EP0561256A1 - Verfahren zum Lufttrocknen von freigeführten Materialbahnen sowie Blasluftdüse und Papiertrockner zur Durchführung des Verfahrens - Google Patents

Verfahren zum Lufttrocknen von freigeführten Materialbahnen sowie Blasluftdüse und Papiertrockner zur Durchführung des Verfahrens Download PDF

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Publication number
EP0561256A1
EP0561256A1 EP93103768A EP93103768A EP0561256A1 EP 0561256 A1 EP0561256 A1 EP 0561256A1 EP 93103768 A EP93103768 A EP 93103768A EP 93103768 A EP93103768 A EP 93103768A EP 0561256 A1 EP0561256 A1 EP 0561256A1
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EP
European Patent Office
Prior art keywords
web
nozzle
blow
air
face
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Application number
EP93103768A
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English (en)
French (fr)
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EP0561256B1 (de
Inventor
Pertti Heikkilä
Iikka Jokioinen
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Valmet Technologies Oy
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Valmet Paper Machinery Inc
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    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F5/00—Dryer section of machines for making continuous webs of paper
    • D21F5/18—Drying webs by hot air
    • D21F5/185—Supporting webs in hot air dryers
    • D21F5/187—Supporting webs in hot air dryers by air jets
    • D21F5/188—Blowing devices
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B13/00—Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
    • F26B13/10—Arrangements for feeding, heating or supporting materials; Controlling movement, tension or position of materials
    • F26B13/101—Supporting materials without tension, e.g. on or between foraminous belts
    • F26B13/104—Supporting materials without tension, e.g. on or between foraminous belts supported by fluid jets only; Fluid blowing arrangements for flotation dryers, e.g. coanda nozzles

