WO1981002704A1 - Procedure and paper machine for manufacturing creped paper web - Google Patents

Procedure and paper machine for manufacturing creped paper web Download PDF

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Publication number
WO1981002704A1
WO1981002704A1 PCT/FI1981/000019 FI8100019W WO8102704A1 WO 1981002704 A1 WO1981002704 A1 WO 1981002704A1 FI 8100019 W FI8100019 W FI 8100019W WO 8102704 A1 WO8102704 A1 WO 8102704A1
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WO
WIPO (PCT)
Prior art keywords
creping
web
cylinder
roll
paper machine
Prior art date
Application number
PCT/FI1981/000019
Other languages
French (fr)
Inventor
F Weisshuhn
Original Assignee
Valmet Oy
F Weisshuhn
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Valmet Oy, F Weisshuhn filed Critical Valmet Oy
Priority to AU69209/81A priority Critical patent/AU6920981A/en
Publication of WO1981002704A1 publication Critical patent/WO1981002704A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B31MAKING ARTICLES OF PAPER, CARDBOARD OR MATERIAL WORKED IN A MANNER ANALOGOUS TO PAPER; WORKING PAPER, CARDBOARD OR MATERIAL WORKED IN A MANNER ANALOGOUS TO PAPER
    • B31FMECHANICAL WORKING OR DEFORMATION OF PAPER, CARDBOARD OR MATERIAL WORKED IN A MANNER ANALOGOUS TO PAPER
    • B31F1/00Mechanical deformation without removing material, e.g. in combination with laminating
    • B31F1/12Crêping
    • B31F1/14Crêping by doctor blades arranged crosswise to the web
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F11/00Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
    • D21F11/14Making cellulose wadding, filter or blotting paper

