US20070113998A1 - Paper product and method of making - Google Patents

Paper product and method of making Download PDF

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Publication number
US20070113998A1
US20070113998A1 US11/538,224 US53822406A US2007113998A1 US 20070113998 A1 US20070113998 A1 US 20070113998A1 US 53822406 A US53822406 A US 53822406A US 2007113998 A1 US2007113998 A1 US 2007113998A1
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Prior art keywords
paper
citric acid
cockle
mono
water
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US11/538,224
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David Park
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Domtar Paper Co LLC
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Weyerhaeuser Co
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Publication date
Priority claimed from US10/744,856 external-priority patent/US20050133182A1/en
Priority claimed from US10/743,846 external-priority patent/US20050133181A1/en
Application filed by Weyerhaeuser Co filed Critical Weyerhaeuser Co
Priority to US11/538,224 priority Critical patent/US20070113998A1/en
Assigned to WEYERHAEUSER COMPANY reassignment WEYERHAEUSER COMPANY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: PARK, DAVID W.
Publication of US20070113998A1 publication Critical patent/US20070113998A1/en
Assigned to DOMTAR PAPER COMPANY, LLC reassignment DOMTAR PAPER COMPANY, LLC PATENT ASSIGNMENT Assignors: WEYERHAEUSER COMPANY
Assigned to JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT reassignment JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT SECURITY AGREEMENT Assignors: DOMTAR PAPER COMPANY, LLC
Abandoned legal-status Critical Current

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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/16Sizing or water-repelling agents
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/46Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/54Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
    • D21H17/57Polyureas; Polyurethanes
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63Inorganic compounds
    • D21H17/66Salts, e.g. alums
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H19/00Coated paper; Coating material
    • D21H19/10Coatings without pigments
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • D21H17/05Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/14Carboxylic acids; Derivatives thereof
    • D21H17/15Polycarboxylic acids, e.g. maleic acid
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/30Luminescent or fluorescent substances, e.g. for optical bleaching