Definitions

  • the invention concerns a method in air-drying of material webs, in particular of material webs of relatively high grammage, such as pulp webs, in which method, to the web to be dried, from underneath the web, air blowings substantially perpendicular to the web and air blowings substantially parallel to the plane of the web are applied, by means of which blowings both heat is transferred to the web and the web is supported by air free of contact, and the run of the web through the dryer is stabilized.
  • the invention concerns a nozzle-blow-box of an air dryer, through which box air blowings are applied to the material web to be dried, by means of which blowings both transfer of heat is produced from the drying air to the web and contact-free air support and stabilization of the run of the web are obtained
  • said nozzle-blow-box comprising a box part, in which there is a nozzle-carrier face placed against the web, in the middle of which face there is a substantially V-section groove transverse to the running direction of the web, which groove is opened towards the web and in whose opposite walls there are series of nozzle holes so that, out of said series of nozzle holes, support and stabilization air blowings can be applied which are cross-wise and of opposite directions in relation to each other, and in which nozzle-carrier face, at both sides of its V-section groove, there are plane nozzle-carrier-face portions placed in the same plane with each other.
  • the invention concerns a pulp dryer that makes use of the method of the invention and/or of the nozzle-blow-box of the invention.
  • blow boxes are commonly used whose nozzle-carrier face consists of a plane plate, into which blow holes have been punched. Such nozzles are placed either at one side or at both sides of the airborne web to be dried.
  • the nozzle-carrier-face commonly includes a number of rows of holes, one row after the other in the running direction of the web. The blow air flows in the space between the web and the nozzle-carrier-face, and the blow air is collected away through suction slots placed between the nozzle boxes.
  • lateral flow is understood as meaning air flows parallel to the plane of the carrier face and of the web, which flows are additionally parallel to or opposite to the running direction of the web. Since the air must escape from the treatment gap, a lateral flow cannot be avoided. Said lateral flow deteriorates the transfer of heat in the prior-art blow-nozzle boxes, and the disturbing effect is increased with an increase in the velocity of the exhaust-air flow.
  • the loss of pressure produced by the blow box is increased when the velocity increases in the lateral flow.
  • it is preferable to make use of the lateral flow by shaping the blow face and the geometry of its nozzle openings such that, on the carrier face of the blow box, a zone of negative pressure is formed, which stabilizes the run of the web and by whose means a stable and unstrained run of the web is ensured.
  • the present invention is above all related to the nozzle-blow-boxes employed in pulp dryers, in which the web runs above the nozzle and carrier faces of the boxes.
  • the function of the air blowings is both to transfer heat from the blown air to the web and to support the web free of contact.
  • it is preferable to blow part of the air parallel to the plane of the nozzle in which case the web is stabilized at a distance of 3...6 mm from the carrier face.
  • the velocity of the exhaust air in the space between the web and the nozzle becomes high. This results in deterioration of the transfer of heat and in extra pressure losses.
  • the detrimental effect of the high velocity of the exhaust air can be reduced by making the nozzles sufficiently narrow, but then the number of the nozzles becomes so high that the cost of manufacture of the dryer is increased substantially.
  • An object of the present invention is to provide a novel method and a novel nozzle-blow-box construction by whose means it is possible to avoid the drawbacks discussed above and to improve the transfer of heat from the drying air to the airborne web to be dried. Said improvement of the transfer of heat can be utilized most efficiently in the form of smaller size of the dryer. In this way, the cost of construction, e.g., of a pulp dryer and the cost of the machine hall can be lowered decisively.
  • An object of the present invention is to reduce the effect of deteriorating of the transfer of heat by the lateral flow while the run of the web is stabilized by means of said flow.
  • the method of the invention is mainly characterized in that, in order to improve the transfer of heat in comparison with a plane carrier face, the air flow velocity parallel to the plane of the web to be dried and air-supported in connection with the nozzle-carrier face is initially kept substantially invariable, whereupon the air flow velocity is lowered in the lateral areas of said carrier face by employing lateral areas of the nozzle-carrier face that become rampwise and/or stepwise lower in the air-flow direction.
  • the nozzle-blow-box in accordance with the invention is mainly characterized in that extensions of said nozzle-carrier-face portions are constituted by stepwise and/or ramp-shaped carrier-face portions placed further apart from the material web to be supported, in the area of which carrier-face portions the velocities of said support and stabilization air flows, as compared with the velocity prevailing in connection with the plane nozzle-carrier-face portions, are lowered, and that the nozzle-carrier face is provided with nozzle perforations, through which additional blowings substantially perpendicular to the plane of the material web to be supported can be applied from the nozzle-blow-box.
  • the effect of deteriorating of the transfer of heat by the lateral flow has been minimized by lowering the lateral portions of the nozzle to a level lower than the plane middle portion, whereby the velocity of the lateral flow is lowered.
  • the lateral flows are preferably directed so that they do not directly collide against the air jets of the direct blowing on the plane face or on the lowered lateral portions.
  • the lowering of the lateral areas of the nozzle-carrier-face portions in accordance with the invention is based on the idea that a high flow velocity of the exhaust air between the web and the nozzle-carrier face deteriorates the coefficient of heat transfer.
