序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
241 METHOD AND APPARATUS IN MOISTENING OF A WEB EP99934752.9 1999-07-09 EP1097268A1 2001-05-09 HEIKKINEN, Antti; TANI, Mikko
In the method in moistening of a web, water is applied with a wetting device (2) in a predetermined point on the surface of a paper web (W) or the like passing by the point, and the web is thereafter passed to a calender (C). The liquid is applied at such an early stage that before the surface treatment, the fibres exposed to wetting in the paper web (W) or the like have the time to absorb it at least 80 % of the amount of liquid they are capable of absorbing. The distance travelled by the web between the drying section and the calender is increased with rolls (1) which guide the web (W) along a winding path.
242 INTEGRATED PAPER MACHINE EP99955509.7 1999-05-27 EP1086271A1 2001-03-28 KERTTULA, Reima
The invention concerns an integrated paper machine, which comprises, in the running direction of the web, a multi-layer headbox (100), a gap former (200), in which there is at least one pre-press (303, 304), a press section (300), in whcih there is at least one extended-nip press (308, 309), a pre-dryer section (400), in which the web (W) is dried by means of a high-capacity dryer unit, a dryer section (500), in which there is at least one dryer group (R1, R2, R3) which makes use of single-wire draw, as well as a surface treatment device (P) for the web. Further, the paper machine is provided with a closed web draw at least to the end of the dryer section (500).
243 METHOD FOR CONTROLLING THE CURL OF PAPER AND A PAPER OR BOARD MACHINE LINE THAT APPLIES THE METHOD EP98921505.8 1998-05-08 EP1009876A1 2000-06-21 KAIHOVIRTA, Juha; PAKARINEN, Pekka; LUONTAWA, Matti
The invention concerns a method for controlling the curl of paper, in which method steam treatment and/or moistening of the paper web (W) and/or equivalent operations are employed in order to control the curl of the paper web (W). In the method, the operations for controlling the curl of the paper web (W) are carried out after the calendering process carried out in the calender (40) or, in processes in which calendering is not employed, in connection with the machine reel-up or in process steps carried out after the machine reel-up. The invention also concerns a paper or board machine, which comprises at least a headbox, a former, a press, and a dryer section, in which paper or board machine steam boxes and/or moistening devices and/or an IR dryer and/or equivalent devices for the control of the curl are employed. The steam boxes and/or moistening devices and/or IR dryers and/or the equivalent curl control devices for the control of the curl of the paper web (W) are placed after the calender (40) or, if no calender is employed, in connection with the machine reel-up or in connection with a finishing process carried out after the machine reel-up.
244 Infrared paper drying machine and method for drying a paper web in an infrared paper drying machine EP96117531 1996-10-31 EP0771904A3 1998-06-17 THORP BENJAMIN A
A paper drying apparatus and method therefor including an infrared drying unit and a vacuum unit, wherein the infrared drying unit emits infrared radiation in a direction toward the vacuum unit. A fabric sheet for carrying a paper web is provided, wherein the fabric sheet passes between the infrared drying unit and the vacuum unit. The infrared drying unit is positioned on the side of the fabric sheet adjacent to the paper web and the vacuum unit is juxtaposed on the opposite side of the fabric sheet from the infrared drying unit, wherein the vacuum unit draws air through the paper web in a direction from the infrared drying unit toward the vacuum unit. The combination of the infrared drying unit with the vacuum units provides a compact arrangement which efficiently removes moisture from the paper web. After passing by the infrared drying unit, the fabric sheet then conveys the paper web toward a final drying drum where the paper web is transferred from the fabric sheet to the final drying drum through the use of a pressure roll.
245 Infrared paper drying machine and method for drying a paper web in an infrared paper drying machine EP96117531.2 1996-10-31 EP0771904A2 1997-05-07 Thorp, Benjamin A.