Definitions

  • the present invention is directed to printing paper, and the method of making this paper.
  • Hardwood and softwood wood pulp fibers are used in the manufacture of printing paper and newsprint. These fibers are produced in a chemical pulping process, either sulfate or sulfite, or in a mechanical pulping process. Mechanical processes would include thermomechanical and chemithermomechanical.
  • these hardwood or softwood pulp fibers and wet end chemicals are mixed with water in the headbox of the paper machine to form a suspension of fibers is and chemicals.
  • the wet end chemicals may include fillers such as calcium carbonate and clay.
  • the suspension of fibers and chemicals flow from the headbox onto a wire.
  • the water is removed from the fibers and chemicals by both gravity and vacuum to form a wet web of pulp fibers into which the chemicals are incorporated.
  • the chemicals are throughout the sheet.
  • the sheet may be pressed and dried to remove more water.
  • Starch, optical brightener additives and surface size may be placed on surface of the sheet in a surface sizing step at the size press Some of the materials may enter into the web if the pressure of the nip at the press is great enough.
  • the resulting product is referred to as an uncoated or lightly coated paper sheet or web.
  • the uncoated sheet may be coated in another application of one or more coating layers placed on the sheet in an off-line coating operation.
  • the uncoated sheet passes through a coating station and a second drying station. It may pass through a second calendering operation.
  • the resulting product is referred to as a coated paper sheet or web.
  • Uncoated or coated printing paper has a basis weight of from 16 to 180 pounds per 3300 square feet.
  • a digital printing technology such as web-fed ink jet printing presents new and different challenges for the paper maker as the optimum surface physics and chemistry of paper for these printers are very different than those required for conventional offset inks.
  • Standard desk top ink jet printers are increasing in speed and some of the same challenges are found when printing with these printers because of the water placed on the paper and the difficulty of completely drying the paper before it leaves the printer.
  • optical density of the printed image is also of primary concern for many print jobs as high levels of ink are required to provide vivid, robust colors. This is known as high optical density.
  • Uncoated papers are limited in the amount of ink they can tolerate because of their tendency to curl and cockle. Thus more expensive coated papers are generally required when high optical densities are needed.
  • the inks are anionic. Highly cationic chemicals are usually added to the paper in order to precipitate the ink and cause the ink to be water fast.
  • Hexasulfonate optical brighteners are used to enhance the brightness of the paper and make it appear better visually. These optical brighteners are also anionic and the highly cationic chemicals will react with the optical brightener also. This reduces the ability of the brightener to brighten the paper.
  • the present invention is directed to an uncoated paper usable with ink having a water content and which has a maximum Cockle Value of 0.25.
  • the Cockle Value is used to determine the amount of cockle or water induced curt in the paper.
  • An embodiment of the invention is an uncoated paper having a paper basis weight of 16 to 180 pounds per 3300 square feet and a maximum Cockle Value of 0.25.
  • An embodiment of the invention is a paper that has been treated with a at least 50 pounds per ton of paper with a mono alkali metal salt of citric acid, a mono sodium or potassium citrate, that is capable of being added at the size press, blade coater or by a spray before the heated drying section.
  • Another embodiment is a paper that has been treated with at least 75 pounds of the citrate per ton of paper.
  • Another embodiment is a printing paper that has been treated with up to 250 pounds of the citrate per ton of paper.
  • Another embodiment is a paper that has been treated with up to 300 pounds of the citrate per ton of paper.
  • a mono alkali metal salt of citric acid such as mono sodium or potassium citrate has enough cationicity to react with the ink jet inks to cause them to be water fast.
  • the mono alkali metal salt of citric acid also causes the paper to have a Cockle Value of 0.25 or less.
  • the mono alkali metal salt of citric acid does not have enough cationicity to react with an optical brightener, including hexasulfonate optical brighters, or to react with offset printing inks. It provides a paper that is water fast,that has a reduced cockle and can be preprinted in an offset press.
  • the paper also contains a binder such as starch, ethylated starch, latex, polyvinyl alcohol, styrene acrylic acid or an ester in addition to the mono alkali metal salt of citric acid and tne low viscosity of the additive can be maintained.
  • a binder such as starch, ethylated starch, latex, polyvinyl alcohol, styrene acrylic acid or an ester in addition to the mono alkali metal salt of citric acid and tne low viscosity of the additive can be maintained.
  • the paper also contains a florescent whitening agent, an optical brightener or a hexasulfonated optical brightener in addition to the mono alkali metal salt of citric acid.
  • FIG. 1 is a drawing of the work station for carrying out the second side cockle test method.
  • FIG. 2 is a schematic diagram of a paper machine.