Definitions

  • the present invention concerns a procedure for manufacturing a creped paper web, wherein the web is formed in the forming section of a paper machine and the web is dewatered in the press section, whereupon the web is conducted to the drying section, where the web is dewatered by evaporating.
  • the invention further concerns a paper machine comprising at least one drying cylinder, such as a Yankee cylinder or a flow-through cylinder, and a reeling means.
  • the present invention concerns equipment associated with the manufacturing of creped paper or tissue in general and, in particular, with web creping which does not take place on the Yankee cylinder and its after-drying.
  • the wet paper web which is to be dried and treated is conducted onto the Yankee cylinder, which brings about the drying event, and where it is pressed thereagainst.
  • the drying capacity of the Yankee cylinder has constituted a limitation for the production capacity of the paper machine.
  • the softness and adsorption characteristics of the final product are significantly impaired in this case.
  • the press section of the tissue paper machine may consist either of a conventional wet press with a press nip defined between two press rolls before the Yankee cylinder and/or of one or two press rolls which define press nips against the Yankee cylinder.
  • the drying section again, is constituted either by the said Yankee cylinder and/or of flow-through drier alone or with a socalled after-drier. In both instances the drying of the web takes place by evaporation effect as the moist web is in contact with the Yankee cylinder and the cylinders of the after-drier, if any, all of which are heated by internal pressurized steam.
  • the web which has become adherent the smooth surface of the Yankee cylinder is detached therefrom with the aid of a special doctor blade, which causes in the web a creping created by an upsetting effect.
  • the after-drier most commonly consists of a plurality of conventional steam-heated drying cylinders. Particularly, in the case of thin paper grades or tissue the after-drying may be totally omitted.
  • tissue paper machines of prior art thin paper grades are usually dry-creped as a rule with web moisture content about 5 to 10%, whereas for thicker grades (basis weight over 25 g per m 2 ) most often a wet creping procedure is used, in which the moisture content of the web is about 30 to 40%. In the latter case a separate after-drier is needed to remove the residual moisture prior to reeling.
  • Creping is carried out by scraping the web off from the surface of the Yankee cylinder by means of a doctor blade.
  • the creping takes place in that the web is made to impinge against the side of the doctor blade, thereby causing in the web a deformation due to upsetting, and formation of waves and wave packages transversal to the direction in which the web runs, and inter-fibre tensions which at least partially remain permanent during the after-drying of the web.
  • the creping doctor blade is a component subject to wear and therefore it requires to be replaced at comparatively short intervals for a constant quality of creping. Such replacements are made about five to ten times daily. This causes breaks in the production of the paper machine.
  • Finnish patent application No. 763657 to make the blade of the creping doctor of one or several parts so that the blade has a length considerably in excess of the breadth of the Yankee cylinder and to make provisions for displacement of the blade in its longitudinal direction in the guide constituted by the doctor beam.
  • creping may be done on a separate creping cylinder after the drying. But this is a method in which the desired properties of the creped product are achieved by admixing to the stock elastomer materials before the drying and creping processes, and in which the web-transporting fabric operates at the same time as pick-up fabric by the aid of which the web is detached from the forming wire. It is very difficult in practice to find any such fabric which would serve both as pick-up fabric, as flow-through fabric and as transfer fabric so that all these tasks would be managed, if not more than satisfactorily even.
  • the specific object of the present invention is to provide a tissue paper machine in which the above-mentioned drawbacks are avoided. It is an additional object of the invention: to provide a paper machine for creped grades wherein the web can be transported all the way up to the reeling means to highest possible extent in no-draw con duction, without unsupported web runs which are apt to cause breaks and shut-downs. Above all, this aims towards making it possible to increase the speed of tissue paper machines and their production capacity as far as other preconditions permit.
  • the procedure of the invention is mainly characterized in that the web is detached in no-draw conduction from the surface of the last drying cylinder of the drying section by means of a transfer suction roll, by which the web is further transported to a smooth-surfaced creping roll or cylinder, and that the web is creped on the smooth surface of said creping roll or cylinder by means of a creping doctor, whereupon the web is transported to the subsequent after-treatment steps.
  • the paper machine for producing creped paper according to the invention is mainly characterized in that the creping unit in this paper machine comprises, in combination:-
  • Fig. 1 presents in schematic elevational view, a paper machine applying the procedure of the invention.
  • Fig. 2 presents in schematic elevational view in greater detail the creping means of the invention, disposed in connection with a Yankee cylinder.
  • Fig. 3 presents in partial projection an embodiment of the invention in which a flow-through drying cylinder is used.
  • the paper machine comprises a forming and wire section, of which in Fig. 1 only the trailing end 70 of the wire section is visible.
  • the tissue web is transferred by means of a pick-up roll 72 known in itself in the art, onto a felt 73, the web W being carried, made adherent to its underside, to the same applicant's so-called Sym-Press press section 80.
  • the no-draw press section 80 comprises a first double-felted nip and thereafter two press nips associated with the smooth-surfaced central roll of the press. After the last press nip, the web W is conducted to the first drying cylinder 91 of the multiple cylinder drier 90.
  • the multiple cylinder drier 90 is in itself known in the art, and it consists of steam-heated, smooth-surfaced drying cylinders disposed in two rows one upon the other, in connection with these cylinders an upper felt 92 and a lower felt 93 being provided. Uno-Run system is also possible.
  • the web W is detached and conducted in accordance with the procedure of the invention, using a transfer suction roll 11, onto the creping roll 10 or cylinder.
  • This has a smooth surface 10a, from which the web W is detached, and creped, by the first creping doctor 17a.
  • the doctors 17a and 17b There are two creping doctors one after the other, namely, the doctors 17a and 17b, the latter being placed in operation in case the first doctor 17a has to be serviced, e.g. in connection with blade replacement.
  • the web denoted by W out which is detached from the surface of the creping cylinder 10, and which has been creped, is conveyed to the subsequent treatment steps which are shown in Figs 2 and 3.
  • the invention shall be described in greater detail with reference being made to these figures .
  • the creping means has been disposed in connection with the Yankee cylinder 100, which is steam-heated in a manner known in itself in the art and has a smooth cylinder surface 110.
