[go: up one dir, main page]

US3908071A - External sizing of extensible paper - Google Patents

External sizing of extensible paper Download PDF

Info

Publication number
US3908071A
US3908071A US295919A US29591972A US3908071A US 3908071 A US3908071 A US 3908071A US 295919 A US295919 A US 295919A US 29591972 A US29591972 A US 29591972A US 3908071 A US3908071 A US 3908071A
Authority
US
United States
Prior art keywords
starch
web
paper
compacted
tea
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.)
Expired - Lifetime
Application number
US295919A
Other languages
English (en)
Inventor
Albert Heim
Ernest J Groome
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.)
Clupak Inc
Original Assignee
Clupak Inc
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 Clupak Inc filed Critical Clupak Inc
Priority to US295919A priority Critical patent/US3908071A/en
Priority to GB1928573A priority patent/GB1405720A/en
Priority to BR3616/73A priority patent/BR7303616D0/pt
Priority to AU60731/73A priority patent/AU486816B2/en
Priority to ZA737822*A priority patent/ZA737822B/xx
Priority to SE7313676A priority patent/SE416063B/xx
Priority to DE2350483A priority patent/DE2350483C2/de
Priority to JP48113755A priority patent/JPS5916039B2/ja
Priority to FR7336048A priority patent/FR2202192B1/fr
Priority to DD173950A priority patent/DD109243A5/xx
Priority to CA182,892A priority patent/CA1013216A/en
Priority to NO3915/73A priority patent/NO144223C/no
Priority to BE136541A priority patent/BE805909A/xx
Priority to AR250468A priority patent/AR200883A1/es
Priority to PH15249A priority patent/PH9752A/en
Priority to AT1056273A priority patent/AT333590B/de
Application granted granted Critical
Publication of US3908071A publication Critical patent/US3908071A/en
Priority to CA274,716A priority patent/CA1043556A/en
Priority to YU172/80A priority patent/YU41693B/xx
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
    • D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
    • D21H23/22—Addition to the formed paper
    • D21H23/52—Addition to the formed paper by contacting paper with a device carrying the material
    • D21H23/56—Rolls
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21G—CALENDERS; ACCESSORIES FOR PAPER-MAKING MACHINES
    • D21G9/00—Other accessories for paper-making machines
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21G—CALENDERS; ACCESSORIES FOR PAPER-MAKING MACHINES
    • D21G9/00—Other accessories for paper-making machines
    • D21G9/009—Apparatus for glaze-coating paper webs
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24—Polysaccharides
    • D21H17/28—Starch
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H25/00—After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
    • D21H25/005—Mechanical treatment
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H5/00—Special paper or cardboard not otherwise provided for
    • D21H5/0005—Processes or apparatus specially adapted for applying liquids or other fluent materials to finished paper or board, e.g. impregnating, coating
    • D21H5/0025—Processes or apparatus specially adapted for applying liquids or other fluent materials to finished paper or board, e.g. impregnating, coating by contact with a device carrying the treating material
    • D21H5/003—Processes or apparatus specially adapted for applying liquids or other fluent materials to finished paper or board, e.g. impregnating, coating by contact with a device carrying the treating material with a roller
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H5/00—Special paper or cardboard not otherwise provided for
    • D21H5/24—Special paper or cardboard not otherwise provided for having enhanced flexibility or extensibility produced by mechanical treatment of the unfinished paper
    • D21H5/245—Special paper or cardboard not otherwise provided for having enhanced flexibility or extensibility produced by mechanical treatment of the unfinished paper obtained by compressing the (moist) paper in directions lying in, and optionally perpendicular to, the paper plane, e.g. plain-surfaced Clupak papers
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/25—Web or sheet containing structurally defined element or component and including a second component containing structurally defined particles
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/31504—Composite [nonstructural laminate]
    • Y10T428/31971—Of carbohydrate
    • Y10T428/31993—Of paper