A paper drying apparatus and method therefor including an infrared drying unit and a vacuum unit, wherein the infrared drying unit emits infrared radiation in a direction toward the vacuum unit. A fabric sheet for carrying a paper web is provided, wherein the fabric sheet passes between the infrared drying unit and the vacuum unit. The infrared drying unit is positioned on the side of the fabric sheet adjacent to the paper web and the vacuum unit is juxtaposed on the opposite side of the fabric sheet from the infrared drying unit, wherein the vacuum unit draws air through the paper web in a direction from the infrared drying unit toward the vacuum unit. The combination of the infrared drying unit with the vacuum units provides a compact arrangement which efficiently removes moisture from the paper web. After passing by the infrared drying unit, the fabric sheet then conveys the paper web toward a final drying drum where the paper web is transferred from the fabric sheet to the final drying drum through the use of a pressure roll.

246 Arrangement for lowering the noise level in connection with the cooling layer in a pulp dryer EP95850122.3 1995-06-28 EP0690168A3 1997-04-16 Karlstedt, Bertel; Petterson, Henrik

The invention concerns an arrangement for lowering the noise level in connection with the cooling layer (12) in a pulp dryer (10). The heat-insulated bottom wall and top wall of the cooling layer (12) are accomplished by means of a sound-attenuating construction (21,22), and the wall at the inlet side of the cooling layer (12) is also accomplished by means of a sound-attenuating construction (23). At the outlet side of the air flow from the cooling layer (12) in a pulp dryer (10), sound-attenuation baffles (26) are provided, which are preferably perpendicular or inclined in relation to the direction of the air flow and which are placed at a distance from one another.

247 Method and device for drying of paper EP93850038.6 1993-02-26 EP0559628B1 1997-04-16 Ilmarinen, Antti
248 Beheizbare Walze zur Behandlung von Warenbahnen sowie Verfahren zu deren Betrieb EP95106745.3 1995-05-04 EP0690169B1 1997-03-26 Conrad, Hans-Rolf; Cramer, Dirk
249 Process and apparatus for drying sheet materials EP94308397.2 1994-11-14 EP0653514A3 1996-02-14 Hanaya, Morimasa

An apparatus and method for drying a wet sheet material such as a paper web is presented. The apparatus is provided with a suitable number of dryer cylinders operating in conjunction with a plurality of steam blast ports disposed adjacent to the dryer cylinders. A vertically movable canopy hood and a middle hood having sheet entry/exit opening and a door opening device are provided. The wet sheet material is held between two endless fabric belt, and passed through the dryer cylinders alternatively by means of suction fabric rolls, fabric rolls and fabric tension rolls. The drying process is carried out in an atmosphere of superheated steam of over 100°C inside the canopy hood and the middle hood, and the steam generated from the wet sheets is recirculated through an exhaust screen, a super heated steam circulating fan, an adiabatic compressor and a supply duct. Another atmosphere of heated moist air having a dew point of at least 80°C is also employed. The dried paper product manufactured has high dimensional stability and exhibits superior printing characteristics and substantially increased paper strength, and the process is highly energy conserving.

