EP1469999A1 - Method for producing paper imprinted with a pattern - Google Patents

Method for producing paper imprinted with a pattern

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Publication number
EP1469999A1
EP1469999A1 EP02806646A EP02806646A EP1469999A1 EP 1469999 A1 EP1469999 A1 EP 1469999A1 EP 02806646 A EP02806646 A EP 02806646A EP 02806646 A EP02806646 A EP 02806646A EP 1469999 A1 EP1469999 A1 EP 1469999A1
Authority
EP
European Patent Office
Prior art keywords
paper
printing
printed
paper web
solution
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP02806646A
Other languages
German (de)
French (fr)
Other versions
EP1469999B1 (en
Inventor
Ernst Brunbauer
Markus Eibl
Berndt KÖLL
Andreas Windischbauer
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tricon Consulting & Co KG GmbH
Original Assignee
Tricon Consulting & Co KG GmbH
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 Tricon Consulting & Co KG GmbH filed Critical Tricon Consulting & Co KG GmbH
Priority to AT02806646T priority Critical patent/ATE329764T1/en
Publication of EP1469999A1 publication Critical patent/EP1469999A1/en
Application granted granted Critical
Publication of EP1469999B1 publication Critical patent/EP1469999B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24DCIGARS; CIGARETTES; TOBACCO SMOKE FILTERS; MOUTHPIECES FOR CIGARS OR CIGARETTES; MANUFACTURE OF TOBACCO SMOKE FILTERS OR MOUTHPIECES
    • A24D1/00Cigars; Cigarettes
    • A24D1/02Cigars; Cigarettes with special covers
    • A24D1/025Cigars; Cigarettes with special covers the covers having material applied to defined areas, e.g. bands for reducing the ignition propensity
    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24CMACHINES FOR MAKING CIGARS OR CIGARETTES
    • A24C5/00Making cigarettes; Making tipping materials for, or attaching filters or mouthpieces to, cigars or cigarettes
    • A24C5/005Treatment of cigarette paper
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41MPRINTING, DUPLICATING, MARKING, OR COPYING PROCESSES; COLOUR PRINTING
    • B41M3/00Printing processes to produce particular kinds of printed work, e.g. patterns
    • B41M3/006Patterns of chemical products used for a specific purpose, e.g. pesticides, perfumes, adhesive patterns; use of microencapsulated material; Printing on smoking articles

