EP3177408A1 - Procédé de revêtement en continu d'une bande de substrat fibreux à base de cellulose avec du chlorure d'acide gras - Google Patents

Procédé de revêtement en continu d'une bande de substrat fibreux à base de cellulose avec du chlorure d'acide gras

Info

Publication number
EP3177408A1
EP3177408A1 EP15829002.3A EP15829002A EP3177408A1 EP 3177408 A1 EP3177408 A1 EP 3177408A1 EP 15829002 A EP15829002 A EP 15829002A EP 3177408 A1 EP3177408 A1 EP 3177408A1
Authority
EP
European Patent Office
Prior art keywords
fatty acid
acid chloride
cellulose
fibrous substrate
substrate web
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
EP15829002.3A
Other languages
German (de)
English (en)
Other versions
EP3177408A4 (fr
EP3177408B1 (fr
Inventor
Christian Eichholz
Hubertus KRÖNER
Benjamin SCHMIDT-HANSBERG
Lukas WENGELER
Jochen GATTERMAYER
Nils LAWRENZ
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.)
Delfortgroup AG
Original Assignee
BASF SE
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 BASF SE filed Critical BASF SE
Priority to PL15829002T priority Critical patent/PL3177408T3/pl
Publication of EP3177408A1 publication Critical patent/EP3177408A1/fr
Publication of EP3177408A4 publication Critical patent/EP3177408A4/fr
Application granted granted Critical
Publication of EP3177408B1 publication Critical patent/EP3177408B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • D21H25/00—After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
    • D21H25/02—Chemical or biochemical treatment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05C—APPARATUS FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05C9/00—Apparatus or plant for applying liquid or other fluent material to surfaces by means not covered by any preceding group, or in which the means of applying the liquid or other fluent material is not important
    • B05C9/08—Apparatus or plant for applying liquid or other fluent material to surfaces by means not covered by any preceding group, or in which the means of applying the liquid or other fluent material is not important for applying liquid or other fluent material and performing an auxiliary operation
    • B05C9/12—Apparatus or plant for applying liquid or other fluent material to surfaces by means not covered by any preceding group, or in which the means of applying the liquid or other fluent material is not important for applying liquid or other fluent material and performing an auxiliary operation the auxiliary operation being performed after the application
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D3/00—Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials
    • B05D3/02—Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials by baking
    • B05D3/0254—After-treatment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D3/00—Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials
    • B05D3/04—Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials by exposure to gases
    • B05D3/0406—Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials by exposure to gases the gas being air
    • 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
    • D21H17/03—Non-macromolecular organic compounds
    • D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/11—Halides
    • 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
    • D21H17/03—Non-macromolecular organic compounds
    • D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/14—Carboxylic acids; Derivatives thereof
    • 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
    • D21H19/00—Coated paper; Coating material
    • D21H19/10—Coatings without pigments
    • D21H19/14—Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
    • 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
    • D21H21/00—Non-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
    • D21H21/14—Non-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
    • D21H21/16—Sizing or water-repelling agents
    • 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
    • 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
    • D21H25/04—Physical treatment, e.g. heating, irradiating
    • 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
    • D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
    • D21H27/002—Tissue paper; Absorbent paper
    • 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
    • D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
    • D21H27/08—Filter paper
    • 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
    • D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
    • D21H27/10—Packing paper

Definitions

  • the present invention relates to a process for the continuous coating of a cellulose-based fibrous substrate web with fatty acid chloride and a coating device for continuously coating the fibrous substrate web with a liquid fatty acid chloride composition.
  • cellulose-based pulp substrates such as paper, paperboard or cardboard with water repellents
  • water repellents one way to reduce the penetration of moisture into pulp substrates.
  • the stability of cellulose-based pulp substrates can be at least partially maintained even under the action of moisture.
  • the fatty acid chloride is dissolved in an organic solvent prior to application to a fibrous substrate web.
