Press section of paper machine, in particular for printing paper qualities

Abstract: Press section of a paper machine, in particular for printing paper qualities whose grammage is in the range of 40...80 g/m 2 . The press section comprises a pick-up roll (13), on whose suction zone (13a) the web (W) is detached at the pick-up point (P) from the forming wire (10) and is passed on the pick-up felt (15) into the first press nip (Np) in the press section, in which nip said pick-up felt (15) acts as a press fabric. After the first press nip the web (W) is transferred as a closed or open draw (Wp) onto the drying wire (50) of the drying section, or into the last nip (N 2 ) in the press section, which nip is a roll nip. The press section is preceded by a wire nip (N o , Np o ) which dewaters the web (W) substantially and which is formed between a press roll (11) placed inside the loop of the forming wire (10) and a hollow-faced (60') press roll (60) or a hose roll (20) which is provided with an extended-nip zone and which operates opposite to said press roll (11), and through which wire nip (N o , Np o ) a relatively open press fabric (61 ) is passed.

Description: The invention concerns a press section of a paper machine, in particular for printing paper qualities whose grammage is in the range of 40... 80 g/m 2 . One of the most important quality requirements of all paper and board qualities is the homogeneity of the structure both on the micro scale and on the macro scale. The structure of paper, in particular of printing paper, must also be symmetric. The good printing qualities to be required from printing paper mean good smoothness, evenness, and certain absorption properties of both faces. The properties of paper, in particular the symmetry of density, are affected to a considerable extent by the operation of the press section of the paper machine, which has also a decisive significance for the evenness of the transverse profiles of the paper and of the profiles of the paper in the machine direction. Increasing running speeds of paper machines create new problems to be solved, which problems are mostly related to the running quality of the machine. At present, running speeds of up to about 1400 m/min are used. At these speeds, so-called closed press sections, which comprise a compact combination of press rolls fitted around a smooth-faced centre roll, usually operate satisfactorily. As examples of such press sections should be mentioned the applicant's Sym-Press II™ and Sym-Press O™ press sections. One item that requires development is the centre roll of the compact press sections and its material, which has commonly been rock, which material, however, being a natural material, has certain drawbacks. Dewatering by means of pressing is energy-economically preferable to dewatering by evaporation. This is why attempts should be made to remove a maximum proportion of water out of a paper web by pressing in order that the proportion of water that must be removed by evaporation could be made as low as possible. The increased running speeds of paper machines, however, provide new, so far unsolved problems expressly in the dewatering taking place by pressing, because the press impulse cannot be increased sufficiently by the means known in prior art, above all because, at high speeds, the nip times remain unduly short and, on the other hand, the peak pressure of compression cannot be increased beyond a certain limit without destruction of the structure of the web. When running speeds of paper machines are increased, the problems of running quality of paper machines are also manifested with increased emphasis, because a watery web of low strength cannot withstand an excessively high and sudden impulse of compression pressure or the dynamic forces produced by high speeds, but web breaks and other disturbance in operation are produced with resulting standstills. With a modern printing paper machine, the cost of a break standstill is at present about 40,000 FIM per hour. Further drawbacks of the prior-art press sections include the requirement of suction energy of the suction rolls commonly employed in them as well as the noise problems arising from the suction rolls. Also, the suction rolls with their perforated mantles, interior suction boxes, and other suction systems are components that are expensive and require repeated servicing. Further problems which are manifested with more emphasis at high speeds of paper machines and for which, at least not for all of them, satisfactory solutions have not yet been found, include the quality problems related to the requirements of evenness of the longitudinal and transverse property profiles of the paper web. The evenness of the web that is produced also affects the running quality of the whole paper machine, and it is also an important quality factor of finished paper, which is emphasized in respect of copying and printing papers when the requirements on the speeds of copying and printing machines and on the uniformity of the printing result are increased. The property profiles of the paper that is produced in the machine direction are also affected significantly by oscillations of the press section, the transverse variations of properties by the transverse profiles of the nip pressures in the press nips, and with increasing running speeds of the machine these profile problems tend to be increased remarkably. With respect to the