  • One embodiment of the present invention is directed to an uncoated or lightly coated paper having a mono alkali metal salt of citric acid and which may be used for printing on ink jet printers and which has a maximum Cockle Value of 0.25 after such printing.
  • Another embodiment is directed to an uncoated or lightly coated printing paper having a mono alkali metal salt of citric acid and which is water fast.
  • a mono alkali metal salt of citric acid such as mono sodium or potassium citrate has enough cationicity to react with the ink jet inks to cause them to be water fast.
  • the mono alkali metal salt of citric acid also causes the paper to have a Cockle Value of 0.25 or less.
  • the mono alkali metal salt of citric acid does not have enough cationicity to react with an optical brightener, including hexasulfonate optical brighters, or to react with offset printing inks. It provides a paper that is water fast, that has a reduced cockle and can be preprinted in an offset
  • the paper also contains a binder such as starch, ethylated starch, latex, polyvinyl alcohol, styrene acrylic acid or an ester in addition to the mono alkali metal salt of citric acid and the low viscosity of the additive can be maintained.
  • a binder such as starch, ethylated starch, latex, polyvinyl alcohol, styrene acrylic acid or an ester in addition to the mono alkali metal salt of citric acid and the low viscosity of the additive can be maintained.
  • the paper also contains a florescent whitening agent, an optical brightener or a hexasulfonated optical brightener in addition to the mono alkali metal salt of citric acid.
  • a quantitative test has been developed to determine the curl and cockle of paper. It replaces the subjective test of viewing the paper to determine whether there was curl and cockle and the amount of curl and cockle. This prior subjective test also determined whether a sheet of paper had sufficient treatment.
  • the quantitative test is the second side cockle test method.
  • the second side cockle test method is used to evaluate the amount of cockle that an inkjet print, at an ink application level of 5.9 grams/square meter, produces in the unprinted or second side of a paper printed with a block print.
  • the present test used a Scitex Test Cockle Form Print.
  • the unprinted side of the inkjet print is illuminated using low angle (15°) lighting.
  • a digital image is made of the cockled area on the unprinted side associated with a 3.5 by 3.5 inch half-tone printed square on the printed side of the sample. The image is then evaluated to determine the amount of second side cockle.
  • the apparatus used for the second side cockle test method is shown in FIG. 1 . It includes a test platform 10 , a Kodak® megaplus 8-bit digital camera 12 , and a Dedolight® light 14 .
  • the camera 12 is mounted above surface 16 of the test platform 10 and at 90° to the surface 16 of the test platform 10 .
  • the camera is aimed directly at the center of the surface 16 of the platform.
  • the Dedolight light 14 is mounted at an angle of 15° to the surface 16 and also aimed at the center of the surface 16 . Mathworks, Inc. Matlab® computer software is used to analyze the images.
  • the samples of paper to be tested are printed on one side with a Scitex Test Cockle Form using an inkjet printer and inkjet ink.
  • a Hewlett Packard ink jet printer HP560C was used.
  • the ink used was Scitex Ink 2002 and the ink application level was 5.9 g/square meter.
  • the ink should be a water based ink.
  • the paper was handled carefully so as not to crease or wrinkle the paper because creases or wrinkles would be analyzed as cockle.
  • the settings of the camera 12 were adjusted to a pixel resolution of 100 microns/pixel and an f-stop of F 8 .
  • the camera control was on Fixed and the image centering was at 127.
  • the Dedolight light 14 was adjusted for uniform low angle lighting. All lighting was from the Delolight light 14 . Other room lights were turned off.
  • the paper sample 18 was placed on the surface 16 of the test stand 10 with the unprinted side of the paper turned to the camera and facing up.
  • the 3.5 by 3.5 inch cockle area was centered in the camera field of view with the light aimed at the center of the cockle area.
  • the camera's exposure was adjusted until the average image pixel value was 127.
  • the image was collected and saved to a disk.
  • the images were analyzed using the Mathworks, Inc. Matlab® computer software. Version 6, release 13 was used.
  • the image is read into the program and smoothed with a 5 ⁇ 5 median filter to remove high frequency noise.
  • the mean, standard deviation and coefficient of variation were calculated for each row and column.
  • the larger of the maximum row coefficient of variability and maximum column coefficient of variability is taken as the sample Cockle Value.
  • the program is evaluating the differences between the light and dark areas of the image and determining the variability.
  • Cockle Value means the cockle value determined by this test.
  • An embodiment is an uncoated paper that has been treated with a hexasulfonated optical brightener and at least 50 pounds per ton of paper with a mono alkali metal salt of citric acid, a mono sodium or mono potassium citrate.
  • the maximum Cockle Value of the treated printing paper is 0.25.
  • a ton is defined here as 2000 pounds.
  • the salt of citric acid would be applied in a solution at a concentration of 20-50% of the total weight of the solution at room temperature or at temperatures of 50° C. or less.