  • the velocity of the exhaust air is increased in both directions from the centre line of the nozzles towards the edges when more air is introduced.
  • the flow velocity in this area is lowered.
  • the nozzle-blow-box in accordance with the invention is a combination of a nozzle with positive/negative pressure, in which the magnitude of the lateral flow that produces the negative pressure is chosen appropriately in relation to the amount of air in the direct blowing.
  • the coefficient of heat transfer is not essentially dependent on the distance, provided that the exhaust air does not disturb the air jets blown out of the nozzle holes to a significant extent.
  • the air discharged out of the nozzles must pass towards the edges in the space between the nozzle and the web, and the higher this flow velocity is, the more does it disturb the air jets blown out of the holes and the more does it deteriorate the coefficient of heat transfer.
  • air jets are directed, crosswise in relation to one another, at continuous rounding points between the plane carrier face placed at each side of the walls of said V-section groove.
  • the air jets are tangential to the rounding points, they turn and become parallel to the plane portions of the carrier face by the Coanda effect.
  • a zone of negative pressure is formed, which stabilizes the web at a certain distance from the carrier face, as a rule, of an order of 3...6 mm.
  • attempts are made to avoid direct collisions between the jets of direct blowing and the air jets that flow in the lateral direction.
  • the lateral areas of the nozzle-carrier face of the nozzle-blow-box have been lowered so that the velocity of the lateral flow is lowered as the cross-sectional flow area becomes larger, whereby the heat-transfer effect of the blow jets coming from the holes of direct blowing placed in the lowered inclined and/or straight nozzle-carrier-face portion is improved.
  • the nozzle-blow-box in accordance with the invention is suitable for use for drying of the web both in one-sized/two-sided drying, in the case of low-grammage webs ( ⁇ 200 g/sq.m), and both underneath and above the web.
  • the nozzle-blow-boxes in accordance with the invention are best suitable for lower nozzles together with direct-blow boxes that operate as upper nozzles, or alone as lower nozzle boxes in one-sided drying.
  • a further advantage that is achieved by means of the geometry of the blow-carrier faces of the nozzle-blow-boxes in accordance with the invention is a smooth blow face with no sharp edges, as the air of the lateral flow is introduced out of the central V-section groove while guided by rounded faces.
  • the transfer of heat to the web can be improved by about 5...10 %, this improvement can be taken to useful use immediately in the form of reduced size of the dryer, which lowers the cost of investment of the dryer and of the machine hall substantially, and which also, indirectly, reduces the number of production interruptions and improves the operating time ratio of the dryer.
  • the advantages mentioned above are particularly important in the case of large and complicated pulp dryers.
  • a V-section groove in the middle of its carrier face, through which groove the blowings parallel to the carrier face are applied crosswise, in addition to a favourable blow/heat-transfer technique, a rigid mechanical construction is obtained, in which the V-section groove rigidifies the nozzle-carrier-face efficiently without any other rigidifying structures, which would be necessary otherwise.
  • Figure 1 is a schematic vertical sectional view in the machine direction of a pulp dryer that makes use of the method and of a set of nozzle-blow-boxes in accordance with the invention.
  • Figure 2 is an axonometric view of the modular construction of a pulp dryer that makes use of the method and of a set of nozzle-blow-boxes of the invention.
  • Figure 3 is a schematic vertical sectional view in the machine direction of a set of nozzle-blow-boxes in accordance with the invention and of a set of boxes of direct blowing placed above said set of boxes.
  • Figure 4 is an axonometric illustration of a nozzle-blow-box in accordance with the invention and of the principle of its blowings.
  • Figure 5 is an axonometric view of the construction of an upper direct-blow box.
  • Figure 6 shows an embodiment of a carrier face of a nozzle-blow-box in accordance with the invention and of the blow nozzles of said carrier face in more detail, together with the most important parameters of dimensioning.
  • Figures 7A, 7B, 7C, 7D, and 7E illustrate different variations of different embodiments and dimensions of bevel and step formations of the nozzle-carrier faces of a nozzle-blow-box in accordance with the invention and of a nozzle-blow-box of reference.
  • Figure 8A shows a nozzle-blow-box as shown in Figs. 4 or 5, seen from the side of the nozzle-carrier face.
  • Figure 8B is an enlarged schematic vertical sectional view in the machine direction of a preferred geometry and dimensioning of the V-section groove of the nozzle.
  • Figure 9 illustrates different relative coefficients of heat transfer in the cases illustrated in Figs. 7A to 7E as a function of the distance of the web at a first air-blow velocity.
  • Figure 10 illustrates the corresponding measurement results in a way corresponding to Fig. 9, at a second, higher air-blow velocity.
  • Fig. 1 is a schematic vertical sectional view in the machine direction of a pulp dryer that makes use of the method and of a set of nozzle-blow-boxes in accordance with the invention.
  • the dryer comprises a closed hood 12, in whose interior there is a set of nozzle-blow-boxes 30 in accordance with the invention and, placed facing said set of boxes, a set of boxes 40 of direct blowing, the web W to be dried being passed through the treatment gaps 25 formed by said sets of boxes as supported by air free of contact.
  • the pulp web W in or equivalent that is passed into the dryer is passed through the wet press 10 and over the roll 11 for regulation of the tension of the web, through an inlet opening 12a, into the hood 12, in which the web W to be dried runs as horizontal draws back and forth, being guided by guide rolls 13.