  • the surface 110 of the Yankee cylinder 100 is an uncoated, ground and polished cast surface or a welded steel surface.
  • the web W is carried onto the Yankee cylinder in conventional manner from the paper machine's press section, which has not been depicted.
  • the web W is detached from the surface 110 of the cylinder 100 without using any creping doctor.
  • the detachment and further conveying of the web W in accordance with the invention takes place with the aid of a suction transfer roll 11, which defines a first transfer nip N 1 together with the cylinder 100.
  • the transfer suction roll 11 has been provided with an extensive suction zone 11 , which ensures that the web W is maintained on the surface of the roll 11 as it moves from the transfer nip N 1 to the second transfer nip N 2 , which is defined between the transfer suction roll 11 and the creping roll or cylinder 10 of the invention.
  • the transfer roll 11 may be steeljacketed and/or provided with a coating 11a of rubber or equivalent elastic material known in itself in the art, which has for instance the effect that the nip N 1 will be comparatively broad and it will at all events be such that it does not substantially detract from the softness and fluffiness of the tissue web.
  • the transfer suction roll 11 is lapped by a fabric 13, for instance a suitable metal or plastic-fabric, which serves the purpose to prevent the marking of the web W by the drilling or grooving pattern of the suction roll 11.
  • the fabric 13 serves as member carrying the web to the nip N 2 against the smooth surface 10a of the creping roll or cylinder 10.
  • the creping roll 10 may be provided with heating means.
  • the creping cylinder 10 may have a structural design equivalent either to a paper machine cylinder or e.g. a press roll.
  • the creping roll 10 has a diameter considerably smaller than that of conventional Yankee cylinders 100, but its diameter is appropriately larger than that of the transfer suction roll 11.
  • the smoot surface 10a of the creping cylinder 10 has been made of a material as hard as possible, for instance of chrome steel or equivalent.
  • non-metallic coatings may also be used.
  • the use of extra hard special materials on the surface 10a of the roll 10 is feasible and economically advantageous because the roll 10 has a comparatively small diameter and therefore the area coated with a special coating will not be very large.
  • the creping roll 10 is provided with a drive of its own, indicated by the reference numeral 12. As shown schematically in Fig. 2, the creping roll 10 and the transfer suction roll 11 have been suspended from lever arms 50 and 51, which have been attached to the machine frame at the pivot point 52.
  • the arms 50 and 51, or an equivalent unitary frame element, have been provided with force means (not depicted), by means of which an appropriate, comparatively low nip pressure is obtained in the nips N 1 and N 2 .
  • the rolls 10 and 11 are preferentially rotatably carried in one unitary frame unit. In that case, however, one has to use in the suspension of rolls 10,11 such spring elements which enable a suitable nip pressure to be obtained in both transfer nips N 1 and N 2 when said frame unit is urged against the cylinder 100 with one single set of force means.
  • the web W made adherent to the smooth surface 10a of the creping roll 10 is detached with the aid of a creping doctor 17 known in itself in the art.
  • the web, wet-creped in this manner, is indicated by W c in the figure.
  • the Yankee cylinder 100 has no creping doctor at all, merely a cleaning scraper 130 and which at the same time serves as doctor, detaching in the event of running trouble the paper waste from the surface 110 of the Yankee cylinder 100 and transporting it into the waste tray below (not depicted).
  • the creping means an afterdrier substantially consisting of the fabrics 20 and 21.
  • the throat G constituted by the fabrics 20 and 21 - guided by rolls 22 and 23 - and into which the web proceeds by effect of dynamic forces and mainly of gravity action.
  • the fabrics 20 and 21 forming it have a joint run, within which the web W is interposed between the fabrics 20 and 21.
  • the guide rolls of fabrics 20 and 21 carry the reference numerals 22,23, 24.
  • an air drying means for instance a blower 30, which is a component known in itself in the art and which operates with differential pressure effect in likeness of a flowthrough drier.
  • This may also be an AIRFOIL system, e.g. in accordance with the same applicant's patent applications No.
  • the web W attains the desired ultimate moisture content and it goes by effect of the suction zone 2 . of the roll 25 to the reeling means 41.
  • the reel 41 is so located that it is in constant contact with the roll 25, or immediately adjacent thereto. In this way a fully supported conduction of the web W is achieved after the creping doctoring, without any open draws.
  • a flow-through cylinder 100' As shown in Fig. 3, there is used instead of the smooth-surfaced cylinder 100, a flow-through cylinder 100'.
  • This cylinder has been provided, in a manner known in itself in the art, with a shell 120 having holes 121.
  • the flow of hot gases through the web W' and the foraminous cylinder shell 120 is accomplished with the aid of differential pressure between the hood (not depicted) enclosing the cylinder 100' and the interior cylinder space.
  • the passage of drying gases through the web W' and through the surface 120 has been illustrated in Fig. 2 by arrows A.
  • the flow-through cylinder 100' is not fitted with any cleaning doctor; instead an air blowing device (pipe) 140 has been mounted in a proper position, and this device detaches the waste from the surface 120 of the cylinder 100' and directs it into the waste tray (not depicted).
  • the air blow tube 140 may also serve as a member by the aid of which one makes sure when the leading strip of the web 100' is being threaded, that the end of the web W' follows along with the surface of the transfer suction roll 11.
  • the design shown in Fig. 3 may be carried out in substantially equal manner as has been done in Fig. 2, but a modification is likewise possible in which no belt, fabric or mat lapping the suction transfer roll 11 is used.
  • the purpose of the press nip N 3 thereby defined is to urge the web W' against the smooth surface 10a of the roll 10 so that an appropriate, and uniform, contact and adhesion - with a vie to the creping event - is achieved between the surface 10a and the web W.
  • the adhesion between the web W and the smooth surface 10a of the creping cylinder 10 may also be improved by using special chemicals known in themselves in the art, which are brought into contiguity with the web at a suitable stage and in suitable form, most usually in the form of liquid sprays. Such chemicals may be added to the pulp stock suspension already on the wire section 100'. In such case the "curing time" characteristic of such chemicals is utilized, which makes that the web will not adhere to the surface of cylinders 100,100', but the chemicals begin to act in controlled manner only at the time when the web arrives on the surface 10a of the creping cylinder 10.
  • transfer suction roll 11 with internal suction zone 11
  • suction rolls for instance those provided with a perforated and/or grooved shell and having an external suction box, which will be placed over the sector opposite to the suction sector 11 .
  • the Yankee cylinder 100 and the flow-through cylinder 100' naturally require hoods, and the flow-through cylinder 100' also requires sealing means by which the surface of the cylinder external with reference to the hood is closed off.
  • hoods and equivalent members known in themselves in the art have not been depicted in figures.