  • At least 75 pounds of citrate per ton of paper is used. In another embodiment of the invention as much as 300 pounds of citrate per ton of paper may be used. In another embodiment as much as 250 pounds of citrate per ton of paper may be used.
  • the citrate is applied at the size press or the blade coater. It may be applied using a puddle, gate roll or metered size press, or a knife or blade coater. In one embodiment the citrate may be applied in a solution containing at least 20% by weight of material. In another embodiment the citrate may be applied in a solution containing 20 to 50% by weight of the material.
  • 60 gm./m 2 unsized paper was used as the base paper for the sheets in this example.
  • the percentages in this example are weight percentages.
  • a control sample of paper was coated in a laboratory size press with ethylated starch at 12% concentration. Both side of the paper were coated to a coat weight of 40 pounds of starch per ton of paper per side. This is typical of most uncoated paper grades (Formula I).
  • a sample of paper was treated in a lab size press with a solution containing a concentration a 25% of the monosodium salt of citric acid (monosodium citrate), heated to 50 degrees C. Both side of the paper were coated to a coat weight of 37.5 pounds of material per ton of paper per side (Formula II).
  • the sheets were then dried and conditioned at 50% R.H.
  • One set of the sheets was printed using an HP 560 printer and Scitex High Speed ink jet ink.
  • the image was a 3′′ ⁇ 3′′ square, printed at 60% density, using Corel Draw, Version 10.
  • the printed sheets were then placed in a darkroom, face down and viewed under a LANDSCO triple-bulb, low angle light. The degree of curl and cockle were then visually estimated. The sheets were judged against the starch control. The results are shown in Table 1. 100% is the base case for a starch control.
  • Water fast means the ability of ink to remain intact when exposed to water or moisture. Water fast inks do not bleed. Water based inks must be treated to be water fast. The inks are anionic. It has been found that the mono alkali metal salt of citric acid has enough cationicity to react with the anionic ink and make it water fast. It does not, however, have enough cationicity to react with offset printing inks.
  • Water fastness is typically obtained with a nitrogen-containing organic compound of a cationic nature and functions by precipitating the dye in the ink, rendering it immobile, when exposed to moisture after printing.
  • these types of materials are incompatible with anionic fluorescent whitening agents, optical brighteners, or hexasulfonated optical brighteners which are typically applied at the size press to brighten paper.
  • these types of additives reduce the overall paper brightness, often times to levels below customer acceptance.
  • the mono alkali metal salts of citric acid such as sodium and potassium citrate, do not have enough cationicity to react with the optical brighteners, the flourescent whitening agents or the hexasulfonated optical brighteners.
  • the pH of the mono alkali metal salts of citric acid is acid enough to react with the ink jet inks but not acid enough to react with the optical brighteners or the offset printing inks.
  • Monosodium citrate maintains the brightness of the paper with fluorescent whitening agents, optical brighteners or hexasulfonated optical brighteners while providing water fastness and a low degree of curl and cockle.
  • Water based inks those found in ink jet printing, are anionic. Water based inks will bleed when placed in water. The inks must be fixed by precipitating the dye in the ink. This is usually done with highly cationic fixatives.
  • the mono alkali metal salt of citric acid is acid enough to react with the ink jet inks but not acid enough to react with the optical brighteners or offset printing inks.
  • the percentage shown are weight percentages.
  • 60 gm./m2 unsized paper was used as the base paper for the sheets in this example.
  • the Formula 1 control samples were also used as the control samples.
  • a second sample of paper was treated in a lab size press with a solution containing a concentration a 25% of the monosodium salt of citric acid, heated to 50 degrees C. This percentage is a weight percentage. Both side of the paper were coated to a net coat weight of 37.5 pounds of material per ton of paper per side. The amount of citrate was 37.5 pounds per ton of paper per side.
  • FIG. 2 is a schematic drawing of a paper machine. Wood pulp fiber furnish and wet end chemicals are mixed with water in a headbox 20 to form a slurry. The slurry exits the headbox through a slice 22 onto a wire 24 . The water in the slurry drains from the wire. A vacuum chest 26 is also used to draw water from the slurry to form a wet paper web. The web is carried through press rolls 28 and a drier 30 that remove additional water.
  • the size press may be a horizontal type with the rolls horizontally aligned, a vertical type with the rolls vertically aligned.
  • the materials may be placed on the web from the rolls or from a puddle between the rolls.
  • the web may, in some instances, be coated with material by the spraying apparatus 34 .
  • the materials described in the various embodiments in the present application would also be applied at the size press 32 or the spraying apparatus 34 .
  • the paper web then passes through a drying section 36 .
  • the drying is usually done by steam heated drier cans through which the paper web is threaded.
  • the paper is then calendered by calender rolls 38 and rolled into paper rolls at the winder 40 .
  • the resulting product is known as uncoated paper.