  • the dried web W is removed through an outlet opening 12b placed in the bottom part of the hood 12, being passed by the intermediate of an alignment roll 14 through a set of drive rolls 15 further (W out ).
  • the path of the web threading belt or rope is illustrated by the reference numeral 16 and by the dashed-dotted line.
  • Fig. 1 the circulation of drying air taking place inside the hood 12 is illustrated schematically by means of arrows A1...A2.
  • the arrows A1 and the air ducts 17 placed in connection with them represent the introduction of replacement air from the heat recovery, and the arrows A2 and the air ducts 18 placed in connection with them represent the passage of the exhaust air to the heat recovery.
  • Fig. 2 illustrates the modular construction of a pulp dryer that makes use of the method and of a nozzle-blow-box in accordance with the invention and whose basic principle is, e.g., similar to that illustrated in Fig. 1.
  • the dryer-blower module comprises blower towers 21 and blowers, which are provided with blade wheels 22.
  • the module construction comprises heating radiators 24, through which the blow air is passed into the gap between the upper nozzles and the lower nozzles, i.e. into the web gap 25. Further, the module construction includes air filters 26.
  • At the operating side of the blower module there is a tending bridge 28, in connection with which there are servicing gates 27 for the blower motors and servicing doors 29 for the blower modules.
  • Fig. 2 shows the circulation of the drying air as illustrated by the arrows, and also the nozzle-blow-boxes 30,40 in accordance with the invention and the web gaps 25 between them.
  • Figs. 1 and 2 it is to be emphasized that, above, they have been described just as one field of application of the method and of the set of nozzle-blow-boxes 30,40 in accordance with the invention and that the method and the set of nozzle-blow-boxes 30,40 in accordance with the invention can also be applied in a great number of other environments and also in other than pulp dryers, for example in board and paper-web dryers, even though the pulp dryers are the most advantageous and primary field of application of the invention, in which several different advantages of the invention are best used for a useful purpose.
  • Fig. 3 is a schematic illustration of a set of nozzle-blow-boxes 30 in accordance with the invention and of an opposite set of boxes 40 of direct blowing.
  • the shorter name "lower box” will be used for the nozzle-blow-boxes 30, because they are preferably placed underneath the horizontally running web W.
  • the blow air is passed further through the healing radiators 24 shown in Fig. 2, being carried by the blower 22, back to the blow boxes.
  • the healing radiators 24 shown in Fig. 2 being carried by the blower 22, back to the blow boxes.
  • the web W to be dried runs as a horizontal run through the web gap 25.
  • the web gap 25 is defined from below by the lower boxes 30, which are placed as uniformly spaced in one horizontal plane, and from above by the direct-blow boxes 40, which are placed as uniformly spaced in a horizontal plane.
  • the web W which is usually heavy (the weight of a wet pulp web may be up to ⁇ 2000 g/sq.m), is supported by means of the blowings B2 and B3.
  • blowings B1 perpendicular to the plane of the web W are applied to the web W, the web W being dried from above by means of said blowings B1.
  • Figs. 4, 6, and 8A and 8B illustrate the construction of the lower boxes 30 in more detall.
  • a transverse groove 32 i.e. a groove 32 passing across the width of the web W, which groove is opened towards the web W.
  • the opening angle of the V-section groove 32 is denoted with a.
  • the inclined walls of the V-section groove 32 which walls are preferably plane, turn and join the horizontal plane portion 34 of the carrier face at an angle b by the intermediate of rounded portions 31b with a curve radius R.
  • Both of the inclined plane faces of the V-section groove 32 have rows of blow holes 33. These blow holes 33 are placed and directed so that the air jets B3 coming from them are tangential to the rounded portions 31b between the plane faces, said rounded portions turning the air jets B3, by the Coanda effect, onto the plane portions 34 of the carrier face 31 and making the jets parallel to said plane portions.
  • the blow holes 33 are placed in the opposite sides of the V-section groove 32 as fitted in such a way staggered in relation to one another (Fig. 8) that the blowings B3 are inter-locked with one another crosswise in opposite directions.
  • one set of the blowings B3 is parallel to the running direction of the web W and to its plane, whereas the other set of the blowings is parallel to the plane of the web W but of a direction opposite to the running direction of the web W.
  • the blowings B3 induce a zone of negative pressure between the web W and the carrier face 31, which zone stabilizes the web W at a certain distance H from the carrier face 31.
  • lateral portions 35 are placed, whose height in relation to the web W is lower than the height of the middle-plane portions 34 of the carrier face 31.
  • said lateral portions 35 are inclined plane bevel parts, whose distance in relation to the plane parts 34 at the edges of the nozzle box 30 is denoted with h2.
  • the air velocity is first substantially invariable in connection with the plane carrier-face portions 31, whereupon the air velocity is lowered in connection with the carrier-face portions 35;35b,35d,35e stepwise or continuously when moving towards the edges of the box 30 and towards the spaces 30a in the treatment gap 25.
  • the transfer of heat can be intensified considerably, as will come out later from the test results illustrated in Figs. 9 and 10.
  • the lower box 30 and the direct-blow box 40 as shown in Figs. 4 and 5 are placed one above the other and one facing the other, so that the faces 41 and 31 are substantially parallel to one another and, as a rule, horizontal.
  • the faces 41 of the direct-blow boxes 40 there may be rounded portions 43a, and at the edges of the carrier faces 31 of the lower boxes 30, there may be corresponding rounded portions 31a.
  • the opposite faces 31 and 41 on the lower box 30 and on the direct-blow box 40 are provided with nozzle perforations 42;36.
  • a preferred distribution of the perforations 36 on the blow box 30 comes out from Fig. 8.
