203395U1 (de) * | 1992-03-13 | 1992-05-07 | J.M. Voith Gmbh, 7920 Heidenheim, De | |
DE4216968A1 (de) * | 1992-05-22 | 1994-01-20 | Schenk Filterbau Gmbh | Verfahren und Vorrichtung zum Entwässern von Produkten |
DE19633958A1 (de) * | 1996-04-03 | 1997-10-09 | Voith Sulzer Papiermasch Gmbh | Saugpreßwalze |
DE19650396A1 (de) * | 1996-12-05 | 1998-06-10 | Voith Sulzer Papiermasch Gmbh | Entwässerungspresse |
DE19654200A1 (de) * | 1996-12-23 | 1998-06-25 | Voith Sulzer Papiermasch Gmbh | Naßpresse |
-
1998
- 1998-02-12 DE DE19805593A patent/DE19805593A1/de not_active Withdrawn
-
1999
- 1999-02-10 CA CA002320997A patent/CA2320997A1/en not_active Abandoned
- 1999-02-10 DE DE59911950T patent/DE59911950D1/de not_active Expired - Fee Related
- 1999-02-10 WO PCT/DE1999/000359 patent/WO1999040994A1/de active IP Right Grant
- 1999-02-10 ES ES99914409T patent/ES2242390T3/es not_active Expired - Lifetime
- 1999-02-10 EP EP99914409A patent/EP1100605B1/de not_active Expired - Lifetime
- 1999-02-10 US US09/600,170 patent/US6514381B1/en not_active Expired - Fee Related
- 1999-02-10 AT AT99914409T patent/ATE293487T1/de not_active IP Right Cessation
Non-Patent Citations (1)
Title |
---|
See references of WO9940994A1 * |
Also Published As
Publication number | Publication date |
---|---|
CA2320997A1 (en) | 1999-08-19 |
EP1100605B1 (de) | 2005-04-20 |
ES2242390T3 (es) | 2005-11-01 |
US6514381B1 (en) | 2003-02-04 |
DE19805593A1 (de) | 1999-08-19 |
ATE293487T1 (de) | 2005-05-15 |
WO1999040994A1 (de) | 1999-08-19 |
DE59911950D1 (de) | 2005-05-25 |
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