  • the solvent evaporates in a thermal dryer, the applied fatty acid chloride reacts with the hydroxyl groups of the paper pulp substrate with elimination of hydrogen chloride to covalently bound fatty acid.
  • Safe handling of the solvent is not unproblematic in the solvent-based process and there is danger of explosion at usually high solvent contents.
  • Solvent-free processes for coating with fatty acid chlorides in turn have the disadvantage of poorer hydrophobing properties and of high, not to the fiber substance substrate web bound, fatty acid fractions, which pollutes the production cycle.
  • WO 99/08784 describes a method of treating a solid hydrophilic material, e.g. As paper or glass, with a composition containing a reactive hydrophobing reagent, in particular a fatty acid chloride, which reacts with the hydrophilic material to form covalent bonds, to obtain a hydrophobic impregnation.
  • a solution of the reactive hydrophobization reagent in an organic solvent is applied to the material in such a way that the hydrophobing reagent is deposited on the material in finely divided form, ie in the form of a microdispersion.
  • the material thus treated is subjected to an air flow, wherein the hydrophobizing reagent reacts with the substrate to form a covalent bond and volatile substances, in particular the liberated in the reaction of the hydrophobizing reagent with the substrate hydrogen chloride is removed.
  • the process requires the use of large amounts of organic solvents.
  • US 2013 / 0236647A1 describes a method for treating cellulose-based pulp substrates, such as paper, cardboard or cardboard with fatty acid chloride by means of a gravure coating. After the gravure coating of the cellulose-based fibrous substrate with fatty acid chloride, the cellulose-based fibrous substrate web is passed over a drying cylinder for drying and dried by means of contact drying. Disadvantages are high fatty acid fractions, which are not bound to the cellulose-based fibrous substrate and thus burden the production cycle.
  • the present invention is therefore based on the object to provide an improved process for the continuous coating of a fibrous substrate web with fatty acid chloride, in which the aforementioned disadvantages are largely avoided.
  • the process should lead to products which, with regard to the
  • the hydrophobing and durability of the coating should be comparable to waxes, thus permitting "wax replacement.”
  • the products made by the process of the present invention should meet the requirements for the paper recycling cycle and be recyclable.
  • a process for the continuous coating of a cellulose-based fibrous substrate web with fatty acid chloride comprising the steps of a) predrying a cellulose-based fibrous substrate web to a moisture content according to EN ISO 638: 2008 of less than 5%. in particular less than 4%, particularly preferably not more than 3% or not more than 2%;
  • step b) coating the cellulose-based fibrous substrate web predried in step a) with a liquid fatty acid chloride composition at a relative humidity to DIN EN 20187 of less than 20% RH and a temperature below the boiling point of the liquid fatty acid chloride composition;
  • the fibrous substrate webs produced by the process according to the invention fulfill the requirements of recyclability in conventional paper recycling cycles or improve their recyclability.
  • the products produced by the process according to the invention also have good hydrophobing properties at low application weights of the fatty acid chloride and show good, in particular sufficient strength properties even under and / or after exposure to moisture, for example at 30 minutes exposure to moisture and meet the requirements of test standards. Examples of test standards are the breaking length according to EN ISO 1924 -05/2009, the short-crush test according to DIN 54518 - 03/2004, the Edge Wicking Test
  • the invention therefore provides a process for the continuous coating of a cellulose-based fibrous substrate web with fatty acid chloride, comprising the steps a) to c) as defined above and below.
  • a further subject of the invention is a coating device which is suitable for the continuous coating of a cellulose-based fibrous substrate web with a liquid fatty acid chloride composition by the process according to the invention and which comprises the following components:
  • At least one of the modules of the coating device is encapsulated and has an atmosphere of dry air with a relative humidity according to DIN EN 20187 of less than 20% RH, preferably less than 10% RH, more preferably less than 5% RH.
  • the modules 1 - 3 are arranged so that the cellulose-based pulp substrate web can be continuously passed through the modules in the order given.