  • perpendicular blowings B1;B2 are directed against the web W, the drying of the web W being promoted by means of said blowings.
  • the direct blowings B2 will have a longer time of effect on the lower face of the web W.
  • Fig. 8B is a schematic illustration of a preferred embodiment of the geometry and of a dimensioning example of the V-section groove 32 described above.
  • the geometry shown in Fig. 8B is symmetric in relation to the transverse vertical centre plane K-K. It is the starting point of the design of the V-section groove 32 that the air jets F1 and F2 blown from the opposite sides can be made tangential to the rounded portions 31b connected with the edges of the groove 32 so that, by the Coanda effect, said air jets turn and become parallel to the carrier face 34.
  • the area between the groove 33 and the carrier face 34 must be expressly rounded in such a way that the air starts following the carrier face 34.
  • Figs. 7A...7E show some alternative embodiments of the carrier face of the blow box 30.
  • the nozzle box 30A as shown in Fig. 7A comprises a carrier face 31, in which there are plane portions 34 at both sides of the V-section groove 32 and, after them, plane inclined bevel portions 35.
  • Fig. 7B shows a particularly advantageous blow box 30B, in which, at both sides of the V-section groove 32, there are plane portions 34b of the carrier face and, after them, step portions 37, which are perpendicular both to the first plane portions 34b of the carrier face and to the plane portions 35b of the carrier face that follow after the step portion 37.
  • the initial parts 34b of the carrier face 31 are parallel to one another and in the same horizontal plane.
  • the lateral portions of the carrier face 31 are parallel to one another and in the same horizontal plane.
  • Fig. 7B also shows a preferred dimensioning example of the nozzle box 30B.
  • a nozzle box 30C is illustrated as a reference, which box has a fully plane carrier face 31c.
  • this nozzle box 30C is not in accordance with the present invention, and it is illustrated in this connection for the sake of reference only, the results of said comparison coming out from Figs. 9 and 10, which will be described in more detail later.
  • Fig. 7D illustrates a blow box 30D in accordance with the invention, which box has relatively long plane carrier-face portions 34d and relatively short and steep, inclined lateral portions 35d.
  • a preferred dimensioning example is also given.
  • FIG. 7E an alternative modification of the blow box as shown in Fig. 7B is illustrated, which modification has relatively long plane carrier-face portions 34e and step portions 37, which are followed by relatively short carrier-face portions 35e.
  • Fig. 7E also shows an example of the construction of said blow box 30E.
  • Fig. 8A shows the relative locations and staggering of the nozzle holes 33 in the V-section groove 32 so that the blowings B3 of opposite directions are blown crosswise.
  • the perforations 36 in the nozzle-carrier face 31 are placed in four lines, one line after the other, as staggered in such a way that the blowings B2 and B3 neither meet each other nor disturb each other.
  • the mutual spacing of the nozzle holes 33 is, as a rule, in a range of 20...50 mm, and, in a corresponding way, the mutual spacing of the nozzle holes 36 in the transverse direction and in the machine direction is, as a rule, in a range of 40...100 mm.
  • the diameter ⁇ of the nozzle holes 33 is chosen as related to the diameter of the direct-blow nozzles 36 in the carrier face so that the air quantity in the carrier-blowings B3 blown through the nozzle holes 33 is about 30...60 %, preferably 35...45 %, of the overall air quantity of the blowings B2 and B3.
  • the length L1 of the bevelled or step-formed lateral portions 35,35b,35d,35e in the carrier face 31 is chosen so that it is (0.1...0.3) x L, preferably (0.2...0.25) x L, wherein L is the total length of the blow box 30 in the machine direction. Said length L is, as a rule, in a range of L ⁇ 300...500 mm.
  • Figs. 9 and 10 illustrate test results obtained with nozzles as shown in Figs. 7A...7E graphically.
  • the vertical axis represents the relative heat transfer coefficient ⁇ R
  • the horizontal axis represents the distance of the web W from the carrier face 31, expressly from its plane portion 34.
  • the letter symbol corresponds to the curves A...E in Figs. 9 and 10.
  • the most advantageous embodiment of the invention is, according to the present-day opinion and on the basis of the available measurement results, the blow-nozzle box 30A as shown in Fig. 7A.
  • a carrier face 34b,35b with a steep step formation (37), as shown in Fig. 7B is optimal in view of the transfer of heat, but a nozzle-blow-box 30A as shown in Fig. 7A, which is provided with continuously lowering ramp-formed lateral portions 35 of the carrier face, is preferable in an overall consideration, because, in it, the risk of formation of a "cigar" is lower, for the geometry of the blow face does not include sharp angles.
  • a nozzle-blow-box 30A as shown in Fig. 7A (also in respect of its dimensions) is the best embodiment of the invention in a case in which the distance, e.g., of a pulp web W from the horizontal portion 34 of the carrier face 31 is ⁇ 5 mm.
  • the invention concerns a method in air-drying of material webs, in particular of material webs of relatively high grammage, such as pulp webs. Also, the invention concerns a nozzle-blow-box and a pulp dryer that make use of the method.
  • air blowings (B2) substantially perpendicular to the web and air blowings (B3) substantially parallel to the plane of the web (W) are applied.
  • B2,B3 By means of these blowings (B2,B3), both heat is transferred to the web (W) and the web is supported by air free of contact, and the run of the web through the dryer is stabilized.
  • a plane carrier face FIG.
  • the air flow velocity parallel to the plane of the web (W) to be dried and air-supported in connection with the nozzle-carrier face (31) is initially (34) kept substantially invariable, whereupon the air flow velocity is lowered in the lateral areas (35;35b;35d;35e) of said carrier face (31) by employing lateral areas (35, 35b,35e) of the nozzle-carrier face (31) that become rampwise and/or stepwise lower in the air-flow direction.