Definitions

  • Extensible (compacted) paper produced, for example, in accordance with the apparatus and process disclosed in US. Pat. No. 2,624,245 has certain well recognized advantages and commercial uses. Such paper is subjected, while in a partially moistened condition, to compressive compaction in the direction of web movement (machine direction or MD) between a pres sure nip, thus compacting and forcing the fibers together to produce an inherent stretchability without creping.
  • Compacted paper has improved tensile energy absorption (TEA) burst and tear characteristics which are highly desirable for such end uses as the manufacture of paper sacks.
  • extensible paper has reduced tensile strength and stiffness, the diminution of the latter characteristic increasing the difiiculty of converting this paper into sacks.
  • a method for externally sizing compacted paper web has been devised wherein starch in solution, eg. potato, corn or wheat starch is impregnated under pressure into both sides of the web by percentage weight of l to 10% while moisture absorbed by the web is controlled such that after drying the web retains essentially all of the improved qualities afforded by compaction and is further improved in its tensile, burst, TEA and stiffness qualities.
  • the stiffness imparted by such treatment produces compacted paper approximately as stiff as noncompacted paper (rendering such paper easily convertible into sacks) while the other enumerated strength qualities are drastically improved in comparison to compacted paper and of course non-compacted paper.
  • internal resin sizing may be used to control the degree of moisture absorption during the application of the starch solution to the web.
  • Other techniques for selectively controlling moisture absorption may also be used, for example, the strength of the starch solution may be regulated in accordance with the elapsed time from the application of the starch solution to the web to the subsequent drying of the web.
  • relatively unrefined or unbeated paper fibers may be treated in accordance with the inventive method to produce a paper product having optimum or near optimum tensile and tear strengths.
  • Unrefined paper fibers in a web exhibit relatively greater tear strengths and lesser tensile strengths than does a web produced from refined fibers.
  • the impregnation of starch sizing as disclosed herein can produce a commensurate increase in tensile strength with respect to unrefined fiber webs, without substantial loss in tear strength.
  • FIG. 1 is a schematic representation of a compactor for producing extensible paper
  • FIG. 2 is a schematic representation of dryer sections which receive the compacted web after processing by the apparatus of FIG. 1 and a size press intermediate said dryer sections for applying a solution of starch into the web;
  • FIG. 3 is a schematic illustration of an alternate form of the invention wherein the compacted web is fed directly to a size press and therefrom to a dryer section, and
  • FIGS. 49 illustrate graphically the effects of varying percentages of starch vis a vis different strength factors, compacted and uncompacted paper.
  • FIG. 1 illustrates generally a compactor 10 for producing an uncreped extensible paper web 11.
  • the apparatus 10 includes a loopedelastomeric traveling belt 12, and a rotary cylin 'der 13 having a smooth (chrome plated) outer surface for receiving the web 11 thereon.
  • a plurality of guide rolls l4, l5, l6 and 17 are positioned within the loop of the belt 12, guide roll 14 operating to squeeze the belt 12 against the cylinder 13 at a press nip N wherein the belt 12 is temporarily reduced in thickness as it travels therethrough.
  • a section of the guide rolls 15 is spaced from the first guide roll 14 and urges a portion 12a of the belt against the cylinder 13 at the offrunning side of the nip N, and web guide means 18, 19 feed the web onto the cylinder 13 for movement through the nip N.
  • the apparatus 10 is shown located in a paper machine between the second and third dryer sections.
  • a dryer roll shown fragmentarily at 20 indicates the last roll of the second dryer section and the roll 33 (also shown fragmentarily) indicates the first roll of the third dryer section 30.
  • the web is conveyed from the dryer roll 20 beneath the paper roll 19 and over an expander (paper guide) roll 18, and then into the nip N.
  • the web 11 is brought into contact with the surface of the chrome plated roll 13 before it enters the nip N.
  • the web 11 is then held against the surface of the roll 13 for an appreciable angular distance by the belt portion 12a and the web is then separated from both the belt 12 and the surface of the roll 13 and trained around a paper guide roll 22 and over another expander guide roll 23 and onto the dryer roll 33.
  • the web 11 coming off the dryer drum 20 has the optimum amount of moisture required for the compacting treatment. This optimum may vary between 20 to 50 percent moisture as the web 11 enters the apparatus 10.
  • the roll 13 has a smooth surface, preferably chrome plated.
  • the roll 13 is mounted on bearings 13a for rotation and is driven by a suitable source of power, such as a motor indicated diagrammatically at M.
  • the motor M is the driving power for the entire device 10.
  • the roll 13 drives the belt 12 primarily through pressure engagement at the nip N so that tension in the belt 12 is reduced at the nip N.
  • some power is required to drive the belt 12 around the various guide rolls, such as the rolls 14, l5, l6 and 17 and the point at which the belt 12 is driven (which in this case is at the nip N) is a point at which tension in the belt is reduced.
  • a lubricant shower 25 is provided just beneath the web 11 at the oncoming side of the nip N.
  • the lubricant shower 25 is a silicone shower but other release agents are suitable which applies a relatively small amount of liquid, in the form of a film, to the surface of the roll 13.
  • the roll 13 is heated, as shown here diagrammatically, by a suitable source of steam S fed axially into the roll 13 in the manner in which steam is fed into the usual paper machine dryer drum.
  • the steam maintains a relatively high temperature about 212 and up to 350 F. at the surface of the roll 13 so as to create a very thin steam film or cushion between the web 11 and the drum 13. This steam cushion assists in permitting relative sliding between the web 11 and the drum 13 (which is essential to permit the web to be compacted by the belt) and tends to soften some of the ingredients of certain types of paper.
  • the web 11 After leaving the compacting apparatus 10, the web 11 will pass through the dryer section 30 which includes conventional drying rolls 31-36, the web 1 1 first passing over drying roll 33 thence to roll 34 etc. as shown.
  • Felt dryer belts 37 and 38 are arranged upon guide rolls 39 and in contact with the respective dryer rolls 3l36 to assure the intimate engagement between the web 11 and the respective dryer rolls.