Abstract

Paper having improved curl and cockle properties for water based, ink jet printing applications and a method of producing them. The paper contains at least 50 pounds per ton of a mono alkali metal salt of citric acid. The paper has a maximum Cockle Value of 0.25. It also contain a hexasulfonated optical brightener. The paper is also water fast and can be preprinted with offset printing inks. A method for making the paper.

Description

    RELATION TO OTHER APPLICATIONS
  • This application is a continuation-in-part of application Ser. No. 10/743,846 and 10/744,856, both filed Dec. 22, 2003.
  • FIELD
  • The present invention is directed to printing paper, and the method of making this paper.
  • BACKGROUND
  • Hardwood and softwood wood pulp fibers are used in the manufacture of printing paper and newsprint. These fibers are produced in a chemical pulping process, either sulfate or sulfite, or in a mechanical pulping process. Mechanical processes would include thermomechanical and chemithermomechanical. To form the printing paper or newsprint, these hardwood or softwood pulp fibers and wet end chemicals are mixed with water in the headbox of the paper machine to form a suspension of fibers is and chemicals. The wet end chemicals may include fillers such as calcium carbonate and clay. The suspension of fibers and chemicals flow from the headbox onto a wire. The water is removed from the fibers and chemicals by both gravity and vacuum to form a wet web of pulp fibers into which the chemicals are incorporated. The chemicals are throughout the sheet. The sheet may be pressed and dried to remove more water.
  • Starch, optical brightener additives and surface size may be placed on surface of the sheet in a surface sizing step at the size press Some of the materials may enter into the web if the pressure of the nip at the press is great enough.
  • Thereafter the web of fiber, wet end chemicals and other materials is dried by heat, calendered and rolled into rolls. The resulting product is referred to as an uncoated or lightly coated paper sheet or web.
  • The uncoated sheet may be coated in another application of one or more coating layers placed on the sheet in an off-line coating operation. The uncoated sheet passes through a coating station and a second drying station. It may pass through a second calendering operation. The resulting product is referred to as a coated paper sheet or web.
  • Uncoated or coated printing paper has a basis weight of from 16 to 180 pounds per 3300 square feet.
  • The application of high speed, variable printing is experiencing tremendous growth in the printing industry, displacing conventional offset printing for many applications. A digital printing technology such as web-fed ink jet printing presents new and different challenges for the paper maker as the optimum surface physics and chemistry of paper for these printers are very different than those required for conventional offset inks.
  • High speed, ink jet printing is exceptionally challenging because it employs aqueous inks and a great deal of water is placed on the paper surface during the printing process. In the process, these water based inks may be applied at high coverage at paper speeds of 500-1,000 ft. per minute. It is difficult to completely dry the paper before the paper leaves the printer. If uncoated paper is used, the water from the ink penetrates the sheet and disrupts the bonding between the paper fibers. This creates a deformation of the paper surface, which results in unacceptable curling, cockling, or puckering of the printed paper.
  • Standard desk top ink jet printers are increasing in speed and some of the same challenges are found when printing with these printers because of the water placed on the paper and the difficulty of completely drying the paper before it leaves the printer.
  • Wide printers have similar challenges because of the amount of ink and water placed on the paper.
  • Because of these factors, special papers are used when the print job requires high levels of ink coverage. These special papers are coated with water-absorbent silica or swellable gel materials such as polyvinyl pyrilodone, or combinations of these materials. Typically, these materials are applied by an off-line coating operation. The price of these materials and the off-line application significantly increases the cost of paper for these applications.
  • The optical density of the printed image is also of primary concern for many print jobs as high levels of ink are required to provide vivid, robust colors. This is known as high optical density. Uncoated papers are limited in the amount of ink they can tolerate because of their tendency to curl and cockle. Thus more expensive coated papers are generally required when high optical densities are needed.
  • The inks are anionic. Highly cationic chemicals are usually added to the paper in order to precipitate the ink and cause the ink to be water fast.
  • Hexasulfonate optical brighteners are used to enhance the brightness of the paper and make it appear better visually. These optical brighteners are also anionic and the highly cationic chemicals will react with the optical brightener also. This reduces the ability of the brightener to brighten the paper.
  • Many of these papers are preprinted in an offset press before being printed in an ink jet system. An example would be placing a watermark or logo on the paper. These inks are also anionic and a highly cationic chemical reacts with these inks also. This creates a problem in cleanup of the offset presses.
  • It is desirable to find a material that may be placed on an uncoated paper in a size press operation, that will reduce the cockle in paper so that it may be used in high speed ink jet printing, make the ink water fast so that it does not bleed when sprayed with water, and may allow the paper to be pre-printed in an offset press.
  • SUMMARY
  • The present invention is directed to an uncoated paper usable with ink having a water content and which has a maximum Cockle Value of 0.25. The Cockle Value is used to determine the amount of cockle or water induced curt in the paper. An embodiment of the invention is an uncoated paper having a paper basis weight of 16 to 180 pounds per 3300 square feet and a maximum Cockle Value of 0.25.
  • An embodiment of the invention is a paper that has been treated with a at least 50 pounds per ton of paper with a mono alkali metal salt of citric acid, a mono sodium or potassium citrate, that is capable of being added at the size press, blade coater or by a spray before the heated drying section. Another embodiment is a paper that has been treated with at least 75 pounds of the citrate per ton of paper. Another embodiment is a printing paper that has been treated with up to 250 pounds of the citrate per ton of paper. Another embodiment is a paper that has been treated with up to 300 pounds of the citrate per ton of paper.