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Drying Of Solid Materials (AREA)
  • Paper (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
EP93103768A 1992-03-19 1993-03-09 Verfahren zum Lufttrocknen von freigeführten Materialbahnen and Lufttrockner zur Durchführung des Verfahrens Expired - Lifetime EP0561256B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI921193A FI92421B (fi) 1992-03-19 1992-03-19 Menetelmä ainesratojen ilmakuivatuksessa, ilmakuivattimen suutin-puhalluslaatikko ja sellukuivatin
FI921193 1992-03-19

Publications (2)

Publication Number Publication Date
EP0561256A1 true EP0561256A1 (de) 1993-09-22
EP0561256B1 EP0561256B1 (de) 2001-07-11

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EP93103768A Expired - Lifetime EP0561256B1 (de) 1992-03-19 1993-03-09 Verfahren zum Lufttrocknen von freigeführten Materialbahnen and Lufttrockner zur Durchführung des Verfahrens

Country Status (10)

Country Link
EP (1) EP0561256B1 (de)
JP (1) JP3305802B2 (de)
KR (1) KR0172974B1 (de)
CN (1) CN1031656C (de)
AT (1) ATE203071T1 (de)
BR (1) BR9301228A (de)
CA (1) CA2092004C (de)
DE (1) DE69330413T2 (de)
ES (1) ES2159510T3 (de)
FI (1) FI92421B (de)

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995010473A1 (de) * 1993-10-11 1995-04-20 Krieger Gmbh & Co. Kg Vorrichtung zum schwebendführen einer laufenden bahn
WO1996018074A1 (en) * 1994-12-06 1996-06-13 W.R. Grace & Co.-Conn. Combination air bar and hole bar flotation dryer
WO1997016594A1 (en) * 1995-10-31 1997-05-09 ABB Fläkt AB Blowbox for use in a plant for drying a material web
WO1997048853A1 (en) * 1996-06-19 1997-12-24 Valmet Corporation Method and device in connection with impingement drying and/or through-drying of a paper web or of an equivalent web-like material
US6119362A (en) * 1996-06-19 2000-09-19 Valmet Corporation Arrangements for impingement drying and/or through-drying of a paper or material web
WO2001002643A1 (en) * 1999-06-30 2001-01-11 Metso Paper, Inc. Nozzle arrangement in airborne web-drying and method for improving heat transfer in airborne web-drying
DE19882574C2 (de) * 1997-08-18 2002-05-16 Metso Paper Inc Verfahren und Vorrichtung zur Trocknung einer Stoffbahn
US6564473B2 (en) 2001-10-22 2003-05-20 The Procter & Gamble Company High efficiency heat transfer using asymmetric impinging jet
EP1502991A1 (de) * 2003-07-31 2005-02-02 Voith Paper Patent GmbH Vorrichtung zur Führung und Trocknung einer laufenden Faserstoffbahn
EP1630284A1 (de) * 2004-08-18 2006-03-01 Voith Paper Patent GmbH Modularer lufttrockner
WO2008059102A1 (en) * 2006-11-14 2008-05-22 Metso Paper, Inc. End part of an air dryer, air dryer, method in the end part of an air dryer and use of fan
WO2008069728A1 (en) 2006-12-06 2008-06-12 Andritz Technology And Asset Management Gmbh Drying box
WO2009129056A1 (en) * 2008-04-18 2009-10-22 Honeywell International Inc. Sheet stabilizer with dual inline machine direction air clamps and backsteps
WO2013004915A1 (en) * 2011-07-06 2013-01-10 Balance Engineering Oy Method and apparatus for increasing drying efficiency and energy efficiency in connection with the dryer section in the manufacture of pulp
CN114993017A (zh) * 2022-07-29 2022-09-02 佛山市新飞卫生材料有限公司 离型纸细散式气流悬浮烘箱
AT525833A3 (de) * 2022-02-04 2023-08-15 Valmet Technologies Oy Luftgestützter Pulpetrockner mit Querrichtungsblaskästen