Definitions

  • the invention relates to a method for the production of pattern-printed paper, in particular of strip-like impregnated with fire-retardant materials cigarette paper, being printed with an aqueous printing solution on a self-supporting paper web.
  • aqueous pressure solution a solution of a polymer in water.
  • the printing solution may contain organic and inorganic pigments, dyes and salts.
  • annular bands surrounding a cigarette are fire retardant, especially when the permeability of the cigarette wrapper in this area is reduced.
  • US-A 1 555, 320 from 1923 the proposal is made to form such a band as an integral part of the cigarette paper.
  • a corresponding method is known, for example, from EP 0 486 213 B1, where the production of fire-retardant transverse ribs on the wire of a paper machine is disclosed by increased application of pulp or fillers. In this method, the order takes place during a process step in which the paper web is not yet self-supporting and can not be exposed to a free train. The first free train experiences the paper web only after the press section.
  • the edge definition is a determining criterion for the quality of the print on paper. Especially when printing from aqueous solutions, it may come in the edge region to float out of the printing solution, whereby the boundary between printed and. blurred unprinted area. In order to prevent bleeding of the printing solution on the paper, coated or coated papers are usually used. Uncoated or uncoated papers result in the use of aqueous printing solutions to blurred contours. Therefore, these papers are often printed from organic solvents such as ethyl acetate or ethanol.
  • the printing solution contains water-soluble polymers and the paper before or is heated to over 50 ° C during pressing.
  • the rapid evaporation of water from the printed area then prevents the floating of the printing solution in the edge areas, and you get a sharp-edged image even on uncoated, uncoated, absorbent paper.
  • the viscosity of the pressure solution can be kept low. Thus, printing speeds of> 70 m / min are possible.
  • the preheating of the paper may be achieved by contact heating, such as a cylinder, or by radiant heating, e.g. an infrared radiator, or by other electromagnetic waves, such. Microwaves, done.
  • both gravure, digital (ink-jet) or screen printing can be used in conventional, the prior art forms.
  • a preferred form is rotary screen printing.
  • uncoated, uncoated paper of pulp and inorganic filler with a basis weight of 25 g / m 2 and a suction height of 9 mm / 10 min is with a aqueous solution of methyl cellulose (cloud point at 70 ° C) and Solophenyl blue GL printed by gravure printing.
  • the viscosity of the pressure solution is 90 mPa s.
  • the design of the printing cylinder has strips parallel to the axis of rotation.
  • the printing speed is 150 m / min.
  • the paper is preheated by means of a heatable cylinder in front of the printing unit to different temperatures.
  • An uncoated, uncoated paper with a basis weight of 32 g / m 2 and a suction height of 12 mm / 10 min is printed by rotary screen printing with a solution of 15% polyvinyl alcohol and Solophenyl blue GL.
  • the viscosity of the pressure solution is 18 mPa s.
  • the template has bands parallel to the axis of rotation with a width of 7 mm and a spacing of 18.6 mm.
  • the preheating of the paper takes place by means of a heatable cylinder and an infrared radiator.
  • An uncoated, uncoated paper with a basis weight of 38 g / m 2 and a suction height of 14 mm / 10 min is printed by rotary screen printing with a solution of 6% methylhydroxypropylcellulose having a cloud point of about 60 ° C and Solophenyl blue GL.
  • the template has bands with a width of 7 mm.
  • the preheating of the paper takes place by means of a heatable cylinder and a heatable impression roller.
  • the humidity of the paper in front of the printing unit is 40%.
  • the illustrated device is a conventional paper machine with headbox 1 and a paper screen 8, through which a mixture of pulp and fillers (dry content less than 1%) is sucked.
  • the paper web 9 is dried in a press section 3 to a dry content of about 40%.
  • the paper web 9 is solidified so far that it can be self-supporting exposed to a free train.
  • a drying section 4 is provided with a series of drying cylinders 7, at the end of which the moisture content is about 2-3%.
  • the invention also works with damp before printing from 2 - 40%, especially since the pattern-wise watering the paper web, the water content is greatly increased anyway. If the temperature of the paper is adequate, the printed image will never flow.
  • the printing of the web 9 can take place in the region of the dryer section 4a or 4c, one of the heated cylinders 7 forming the printing substrate 4, or in the region 4b, in which case the use of a heated impression roller leads to a further improvement.
  • the position 4a is preferred, since stresses caused by the pressure in the paper can be broken down by the full-surface impregnation in the size press 5.
  • the temperature of the size press must be adapted to the dissolution behavior of the polymer used. For example, fully hydrolyzed polyvinyl alcohol solves only at temperatures above 90 ° C, accordingly, the size press must be run as cold as possible. For polymers with a poor solution behavior in the heat, the size press is driven hot. Then the increase in the moisture content by impregnation to about 40% no longer causes the printed image to move. After renewed drying, the web 9 is rolled onto the winding roll 6.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Pest Control & Pesticides (AREA)
  • Paper (AREA)
  • Laminated Bodies (AREA)

Abstract

The invention relates to a method for producing paper imprinted with a pattern, especially cigarette paper that is impregnated stripwise with fire-retardant materials. According to said method, a self-supporting web of paper is imprinted with an aqueous printing solution. Said printing solution contains water-soluble polymers and the paper is heated to above 50 °C before or during printing.