250 Method and device for preventing cross direction web shrinkage in the drying section of a paper machine EP85850026.7 1985-01-25 EP0152384B1 1990-04-25 Fellers, Nils Christer; Hansson, Hans Torbjörn; Htun, Myat Thoung
251 A METHOD FOR CONTROLLING SHRINKAGE AND/OR STRETCHING OF A PAPER WEB IN THE DRYING SECTION OF A PAPER MACHINE, IN THE FORM OF A CYLINDER DRIER AND/OR FAN DRYER, TRANSVERSELY TO THE FEED DIRECTION OF THE WEB; AND ARRANGEMENTS FOR CARRYING OUT THE METHOD EP85901109.0 1985-02-11 EP0174945B1 1989-05-10 FELLERS, Christer; HTUN, Myat; HANSSON, Torbjörn
Arrangement and method for controlling or regulating shrinkage and/or stretching of a paper web transversely to the transport direction thereof in a drying section of a paper machine, this drying section having the form of a cylinder dryer (6) and/or a fan dryer. At a point in the drying process at which the paper web exhibits a dry solids content of at most 75% the paper web (10) is subjected to an outwardly directed force which is forced to act in the edge portion (10a, 10b) of the web. The forces are caused to act adjacent parallel edge portions (10a, 10b) of the paper web and are directed away from each other. The magnitude of these forces is selected so that they fall beneath shrinkage forces occurring momentary on the paper web at the dry solids content in question by at most 50%.
252 FLOATER DRYER AND PROCEDURE FOR ENHANCING ITS OPERATION EP87902091.0 1987-03-13 EP0263136A1 1988-04-13 KORPELA, Matti
Un séchoir à matériau en bande flottant, servant à sécher un matériau en déplacement en forme de bande (W), tel que notamment une bande de papier ou de carton, comprend plusieurs unités de rayonnement/soufflage d'air (10) placées sur un des côtés de la bande (W) ou sur les deux côtés (10A, 10B). Lesdites unités forment des boîtes de soufflage, qui présentent sur leur côté faisant face à la bande (W) une surface portante libre de tout contact (21R, 27) et en association avec lesquelles un jet d'air (Ful) ou des jets d'air (Fua, Fub) est/sont soufflé(s) à travers une ouverture d'ajutage (20a, 20b) ménagée sur le côté avant et/ou arrière de ladite surface portante. Lesdits jets doivent avoir une composante essentiellememt étendue parallèle à ladite surface portante. En association avec les unités de rayonnement/soufflage d'air (10), des éléments de rayonnement (30) sont prévus, depuis lesquels un rayonnement (SO) est dirigé à travers une fenêtre (27) pendant l'intervalle du traitement (P1, P2, P-). Ladite fenêtre sert en même temps de surface portante pour le support pneumatique de la bande (W). Les écoulements d'air (F3, F4) provenant de la boîte de soufflage sont égalements conduits pour servir d'air de refroidissement aux éléments de rayonnement (30) et pour leur servir de composantes en association avec eux. Un agencement de miroirs (32, 33), destinés à renvoyer en retour sur la bande (W) le rayonnement ayant traversé ladite bande (W), peut être disposé sur le côté opposé à la surface portante (27, 21) des unités de rayonnement/soufflage d'air (10).
253 Method and device for preventing cross direction web shrinkage in the drying section of a paper machine EP85850026.7 1985-01-25 EP0152384A2 1985-08-21 Fellers, Nils Christer; Hansson, Hans Torbjörn; Htun, Myat Thoung

It is a known phenomenon that the web during the drying moment in a paper machine shrinks. The shrinkage in the machine direction can be controlled by arranging the different driving groups in the drying section to operate at different speeds. The shrinkage in cross direction, however, heretofore was not brought under control. The present invention has the object to solve thos problem.

According to the invention, the problem of shrinkage is solved in that the web during a certain drying interval is subjected to outward directed forces, which are applied during a suitable drying interval and preferably at a low dry content, for example directly after the press section.

254 Manufacturing of Kraft paper EP84850100 1984-03-28 EP0124496A3 1985-06-05 Landqvist, Nils; Spangenberg, Sven; Järnberg, Torsten; Nordin, Bengt

A process for manufacturing of kraft paper, especially kraft sack paper, on a multi-wire machine in which the web is dried by a combined cylinder drying and free drying and is optionally creped or micro-creped and optionally also glazed. By forming the web into two or more layers which are couched together in the wire part of the machine and subsequent shrinkage in order to obtain a stretch at break of at least 2.5% in the machine direction and of at least 5% in the cross direction, improved strength properties are provided.