  • It has been found that a mono alkali metal salt of citric acid such as mono sodium or potassium citrate has enough cationicity to react with the ink jet inks to cause them to be water fast. The mono alkali metal salt of citric acid also causes the paper to have a Cockle Value of 0.25 or less. The mono alkali metal salt of citric acid does not have enough cationicity to react with an optical brightener, including hexasulfonate optical brighters, or to react with offset printing inks. It provides a paper that is water fast,that has a reduced cockle and can be preprinted in an offset press.
  • In another embodiment of the invention the paper also contains a binder such as starch, ethylated starch, latex, polyvinyl alcohol, styrene acrylic acid or an ester in addition to the mono alkali metal salt of citric acid and tne low viscosity of the additive can be maintained.
  • In another embodiment of the invention the paper also contains a florescent whitening agent, an optical brightener or a hexasulfonated optical brightener in addition to the mono alkali metal salt of citric acid.
  • BRIEF SUMMARY OF THE DRAWINGS
  • FIG. 1 is a drawing of the work station for carrying out the second side cockle test method.
  • FIG. 2 is a schematic diagram of a paper machine.
  • DETAILED DESCRIPTION
  • One embodiment of the present invention is directed to an uncoated or lightly coated paper having a mono alkali metal salt of citric acid and which may be used for printing on ink jet printers and which has a maximum Cockle Value of 0.25 after such printing. Another embodiment is directed to an uncoated or lightly coated printing paper having a mono alkali metal salt of citric acid and which is water fast.
  • It has been found that a mono alkali metal salt of citric acid such as mono sodium or potassium citrate has enough cationicity to react with the ink jet inks to cause them to be water fast. The mono alkali metal salt of citric acid also causes the paper to have a Cockle Value of 0.25 or less. The mono alkali metal salt of citric acid does not have enough cationicity to react with an optical brightener, including hexasulfonate optical brighters, or to react with offset printing inks. It provides a paper that is water fast, that has a reduced cockle and can be preprinted in an offset
  • In another embodiment of the invention the paper also contains a binder such as starch, ethylated starch, latex, polyvinyl alcohol, styrene acrylic acid or an ester in addition to the mono alkali metal salt of citric acid and the low viscosity of the additive can be maintained.
  • In another embodiment of the invention the paper also contains a florescent whitening agent, an optical brightener or a hexasulfonated optical brightener in addition to the mono alkali metal salt of citric acid.
  • A quantitative test has been developed to determine the curl and cockle of paper. It replaces the subjective test of viewing the paper to determine whether there was curl and cockle and the amount of curl and cockle. This prior subjective test also determined whether a sheet of paper had sufficient treatment. The quantitative test is the second side cockle test method.
  • The second side cockle test method is used to evaluate the amount of cockle that an inkjet print, at an ink application level of 5.9 grams/square meter, produces in the unprinted or second side of a paper printed with a block print. The present test used a Scitex Test Cockle Form Print. The unprinted side of the inkjet print is illuminated using low angle (15°) lighting. A digital image is made of the cockled area on the unprinted side associated with a 3.5 by 3.5 inch half-tone printed square on the printed side of the sample. The image is then evaluated to determine the amount of second side cockle.
  • The apparatus used for the second side cockle test method is shown in FIG. 1. It includes a test platform 10, a Kodak® megaplus 8-bit digital camera 12, and a Dedolight® light 14. The camera 12 is mounted above surface 16 of the test platform 10 and at 90° to the surface 16 of the test platform 10. The camera is aimed directly at the center of the surface 16 of the platform. The Dedolight light 14 is mounted at an angle of 15° to the surface 16 and also aimed at the center of the surface 16. Mathworks, Inc. Matlab® computer software is used to analyze the images.
  • The samples of paper to be tested are printed on one side with a Scitex Test Cockle Form using an inkjet printer and inkjet ink. In the following tests a Hewlett Packard ink jet printer HP560C was used. The ink used was Scitex Ink 2002 and the ink application level was 5.9 g/square meter. The ink should be a water based ink. The paper was handled carefully so as not to crease or wrinkle the paper because creases or wrinkles would be analyzed as cockle.
  • The settings of the camera 12 were adjusted to a pixel resolution of 100 microns/pixel and an f-stop of F8. The camera control was on Fixed and the image centering was at 127. The Dedolight light 14 was adjusted for uniform low angle lighting. All lighting was from the Delolight light 14. Other room lights were turned off.
  • The paper sample 18 was placed on the surface 16 of the test stand 10 with the unprinted side of the paper turned to the camera and facing up. The 3.5 by 3.5 inch cockle area was centered in the camera field of view with the light aimed at the center of the cockle area. The camera's exposure was adjusted until the average image pixel value was 127. The image was collected and saved to a disk.
  • This process was repeated for each sample.
  • The images were analyzed using the Mathworks, Inc. Matlab® computer software. Version 6, release 13 was used. The image is read into the program and smoothed with a 5×5 median filter to remove high frequency noise. The mean, standard deviation and coefficient of variation were calculated for each row and column. The larger of the maximum row coefficient of variability and maximum column coefficient of variability is taken as the sample Cockle Value. The program is evaluating the differences between the light and dark areas of the image and determining the variability.
  • Cockle Value means the cockle value determined by this test.
  • An embodiment is an uncoated paper that has been treated with a hexasulfonated optical brightener and at least 50 pounds per ton of paper with a mono alkali metal salt of citric acid, a mono sodium or mono potassium citrate. The maximum Cockle Value of the treated printing paper is 0.25. A ton is defined here as 2000 pounds. The salt of citric acid would be applied in a solution at a concentration of 20-50% of the total weight of the solution at room temperature or at temperatures of 50° C. or less.
  • In another embodiment of the invention at least 75 pounds of citrate per ton of paper is used. In another embodiment of the invention as much as 300 pounds of citrate per ton of paper may be used. In another embodiment as much as 250 pounds of citrate per ton of paper may be used.