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Abstract

Procedure for manufacturing a tissue web (W), which is dewatered in a press section (80), whereafter the web (W) is conducted to a drying section (94; 100; 100'), where the web (W) is dewatered by evaporation. The web (W) is conveyed in closed conduction from the surface of the last drying cylinder (94; 100; 100') in the drying section onto the suction zone (11 (Alpha)) of a transfer suction roll (11). The web (W) is further transported in closed conduction to a smooth-surfaced creping roll (10) or creping cylinder. Then the web (W) is detached from the smooth surface (10a) of a said creping roll (10) or creping cylinder by means of a creping doctor (17a, 17b) and the web (W) is transferred to the subsequent treatment steps. The tissue paper machine comprises a Yankee cylinder or a flow-through cylinder and a reeling means (41). The paper machine further comprises a transfer suction roll (11) with a suction zone (11 (Alpha)) defining a transfer nip (N1) together with the drying cylinder (100, 100'). A smooth-surfaced creping roll (10) or creping cylinder defines a transfer nip (N2) together with said transfer suction roll (11). A creping doctor (17), which detaches the tissue web (W) from the surface of said creping roll (10) or creping cylinder.

Description

PROCEDURE ANDPAPERMACHINE FORMANUFACTURING CREPED PAPERWEB
The present invention concerns a procedure for manufacturing a creped paper web, wherein the web is formed in the forming section of a paper machine and the web is dewatered in the press section, whereupon the web is conducted to the drying section, where the web is dewatered by evaporating.
The invention further concerns a paper machine comprising at least one drying cylinder, such as a Yankee cylinder or a flow-through cylinder, and a reeling means.
The manufacturing of a creped paper web or tissue takes place traditionally on a so-called Yankee machine, and it comprises the following steps:-
- dewatering of the fiber suspension and web forming on the wire section of the paper machine, which may be of the single-wire or twin-wire type;
- dewatering of the web by pressing, which may be accomplished in a nip between two press rolls before the Yankee cylinder or in a nip defined by a press roll against the Yankee cylinder;
- web drying on the Yankee cylinder, in addition to or instead of which sometimes a so-called flow-through drier may be used;
- web creping by the aid of a doctor operating against the surface of the Yankee cylinder; - after-drying of the creped web in case the creping has been done with the web still moist or wet; and
- reeling of the web.
The present invention concerns equipment associated with the manufacturing of creped paper or tissue in general and, in particular, with web creping which does not take place on the Yankee cylinder and its after-drying. In the most commonly applied procedures serving the manufacturing of creped paper web, the wet paper web which is to be dried and treated is conducted onto the Yankee cylinder, which brings about the drying event, and where it is pressed thereagainst. It is well known that in attempts to increase the machine speeds the drying capacity of the Yankee cylinder has constituted a limitation for the production capacity of the paper machine. In order that the drying capacity of the Yankee cylinder might be fully utilized in a paper machine proceducing creped grades, it is usual to remove water as much as possible from the wet paper web before commencement of the evaporation drying proper, by heavy pressing. This is accomplished with the aid of one or two Yankee cylinder presses. However, the softness and adsorption characteristics of the final product are significantly impaired in this case.
As is known in the art the press section of the tissue paper machine may consist either of a conventional wet press with a press nip defined between two press rolls before the Yankee cylinder and/or of one or two press rolls which define press nips against the Yankee cylinder. The drying section, again, is constituted either by the said Yankee cylinder and/or of flow-through drier alone or with a socalled after-drier. In both instances the drying of the web takes place by evaporation effect as the moist web is in contact with the Yankee cylinder and the cylinders of the after-drier, if any, all of which are heated by internal pressurized steam. The web which has become adherent the smooth surface of the Yankee cylinder is detached therefrom with the aid of a special doctor blade, which causes in the web a creping created by an upsetting effect.
The after-drier most commonly consists of a plurality of conventional steam-heated drying cylinders. Particularly, in the case of thin paper grades or tissue the after-drying may be totally omitted.
In tissue paper machines of prior art, thin paper grades are usually dry-creped as a rule with web moisture content about 5 to 10%, whereas for thicker grades (basis weight over 25 g per m2) most often a wet creping procedure is used, in which the moisture content of the web is about 30 to 40%. In the latter case a separate after-drier is needed to remove the residual moisture prior to reeling.
Creping is carried out by scraping the web off from the surface of the Yankee cylinder by means of a doctor blade. The creping takes place in that the web is made to impinge against the side of the doctor blade, thereby causing in the web a deformation due to upsetting, and formation of waves and wave packages transversal to the direction in which the web runs, and inter-fibre tensions which at least partially remain permanent during the after-drying of the web.
The creping doctor blade is a component subject to wear and therefore it requires to be replaced at comparatively short intervals for a constant quality of creping. Such replacements are made about five to ten times daily. This causes breaks in the production of the paper machine. In view of this it is suggested in the Applicant's Finnish patent application No. 763657, to make the blade of the creping doctor of one or several parts so that the blade has a length considerably in excess of the breadth of the Yankee cylinder and to make provisions for displacement of the blade in its longitudinal direction in the guide constituted by the doctor beam.
It is also known that creping may be done on a separate creping cylinder after the drying. But this is a method in which the desired properties of the creped product are achieved by admixing to the stock elastomer materials before the drying and creping processes, and in which the web-transporting fabric operates at the same time as pick-up fabric by the aid of which the web is detached from the forming wire. It is very difficult in practice to find any such fabric which would serve both as pick-up fabric, as flow-through fabric and as transfer fabric so that all these tasks would be managed, if not more than satisfactorily even.
Regarding the state of art relevant to the present invention, reference is further made to the same applicant's Finnish patent application No. 790924, disclosing a tissue paper machine with the characteristic feature that a particular fabric is conducted against the tissue web lodged on the surface of a drying cylinder, this fabric serving as member conveying the web onward from said drying cylinder and by its aid being achieved, due to the differential velocity between the drying cylinder and said fabric, an upsetting of the web and/or a surface pattern embossed by said fabric.