prior art related to the present invention, reference is made to the applicant's FI Patent Applications Nos. 842114, 842115, 850627 and to the published FI Patent Application 78,941 as well as to the FI Patent Application No. 875715 of Beloit Corporation, to the published FI Patent Application 80,094, and to the EP Patent No. 0267 186. An object of the present invention is the further development of the prior art known from the publications mentioned above. In the applicant's EP-patent application 0 487 483 published on May 27, 1992 and claiming priority from FI-patent application 905798 filed on November 23, 1990 (prior art under Art. 54(3) EPC), a method is described which comprises a combination of the following steps: the paper web is transferred from the forming wire onto the wire in the drying section while constantly on support of a fabric that receives water, a transfer fabric, or of any other, corresponding transfer surface as a closed draw, preferably at a speed that is higher than about 25...30 m/s; dewatering of the paper web is carried out by means of at least two subsequent press nips, of which nips at least one press nip is a so-called extended-nip zone, whose length in the machine direction is larger than z > about 100 mm, and said extended-nip zone is formed in connection with a mobile flexible press-band loop; and the distribution of the compression pressure employed within said extended-nip press zone is regulated and/or selected both in the transverse direction of the web and in the machine direction so as to set or to control the different profiles of properties of the web. It is a further essential feature of the method and the device of the above EP-patent application 0 487 483 that the paper web is not passed through the press section on one press fabric, but, to guarantee an adequate dewatering capacity, an arrangement of fabrics is employed in which the web is transferred from the pick-up point on the first upper fabric through the first press zone, preferably an extended-nip zone, through which zone the first lower fabric runs, onto which the web is transferred after said nip zone, and from said first lower fabric the web is transferred onto the second upper fabric, which carries the web into the second nip zone, which consists of a roll nip or preferably of an extended-nip zone, after which the web is transferred onto the second lower fabric, which runs through said nip zone and carries the web on its upper face as a closed draw onto the drying wire or into the next nip zone. In one embodiment in said EP-patent application 0 487483 a first wire press nip is formed between a suction roll inside the wire loop and a hollow faced press roll through which wire nip a relatively open press fabric is passed. The web is detached at a first pick-up point from the forming wire and is passed as a closed draw on a pick-up felt into a second extended press nip, which is a double felt press nip. After the second extended press nip the web is transferred as a closed draw on a first lower press felt to a second pick-up point where the web is detached from the lower press felt and passed as a closed draw on a upper press felt to a third roll press nip, which also is a double felt press nip. After the third roll press nip the web is transferred as a closed draw on a second lower press felt to a third pick-up point where the web is detached from the second lower press felt and passed as a closed draw on a drying wire into a drying section, which follows after the press section. The first wire press nip can also be formed between the suction roll inside the wire loop and a hose roll with an extended nip zone. Both press nips in the press section are thus double felted press nips. An object of the present invention is further development of the prior-art press sections so that they are suitable above all for printing paper qualities whose grammage is in the range of 40...80 g/m 2 . These qualities also include the copying papers, whose consumption is abundant at present. An object of the present invention is to provide a press section in which it is more efficiently possible to utilize the high dewatering capacity of the prior-art extended nips in combination with the fact that, under certain conditions, the extended nips are also capable of providing quite a high dry solids content of the web. In relation to this, an object of the invention is to provide a press section in which a certain kind of a front nip with light loading is employed, so that the extended nip can be made to operate in the preferred range of dry solids content while substantially reducing its water load in view of achieving a sufficiently high dry solids content of the web. An object of the present invention is to provide a press section in which, in the case of modernizations, said front nip can be combined with existing components or with other components that are necessarily needed, so that the construction becomes relatively simple and economical. In relation to this, an object of the invention is to provide a press section in which, in said front nip, it is possible to employ a relatively low linear load, which, for its part, permits simple and inexpensive components. The objectives stated above and those that will come out later are achieved with a press section according to claim 1. In the invention, before the first extended-nip press, there is one front nip with relatively light