  • The citrate is applied at the size press or the blade coater. It may be applied using a puddle, gate roll or metered size press, or a knife or blade coater. In one embodiment the citrate may be applied in a solution containing at least 20% by weight of material. In another embodiment the citrate may be applied in a solution containing 20 to 50% by weight of the material.
  • 60 gm./m2 unsized paper was used as the base paper for the sheets in this example.
  • The percentages in this example are weight percentages.
  • A control sample of paper was coated in a laboratory size press with ethylated starch at 12% concentration. Both side of the paper were coated to a coat weight of 40 pounds of starch per ton of paper per side. This is typical of most uncoated paper grades (Formula I).
  • Each of the sheets were then dried and conditioned at 50% R.H.
  • Two commercial paper products A and B, printed with a HP 560 printer using Scitex high speed ink jet ink were digitally recorded with a SONY Mavica digital camera, under low angle light.
  • A sample of paper was treated in a lab size press with a solution containing a concentration a 25% of the monosodium salt of citric acid (monosodium citrate), heated to 50 degrees C. Both side of the paper were coated to a coat weight of 37.5 pounds of material per ton of paper per side (Formula II).
  • The sheets were then dried and conditioned at 50% R.H.
  • One set of the sheets was printed using an HP 560 printer and Scitex High Speed ink jet ink. The image was a 3″×3″ square, printed at 60% density, using Corel Draw, Version 10.
  • The printed sheets were then placed in a darkroom, face down and viewed under a LANDSCO triple-bulb, low angle light. The degree of curl and cockle were then visually estimated. The sheets were judged against the starch control. The results are shown in Table 1. 100% is the base case for a starch control.
  • The sheets were also tested for water fastness via submersion in water for 60 seconds and the ink dye was completely immobilized by the salt. The results are also shown in Table 1.
    TABLE 1
    Degree of Curl/
    Cockle: Water
    Formula Scitex ink Fastness
    Formula I 100% Poor
    Formula II <5% Excellent
  • Water fast means the ability of ink to remain intact when exposed to water or moisture. Water fast inks do not bleed. Water based inks must be treated to be water fast. The inks are anionic. It has been found that the mono alkali metal salt of citric acid has enough cationicity to react with the anionic ink and make it water fast. It does not, however, have enough cationicity to react with offset printing inks.
  • Water fastness is typically obtained with a nitrogen-containing organic compound of a cationic nature and functions by precipitating the dye in the ink, rendering it immobile, when exposed to moisture after printing. Unfortunately, these types of materials are incompatible with anionic fluorescent whitening agents, optical brighteners, or hexasulfonated optical brighteners which are typically applied at the size press to brighten paper. As such, these types of additives reduce the overall paper brightness, often times to levels below customer acceptance. Again, the mono alkali metal salts of citric acid, such as sodium and potassium citrate, do not have enough cationicity to react with the optical brighteners, the flourescent whitening agents or the hexasulfonated optical brighteners.
  • The pH of the mono alkali metal salts of citric acid is acid enough to react with the ink jet inks but not acid enough to react with the optical brighteners or the offset printing inks.
  • Monosodium citrate maintains the brightness of the paper with fluorescent whitening agents, optical brighteners or hexasulfonated optical brighteners while providing water fastness and a low degree of curl and cockle.
  • Water based inks, those found in ink jet printing, are anionic. Water based inks will bleed when placed in water. The inks must be fixed by precipitating the dye in the ink. This is usually done with highly cationic fixatives. The mono alkali metal salt of citric acid is acid enough to react with the ink jet inks but not acid enough to react with the optical brighteners or offset printing inks.
  • Samples were also evaluated using the second side cockle test method.
  • The percentage shown are weight percentages.
  • 60 gm./m2 unsized paper was used as the base paper for the sheets in this example.
  • The Formula 1 control samples were also used as the control samples.
  • A second sample of paper was treated in a lab size press with a solution containing a concentration a 25% of the monosodium salt of citric acid, heated to 50 degrees C. This percentage is a weight percentage. Both side of the paper were coated to a net coat weight of 37.5 pounds of material per ton of paper per side. The amount of citrate was 37.5 pounds per ton of paper per side.
  • Two commercial papers were added to the study.
  • The samples were evaluated both visually and using the second side cockle test method. The image evaluation test correlated well with the visual observation. The results are given in Table 2.
    TABLE 2
    Formula Subjective Value Cockle Value
    25% mono sodium Acceptable 0.2296
    salt of citric acid
    12% Starch control Unacceptable 0.2658
    First Choice ™ Unacceptable 0.2851
    CI-2000 ™ Unacceptable 0.3211
  • It was determined that paper sheets having Cockle values of 0.25 or less were acceptable.
  • FIG. 2 is a schematic drawing of a paper machine. Wood pulp fiber furnish and wet end chemicals are mixed with water in a headbox 20 to form a slurry. The slurry exits the headbox through a slice 22 onto a wire 24. The water in the slurry drains from the wire. A vacuum chest 26 is also used to draw water from the slurry to form a wet paper web. The web is carried through press rolls 28 and a drier 30 that remove additional water.
  • Additional size press chemicals or materials are placed on the wet paper web at the size press 32. The size press may be a horizontal type with the rolls horizontally aligned, a vertical type with the rolls vertically aligned. The materials may be placed on the web from the rolls or from a puddle between the rolls. The web may, in some instances, be coated with material by the spraying apparatus 34. The materials described in the various embodiments in the present application would also be applied at the size press 32 or the spraying apparatus 34.
  • The paper web then passes through a drying section 36. The drying is usually done by steam heated drier cans through which the paper web is threaded. The paper is then calendered by calender rolls 38 and rolled into paper rolls at the winder 40. The resulting product is known as uncoated paper.
  • This is the product of the present invention. Additional expensive off-machine coatings would not be required to provide a paper that has a maximum Cockle Value of 0.25.
  • Those skilled in the art will note that various changes may be made in the embodiments described herein without departing from the spirit and scope of the present invention.