  • step a) takes place, in the coating module the coating step b) and in the thermal after-treatment module the non-contact thermal aftertreatment.
  • Another object of the invention is the use of a cellulose-based pulp substrate web, obtainable by the process according to the invention, for the production of corrugated base paper, packaging paper, cardboard, cardboard, tissue paper, tissue, printing paper, writing paper, and combinations thereof.
  • a cellulose-based fibrous substrate web is understood as meaning a cellulose-based substrate which is processed in web form and contains at least one fibrous material based on cellulose as the main constituent.
  • cellulosic fibrous materials include cellulosic fibers, pulp, chemo-thermo-mechanical pulp (CTMP), thermomechanical pulp (TMP), deinked pulp (DIP), wood pulp, groundwood, pulp having hydrophilic properties, and a combination of these.
  • Typical fibrous substrate webs are paper, cardboard and paperboard. The main ingredient of the fibrous substrate webs is the cellulosic fibrous material.
  • Further constituents of the fibrous substrate webs may include fillers, such as mineral and / or organic pigments, fines, in particular hemicelluloses, (Nuan cier) dyes, chemical additives, in particular retention aids, fixing agents, Störstofffworder, (dry) solidifiers, sizing agents, defoamers and other process auxiliaries.
  • Fillers such as mineral and / or organic pigments, fines, in particular hemicelluloses, (Nuan cier) dyes, chemical additives, in particular retention aids, fixing agents, Störstoffffiter, (dry) solidifiers, sizing agents, defoamers and other process auxiliaries.
  • Cellulose-based fibrous substrate webs may be uncoated or coated.
  • the coatings may typically be a coating with a conventional starchy paper coating.
  • no cellulose-based fiber substrate webs are used, which have been previously treated with polyvinyl alcohol.
  • Polyvinyl alcohol is understood here and below as meaning partially hydrolyzed polyvinyl acetates, in particular those having a degree of hydrolysis of> 80%.
  • fatty acid chlorides are understood as meaning chlorides of aliphatic monocarboxylic acids which generally have at least 6, in particular at least 8, carbon atoms.
  • the monocarboxylic acids have 12 to 26 carbon atoms.
  • the fatty acids can be saturated or unsaturated.
  • they are fatty acid chlorides of saturated aliphatic monocarboxylic acids, in particular saturated aliphatic fatty acid chlorides containing 12 to 26 carbon atoms, such as the fatty acid chlorides myristic acid, palmitic acid, margaric acid, stearic acid, arachic acid or behenic acid and mixtures thereof.
  • liquid fatty acid chloride composition is understood to mean a fatty acid chloride composition which is flowable at processing temperatures and can be applied to a substrate by conventional application processes with the fatty acid chloride composition.
  • Typical viscosities of liquid fatty acid chloride compositions are in the range of 0.1 to 5000 mPa ⁇ s, in particular in the range of 0.2 to 50 mPa ⁇ s. The determination of the viscosities is carried out according to DIN53019 - 09/2008.
  • the predrying of the cellulose-based fibrous substrate web in step a) takes place by customary drying methods, for example by convection drying, in particular with impact jet dryers.
  • Another drying method is contact drying, for example with drying cylinders on which the cellulose-based fibrous substrate web is guided.
  • drying by radiation drying, such as infrared radiators. Preference is given to convection drying.
  • the cellulose-based fibrous substrate web is adjusted to a moisture content according to EN ISO 638: 2008 of less than 5%, in particular less than 4%, particularly preferably maximum 3% or at most 2%, ie a dry content> 95%, in particular> 96%, particularly preferably dried of at least 97% or at least 98%.
  • a pre-drying module with dry air preferably with a relative humidity to DIN EN 20187 of less than 20% RH, is flowed through in particular, and the cellulose-based fibrous substrate web is thus cooled to a moisture content according to EN ISO 638: 2008 of less than 5%.