loading, by whose means, however, a remarkable volume of water can be removed from the web, so that, by means of said front nip, the overall water quantity in the web can be reduced to about one half. In such a case, if the distribution of the nip pressure in the machine direction of the first extended nip that is applied in the invention is adjusted to make it suitable for the purpose, said first extended nip, which is expressly a single-felt nip, can be made to operate particularly favourably and to increase the dry solids content of the web to a sufficiently high level. The primary purpose of the second press nip in the press section is to improve the symmetry of the web in the direction z. The second press nip is most appropriately a single-felt hard roll nip, whose dewatering direction is opposite to that in the preceding first extended nip. When the web has been formed by means of a hybrid or single-wire former, in the first extended nip the dewatering takes place expressly through the upper face of the web, i.e. through the face that is placed facing away from the only forming wire or the lower wire, in view of achieving a symmetry of fines and fillers in the direction z in the web. In the following, the invention will be described in detail with reference to some exemplifying embodiments of the invention illustrated in the figures in the accompanying drawing, the invention being in no way strictly confined to the details of said embodiments. Figure 1 shows one embodiment of the invention in which the front nip is a roll nip that is placed in connection with the forming wire. Figure 2 shows a variation of the embodiment shown in Fig. 1, wherein, in stead of a roll nip, an extended nip placed on the forming wire is used as the front nip. Figure 3 is an axonometric view partly in section of a hose roll used as the upper roll in an extended nip in accordance with the invention. Figure 4 is an axonometric view of a press shoe, which is placed inside the hose roll as shown in Fig.3 and which can be loaded and profiled in a variety of ways. Figure 5 illustrates advantageous distributions of compression pressures of an extended nip applied in accordance with the invention in the machine direction. Figure 6 is a sectional view of a preferred press shoe employed in a "hose roll" as shown in Figs. 7 and 8, by means of which press shoe the distributions of compression pressure in the machine direction, as shown in Fig. 9 placed above Fig. 10, can be accomplished. According to Fig. 1, the paper web W, which has been formed on the forming wire 10, is separated from the forming wire 10 on the run between the rolls 11 and 12 in the former at the pick-up point P. From the pick-up point P, aided by the suction zone 13a of the pick-up roll 13, the web W is transferred onto the pick-up felt 15, which is guided by the guide rolls 14 and conditioned by the devices 15a. A front nip which is a wire nip N o has been formed on the suction zone 11a of the lower suction roll 11 placed inside the loop of the forming wire 10 together with an upper press roll 60 that is provided with a very open hollow face 60'. A relatively open and permeable press fabric 61, which is guided by the guide rolls 62, runs through the wire nip N o . In the wire nip No, a relatively low linear load must be used, which is of an order of 10...40 kN/m, in order that the just weakly developed structure of the relatively wet web W should not be destroyed. In the wire nip N o , the dry solids content is raised, e.g., from 18 % to 22 %. Fig. 2 shows a variation of the wire nip applied in Fig.1. According to Fig. 2 the wire nip is an extended nip Np o , through which a relatively pervious press fabric 61 runs, being guided by the guide rolls 62. The upper roll in the extended nip Np o is a "hose roll" 20, and the lower roll is a press roll 11, whose face 11' is to some extent water-receiving. The length of the extended nip Np o in the machine direction is quite large, as a rule 250...400 mm, and the distribution of the pressure compression in the machine direction is preferably uniform, for example within the range of 1...15 bar. In the other respects, the construction shown in Fig. 1. According to Fig. 1, owing to the adhesion properties of the upper felt 15 and/or owing to the negative pressure in the suction zone 13a, after the pick-up point P, the web W follows the upper felt 15 and is transferred on its lower face into the extended-nip press, and the web W runs through the press zone NP in the extended nip Np of said press. The extended nip Np is formed between an upper "hose roll" 20, which will be described in more detail later, and a lower smooth-faced 40' press roll. The extended nip Np is expressly a nip provided with one press fabric 15 and formed expressly against a smooth-faced lower roll. If the web W has been formed by means of a hybrid former or a Fourdrinier wire part, the dewatering direction in the extended nip Np is through the face of the web W that is placed facing away from the face that is at the side of the forming wire 10, i.e., as a rule, through the upper face. According to the invention, when a front nip N o , Np o with light load is employed before the extended nip Np, quite a considerable volume of water can be drained, as a rule almost or about one half of the amount of water in the web that enters into this nip. In such a case, the water load that enters into the extended nip, which