Claims (6)

1. A method of manufacturing uncoated printing paper comprising
forming a wet web of cellulosic fibers,
applying to the web at least 50 pounds of a mono alkali metal salt of citric acid per ton of paper,
applying-to the web hexasulfonate optical brightener,
drying the web to provide an uncoated paper having water fastness.
2. The method of claim 1 wherein the salt of citric acid is mono sodium citrate.
3. The method of claim 1 wherein the salt of citric acid is mono potassium citrate.
4. The method of claim 1 further comprising applying to the web prior to drying a starch, ethylated starch or polyvinyl alcohol.
5. The method of claim 4 wherein the salt of citric acid is mono sodium citrate.
6. The method of claim 4 wherein the salt of citric acid is mono potassium citrate.
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US20110151148A1 (en) * 2009-12-17 2011-06-23 International Paper Company Printable Substrates with Improved Dry Time and Acceptable Print Density by Using Monovalent Salts
US20110151149A1 (en) * 2009-12-17 2011-06-23 International Paper Company Printable Substrates with Improved Brightness from OBAs in Presence of Multivalent Metal Salts
US8382947B2 (en) 2006-06-01 2013-02-26 International Paper Company Surface treatment of substrate or paper/paperboard products using optical brightening agent
US20170260695A1 (en) * 2011-08-18 2017-09-14 Ahlstrom-Munksjö Oyj Fibre-based support containing a layer of a functionalized water-soluble polymer, method of production and use thereof
US10036124B2 (en) 2012-01-23 2018-07-31 International Paper Company Separated treatment of paper substrate with multivalent metal salts and OBAs

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US5161550A (en) * 1990-04-26 1992-11-10 P. H. Glatfelter Company Wrappers for smoking articles, methods of making such wrappers and smoking articles made from such wrappers--case V
US20030131860A1 (en) * 2001-08-14 2003-07-17 Ashcraft Charles Ray Wrapping materials for smoking articles

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US5152304A (en) * 1989-10-31 1992-10-06 Philip Morris Incorporated Wrapper for a smoking article
US5161550A (en) * 1990-04-26 1992-11-10 P. H. Glatfelter Company Wrappers for smoking articles, methods of making such wrappers and smoking articles made from such wrappers--case V
US20030131860A1 (en) * 2001-08-14 2003-07-17 Ashcraft Charles Ray Wrapping materials for smoking articles

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8382947B2 (en) 2006-06-01 2013-02-26 International Paper Company Surface treatment of substrate or paper/paperboard products using optical brightening agent
US20110151148A1 (en) * 2009-12-17 2011-06-23 International Paper Company Printable Substrates with Improved Dry Time and Acceptable Print Density by Using Monovalent Salts
US20110151149A1 (en) * 2009-12-17 2011-06-23 International Paper Company Printable Substrates with Improved Brightness from OBAs in Presence of Multivalent Metal Salts
US8574690B2 (en) 2009-12-17 2013-11-05 International Paper Company Printable substrates with improved dry time and acceptable print density by using monovalent salts
US8652593B2 (en) 2009-12-17 2014-02-18 International Paper Company Printable substrates with improved brightness from OBAs in presence of multivalent metal salts
US20170260695A1 (en) * 2011-08-18 2017-09-14 Ahlstrom-Munksjö Oyj Fibre-based support containing a layer of a functionalized water-soluble polymer, method of production and use thereof
US10760217B2 (en) * 2011-08-18 2020-09-01 Ahlstrom-Munksjö Oyj Fibre-based support containing a a layer of a functionalized water-soluble polymer, method of production and use thereof
US10036124B2 (en) 2012-01-23 2018-07-31 International Paper Company Separated treatment of paper substrate with multivalent metal salts and OBAs

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