  • the moisture contained in the web is approximately 35 to 45% moisture by weight.
  • the moisture content of the web 11 will be approximately 7 to 15 percent of moisture by weight.
  • Reference numeral 40 indicates a size press arrangement for treating the dried compacted web 1 l in accordance with the present invention.
  • Web 11 first passes over guide rolls 41, 42 and therefrom proceeds between a nip formed by two counter-rotating size press rolls 43 and 44.
  • Nozzles 46, 47 control the starch metering valves 48, 49 in conduit 50, 51 which permit a metered quantity of a starch solution 52 to flow into the nip between size press rolls 43, 44.
  • Edge catch pans 53 collect the excess starch solution at each end of the nip.
  • the starch solution is supplied from a starch solution supply tank 54 having therein an agitator 56, starch in solution being drawn from the tank 54 through conduit 57 to the pump 58 which supplies metering valves 48 and 49.
  • a starch return pump 60 serviced by line 61 from catch pans 53 returns the starch solution via line 62 to the supply tank 54.
  • a solution of starch is applied under pressure to both sides of the web in accordance with varying percentages indicated below by way of specific examples.
  • the passage of the web 11 through the starch solution and between the rolls 43, 44 will be sufficient and will be so regulated as to the speed of application and the strength of the starch solution to permit and to cause impregnation of starch into both surfaces of the web 11 in accordance with a predetermined amount.
  • the weight of starch impregnated and deposited in the web will be from 1 percent to 10 percent by weight to the total weight of the web after drying in order to achieve good results, with optimums of different strength characteristics being obtained by impregnating starch in accordance with the percentage shown in FIGS. 4-9. During this process the moisture content of the web will increase from the 7 to 15 percent value at the outlet of the dryer section 30 to a value of 35 to 45 percent. v
  • Dryer section 66 contains a plurality of dryer rollers 67, 68, 69, 70, etc. about which pass dryer felts 71, 72 guided by rolls 73.
  • the dryer section 66 is similar in all respects to the dryer section 30 and the web 11 passing therethrough will lose the moisture imparted by the size press existing from the dryer section 66 with moisture content of approximately 5 to percent by weight.
  • FIG. 3 discloses an alternate embodiment of the invention wherein the same reference numerals have been used for similar parts as shown in FIG. 2.
  • the web 11 proceeds directly from the compactor 10 without first going through dryer section 30.
  • the web 11 contains approximately 30 to 40 percent moisture by weight prior to passing between the size press rolls 43, 44.
  • the web 11 contains this amount of moisture, lesser amounts of the starch solution will be caused to impregnate the web; however, a sufficient amount of starch in solution will impregnate the web to provide significant and beneficial results in regard to increasing tensile, burst and TEA characteristics, and may be expected to be in the order of approximately 50 percent of the improvement achieved with the configuration of FIG. 2.
  • the web 11 feeds into the dryer section 66 which reduces the moisture content of the web to a moisture level of 5 to 10 percent by Weight.
  • the advantage of the arrangement shown in section 3 is the use of asimgle dryer section to receive the web from the size press, although the moisture content of a web will ordinarily require a larger dryer sec tion to reduce the moisture content to acceptable levels.
  • FIGS. 2 and 3 it should be possible to obtain glazing of the paper web 11 by feeding the web downstream of the size press 40 around a single dryer roll provided that the starch solution when applied in the press 40 provides sufficient bonding of the web to the cylinder.
  • a pressure contact with the drying cylinder as shown for example in US. Pat. No. 3,362,869. The difference between the pressed arrangement and that shown in US. Pat. No.
  • 3,362,869 referred to above in describing the background of the present invention, is that the starch applied in the said United States Patent is a surface coating used to achieve adhesive bonding between the web and the dryer roll, whereas in the present invention the web becomes impregnated with starch on both sides to achieve the subsequent additional improvements of radically increased tensile, burst and TEA strengths.
  • the size press which includes the size press rolls for forcing the starch solution into both web surfaces.
  • Example No. 1
  • slightly converted starch should be superior to highly converted starches, particularly at high percentage levels of starch impregnation.
  • plasticized starch should be highly compatible'with the extensible qualities of compacted paper. This is not, however, in any way to suggest that the use of unconverted starch is undesirable, since the examples disclosed herein were made using starch in the highly converted form.
  • FIG. 7 show MD tensile results for potato and corn starch at different levels. Two different refininglevels were explored in each instance. Notethat whereas tensile gains for potato starch occur during the first 3% addition, increased tensile with corn starch continues to higher additive levels. Also it may be observed that the addition of 3% starch to compacted paper brings the tensile up to the level of the untreated (uncompacted) sample. This may be understood by recalling that the molecular structure of corn starch, having a more linear orientation than potato starch, creates a film with higher tensile strength.
  • a method for treating a compacted paper web to improve its tensile strength and stiffness while further improving its burst and TEA characteristics comprising the steps of: taking paper which is extensible by having been compacted without creping, thus'having improved burst, TEA and tear characteristics, and impregnating under pressure 'both sides of said web with a solution containing starch, while controlling the degree of moisture absorption from said solution by said web; and causing said web to be dried after impregnation with said starch solution; said web containing about Im 10% by weight starch.
  • an extensible paper web containing fibers which have been compacted without creping to provide improved stretch, tear, burst and TEA characteristics, said web further having impregnated under pressure into both surfaces thereof a predetermined amount of finely divided particles of starch to provide substantially increased tensile, TEA and stiffness properties, said web containing about 1 to 10% by weight of starch.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Paper (AREA)
  • Making Paper Articles (AREA)
US295919A 1972-10-10 1972-10-10 External sizing of extensible paper Expired - Lifetime US3908071A (en)