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CN100404990C (zh) * 2000-09-24 2008-07-23 3M创新有限公司 蒸气收集方法
FI110626B (fi) 2000-11-29 2003-02-28 Metso Paper Inc Menetelmä ja laitteisto kuitupohjaisen massarainan kuivaamiseksi
CN1329586C (zh) * 2005-02-28 2007-08-01 陈建辉 热风穿透式卫生纸机及热风穿透干燥卫生纸的加工工艺
SE535179C2 (sv) * 2010-07-14 2012-05-08 Andritz Tech & Asset Man Gmbh Sätt att torka en massabana och anordning för torkning av en sådan bana
SE536108C2 (sv) * 2010-11-16 2013-05-07 Andritz Tech & Asset Man Gmbh Torklåda som innefattar åtminstone två zoner för torkning av en cellulosamassabana
SE535634C2 (sv) * 2010-11-16 2012-10-23 Andritz Tech & Asset Man Gmbh Cellulosatork som har nedre blåslådor samt förfarande för torkning av en bana av cellulosamassa
DE102010052044A1 (de) * 2010-11-23 2012-05-24 Vits Technology Gmbh Verfahren und Anlage zum Imprägnieren und Trocknen einer durchlaufenden Papierbahn
DE102011006698A1 (de) * 2011-04-04 2012-10-04 Voith Patent Gmbh Verfahren zum Trocknen einer Faserstoffbahn in einer Trockenvorrichtung und Trockenvorrichtung
CN102733244B (zh) * 2012-07-12 2015-04-01 山东太阳纸业股份有限公司 一种防止溶解浆板机干燥箱内刮纸的方法及其结构
SE538854C2 (sv) * 2014-01-09 2017-01-03 Valmet Oy Rullstol för mottagande och upprullning av en pappersbana, som kommer från en torkcylinder i en pappersmaskin, till en rulle, samt en pappersmaskin som använder en rullstol
CN106605023B (zh) * 2014-05-15 2020-03-10 灵越工程私人有限公司 一种歧管
CN105066619A (zh) * 2015-07-23 2015-11-18 滁州金春无纺布有限公司 一种可自动穿引布料的纺织烘燥设备
CN107940922A (zh) * 2017-12-12 2018-04-20 深圳市共享能源技术有限公司 箱式热泵干燥箱
EP3916150A1 (de) * 2020-05-26 2021-12-01 Valmet Technologies Oy Düsensystem einer vorrichtung zur berührungslosen behandlung einer laufenden faserstoffbahn