Description

Verfahren zur Herstellung von musterförmig bedrucktem Papier Method for producing pattern-printed paper
Die Erfindung bezieht sich auf ein Verfahren zur Herstellung von musterförmig bedrucktem Papier, insbesondere von streifenförmig mit brandhemmenden Materialien getränktem Zigarettenpapier, wobei mit einer wässrigen Drucklösung auf eine selbsttragende Papierbahn gedruckt wird.The invention relates to a method for the production of pattern-printed paper, in particular of strip-like impregnated with fire-retardant materials cigarette paper, being printed with an aqueous printing solution on a self-supporting paper web.
Unter wässriger Drucklösung ist eine Lösung eines Polymeren in Wasser zu verstehen. Zusätzlich kann die Drucklösung organische und anorganische Pigmente, Farbstoffe und Salze enthalten.By aqueous pressure solution is meant a solution of a polymer in water. In addition, the printing solution may contain organic and inorganic pigments, dyes and salts.
Seit langer Zeit ist es bekannt, daß ringförmige Bänder, welche eine Zigarette umgeben, brandhemmend wirken, insbesondere wenn die Permeabilität der Zigarettenumhüllung in diesem Bereich vermindert ist. Beispielsweise ist in US-A 1 ,555,320 aus dem Jahre 1923 der Vorschlag gemacht, ein solches Band als integralen Teil des Zigarettenpapiers auszubilden. Ein entsprechendes Verfahren ist beispielsweise aus EP 0 486 213 B1 bekannt, wo die Herstellung brandhemmender Querrippen auf dem Sieb einer Papiermaschine durch vermehrten Auftrag von Faserbrei bzw. Füllstoffen geoffenbart ist. Bei diesem Verfahren erfolgt der Auftrag während eines Prozeßschrittes, bei welchem die Papierbahn noch nicht selbsttragend ist und noch keinem freien Zug ausgesetzt werden kann. Den ersten freien Zug erfährt die Papierbahn erst nach der Pressenpartie.For a long time, it has been known that annular bands surrounding a cigarette are fire retardant, especially when the permeability of the cigarette wrapper in this area is reduced. For example, in US-A 1 555, 320 from 1923, the proposal is made to form such a band as an integral part of the cigarette paper. A corresponding method is known, for example, from EP 0 486 213 B1, where the production of fire-retardant transverse ribs on the wire of a paper machine is disclosed by increased application of pulp or fillers. In this method, the order takes place during a process step in which the paper web is not yet self-supporting and can not be exposed to a free train. The first free train experiences the paper web only after the press section.
Alternativ sind Verfahren der eingangs gekennzeichneten Art bekannt geworden, beispielsweise aus US-A 1,996,002. Hier besteht nun das Problem, daß die Streifen schwer mit hinreichender Randschärfe gedruckt werden können. Für die Qualität des Drucks auf Papier ist die Randschärfe ein bestimmendes Kriterium. Besonders beim Druck aus wäßrigen Lösungen kann es im Randbereich zum Ausschwimmen der Drucklösung kommen, wodurch die Grenze zwischen bedrucktem und. unbedrucktem Bereich verschwimmt. Um ein Verlaufen der Drucklösung am Papier zu verhindern, werden üblicherweise gestrichene bzw. beschichtete Papiere verwendet. Ungestrichene bzw. unbeschichtete Papiere führen bei der Verwendung von wäßrigen Drucklösungen zu unscharfen Konturen. Daher werden diese Papiere häufig aus organischen Lösungsmitteln, wie z.B. Ethylacetat oder Ethanol, bedruckt. Diese Lösungsmittel müssen abgesaugt und entsorgt bzw. aufgereinigt werden. Weiters besteht bei der Verwendung von organischen Lösungsmitteln immer die Gefahr der Entzündung. Eine Verbesserung der Randschärfe bei dem Druck aus wäßrigen Lösungen kann auch durch die Erhöhung der Viskosität der Drucklösung erfolgen. Ein entsprechender Vorschlag ist aus der US 4,077,414 bekannt. Hochviskose Drucklösungen