Priority Applications (18)

Application Number Priority Date Filing Date Title
US295919A US3908071A (en) 1972-10-10 1972-10-10 External sizing of extensible paper
GB1928573A GB1405720A (en) 1972-10-10 1973-04-24 External sizing of extensible paper
BR3616/73A BR7303616D0 (pt) 1972-10-10 1973-05-17 Processo e aparelho para o tratamento de uma tela de papel compactada
AU60731/73A AU486816B2 (en) 1972-11-10 1973-09-26 External sizing of extensible paper
SE7313676A SE416063B (sv) 1972-10-10 1973-10-08 Tojbart papper som er utlimmat pa bada sidor med sterkelse samt forfarande for framstellning derav
DE2350483A DE2350483C2 (de) 1972-10-10 1973-10-08 Verfahren und Vorrichtungen zum Verbessern der Eigenschaften von ohne Kreppung verdichtetem Papier
ZA737822*A ZA737822B (en) 1972-10-10 1973-10-08 External sizing of extensible paper
DD173950A DD109243A5 (de) 1972-10-10 1973-10-09
JP48113755A JPS5916039B2 (ja) 1972-10-10 1973-10-09 伸張性紙の外面サイジング
CA182,892A CA1013216A (en) 1972-10-10 1973-10-09 External sizing of extensible paper
NO3915/73A NO144223C (no) 1972-10-10 1973-10-09 Fremgangsmaate til fremstilling av strekkbart papir
FR7336048A FR2202192B1 (de) 1972-10-10 1973-10-09
AR250468A AR200883A1 (es) 1972-10-10 1973-10-10 Metodo para tratar una lamina de papel compactada, aparato para usarse en el mismo y el producto de lamina de papel obtenido
BE136541A BE805909A (fr) 1972-10-10 1973-10-10 Collage exterieur d'un papier extensible
PH15249A PH9752A (en) 1972-10-10 1973-11-22 External sizing of extensible paper
AT1056273A AT333590B (de) 1972-10-10 1973-12-17 Dehnbares papier sowie verfahren und vorrichtung zur herstellung
CA274,716A CA1043556A (en) 1972-10-10 1977-03-25 External sizing of extensible paper
YU172/80A YU41693B (en) 1972-10-10 1980-01-23 Device for treating compressed paper tape