is based on a press shoe, can be reduced considerably, so that the extended nip can be made to operate in a favourable range of dry solids content, and a sufficiently high dry solids content can be accomplished by means of the extended nip. In the following, an example will be given of quantities of water that have been calculated for a fine paper of a grammage of 45 g/m 2 ; if the dry solids content of said paper after the wire part is 20 %, the amount of water in it is 180 g/m 2 . As the dry solids content can be raised by about 10 percentage units, i.e. to about 30 %, by means of the front nip N o , Np o with relatively light load, the amount of water in the web is 105 g/m 2 , so that, by means of the front nip, the overall water quantity in the web W can be lowered almost to one half. The length Z of the extended nip Np in the machine direction is preferably in the range of Z ≈ 150...250 mm, and in any case the length Z > 100 mm. The development of the dry solids content of the web W in the press section is favourably, for example, as follows. When the dry solids content k o on the forming wire at the pick-up point P is k o ≈ 20 %, the dry solids content after the first roll nip, i.e. the front nip N o , Np o is k 1 ≈ 25...33 %. The dry solids content k 2 of the web W after the extended nip Np is k 2 ≈ 48...54 %. In the extended nip Np, the lower roll 40 is a variable-crown smooth-faced 40' roll, e.g. the applicant's Z-roll™, whose coating is a coating that transfers the web W, such as Dynarock™. According to Fig. 1 the web W follows after the extended nip Np the smooth face 40' of the roll 40, from which it is detached as a short free draw Wp, being transferred onto the smooth face 42' of the upper roll 42 of the second roll nip N 2 , on which face 42' the web W is passed into the second nip N 2 . The lower roll of the second roll nip N 2 is a press roll 43 provided with an open hollow face 43', and the lower felt 45, which is guided by the guide rolls 44, runs through the second roll nip N 2 . After the second roll nip N 2 , the web W follows the smooth face 42' of the upper roll 42, from which it is separated as a short free draw Wp, being transferred on the paper guide roll 53 onto the drying wire 50. The second roll nip N 2 in the press section is provided mainly for the purpose that, by its means, the symmetry in the web in the direction z is promoted by still removing a little amount of water through the lower face of the web W, by means of which removal of water fillers and fines are washed towards the lower face of the web W, i.e. in the direction opposite to the removal of water in the extended nip Np. If the dry solids content of the web after the extended nip Np is, for example, k 2 ≈ 48...54 %, preferably k 2 ≈ 52 %, the dry solids content of the web W after the second roll nip N 2 , in the press section, is k 3 ≈ 52...56 %, preferably k 3 ≈ 54 %. In the following, with reference to Figs. 3, 4 and 5, an advantageous hose roll 20 will be described, which has been used in an embodiment of an extended nip Np or wire nip Np o used in the press section in accordance with the invention. According to Fig. 3 the hose roll 20 comprises an elastic mantle 21, which is made, e.g., of fabric-reinforced polyurethane, so that the hose mantle 21 is made of rubberlike stretching material, whose maximum elongation is, e.g., about 1...2 %. The thickness of the hose mantle 21 is, e.g., about 2...5 mm. The outer face of the hose mantle 21 is, as a rule, smooth, but in particular cases it may also be a hollow face that receives water. To the hose mantle 21, annular ends 22a and 22b are fixed permanently, the inner parts of said ends being fixed and sealed against revolving axle journals 27a and 27b, which are mounted on the frame parts of the machine by means of fixed bearing supports. The hose roll 20 includes a stationary inner frame 25, around which the hose mantle 21 with its ends 22a,22b revolves on the bearings 26a and 26b. As is shown in Fig. 4, cylinder block sets 23, two sets side by side, are fitted in the inner frame 25. In the bores placed in the sets of cylinder blocks 23, hydraulic support members 26,27 of the glide shoe 35 operate, which members are, thus, placed in two rows, e.g., with a spacing of about 25 cm in the transverse direction one after the other. The two rows of the hydraulic support members 26,27 support a support plate 29, to which a glide shoe 35, e.g., of aluminium is attached, in whose area an extended-nip zone NP is formed against a backup roll 40;41. The glide shoe 35 is provided with a smooth glide face 38, which operates as a press member against the lubricated smooth inner face of the hose mantle 21. The glide shoe 35 has a series of hydrostatic chambers 39 placed one after the other, which chambers contribute to the formation of a hydrostatic loading pressure and to oil lubrication of the glide face 38. Each of the subsequent cylinder blocks 23 communicates with a connector 36, to which pipes 34 of loading medium pass so that a separately adjustable pressure can be passed into each individual block in the series of cylinder blocks 23. In this way, the pressure profile in an extended-nip zone NP can be regulated and controlled precisely and in a versatile way both in the machine direction and in the transverse direction. The pressure ratio p 2 /p 1 of the two different rows of support members 26,27 is, as a rule, chosen