  • a moisture content according to EN ISO 638: 2008 of less than 5%.
  • less than 4%, particularly preferably not more than 3% or not more than 2% ie a dry content> 95%, in particular> 96%, particularly preferably at least 97% or at least 98% dried.
  • the cellulose-based fibrous substrate web is pre-dried in step a) to a moisture content according to EN ISO 638: 2008 of less than 5%, in particular less than 4%, particularly preferably not more than 3% or not more than 2%.
  • the cellulose-based fibrous substrate web after step a) has a moisture content of at least 0.1% or at least 0.2% or at least 0.5%.
  • step a) is carried out in an encapsulated atmosphere with a dry air stream having a relative humidity to DIN EN 20187 of less than 20% RH, preferably less than 10% RH, more preferably less than 5% RH.
  • a dry air stream having a relative humidity to DIN EN 20187 of less than 20% RH, preferably less than 10% RH, more preferably less than 5% RH.
  • an encapsulated atmosphere is meant an atmosphere which is isolated from the ambient atmosphere, ie, which is encapsulated and therefore may have other atmospheric conditions.
  • the encapsulated atmosphere is usually designed as a housing and flows through a pleasure current.
  • the air flow has a humidity which is below the above-mentioned relative humidity and typically ranges from 0 to 20% RH.
  • the air flow used has a temperature in the range of 20 to 150 ° C at a volume of 0.1 to 100 m 3 per 1 m 2 of paper, or from 0.1 to 100 m 3 / h per 1 m 2 / h production rate, preferably at a volume of 1 to 10 m 3 per 1 m 2 of paper.
  • the coating in step b) is preferably carried out such that a total application in the range of 0.1 to 10 wt .-%, in particular 0.1 to 5 wt .-%, based on fatty acid chloride per g / m 2 basis weight of the cellulose based pulp substrate web, results.
  • the amount of fatty acid chloride applied is such that the fatty acid chloride content is in the range from 0.1 to 10% by weight, in particular in the range from 0.1 to 5% by weight, based on the dry mass of the cellulose based fibrous substrate web lies.
  • the liquid fat Apply acid chloride composition in an amount such that the applied amount of fatty acid chloride in the range of 0.1 to 10 g / m 2 , in particular in the range of 0.1 to 5 g / m 2 .
  • step b) of the cellulose-based fibrous substrate web precoated in step a) with a liquid fatty acid chloride composition is carried out by applying a layer of the liquid fatty acid chloride composition to the cellulose-based fibrous substrate web.
  • Conventional application methods are, in particular, rolling application, roller application, curtain application, spray application,
  • the coating module has at least one device for applying the fatty acid chloride composition to the cellulose-based fibrous substrate web, e.g. a device for a rolling application, roller application, curtain application, spray application or coating application, in particular a device for a roller application.
  • a device for a rolling application, roller application, curtain application, spray application or coating application e.g. a device for a roller application.
  • the following statements relate both to step b) and to the coating module.
  • step b) is configured as a roller application method and in particular as an offset-engraving method.
  • the liquid fatty acid composition is taken up with a metering roll rotating in a sump containing the liquid fatty acid chloride composition and transferred to a transfer roll in contact with the metering roll.
  • the liquid fatty acid chloride composition is transferred to the pre-dried cellulose-based pulp substrate web which passes between the transfer roll and a pulp substrate support roll.
  • the transfer roller can also be preceded by further rollers which regulate the leveling of the application film.
  • the surface of the metering roll has a multiplicity of depressions, in particular wells, in which the liquid fatty acid composition can be absorbed.
  • the number and volume of wells determines what amount of liquid fatty acid composition can be taken up by the metering roll and then delivered to the transfer roll.
  • the amount dispensed from the metering roll onto the transfer roll determines the layer thickness of the applied liquid fatty acid composition on the transfer roll.
  • the layer thickness of the liquid fatty acid composition determines the amount that can be transferred from the transfer roll to the cellulose-based fibrous substrate web.