werden als Druckpasten bezeichnet. Druckpasten können jedoch im Tiefdruckverfahren nicht eingesetzt werden. Bei Siebdruckverfahren vermindert sich die mögliche Druckgeschwindigkeit mit der Erhöhung der Viskosität der Drucklösung stark.Alternatively, methods of the kind characterized in the introduction have become known, for example from US-A 1,996,002. Here is the problem that the stripes can be printed hard with sufficient edge sharpness. The edge definition is a determining criterion for the quality of the print on paper. Especially when printing from aqueous solutions, it may come in the edge region to float out of the printing solution, whereby the boundary between printed and. blurred unprinted area. In order to prevent bleeding of the printing solution on the paper, coated or coated papers are usually used. Uncoated or uncoated papers result in the use of aqueous printing solutions to blurred contours. Therefore, these papers are often printed from organic solvents such as ethyl acetate or ethanol. These solvents must be sucked off and disposed of or purified. Furthermore, there is always the danger of inflammation when using organic solvents. An improvement of the edge sharpness at the pressure from aqueous solutions can also be achieved by increasing the viscosity of the printing solution. A corresponding proposal is known from US 4,077,414. High-viscosity printing solutions are referred to as printing pastes. However, printing pastes can not be used in gravure printing. In screen printing process, the possible printing speed decreases greatly with the increase of the viscosity of the printing solution.
Für bestimmte Anwendungen, beispielsweise Zigarettenpapier, ist ein gutes Saugvermögen des Papiers notwendig. Daher können diese Papiere nicht gestrichen bzw. beschichtet werden. Je höher das Saugvermögen des Papiers, desto höher ist jedoch das Ausschwimmen der Druckfarbe und desto geringer ist die Randschärfe des Druckbildes. Ein Maß für das Saugverhalten ist die Saughöhe in mm/10 min nach DIN 53106:1981.For certain applications, such as cigarette paper, a good suction capacity of the paper is necessary. Therefore, these papers can not be coated or coated. The higher the absorbency of the paper, however, the higher is the floating of the ink and the lower the marginal sharpness of the printed image. A measure of the suction behavior is the suction height in mm / 10 min according to DIN 53106: 1981.
Um insbesondere ungestrichene, unbeschichtete, saugfähige Papiere auch mit hoher Druckgeschwindigkeit (z.B. >70 m/min, insbesondere 100 - 300 m/min) mit zugleich hoher Randschärfe zu bedrucken, wird erfindungsgemäß vorgesehen, daß die Drucklösung wasserlösliche Polymere enthält und das Papier vor oder während des Drückens auf über 50°C erwärmt wird.In order to print especially uncoated, uncoated, absorbent papers also with high printing speed (eg> 70 m / min, especially 100-300 m / min) with high edge definition, it is provided according to the invention that the printing solution contains water-soluble polymers and the paper before or is heated to over 50 ° C during pressing.
Das rasche Verdampfen des Wassers aus der bedruckten Fläche verhindert dann das Ausschwimmen der Drucklösung in den Randbereichen, und man erhält ein randscharfes Druckbild auch auf ungestrichenem, unbeschichteten, saugfähigen Papier. Die Viskosität der Drucklösung kann gering gehalten werden. Somit sind Druckgeschwindigkeiten von >70 m/min möglich. Das Vorwärmen des Papiers kann durch eine Kontaktheizung, wie z.B. einem Zylinder, oder auch durch eine Strahlungsheizung, wie z.B. einem Infrarotstrahler, oder auch durch andere elektromagnetische Wellen, wie z.B. Mikrowellen, erfolgen.The rapid evaporation of water from the printed area then prevents the floating of the printing solution in the edge areas, and you get a sharp-edged image even on uncoated, uncoated, absorbent paper. The viscosity of the pressure solution can be kept low. Thus, printing speeds of> 70 m / min are possible. The preheating of the paper may be achieved by contact heating, such as a cylinder, or by radiant heating, e.g. an infrared radiator, or by other electromagnetic waves, such. Microwaves, done.