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US295919A US3908071A (en) 1972-10-10 1972-10-10 External sizing of extensible paper

Publications (1)

Publication Number Publication Date
US3908071A true US3908071A (en) 1975-09-23

Family

ID=23139788

Family Applications (1)

Application Number Title Priority Date Filing Date
US295919A Expired - Lifetime US3908071A (en) 1972-10-10 1972-10-10 External sizing of extensible paper

Country Status (16)

Country Link
US (1) US3908071A (de)
JP (1) JPS5916039B2 (de)
AR (1) AR200883A1 (de)
AT (1) AT333590B (de)
BE (1) BE805909A (de)
BR (1) BR7303616D0 (de)
CA (1) CA1013216A (de)
DD (1) DD109243A5 (de)
DE (1) DE2350483C2 (de)
FR (1) FR2202192B1 (de)
GB (1) GB1405720A (de)
NO (1) NO144223C (de)
PH (1) PH9752A (de)
SE (1) SE416063B (de)
YU (1) YU41693B (de)
ZA (1) ZA737822B (de)

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4919758A (en) * 1985-08-23 1990-04-24 International Paper Company Heat treatment of paper products having starch additives
US5223092A (en) * 1988-04-05 1993-06-29 James River Corporation Fibrous paper cover stock with textured surface pattern and method of manufacturing the same
EP0695828A3 (de) * 1994-06-10 1996-12-18 Voith Sulzer Papiermasch Gmbh Einrichtung zur wahlweisen Behandlung einer laufenden Bahn
US6171444B1 (en) 1998-04-22 2001-01-09 Sri International Method and composition for the sizing of paper with a mixture of a polyacid and a polybase
US6197880B1 (en) 1998-04-22 2001-03-06 Sri International Method and composition for coating pre-sized paper using azetidinium and/or guanidine polymers
US6197383B1 (en) 1998-04-22 2001-03-06 Sri International Method and composition for coating pre-sized paper with a mixture of a polyacid and a polybase
US6365003B1 (en) * 1999-02-03 2002-04-02 Voith Sulzer Papiertechnik Patent Gmbh Apparatus and process for processing a material web
US6416628B1 (en) * 1997-12-22 2002-07-09 International Paper Company Method of producing dimensionally stable paper and paperboard products
DE10101866A1 (de) * 2001-01-17 2002-07-18 Voith Paper Patent Gmbh Auftragsvorrichtung
US20030173043A1 (en) * 2000-07-10 2003-09-18 Pekka Koivukunnas Method for calendering tissue paper
US6686054B2 (en) 1998-04-22 2004-02-03 Sri International Method and composition for the sizing of paper using azetidinium and/or guanidine polymers
US20040123966A1 (en) * 2002-04-11 2004-07-01 Altman Thomas E. Web smoothness improvement process
DE102009003065A1 (de) * 2009-05-13 2010-11-18 Voith Patent Gmbh Auftragsvorrichtung
US20120255696A1 (en) * 2011-04-05 2012-10-11 P.H. Glatfelter Company Process for making a stiffened paper
US9133583B2 (en) 2011-04-05 2015-09-15 P.H. Glatfelter Company Process for making a stiffened paper
WO2019005739A1 (en) 2017-06-26 2019-01-03 David Paul Goodrich EXPANDABLE PAPER AND ITS USE IN THE PRODUCTION OF EXTENDED SLOT PACKAGING ENVELOPE AND VACUUM FILLING PRODUCTS
WO2020033275A1 (en) 2018-08-05 2020-02-13 David Paul Goodrich Protective products, such as envelopes, having a unique combination of interior padding of expanded slit sheet paper
WO2020227649A1 (en) 2019-05-08 2020-11-12 Goodrich David P Embossed paper in combination with paper cushioning for shipping envelopes
WO2021163453A1 (en) 2020-02-12 2021-08-19 Goodrich David P Expanded slit sheet void fill dispensing systems and methods
US11440305B2 (en) * 2017-06-26 2022-09-13 David Paul Goodrich Embossed paper in combination with paper cushioning for shipping envelopes
US11623810B2 (en) 2019-10-16 2023-04-11 David Paul Goodrich Slit sheet material dispensing pad
US11702261B2 (en) 2017-06-26 2023-07-18 David Paul Goodrich Expanded slit sheet cushioning products with novel reduced dimension slit patterns
US11834240B2 (en) 2013-09-06 2023-12-05 David P. Goodrich Expanded slit sheet cushioning products with novel alternating expansion patterns
EP4364933A2 (de) 2017-10-12 2024-05-08 David Paul Goodrich Versand- und ausgabebehälter für geschlitztes folienmaterial
US12110159B2 (en) 2017-06-26 2024-10-08 HexcelPack, LLC Expanded slit sheet cushioning products with novel slit pattern and paper properties