It is a known fact that the surface of the Yankee cylinder is subject to wear. Above all, this wear and tear is due to the effect of the creping doctor blade. However, the surface quality and smoothness of the Yankee cylinder's surface exerts a decisive influence both on the drying event and, above all, on the creping event. Therefore, in order to keep the Yankee cylinder's surface smooth enough its repeated grinding is necessary. As has already been noted, the creping doctor blades, too, are subject to powerful wear, and they require indeed to be changed at frequent intervals. But such operations cause prolonged shut-downs with attendant, significant production losses.
With a view to increasing the service life of the Yankee cylinder's surface and the length of the grinding interval, it is known in the art to apply surface coatings made by spraying stainless steel, or high-grade steel in general, on the surface of the Yankee cylinder. It has indeed been possible by these expedients of prior art, considerably to lengthen the grinding intervals of the Yankee cylinder surface and also to prolong the service life of the doctor blades. But the use of Yankee cylinder coatings with e.g. about 2.5 to 3 mm thickness made by metal spraying or in another equivalent way is accompanied by the detriment that the Yankee drier's drying capacity is substantially reduced beacuse the thermal conductivity of stainless steel, for instance, is substantially less than that of cast iron for instance. Calculations indicate that said coatings reduce the drying capacity of the Yankee drier up to about 20%.
The specific object of the present invention is to provide a tissue paper machine in which the above-mentioned drawbacks are avoided. It is an additional object of the invention: to provide a paper machine for creped grades wherein the web can be transported all the way up to the reeling means to highest possible extent in no-draw con duction, without unsupported web runs which are apt to cause breaks and shut-downs. Above all, this aims towards making it possible to increase the speed of tissue paper machines and their production capacity as far as other preconditions permit.
In order to achieve the aims mentioned, and others which will become apparent later on, the procedure of the invention is mainly characterized in that the web is detached in no-draw conduction from the surface of the last drying cylinder of the drying section by means of a transfer suction roll, by which the web is further transported to a smooth-surfaced creping roll or cylinder, and that the web is creped on the smooth surface of said creping roll or cylinder by means of a creping doctor, whereupon the web is transported to the subsequent after-treatment steps.
The paper machine for producing creped paper according to the invention, again, is mainly characterized in that the creping unit in this paper machine comprises, in combination:-
(a) a transfer roll with suction zone which defines a first transfer nip with the drying cylinder and by the aid of which the web is detached without creping doctor from the surface of the drying cylinder;
(b) a smooth-surfaced creping roll or cylinder, which defines a second transfer nip together with said transfer suction roll; and
(c) a creping doctor, by the aid of which the paper web is creped and detached from the surface of said creping roll or cylinder.
In the following, the invention is described in detail, with reference being made to three embodiment examples of the invention, presented in the figures of the attached drawing.
Fig. 1 presents in schematic elevational view, a paper machine applying the procedure of the invention. Fig. 2 presents in schematic elevational view in greater detail the creping means of the invention, disposed in connection with a Yankee cylinder.
Fig. 3 presents in partial projection an embodiment of the invention in which a flow-through drying cylinder is used.
As shown in Fig. 1, the paper machine comprises a forming and wire section, of which in Fig. 1 only the trailing end 70 of the wire section is visible. From the forming wire 71, the tissue web is transferred by means of a pick-up roll 72 known in itself in the art, onto a felt 73, the web W being carried, made adherent to its underside, to the same applicant's so-called Sym-Press press section 80. The no-draw press section 80 comprises a first double-felted nip and thereafter two press nips associated with the smooth-surfaced central roll of the press. After the last press nip, the web W is conducted to the first drying cylinder 91 of the multiple cylinder drier 90. The multiple cylinder drier 90 is in itself known in the art, and it consists of steam-heated, smooth-surfaced drying cylinders disposed in two rows one upon the other, in connection with these cylinders an upper felt 92 and a lower felt 93 being provided. Uno-Run system is also possible.
From the last drying cylinder 94, the web W is detached and conducted in accordance with the procedure of the invention, using a transfer suction roll 11, onto the creping roll 10 or cylinder. This has a smooth surface 10a, from which the web W is detached, and creped, by the first creping doctor 17a. There are two creping doctors one after the other, namely, the doctors 17a and 17b, the latter being placed in operation in case the first doctor 17a has to be serviced, e.g. in connection with blade replacement. The web denoted by W out which is detached from the surface of the creping cylinder 10, and which has been creped, is conveyed to the subsequent treatment steps which are shown in Figs 2 and 3. The invention shall be described in greater detail with reference being made to these figures .
As shown in Fig. 2, the creping means has been disposed in connection with the Yankee cylinder 100, which is steam-heated in a manner known in itself in the art and has a smooth cylinder surface 110. In order to ensure good thermal conductivity, the surface 110 of the Yankee cylinder 100 is an uncoated, ground and polished cast surface or a welded steel surface. The web W is carried onto the Yankee cylinder in conventional manner from the paper machine's press section, which has not been depicted.
The web W is detached from the surface 110 of the cylinder 100 without using any creping doctor. The detachment and further conveying of the web W in accordance with the invention takes place with the aid of a suction transfer roll 11, which defines a first transfer nip N1 together with the cylinder 100. The transfer suction roll 11 has been provided with an extensive suction zone 11
Figure imgf000009_0001