  • Further parameters which determine the transfer of liquid fatty acid composition are the diameters, peripheral speeds, spacings and contact forces between the metering and / or transfer roll.
  • the coating in step b) is carried out with a roller application method, in particular an offset-engraving method.
  • the coating in step b) of the cellulose-based fibrous substrate web predried in step a) is carried out with the liquid fatty acid chloride composition at a relative humidity to DIN EN 20187 of less than 10% RH, particularly preferably less than 5% RH.
  • the main component of the liquid fatty acid chloride composition comprises a fatty acid chloride selected from aliphatic monocarboxylic acid chlorides of 6 to 26 carbon atoms, preferably 16 to 20 carbon atoms, and mixtures thereof.
  • the fatty acid chloride is selected from aliphatically saturated fatty acid chlorides having 6 to 26 carbon atoms, preferably 16 to 20 carbon atoms, and mixtures thereof.
  • the liquid fatty acid chloride composition contains at least 5% by weight of fatty acid chloride, preferably 50% by weight of fatty acid chloride, especially at least 90% by weight of fatty acid chloride, each based on the total weight of the fatty acid chloride composition.
  • the liquid fatty acid chloride composition contains greater than 95% by weight of fatty acid chloride, based on the total weight of the fatty acid chloride composition.
  • the liquid fatty acid chloride composition contains less than 10% by weight, in particular less than 5% by weight, of organic solvents having a boiling point below 150 ° C.
  • step b) is carried out in an encapsulated atmosphere with a dry air stream having a relative humidity to DIN EN 20187 of less than 20% RH, preferably less than 10% RH, more preferably less than 5% RH.
  • the encapsulated atmosphere is achieved in particular by an enclosure, which flows through an air flow.
  • the relative humidity of the airflow will be the above mentioned values and can also be lower.
  • the air flow used often has a temperature in the range of 10 to 80 ° C.
  • step b) takes place at temperatures in the range of 10 to 150 ° C, in particular in the range of 20 to 120 ° C.
  • the cellulose-based pulp substrate web will be tempered, e.g. to temperatures in the range of 40 to 120 ° C, in particular in the range of 50 to 100 ° C.
  • the thermal treatment in step c) of the cellulose-based fibrous substrate web coated in step b) with a liquid fatty acid chloride composition can be carried out with conventional non-contact or non-contact drying devices, such as, for example, radiation dryers and / or convection dryers.
  • the thermal treatment is preferably carried out with radiation dryers, in particular infrared radiation dryers.
  • the thermal after-treatment module has at least one device for contactless or contactless drying, in particular at least one radiation dryer, and especially at least one infrared radiation dryer. The following statements relate both to step c) and to the aftertreatment module.
  • a thermal aftertreatment with infrared radiation dryers is carried out at low numbers of air changes in the range of 0 to 20 air changes per hour or in the range of 0 to 20 m 3 / h air volume flow per 1 m 3 of drying volume.
  • Infrared radiation drying typically employs radiation having wavelengths in the range of 780 to 5000 nm.
  • a radiator for radiation drying are usually electrically and / or gas-heated radiator with a power in the range of 5 to 50 W / m 2 is used.
  • the radiation drying causes a reduction in viscosity of the applied liquid fatty acid chloride composition, wherein a loss of substance of the fatty acid chloride composition due to evaporation due to low air exchange rates only to a small extent, if any takes place. With lowered viscosity, the liquid fatty acid chloride composition can penetrate more effectively into the cellulose-based pulp substrate web.
  • step c) is carried out in an encapsulated atmosphere with a dry air stream having a relative humidity to DIN EN 20187 of less than 20% RH, preferably less than 10% RH, more preferably less than 5% RH.
  • the encapsulated atmosphere is achieved in particular by enclosing.
  • the relative humidity of the air flow will usually not exceed the above values and may be lower.
  • the air stream overflows the Cellulose-based substrate web.