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI67586C (fi) * 1981-11-02 1987-12-29 Valmet Oy Foerfarande och anordning i samband med ytlimning av pappersbana och papper tillverkat med foerfarandet och/eller anordningen.
FR2540152B1 (fr) * 1983-01-31 1986-11-21 Gascogne Papeteries Procede de preparation d'une feuille de papier ayant des proprietes mecaniques ameliorees, utile dans le domaine de l'emballage et notamment celui des sacs, et feuille de papier obtenue selon ce procede
JPS63146937U (de) * 1987-03-18 1988-09-28
DE4313628A1 (de) * 1993-04-27 1993-09-30 Voith Gmbh J M Einrichtung zum wahlweisen Behandeln von laufenden Bahnen

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2624245A (en) * 1952-06-11 1953-01-06 Cluett Peabody & Co Inc Modified paper and method for its manufacture
US2999787A (en) * 1957-10-04 1961-09-12 Thilmany Pulp & Paper Company Machine glazed paper
US3293067A (en) * 1963-03-27 1966-12-20 Cons Papers Inc Production of coated paper
US3362869A (en) * 1965-01-12 1968-01-09 Clupak Inc Method of forming machine glazed extensible paper
US3478716A (en) * 1963-03-07 1969-11-18 Kimberly Clark Co Printable paper product having a cellular coating containing pigment and a reaction product of protein and an epoxy resin defining the cell walls
US3533902A (en) * 1969-05-29 1970-10-13 Grace W R & Co Impregnated fibrous materials and process of making the same

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3454463A (en) * 1966-07-12 1969-07-08 Clupak Inc Methods of making newsprint paper
DE1964531C3 (de) * 1969-12-23 1974-10-17 Maizena Gmbh, 2000 Hamburg Verfahren zur Leimung von Papier

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2624245A (en) * 1952-06-11 1953-01-06 Cluett Peabody & Co Inc Modified paper and method for its manufacture
US2999787A (en) * 1957-10-04 1961-09-12 Thilmany Pulp & Paper Company Machine glazed paper
US3478716A (en) * 1963-03-07 1969-11-18 Kimberly Clark Co Printable paper product having a cellular coating containing pigment and a reaction product of protein and an epoxy resin defining the cell walls
US3293067A (en) * 1963-03-27 1966-12-20 Cons Papers Inc Production of coated paper
US3362869A (en) * 1965-01-12 1968-01-09 Clupak Inc Method of forming machine glazed extensible paper
US3533902A (en) * 1969-05-29 1970-10-13 Grace W R & Co Impregnated fibrous materials and process of making the same