, which ensures that the web W is maintained on the surface of the roll 11 as it moves from the transfer nip N1 to the second transfer nip N2, which is defined between the transfer suction roll 11 and the creping roll or cylinder 10 of the invention. The transfer roll 11 may be steeljacketed and/or provided with a coating 11a of rubber or equivalent elastic material known in itself in the art, which has for instance the effect that the nip N1 will be comparatively broad and it will at all events be such that it does not substantially detract from the softness and fluffiness of the tissue web. The transfer suction roll 11 is lapped by a fabric 13, for instance a suitable metal or plastic-fabric, which serves the purpose to prevent the marking of the web W by the drilling or grooving pattern of the suction roll 11. At the same time, the fabric 13 serves as member carrying the web to the nip N2 against the smooth surface 10a of the creping roll or cylinder 10. It is well known, of course, that it is of decisive importance with a view to the creping process that the web is made adherent to the creping substrate reliably and with an appropriate degree of adherence - in the present instance to the smooth surface 10a of the creping roll 10 or cylinder with comparatively small diameter. The creping roll 10 may be provided with heating means. The creping cylinder 10 may have a structural design equivalent either to a paper machine cylinder or e.g. a press roll. The creping roll 10 has a diameter considerably smaller than that of conventional Yankee cylinders 100, but its diameter is appropriately larger than that of the transfer suction roll 11. The smoot surface 10a of the creping cylinder 10 has been made of a material as hard as possible, for instance of chrome steel or equivalent. In some instances non-metallic coatings may also be used. The use of extra hard special materials on the surface 10a of the roll 10 is feasible and economically advantageous because the roll 10 has a comparatively small diameter and therefore the area coated with a special coating will not be very large. The creping roll 10 is provided with a drive of its own, indicated by the reference numeral 12. As shown schematically in Fig. 2, the creping roll 10 and the transfer suction roll 11 have been suspended from lever arms 50 and 51, which have been attached to the machine frame at the pivot point 52. The arms 50 and 51, or an equivalent unitary frame element, have been provided with force means (not depicted), by means of which an appropriate, comparatively low nip pressure is obtained in the nips N1 and N2.
The rolls 10 and 11 are preferentially rotatably carried in one unitary frame unit. In that case, however, one has to use in the suspension of rolls 10,11 such spring elements which enable a suitable nip pressure to be obtained in both transfer nips N1 and N2 when said frame unit is urged against the cylinder 100 with one single set of force means.
The web W made adherent to the smooth surface 10a of the creping roll 10 is detached with the aid of a creping doctor 17 known in itself in the art. The web, wet-creped in this manner, is indicated by Wc in the figure. There has to be two creping doctors.
As shown in Fig. 2, the Yankee cylinder 100 has no creping doctor at all, merely a cleaning scraper 130 and which at the same time serves as doctor, detaching in the event of running trouble the paper waste from the surface 110 of the Yankee cylinder 100 and transporting it into the waste tray below (not depicted). As shown in Fig. 2, there follows after the creping means an afterdrier substantially consisting of the fabrics 20 and 21.
Immediately below the point of detachment effected by the doctor 17, there is the throat G constituted by the fabrics 20 and 21 - guided by rolls 22 and 23 - and into which the web proceeds by effect of dynamic forces and mainly of gravity action. After the convergent throat G, the fabrics 20 and 21 forming it have a joint run, within which the web W is interposed between the fabrics 20 and 21. The guide rolls of fabrics 20 and 21 carry the reference numerals 22,23, 24. On the joint run of fabrics 20 and 21, between the rolls 22,23 and 25,26 there has been placed an air drying means, for instance a blower 30, which is a component known in itself in the art and which operates with differential pressure effect in likeness of a flowthrough drier. This may also be an AIRFOIL system, e.g. in accordance with the same applicant's patent applications No. When passing through this drier 30, the web W attains the desired ultimate moisture content and it goes by effect of the suction zone 2
Figure imgf000011_0001
. of the roll 25 to the reeling means 41. The reel 41 is so located that it is in constant contact with the roll 25, or immediately adjacent thereto. In this way a fully supported conduction of the web W is achieved after the creping doctoring, without any open draws.
As shown in Fig. 3, there is used instead of the smooth-surfaced cylinder 100, a flow-through cylinder 100'. This cylinder has been provided, in a manner known in itself in the art, with a shell 120 having holes 121. The flow of hot gases through the web W' and the foraminous cylinder shell 120 is accomplished with the aid of differential pressure between the hood (not depicted) enclosing the cylinder 100' and the interior cylinder space. The passage of drying gases through the web W' and through the surface 120 has been illustrated in Fig. 2 by arrows A. The flow-through cylinder 100' is not fitted with any cleaning doctor; instead an air blowing device (pipe) 140 has been mounted in a proper position, and this device detaches the waste from the surface 120 of the cylinder 100' and directs it into the waste tray (not depicted). The air blow tube 140 may also serve as a member by the aid of which one makes sure when the leading strip of the web 100' is being threaded, that the end of the web W' follows along with the surface of the transfer suction roll 11. The design shown in Fig. 3 may be carried out in substantially equal manner as has been done in Fig. 2, but a modification is likewise possible in which no belt, fabric or mat lapping the suction transfer roll 11 is used.
As has been mentioned before, it is of decisive significance in view of the producing a tissue web how uniform is the attachment of the web to the smooth surface of the creping cylinder. The degree of attachment must be appropriate as well - it must not be too firm nor too loose either. In order to promote and optimize this attachment, special steps may be undertaken when the present invention is being applied, if necessary. To this purpose there is, as schematically shown in Fig. 1, in connection with the surface of the creping cylinder 10 an applicator roll 60, which takes up adhesive material from a tank 61 and transfers it onto the smooth surface 10a of the creping roll 10. With equivalent purpose, as shown in Fig. 3, the creping roll 10 has been provided with a press roll 70 placed after the nip N2. The purpose of the press nip N3 thereby defined is to urge the web W' against the smooth surface 10a of the roll 10 so that an appropriate, and uniform, contact and adhesion - with a vie to the creping event - is achieved between the surface 10a and the web W.
The adhesion between the web W and the smooth surface 10a of the creping cylinder 10 may also be improved by using special chemicals known in themselves in the art, which are brought into contiguity with the web at a suitable stage and in suitable form, most usually in the form of liquid sprays. Such chemicals may be added to the pulp stock suspension already on the wire section 100'. In such case the "curing time" characteristic of such chemicals is utilized, which makes that the web will not adhere to the surface of cylinders 100,100', but the chemicals begin to act in controlled manner only at the time when the web arrives on the surface 10a of the creping cylinder 10. Instead of the transfer suction roll 11 with internal suction zone 11 , one may equally use other kinds of suction rolls, for instance those provided with a perforated and/or grooved shell and having an external suction box, which will be placed over the sector opposite to the suction sector 11
Figure imgf000013_0001
.
The Yankee cylinder 100 and the flow-through cylinder 100' naturally require hoods, and the flow-through cylinder 100' also requires sealing means by which the surface of the cylinder external with reference to the hood is closed off. These hoods and equivalent members known in themselves in the art have not been depicted in figures.