invariably, whereas the pressure passed into each block is freely adjustable within certain limits. In Fig. 3, a regulation system related to the invention is sketched, by whose means the pressure profiles of the extended nip Np in the transverse direction and in the machine direction can be controlled. The regulation system is illustrated by the block 70, from which a series of regulation signals c, is given which regulate the hydraulic pressures fed through the pipes 213. To the regulation system 34, a feedback signal is received from separate wirings 36, which is illustrated by the series of signals c 2 . Further, the system 34 communicates with a measurement arrangement 71, by whose means the different profiles of the paper web W produced, such as moisture or thickness profiles, are measured, and this provides a series of feedback signals c 3 for the regulation system 70, which produces the series of regulation signals c 1 . The hose roll 20 shown in Fig. 3 is oil-tight, and the interior of the hose 21 can be arranged as slightly pressurized. From the glide faces 38 of the glide shoes 35, a slight leakage of oil takes place, which oil is collected from inside the hose mantle 21 and passed through the pipe 37 back to the oil circulation. The hose roll 20 is preferably mounted on fixed bearing supports, in which case the extended nip Np must be opened by means of a movement of the lower backup roll 40;41. This movement is necessary, because the play of, as a rule, about 15 mm for movement of the glide shoes 35 of the hose roll 20 is not sufficient for opening the nip Np sufficiently, e.g., for replacement of the fabrics 15;30;61. Fig. 5 illustrates some distributions of pressure in the extended-nip zone NP in a system of coordinates of pressure/length in the machine direction (z), which distributions of pressure are preferable expressly in a press section in accordance with the invention. Underneath the pressure curves shown in the Fig., an example is given on the shape of the press shoe 35 and of its glide face 38, by whose means the pressure curves A and B shown in the Fig. can be accomplished when the press shoe 35 is loaded by means of adjustable forces F 1 and F 2 against a smooth-faced lower backup roll 40;41. In the Fig., the running direction of the web is parallel to the z-axis, i.e. parallel to the arrow W. According to the pressure curve A in the Fig., in the first press zone z, of the shoe 35, i.e. after the area of the front edge 38a of the shoe, the pressure rises in an almost linear way to the value of about 3500 kPa, after which, in the second press zone z 2 , the pressure remains substantially uniform. The pressure in the second zone z 2 is determined mainly by the adjustable pressure of the pressure fluid fed through the ducts 39a in the shoe 38 into the hydrostatic zone 39. After the second zone z 2 , the pressure rises from said uniform pressure, in the third zone z 3 , very steeply to a maximum pressure, which is of an order of 7500 kPa. After said maximum pressure, which prevails in the middle area of the third and last zone z 3 , the pressure is lowered to zero very steeply right before the curved rear edge 38b of the shoe 38. In the Fig., a second pressure curve B is shown, in which, in the zone z 1 , the pressure rises in a substantially linear way to the invariable pressure in the second zone z 2 , which pressure is about 4000 kPa. After this, in the third zone z 3 , the pressure rises to the maximum pressure, which is substantially lower than in the case of the pressure curve A. In the Fig., an alternative curve of pressure lowering a, is shown, which is carried into effect with the shape 38a 1 of the front edge 38a of the glide face 38 of the press shoe illustrated by the dashed line. The pressure curve A represents a situation in which the ratio of the loading forces F 1 /F 2 is at the maximum, whereas the curve B represents a curve that carries into effect a minimum value of said force ratio F 1 /F 2 . By means of said ratios of loading forces, it is efficiently possible to control the dewatering process by regulating the form of the pressure curve in the extended-nip zone NP as well as to maximize the dry solids content of the web W after the extended nip zone NP. Moreover, in Fig. 6, a preferred dimensioning of the different portions L 1 , L 2 and L 3 of the glide face 38 of the press shoe is illustrated (L 1 = 70 mm, L 2 = 110 mm, L 3 = 70 mm). Fig. 5 is an illustrative example of the way in which, when a hose roll 20 as shown in Fig. 3 is used in accordance with the invention exactly in the specified position in the press section, the distribution of pressure in the extended-nip zone NP in the machine direction can be controlled to optimize the dewatering. In an extended nip Np fitted in accordance with the invention, the distribution of pressure can also be controlled in the transverse direction so as to control various profiles of properties of the web W, such as the dry-solids profiles, in the transverse direction. In this way, highly versatile possibilities are provided for the control of the dewatering and of the dewatering profiles in the machine direction and in the transverse direction. In the following, the patent claims will be given, and the various details of the invention may show variation within the scope of the inventive idea defined in said claims and differ from the details stated above for the sake of example only.