Als Druckverfahren können sowohl der Tiefdruck-, Digital- (Ink-Jet) oder Siebdruck in üblichen, dem Stand der Technik entsprechenden Formen verwendet werden. Eine bevorzugte Form ist der Rotationssiebdruck.As a printing method, both gravure, digital (ink-jet) or screen printing can be used in conventional, the prior art forms. A preferred form is rotary screen printing.
Beispiele:Examples:
Auf ein ungestrichenes, unbeschichtetes Papier aus Zellstoff und anorganischem Füllstoff mit einem Basisgewicht von 25 g/m2 und einer Saughöhe von 9 mm/10 min wird mit einer wäßrigen Lösung von Methylcellulose (Trübungspunkt bei 70°C) und Solophenyl blau GL mittels Tiefdruck bedruckt. Die Viskosität der Drucklösung beträgt 90 mPa s. Das Design des Druckzylinders weist Streifen parallel zur Rotationsachse auf. Die Druckgeschwindigkeit beträgt 150 m/min. Das Papier wird mittels eines heizbaren Zylinders vor dem Druckwerk auf verschiedene Temperaturen vorgewärmt.On an uncoated, uncoated paper of pulp and inorganic filler with a basis weight of 25 g / m 2 and a suction height of 9 mm / 10 min is with a aqueous solution of methyl cellulose (cloud point at 70 ° C) and Solophenyl blue GL printed by gravure printing. The viscosity of the pressure solution is 90 mPa s. The design of the printing cylinder has strips parallel to the axis of rotation. The printing speed is 150 m / min. The paper is preheated by means of a heatable cylinder in front of the printing unit to different temperatures.
Ein ungestrichenes, unbeschichtetes Papier mit einem Basisgewicht von 32 g/m2 und einer Saughöhe von 12 mm/10 min wird mittels Rotationssiebdruck mit einer Lösung von 15 % Polyvinylalkohol und Solophenyl blau GL bedruckt. Die Viskosität der Drucklösung beträgt 18 mPa s. Die Schablone weist Bänder parallel zur Rotationsachse mit einer Breite von 7 mm und einem Abstand von 18,6 mm auf. Die Vorwärmung des Papiers erfolgt mittels eines heizbaren Zylinders und einem Infrarotstrahler.An uncoated, uncoated paper with a basis weight of 32 g / m 2 and a suction height of 12 mm / 10 min is printed by rotary screen printing with a solution of 15% polyvinyl alcohol and Solophenyl blue GL. The viscosity of the pressure solution is 18 mPa s. The template has bands parallel to the axis of rotation with a width of 7 mm and a spacing of 18.6 mm. The preheating of the paper takes place by means of a heatable cylinder and an infrared radiator.
Ein ungestrichenes, unbeschichtetes Papier mit einem Basisgewicht von 38 g/m2 und einer Saughöhe von 14 mm/10 min wird mittels Rotationssiebdruck mit einer Lösung von 6 % Methylhydroxypropylcellulose mit einem Trübungspunkt von ca. 60°C und Solophenyl blau GL bedruckt. Die Schablone weist Bänder mit einer Breite von 7 mm auf. Die Vorwärmung des Papiers erfolgt mittels eines heizbaren Zylinders und eines heizbaren Presseurs. Die Feuchte des Papiers vor dem Druckwerk beträgt 40 %. An uncoated, uncoated paper with a basis weight of 38 g / m 2 and a suction height of 14 mm / 10 min is printed by rotary screen printing with a solution of 6% methylhydroxypropylcellulose having a cloud point of about 60 ° C and Solophenyl blue GL. The template has bands with a width of 7 mm. The preheating of the paper takes place by means of a heatable cylinder and a heatable impression roller. The humidity of the paper in front of the printing unit is 40%.