Claims

Claims
1. Procedure for manufacturing a tissue web (W) , wherein the web (W) is formed in the forming section of a tissue paper machine and the web (W) is dewatered in a press section (80), whereafter the web (W) is conducted to a drying section (94;100;100'), where the web (W) is dewatered by evaporation, characterized in that the web (W) is conveyed in closed conduction from the surface of the last drying cylinder (94; 100; 100') in the drying section onto the suction zone (11
Figure imgf000014_0001
) of a transfer suction roll (11), supported by which the web (W) is further transported in closed conduction to a smooth-surface creping roll (10) or creping cylinder, and that the web (W) is detached from the smooth surface (10a) of said creping roll (10) or creping cylinder by means of a creping doctor (17a, 17b), whereupon the web (W) is transferred to the subsequent treatment steps.
2. A tissue paper machine applying to the procedure of claim 1, comprising a φrying cylinder such as a Yankee cylinder or a flow through cylinder and a reeling means (41), characterized in that the means comprises in combination:-
(a) a transfer suction roll (11) with suction zone (ll
Figure imgf000014_0002
), which defines a transfer nip (N1) together with the drying cylinder (100,100') and by the aid of which the web (W;W) is without creping doctor detached from the surface of the drying cylinder (100;100');
(b) a smooth-surfaced creping roll (10) or creping cylinder, defining a transfer nip (N2) together with said transfer suction roll (11); and
(c) a creping doctor (17), by means of which the tissue web (W) is detached from the surface of said creping roll (10) or creping cylinder.
3. Tissue paper machine according to claim 2, characterized in that said creping roll (10) or creping cylinder has been provided with a drive (12) of its own.
4. Tissue paper machine according to claim 2 or 3, characterized in that the smooth-surfaced coating (10a) of said creping roll (10) or creping cylinder has been made of a hard material, for instance of chrome steel.
5. Tissue paper machine according to claims 2-4, characterized in that below said creping roll (10) or creping cylinder in register with the creping doctor (17') has been provided a transfer throat
(G) constituted by two fabrics (20,21) and their guide rolls (22,23) and into which the web (W) detached from the surface of the creping roll (10) or creping cylinder, and creped, by the creping doctor (17) is substantially immediately transferred.
6. Tissue paper machine according to claims 2-5, characterized in that the creped tissue web (W) is transported in closed conduction between said fabrics (20,21) up to the reeling means (41) of the tissue paper machine.
7. Tissue paper machine according to claim 5 or 6, characterized in that on the joint run of said fabrics (20,21) has been disposed to serve as after-drier for the web, an air drier or another equivalent after-drier.
8. Tissue paper machine according to claims 2-7, characterized in that a particular fabric (13) has been disposed to lap the transfer suction roll (11) .
9. Tissue paper machine according to claims 2-8, characterized in that the transfer suction roll (11) and the creping roll (10) or creping cylinder have been rotatably carried in a frame structure (50,51) , which has been held turnable about a pivotal axis (52) and so that it is urgable by the aid of force means against the drying cylinder (100;100').
10. Tissue paper machine according to claims 2-9, characterized in that on the sector of the creping roll (10) or creping cylinder left free by the web (W;W) has been placed an applicator roll (60), which applies on the surface (10a) of the creping roll (10) or creping cylinder a substance which promotes the adhesion of the web (W;W') to the surface (10a) of the creping roll (10).
11. Tissue paper machine according to claims 2-10, characterized in that on that sector on which the web (W;W) covers the creping roll (10) or creping cylinder has been disposed a press roll (70) defining a press nip (N3) together with the creping roll (10) or creping cylinder, this press nip (N3) having as its purpose to promote the adhesion of the web (W;W') to the surface (10a) of the creping roll (10) or creping cylinder.
PCT/FI1981/000019 1980-03-18 1981-03-18 Procedure and paper machine for manufacturing creped paper web WO1981002704A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU69209/81A AU6920981A (en) 1980-03-18 1981-03-18 Procedure and means for manufacturing creped paper web