Cited By (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4919758A (en) * 1985-08-23 1990-04-24 International Paper Company Heat treatment of paper products having starch additives
US5223092A (en) * 1988-04-05 1993-06-29 James River Corporation Fibrous paper cover stock with textured surface pattern and method of manufacturing the same
US5314584A (en) * 1988-04-05 1994-05-24 James River Corporation Fibrous paper cover stock with textured surface pattern and method of manufacturing the same
EP0695828A3 (de) * 1994-06-10 1996-12-18 Voith Sulzer Papiermasch Gmbh Einrichtung zur wahlweisen Behandlung einer laufenden Bahn
US6051068A (en) * 1994-06-10 2000-04-18 Voith Sulzer Papiermaschinen Gmbh System for selective treatment of a traveling paper web
US6416628B1 (en) * 1997-12-22 2002-07-09 International Paper Company Method of producing dimensionally stable paper and paperboard products
US6686054B2 (en) 1998-04-22 2004-02-03 Sri International Method and composition for the sizing of paper using azetidinium and/or guanidine polymers
US6197383B1 (en) 1998-04-22 2001-03-06 Sri International Method and composition for coating pre-sized paper with a mixture of a polyacid and a polybase
US6197880B1 (en) 1998-04-22 2001-03-06 Sri International Method and composition for coating pre-sized paper using azetidinium and/or guanidine polymers
US6171444B1 (en) 1998-04-22 2001-01-09 Sri International Method and composition for the sizing of paper with a mixture of a polyacid and a polybase
US6365003B1 (en) * 1999-02-03 2002-04-02 Voith Sulzer Papiertechnik Patent Gmbh Apparatus and process for processing a material web
US20030173043A1 (en) * 2000-07-10 2003-09-18 Pekka Koivukunnas Method for calendering tissue paper
US6712930B2 (en) * 2000-07-10 2004-03-30 Metso Paper, Inc. Method for calendering tissue paper
DE10101866A1 (de) * 2001-01-17 2002-07-18 Voith Paper Patent Gmbh Auftragsvorrichtung
US20040123966A1 (en) * 2002-04-11 2004-07-01 Altman Thomas E. Web smoothness improvement process
DE102009003065A1 (de) * 2009-05-13 2010-11-18 Voith Patent Gmbh Auftragsvorrichtung
US9133583B2 (en) 2011-04-05 2015-09-15 P.H. Glatfelter Company Process for making a stiffened paper
US8496784B2 (en) * 2011-04-05 2013-07-30 P.H. Glatfelter Company Process for making a stiffened paper
US20120255696A1 (en) * 2011-04-05 2012-10-11 P.H. Glatfelter Company Process for making a stiffened paper
US11834240B2 (en) 2013-09-06 2023-12-05 David P. Goodrich Expanded slit sheet cushioning products with novel alternating expansion patterns
US11383906B2 (en) 2017-06-26 2022-07-12 David P. Goodrich Extensible paper and its use in the production of expanded slit packaging wrap and void fill products
US12145784B2 (en) 2017-06-26 2024-11-19 HexcelPack, LLC Extensible paper and its use in the production of expanded slit packaging wrap and void fill products
US12110159B2 (en) 2017-06-26 2024-10-08 HexcelPack, LLC Expanded slit sheet cushioning products with novel slit pattern and paper properties
US12023901B2 (en) 2017-06-26 2024-07-02 HexcelPack, LLC Embossed paper in combination with paper cushioning for shipping envelopes
US12221260B2 (en) 2017-06-26 2025-02-11 HexcelPack, LLC Expanded slit sheet cushioning products with novel reduced dimension slit patterns
WO2019005739A1 (en) 2017-06-26 2019-01-03 David Paul Goodrich EXPANDABLE PAPER AND ITS USE IN THE PRODUCTION OF EXTENDED SLOT PACKAGING ENVELOPE AND VACUUM FILLING PRODUCTS
US11440305B2 (en) * 2017-06-26 2022-09-13 David Paul Goodrich Embossed paper in combination with paper cushioning for shipping envelopes
US10669086B2 (en) * 2017-06-26 2020-06-02 David Paul Goodrich Extensible paper and its use in the production of expanded slit packaging and void fill products
US11702261B2 (en) 2017-06-26 2023-07-18 David Paul Goodrich Expanded slit sheet cushioning products with novel reduced dimension slit patterns
US11760548B2 (en) 2017-06-26 2023-09-19 David P. Goodrich Extensible paper and its use in the production of expanded slit packaging wrap and void fill products
EP4364933A2 (de) 2017-10-12 2024-05-08 David Paul Goodrich Versand- und ausgabebehälter für geschlitztes folienmaterial
US12110165B2 (en) 2018-08-05 2024-10-08 HexcelPack, LLC Protective products, such as envelopes, having a unique combination of interior padding of expanded slit sheet paper and exterior lining of embossed paper
EP4310023A2 (de) 2018-08-05 2024-01-24 David Paul Goodrich Schutzprodukte, wie briefumschläge, mit einer einzigartigen kombination aus innenpolsterung aus expandiertem schlitzbogenpapier
US11926461B2 (en) 2018-08-05 2024-03-12 HexcelPack, LLC Protective products such as envelopes having a unique combination of interior padding of expanded slit sheet paper and exterior lining of embossed paper
US10981712B2 (en) 2018-08-05 2021-04-20 David Paul Goodrich Protective products such as envelopes having a unique combination of interior padding of expanded slit sheet paper and exterior lining of embossed paper
WO2020033275A1 (en) 2018-08-05 2020-02-13 David Paul Goodrich Protective products, such as envelopes, having a unique combination of interior padding of expanded slit sheet paper
WO2020227649A1 (en) 2019-05-08 2020-11-12 Goodrich David P Embossed paper in combination with paper cushioning for shipping envelopes
US11623810B2 (en) 2019-10-16 2023-04-11 David Paul Goodrich Slit sheet material dispensing pad
WO2021163453A1 (en) 2020-02-12 2021-08-19 Goodrich David P Expanded slit sheet void fill dispensing systems and methods