Anschließend wird anhand der Zeichnung eine Einrichtung dargestellt, auf welcher die Erfindung bevorzugt durchgeführt werden kann.Subsequently, a device is shown with reference to the drawing, on which the invention can be preferably carried out.
Bei der dargestellten Einrichtung handelt es sich um eine konventionelle Papiermaschine mit Stoffauflauf 1 und einem Papiersieb 8, durch welche eine Mischung aus Faserbrei und Füllstoffen (Trockengehalt unter 1 %) abgesaugt wird. Nach dem Verlassen der Siebpartie 2 wird die Papierbahn 9 in einer Pressenpartie 3 auf einen Trockengehalt von etwa 40 % getrocknet. Nach der Pressenpartie ist die Papierbahn 9 soweit verfestigt, daß sie selbsttragend einem freien Zug ausgesetzt werden kann. Anschließend ist eine Trockenpartie 4 mit einer Reihe von Trockenzylindern 7 vorgesehen, an deren Ende der Feuchtigkeitsgehalt etwa 2 - 3 % beträgt. Die Erfindung funktioniert auch bei Feuchten vor dem Bedrucken von 2 - 40 %, zumal beim mustermäßigen Tränken der Papierbahn der Wassergehalt ohnedies stark erhöht wird. Bei hinreichender Temperatur des Papiers kommt es auf keinen Fall zu einem Zerfließen des Druckbildes. Das Bedrucken der Bahn 9 kann im Bereich der Trockenpartie 4a oder 4c erfolgen, wobei einer der geheizten Zylinder 7 die Druckunterlage 4 bildet, beziehungsweise im Bereich 4b, wobei hier die Verwendung eines geheizten Presseurs zu einer weiteren Verbesserung führt.In the illustrated device is a conventional paper machine with headbox 1 and a paper screen 8, through which a mixture of pulp and fillers (dry content less than 1%) is sucked. After leaving the wire section 2, the paper web 9 is dried in a press section 3 to a dry content of about 40%. After the press section, the paper web 9 is solidified so far that it can be self-supporting exposed to a free train. Subsequently, a drying section 4 is provided with a series of drying cylinders 7, at the end of which the moisture content is about 2-3%. The invention also works with damp before printing from 2 - 40%, especially since the pattern-wise watering the paper web, the water content is greatly increased anyway. If the temperature of the paper is adequate, the printed image will never flow. The printing of the web 9 can take place in the region of the dryer section 4a or 4c, one of the heated cylinders 7 forming the printing substrate 4, or in the region 4b, in which case the use of a heated impression roller leads to a further improvement.
Bevorzugt ist die Position 4a, da durch die ganzflächige Tränkung in der Leimpresse 5 durch den Druck verursachte Spannungen im Papier abgebaut werden können. Die Temperatur der Leimpresse muß dem Löseverhalten des eingesetzten Polymers angepaßt werden. Beispielsweise löst sich vollhydrolysierter Polyvinylalkohohl erst bei Temperaturen von über 90°C, dementsprechend muß die Leimpresse möglichst kalt gefahren werden. Bei Polymeren mit einem schlechten Lösungsverhalten in der Hitze wird die Leimpresse heiß gefahren. Dann bringt die durch die Tränkung erfolgte Erhöhung des Feuchtegehalts auf etwa 40 % das Druckbild nicht mehr in Bewegung. Nach neuerlichem Trocknen wird die Bahn 9 auf die Wickelrolle 6 aufgerollt. The position 4a is preferred, since stresses caused by the pressure in the paper can be broken down by the full-surface impregnation in the size press 5. The temperature of the size press must be adapted to the dissolution behavior of the polymer used. For example, fully hydrolyzed polyvinyl alcohol solves only at temperatures above 90 ° C, accordingly, the size press must be run as cold as possible. For polymers with a poor solution behavior in the heat, the size press is driven hot. Then the increase in the moisture content by impregnation to about 40% no longer causes the printed image to move. After renewed drying, the web 9 is rolled onto the winding roll 6.