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI800827 1980-03-18
FI800827A FI60583C (en) 1980-03-18 1980-03-18 PROCEDURE FOR THE FRAMEWORK OF FRAMING SYSTEMS

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WO1981002704A1 true WO1981002704A1 (en) 1981-10-01

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EP (1) EP0047767A1 (en)
ES (1) ES500330A0 (en)
FI (1) FI60583C (en)
IT (1) IT1136941B (en)
WO (1) WO1981002704A1 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996024718A1 (en) * 1995-02-06 1996-08-15 Kimberly-Clark Worldwide, Inc. Method for making uncreped throughdried tissue products without an open draw
WO2003054293A1 (en) * 2001-12-19 2003-07-03 Kimberly-Clark Worldwide, Inc. Methods and system for manufacturing and finishing web products at high speed without reeling and unwinding
US6835264B2 (en) 2001-12-20 2004-12-28 Kimberly-Clark Worldwide, Inc. Method for producing creped nonwoven webs
US6998018B2 (en) * 2002-03-29 2006-02-14 Metso Paper Karlstad Ab Method and apparatus for making a creped tissue with improved tactile qualities while improving handling of the web
EP3165673A1 (en) * 2015-11-09 2017-05-10 Valmet Technologies Oy Production line for producing fiber webs
AT516651A3 (en) * 2014-12-17 2019-02-15 Valmet Technologies Inc With a Glättzylinder equipped fiber web machine

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3812000A (en) * 1971-06-24 1974-05-21 Scott Paper Co Soft,absorbent,fibrous,sheet material formed by avoiding mechanical compression of the elastomer containing fiber furnished until the sheet is at least 80%dry
US3821068A (en) * 1972-10-17 1974-06-28 Scott Paper Co Soft,absorbent,fibrous,sheet material formed by avoiding mechanical compression of the fiber furnish until the sheet is at least 80% dry

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3812000A (en) * 1971-06-24 1974-05-21 Scott Paper Co Soft,absorbent,fibrous,sheet material formed by avoiding mechanical compression of the elastomer containing fiber furnished until the sheet is at least 80%dry
US3821068A (en) * 1972-10-17 1974-06-28 Scott Paper Co Soft,absorbent,fibrous,sheet material formed by avoiding mechanical compression of the fiber furnish until the sheet is at least 80% dry

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996024718A1 (en) * 1995-02-06 1996-08-15 Kimberly-Clark Worldwide, Inc. Method for making uncreped throughdried tissue products without an open draw
WO2003054293A1 (en) * 2001-12-19 2003-07-03 Kimberly-Clark Worldwide, Inc. Methods and system for manufacturing and finishing web products at high speed without reeling and unwinding
US6740200B2 (en) 2001-12-19 2004-05-25 Kimberly-Clark Worldwide, Inc. Methods and system for manufacturing and finishing web products at high speed without reeling and unwinding
US6835264B2 (en) 2001-12-20 2004-12-28 Kimberly-Clark Worldwide, Inc. Method for producing creped nonwoven webs
US6998018B2 (en) * 2002-03-29 2006-02-14 Metso Paper Karlstad Ab Method and apparatus for making a creped tissue with improved tactile qualities while improving handling of the web
AT516651A3 (en) * 2014-12-17 2019-02-15 Valmet Technologies Inc With a Glättzylinder equipped fiber web machine
AT516651B1 (en) * 2014-12-17 2019-02-15 Valmet Technologies Inc With a Glättzylinder equipped fiber web machine
EP3165673A1 (en) * 2015-11-09 2017-05-10 Valmet Technologies Oy Production line for producing fiber webs
CN106996051A (en) * 2015-11-09 2017-08-01 维美德技术有限公司 Production line for producing fiber web

Also Published As

Publication number Publication date
FI60583C (en) 1982-02-10
ES8201248A1 (en) 1981-12-16
IT8120389A0 (en) 1981-03-17
EP0047767A1 (en) 1982-03-24
ES500330A0 (en) 1981-12-16
IT1136941B (en) 1986-09-03
FI60583B (en) 1981-10-30

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