Also Published As

Publication number Publication date
YU41693B (en) 1987-12-31
PH9752A (en) 1976-03-12
YU17280A (en) 1983-01-21
DD109243A5 (de) 1974-10-20
JPS4971206A (de) 1974-07-10
DE2350483A1 (de) 1974-04-25
NO144223C (no) 1981-07-15
SE416063B (sv) 1980-11-24
CA1013216A (en) 1977-07-05
AU6073173A (en) 1975-03-27
BE805909A (fr) 1974-02-01
ATA1056273A (de) 1976-03-15
FR2202192B1 (de) 1977-10-07
AR200883A1 (es) 1974-12-27
DE2350483C2 (de) 1982-05-06
GB1405720A (en) 1975-09-10
NO144223B (no) 1981-04-06
ZA737822B (en) 1974-08-28
FR2202192A1 (de) 1974-05-03
JPS5916039B2 (ja) 1984-04-12
AT333590B (de) 1976-11-25
BR7303616D0 (pt) 1974-09-05

Similar Documents

Publication Publication Date Title
US3908071A (en) External sizing of extensible paper
US5753078A (en) Method of making surface coated or impregnated paper or paperboard
US4894118A (en) Recreped absorbent products and method of manufacture
US3014832A (en) Method of fabricating tissue
US6379498B1 (en) Method for adding an adsorbable chemical additive to pulp during the pulp processing and products made by said method
US9347182B2 (en) Methods and apparatus for forming fluff pulp sheets
EP0124496B1 (de) Herstellen von Kraftpapier
AU2001239938A1 (en) Method for adding an adsorbable chemical additive to pulp during the pulp processing and products made by said method
US4040899A (en) Production of high strength packaging papers from straw
JP2006505698A (ja) ウェブの平滑性改善プロセス
US3798121A (en) Wrapped roll press
US2378113A (en) Paper manufacture
JPS6434464A (en) Coating press device and coating method of compression web formed in forming region in paper-making machine
CA2239916C (en) Method of applying dry strength resins for making soft, strong, absorbent tissue structures
US1966458A (en) Method of saturating fibrous stock
CN106715797B (zh) 用于生产纸或纸板的至少一个层的方法以及根据该方法生产的纸或纸板
GB2052586A (en) Drying paper
US1921504A (en) Composite web and method of making the same
US1791248A (en) Felted-cellulose-fiber product
CA1043556A (en) External sizing of extensible paper
US3215589A (en) Two ply printing paper and method of producing the same
DE69007484T2 (de) Verfahren und vorrichtung zur herstellung von glattem und glänzendem papier.
KR800001165B1 (ko) 개선된 종이를 제조하는 방법
US4737242A (en) Apparatus for applying a liquid composition to a fibrous web
FI62157C (fi) Sammanpressad pappersprodukt foerfarande foer dess framstaellning och anordning foer utfoerande av foerfarandet