Claims

P a t e n t a n s p r ü c h e : Patent claim:
1. Verfahren zur Herstellung von musterförmig bedrucktem Papier, insbesondere von streifenförmig mit brandhemmenden Materialien getränktem Zigarettenpapier, wobei mit einer wäßrigen Drucklösung auf eine selbsttragende Papierbahn gedruckt wird, dadurch gekennzeichnet, daß die Drucklösung wasserlösliche Polymere enthält und das Papier vor oder während des Drückens auf über 50°C erwärmt wird.1. A process for the production of patterned printed paper, in particular of strip-like impregnated with fire-retardant materials cigarette paper, being printed with an aqueous printing solution on a self-supporting paper web, characterized in that the printing solution contains water-soluble polymers and the paper before or during the pressing on 50 ° C is heated.
2. Verfahren nach Anspruch 1 , dadurch gekennzeichnet, daß die Polymere aus einer oder mehreren der nachfolgend angeführten Klassen der Polyvinylalkohole, Polysaccharide, modifizierten Polysacchariden oder teilhydrolysierten Polyvinylacetaten stammen.2. The method according to claim 1, characterized in that the polymers originate from one or more of the following classes of polyvinyl alcohols, polysaccharides, modified polysaccharides or partially hydrolyzed polyvinyl acetates.
3. Verfahren nach Anspruch 1 oder 2, dadurch gekennzeichnet, daß die Temperatur höher ist als jener Wert, bei dem die Polymere aus Wasser ausfallen.3. The method according to claim 1 or 2, characterized in that the temperature is higher than that value at which the polymers precipitate from water.
4. Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß das Papier vor oder während des Drückens auf 70 - 90°C erwärmt wird.4. The method according to any one of the preceding claims, characterized in that the paper is heated to 70 - 90 ° C before or during the pressing.
5. Verfahren nach einem der Ansprüche 1 bis 4, dadurch gekennzeichnet, daß die Drucklösung eine Viskosität von maximal 4000 mPas bei 20°C aufweist.5. The method according to any one of claims 1 to 4, characterized in that the pressure solution has a viscosity of at most 4000 mPas at 20 ° C.
6. Verfahren nach einem der Ansprüche 1 bis 5, dadurch gekennzeichnet, daß das Papier ein Basisgewicht von 15 - 40 g/m2 hat.6. The method according to any one of claims 1 to 5, characterized in that the paper has a basis weight of 15 - 40 g / m 2 .
7. Verfahren nach einem der Ansprüche 1 bis 6, dadurch gekennzeichnet, daß das zu bedruckende Papier eine Saughöhe von 6 - 15 mm/10 min, bevorzugt eine Saughöhe von 8 - 13 mm/10 min, aufweist.7. The method according to any one of claims 1 to 6, characterized in that the paper to be printed has a suction height of 6 - 15 mm / 10 min, preferably a suction height of 8 - 13 mm / 10 min.
8. Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß das Bedrucken des Papiers erfolgt, nachdem dieses das Papiersieb und den Pressenteil einer Papiermaschine verlassen hat, jedoch vor die Papierbahn aufgerollt wird.8. The method according to any one of the preceding claims, characterized in that the printing of the paper takes place after it has left the paper wire and the press part of a paper machine, but is rolled up in front of the paper web.
9. Verfahren nach Anspruch 8, dadurch gekennzeichnet, daß die Papierbahn bedruckt wird, wobei als Unterlage ein walzenförmiger Kontakttrockner der Papierbahn dient. 9. The method according to claim 8, characterized in that the paper web is printed, wherein a roller-shaped contact dryer of the paper web serves as a base.
10. Verfahren nach Anspruch 9, dadurch gekennzeichnet, daß die Papierbahn im Anschluß an das Bedrucken ganzflächig mit einer wäßrigen Lösung getränkt wird.10. The method according to claim 9, characterized in that the paper web is impregnated over the entire surface with an aqueous solution following the printing.
11. Verfahren nach Anspruch 10, dadurch gekennzeichnet, daß die wäßrige Lösung Brandförderer enthält. 11. The method according to claim 10, characterized in that the aqueous solution contains fire promoter.
EP02806646A 2002-02-01 2002-04-24 Method for producing gigarette paper imprinted with a pattern Expired - Lifetime EP1469999B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT02806646T ATE329764T1 (en) 2002-02-01 2002-04-24 METHOD FOR PRODUCING CIGARETTE PAPER PRINTED IN A PATTERN

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
AT0017402A AT412608B (en) 2002-02-01 2002-02-01 METHOD FOR PRODUCING PATTERN PRINTED PAPER
AT1742002 2002-02-01
PCT/AT2002/000125 WO2003064165A1 (en) 2002-02-01 2002-04-24 Method for producing paper imprinted with a pattern

Publications (2)

Publication Number Publication Date
EP1469999A1 true EP1469999A1 (en) 2004-10-27
EP1469999B1 EP1469999B1 (en) 2006-06-14

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Family Applications (1)

Application Number Title Priority Date Filing Date
EP02806646A Expired - Lifetime EP1469999B1 (en) 2002-02-01 2002-04-24 Method for producing gigarette paper imprinted with a pattern