Claims: Press section of a paper machine, in particular for printing paper qualities whose grammage is in the range of 40 ... 80 g/m 2 , which press section comprises a first pick-up suction roll (13) with a suction zone (13a) for picking up a web (W) from a pick-up point (P) on a forming wire (10) of a forming section, a first extended single felt press nip (Np)which is formed between a smooth faced (40') roll (40) and a hose roll (20), a first pick-up felt (15) which is looped around the suction pick-up roll (13) and runs through the first press nip (Np), supported by which pick-up felt (15) the web (W) is transferred from the pick-up point (P) on the wire section to the first press nip (Np) in the press section, a second press nip (N 2 ) which is formed between two rolls (42, 43), the web being transferred as a closed or open draw into the second press nip (N 2 ), after which second press nip (N 2 ) the web is transferred as an open draw to a drying wire (50) of a drying section, the press section further comprising a wire front nip (N 0 , Np 0 ), which is formed between a press roll (11) placed inside the loop of the forming wire (10) and a hollow-faced (60') press roll (60) or a hose roll (20) provided with an extended-nip zone that operates opposite to said press roll (11), through which wire front nip (N 0 , Np 0 ) a relaltively open press fabric (61) is passed and which wire front nip (N 0 , Np 0 ) dewaters the web (W) substantially. Press section as claimed in claim 1, characterized in that, the second press nip (N 2 ) is a single felt press nip (N 2 ) formed between a smooth-faced (42') upper roll (42) and a hollow-faced (43') lower roll (43), around which lower roll (43) a press-felt loop (45) of said nip (N 2 ) has been arranged so that the dewatering in the second roll nip (N 2 ) takes place in the opposite direction as compared with the preceding first extended press nip (Np). Press section as claimed in claims 1 or 2, characterized in that said first extended press nip (Np) in the pess section is formed against a hose roll (20), in which hose roll (20), inside its flexible mantle (21), a hydraulically loaded glide shoe (35) is fitted, which has a smooth glide face (38) against the smooth inner face of the hose mantle (21), and that the loading of said glide shoe (35) is arranged so that the distribution of the compression pressure in the extended-nip zone (NP) both in the machine direction and in the transverse direction is arranged adjustable so as to optimize the dewatering taking place in the extended-nip zone (NP) and so as to control the profiles of properties of the web (W) in the transverse direction. Press section as claimed in any of the claims 1 to 3, characterized in that, when the web (W) enters the first extended press nip (Np) in the press section, its dry solids content k 1 is in the range of k 1 = 25 % ... 35 %, preferably k 1 ≈ 30 %, and that the dry solids content of the web (W) is raised in said first extended press nip (Np) by about 15...25 percentage units, preferably by about 20 percentage units. Press section as claimed in any of the claims 1 to 4, characterized in that, in said first extended press nip (Np) in the pess section, the web (W) is pressed so that the compression pressure is raised in a first zone z 1 in the extended-nip zone (NP) in a substantially linear way to a pressure that is of an order of 3000...4000 kPa, at which the compression pressure is kept substantially invariable in a second zone z 2 of the press zone, which second zone is followed by a zone z 3 of pressure increase, in whose middle area the peak pressure of compression is used, which is of an order of 5000...8000 kPa, after which peak pressure the compression pressure is lowered to zero steeply.

Inventors: ILMARINEN ANTTI, ILMARINEN, ANTTI
Applicants: VALMET CORP, VALMET CORPORATION
Application year: 1992
Main classification: D21F3
IPC codes: D21F3