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US6502735B1 (en) 1993-10-11 2003-01-07 Kreiger Gmbh & Co. Device for the suspension guidance of a travelling web
WO1995010473A1 (de) * 1993-10-11 1995-04-20 Krieger Gmbh & Co. Kg Vorrichtung zum schwebendführen einer laufenden bahn
WO1996018074A1 (en) * 1994-12-06 1996-06-13 W.R. Grace & Co.-Conn. Combination air bar and hole bar flotation dryer
WO1997016594A1 (en) * 1995-10-31 1997-05-09 ABB Fläkt AB Blowbox for use in a plant for drying a material web
AU698119B2 (en) * 1995-10-31 1998-10-22 Andritz Technology And Asset Management Gmbh Blowbox for use in a plant for drying a material web
LT4466B (lt) 1995-10-31 1999-02-25 Abb Flaekt Ab Pūtimo dėžė, skirta naudoti medžiagos juostos džiovinimo įrengimuose
US6092304A (en) * 1995-10-31 2000-07-25 Abb Flakt Ab Blow box for use in a plant for drying a material web
CN1075575C (zh) * 1995-10-31 2001-11-28 Abb弗莱克特股份公司 在用于吹干坯料带的装置中使用的吹风箱
WO1997048853A1 (en) * 1996-06-19 1997-12-24 Valmet Corporation Method and device in connection with impingement drying and/or through-drying of a paper web or of an equivalent web-like material
US5845415A (en) * 1996-06-19 1998-12-08 Valmet Corporation Method for impingement drying and/or through-drying of a paper or material web
US6119362A (en) * 1996-06-19 2000-09-19 Valmet Corporation Arrangements for impingement drying and/or through-drying of a paper or material web
DE19882574C2 (de) * 1997-08-18 2002-05-16 Metso Paper Inc Verfahren und Vorrichtung zur Trocknung einer Stoffbahn
US6598315B1 (en) 1999-06-30 2003-07-29 Metso Paper, Inc. Nozzle arrangement in airborne web-drying and method for improving heat transfer in airborne web-drying
WO2001002643A1 (en) * 1999-06-30 2001-01-11 Metso Paper, Inc. Nozzle arrangement in airborne web-drying and method for improving heat transfer in airborne web-drying
US6564473B2 (en) 2001-10-22 2003-05-20 The Procter & Gamble Company High efficiency heat transfer using asymmetric impinging jet
EP1502991A1 (de) * 2003-07-31 2005-02-02 Voith Paper Patent GmbH Vorrichtung zur Führung und Trocknung einer laufenden Faserstoffbahn
EP1630284A1 (de) * 2004-08-18 2006-03-01 Voith Paper Patent GmbH Modularer lufttrockner
AU2007321145B2 (en) * 2006-11-14 2010-12-16 Metso Paper, Inc. End part of an air dryer, air dryer, method in the end part of an air dryer and use of fan
WO2008059102A1 (en) * 2006-11-14 2008-05-22 Metso Paper, Inc. End part of an air dryer, air dryer, method in the end part of an air dryer and use of fan
US7993491B2 (en) 2006-11-14 2011-08-09 Metso Paper, Inc. End part of an air dryer, air dryer, method in the end part of an air dryer and use of fan
CN101535566B (zh) * 2006-11-14 2012-05-30 美卓造纸机械公司 空气干燥机的末端部、空气干燥机、空气干燥机的末端部中的方法和风扇的应用
WO2008069728A1 (en) 2006-12-06 2008-06-12 Andritz Technology And Asset Management Gmbh Drying box
EP2089573A1 (de) * 2006-12-06 2009-08-19 Andritz Technology and Asset Management GmbH Trockenkasten
EP2089573A4 (de) * 2006-12-06 2013-06-05 Andritz Tech & Asset Man Gmbh Trockenkasten
WO2009129056A1 (en) * 2008-04-18 2009-10-22 Honeywell International Inc. Sheet stabilizer with dual inline machine direction air clamps and backsteps
WO2013004915A1 (en) * 2011-07-06 2013-01-10 Balance Engineering Oy Method and apparatus for increasing drying efficiency and energy efficiency in connection with the dryer section in the manufacture of pulp
AT525833A3 (de) * 2022-02-04 2023-08-15 Valmet Technologies Oy Luftgestützter Pulpetrockner mit Querrichtungsblaskästen
AT525833B1 (de) * 2022-02-04 2023-12-15 Valmet Technologies Oy Luftgestützter Pulpetrockner mit Querrichtungsblaskästen
CN114993017A (zh) * 2022-07-29 2022-09-02 佛山市新飞卫生材料有限公司 离型纸细散式气流悬浮烘箱
CN114993017B (zh) * 2022-07-29 2022-10-14 佛山市新飞卫生材料有限公司 离型纸细散式气流悬浮烘箱

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BR9301228A (pt) 1993-09-21
DE69330413D1 (de) 2001-08-16
EP0561256B1 (de) 2001-07-11
FI921193A0 (fi) 1992-03-19
ES2159510T3 (es) 2001-10-16
JPH06248593A (ja) 1994-09-06
FI92421B (fi) 1994-07-29
KR930019930A (ko) 1993-10-19
CN1081485A (zh) 1994-02-02
CA2092004A1 (en) 1993-09-20
KR0172974B1 (ko) 1999-03-30
DE69330413T2 (de) 2002-06-20
ATE203071T1 (de) 2001-07-15
JP3305802B2 (ja) 2002-07-24
CA2092004C (en) 1998-05-19
FI921193A (fi) 1993-09-20
CN1031656C (zh) 1996-04-24

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