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US (1) US20050077021A1 (en)
EP (1) EP1469999B1 (en)
AT (2) AT412608B (en)
CA (1) CA2473533C (en)
DE (1) DE50207233D1 (en)
ES (1) ES2266640T3 (en)
WO (1) WO2003064165A1 (en)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6779530B2 (en) 2002-01-23 2004-08-24 Schweitzer-Mauduit International, Inc. Smoking articles with reduced ignition proclivity characteristics
US7047982B2 (en) 2003-05-16 2006-05-23 R.J. Reynolds Tobacco Company Method for registering pattern location on cigarette wrapping material
US20050005947A1 (en) 2003-07-11 2005-01-13 Schweitzer-Mauduit International, Inc. Smoking articles having reduced carbon monoxide delivery
EP1512541B1 (en) * 2003-09-08 2008-05-21 Hauni Maschinenbau AG Printer for a machine used in the tobacco industry
ATE396052T1 (en) * 2003-09-08 2008-06-15 Hauni Maschinenbau Ag PRINTING UNIT FOR A MACHINE IN THE TOBACCO PROCESSING INDUSTRY
WO2006054403A1 (en) * 2004-11-19 2006-05-26 Japan Tobacco Inc. Cigarette production system
US8151806B2 (en) 2005-02-07 2012-04-10 Schweitzer-Mauduit International, Inc. Smoking articles having reduced analyte levels and process for making same
ES2645221T3 (en) 2006-06-01 2017-12-04 Schweitzer-Mauduit International, Inc. Outdoor combustion smoking articles with reduced ignition tendency characteristics
ATE553252T1 (en) * 2006-06-27 2012-04-15 Basf Se METHOD FOR FINISHING PAPER AND PAPER PRODUCTS
GB201108475D0 (en) 2011-05-20 2011-07-06 British American Tobacco Co Smoking article wrapper
CN102501570B (en) 2011-12-02 2013-10-30 牡丹江恒丰纸业股份有限公司 Gravure press producing cigarette paper with flame retarding zone and production method
EP2906057A1 (en) 2012-10-11 2015-08-19 Schweitzer-Mauduit International, Inc. Wrapper having reduced ignition proclivity characteristics
TW201438607A (en) 2012-10-16 2014-10-16 British American Tobacco Co Smoking article wrapper and method of making a smoking article
FR3022564B1 (en) * 2014-06-18 2017-06-30 Allimand METHOD FOR DRYING CIGARETTE PAPER STRIP AND CIGARETTE PAPER THUS OBTAINED
CN107584915A (en) * 2017-09-25 2018-01-16 青岛嘉泽包装有限公司 A kind of preparation method of volume cigarette tipping paper

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1555320A (en) * 1923-04-11 1925-09-29 Weil Emile Cigarette
US1996002A (en) * 1933-05-25 1935-03-26 Seaman Stewart Elmer Decreasing inflammability of cigarettes
GB1524211A (en) * 1975-01-09 1978-09-06 British American Tobacco Co Smoking articles
US4452259A (en) * 1981-07-10 1984-06-05 Loews Theatres, Inc. Smoking articles having a reduced free burn time
ATE23183T1 (en) * 1982-08-20 1986-11-15 Lawrence Peter Robin B PRINTING INKS AND SUBSTRATES PRINTED WITH THEM.
JPS6116883A (en) * 1984-07-02 1986-01-24 Mitsubishi Paper Mills Ltd Manufacture of recording paper
JPS629956A (en) * 1985-07-08 1987-01-17 株式会社 千代田グラビヤ印刷社 Manufacture of solid-pattern decorative sheet
EP0486213B1 (en) * 1990-11-16 1997-05-28 Philip Morris Products Inc. Paper having crossdirectional regions of variable basis weight
JP3021227B2 (en) * 1993-04-01 2000-03-15 花王株式会社 Absorbent paper and absorbent article comprising the same
JP2947735B2 (en) * 1995-08-09 1999-09-13 三島製紙株式会社 Water dispersible sheet and tobacco using the same
US5830318A (en) * 1996-10-25 1998-11-03 Schweitzer-Mauduit International, Inc. High opacity tipping paper
US5814188A (en) * 1996-12-31 1998-09-29 The Procter & Gamble Company Soft tissue paper having a surface deposited substantive softening agent
US6645605B2 (en) * 2001-01-15 2003-11-11 James Rodney Hammersmith Materials and method of making same for low ignition propensity products
US6779530B2 (en) * 2002-01-23 2004-08-24 Schweitzer-Mauduit International, Inc. Smoking articles with reduced ignition proclivity characteristics

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO03064165A1 *

Also Published As

Publication number Publication date
WO2003064165A1 (en) 2003-08-07
ATE329764T1 (en) 2006-07-15
CA2473533A1 (en) 2003-08-07
AT412608B (en) 2005-05-25
EP1469999B1 (en) 2006-06-14
CA2473533C (en) 2009-09-15
US20050077021A1 (en) 2005-04-14
DE50207233D1 (en) 2006-07-27
ATA1742002A (en) 2004-10-15
ES2266640T3 (en) 2007-03-01

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