255 Manufacturing of Kraft paper EP84850100.3 1984-03-28 EP0124496A2 1984-11-07 Landqvist, Nils; Spangenberg, Sven; Järnberg, Torsten; Nordin, Bengt

A process for manufacturing of kraft paper, especially kraft sack paper, on a multi-wire machine in which the web is dried by a combined cylinder drying and free drying and is optionally creped or micro-creped and optionally also glazed. By forming the web into two or more layers which are couched together in the wire part of the machine and subsequent shrinkage in order to obtain a stretch at break of at least 2.5% in the machine direction and of at least 5% in the cross direction, improved strength properties are provided.

256 Anordnung zur Trocknungsregelung an einer Papiermaschine EP79101045.7 1979-04-05 EP0004915B1 1982-05-12 Grassmann, Hans-Christian, Dipl.-Ing.
257 Drying system EP81102032.0 1981-03-19 EP0036632A2 1981-09-30 Rounsley, Robert R.

A drying system and method for removing volatile liquid from a liquid bearing web of material by evaporation includes means for moving the liquid bearing web (10) of material through a drying station (12) and heating means (14) position at the drying station, for applying evaporation energy to the liquid bearing web (10) of material to effect evaporation of the volatile liquid from the web. Electrostatic means (30) is provided for subjecting the web of material to a static electrical field at the drying station (12), whereby the evaporation of volatile liquid from the web is enhanced. Evaporation energy may be applied to the liquid bearing web (10) by bringing a heated surface (14) in contact with the web or by irradiating the web with infrared energy. Alternatively, evaporation energy may be applied to the liquid bearing web (10) by directing heated air against the web.

258 Verfahren zur Trocknung von feuchten Bahnen aus Papier oder Kartonagen EP79105294.7 1979-12-20 EP0013400A1 1980-07-23 Grassmann, Hans-Christian, Dipl.-Ing.

Zur optimalen Vergleichmässigung des Feuchteprofils wird die Papierbahn zunächst mit konventioneller Zylindertrocknung (3) auf eine Feuchte von 10-20% getrocknet. Anschliessend wird eine kapazitive Hochfrequenztrocknung (4) auf etwa 6-10% Feuchte vorgenommen. Die Trocknung auf die gewünschte Endfeuchte von z.B. 4%wird dann wieder mit einem Zylindertrockner (5) durchgeführt. Die Einsatzgrenzen des Hochfrequenztrockners sind dabei u.a. durch die Kosten für HF-Energie und die Überschlagsgefahr gegeben.

259 Paper products and methods and systems for manufacturing such products US15160612 2016-05-20 US10047481B2 2018-08-14 Marshall Medoff
Methods of producing cellulosic or lignocellulosic materials for use in papermaking include treating a cellulosic or lignocellulosic dry feedstock having a first average molecular weight with ionizing radiation, and controlling the dose of ionizing radiation such that the average molecular weight of the feedstock is reduced to a predetermined level. A method of producing an irradiated paper product includes treating a paper product including a first carbohydrate-containing material having a first molecular weight with ionizing radiation, and controlling the dose of ionizing radiation so as to provide an irradiated paper product with a second carbohydrate-containing material having a second molecular weight higher than the first molecular weight. Pulp and paper products are produced.
260 METHOD FOR MANUFACTURING FILTER MEDIUM FOR AIR FILTER US15743866 2015-08-03 US20180200655A1 2018-07-19 Junji NEMOTO; Akira ISOGAI; Tsuguyuki SAITO
A method for manufacturing a filter medium for an air filter having improved particle collection performance using cellulose nanofibers. The method for manufacturing a filter medium for an air filter comprises: causing a mixed solution containing cellulose nanofibers and a dispersion medium to adhere to an air-permeable support; and subsequently freeze-drying the resulting product, in which a number average fiber diameter of the cellulose nanofibers is 1 to 50 nm, the dispersion medium is a mixed dispersion medium of water and a water-soluble organic solvent, and a solid content concentration of the cellulose nanofibers in the mixed solution is 0.001 to 0.150% by mass.
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