  • the cellulose-based substrate web has a temperature in the range of 20 to 120 ° C at low air change rates in the range of 0 to 20 air changes per hour.
  • the coated and thermally treated cellulose-based fibrous substrate web obtained from step c) undergoes, as a further step d), a post-treatment under a dry air atmosphere with a relative humidity to DIN EN 20187 of less than 20% RH.
  • the cellulose-based fibrous substrate webs coated by the process according to the invention are used, for example, in corrugated board production and are in particular processed into fruit / vegetable trays, stacking crates, water-repellent / solid packaging crates.
  • base papers to be coated with the fatty acid chloride composition for example, all types of paper, preferably liners, in particular liners, kraft liners, testliners, corrugating medium and Schrenz, are used.
  • Tissue papers in particular having a basis weight in the range from 10 to 100 g / m 2
  • the papers may be coated or uncoated. If the papers are coated, they are in particular coatings of materials which contain hydroxyl groups, for example a starchy paper coating.
  • FIG. 1 shows an enlarged detail of FIG. 2 with the modules of the method according to the invention used
  • FIG. 2 schematically shows a modular arrangement of the method according to the invention
  • FIG. 3 schematically shows an embodiment of a coating module according to the invention as a three-roller coater.
  • FIG. 1 shows an enlarged detail of FIG. 2 with inserted modules of the method according to the invention.
  • the cellulose-based fibrous substrate web undergoes preliminary drying in a pre-drying module B, in particular to a dry content of less than 10% according to EN ISO 538: 2008.
  • a coating module C the predried cellulose-based fibrous substrate web is coated with a liquid fatty acid chloride composition, in particular, a three-roller coater is used for the coating by the engraving method.
  • a first thermal after-treatment module D is in particular designed as a jet dryer and heats the cellulose-based fibrous substrate web coated with the liquid fatty acid chloride composition, in particular with infrared radiation.
  • FIG. 2 schematically shows a modular arrangement of the method according to the invention.
  • the cellulose-based fibrous substrate web passes through the modules listed below.
  • a development module A the cellulose-based fibrous substrate web is in particular unwound from a (paper) roll. Thereafter, the cellulose-based pulp substrate web undergoes pre-drying in the pre-drying module B.
  • the coating module C the predried cellulose-based fibrous substrate web is coated with a liquid fatty acid chloride composition. stratified and tempered in the first thermal post-treatment module D.
  • a second thermal post-treatment module E the coated cellulose-based fibrous substrate web is adjusted to the temperature conditions desired for further processing.
  • the second thermal aftertreatment module E serves as a kind of lock for delimiting a dry atmosphere in the modules B to E to a humid ambient air atmosphere, for example.
  • the arrangement of the second thermal post-treatment module E is optional.
  • the coated cellulose-based fibrous substrate web is wound up in a take-up module F.
  • the modules B to E are supplied with a dry air supply G.
  • the dry air After the dry air has flowed through the modules B to E, starting from the dry air supply G, it is discharged via an air discharge J into the atmosphere via one or more scrubber module (s) H, in which residues of hydrochloric acid are washed out ,
  • the wind-up module F is perfused with atmospheric air via an ambient air supply I, then passed through one or more scrubber module (s) H and then via the air discharge J into the atmosphere.
  • FIG. 3 schematically shows an embodiment of the coating module C according to the invention as a three-roller coater.
  • the coating of a cellulose-based fibrous substrate web 7, in particular a paper, paperboard or board web takes place in contact operation according to the offset engraving method.
  • a liquid fatty acid chloride composition is conveyed into a drinking trough 4.
  • a metering roller 1 runs in the impregnation tank 4 .
  • the metering roller 1 is, for example, a ceramic-coated, laser-engraved roller with a small specific cell volume in the range of 1 to 10 ⁇ m depth of well.
  • the metering roller 1 depending on the set parameters, such as the cell volume and the rotation speed, delivers a certain amount of fatty acid chloride composition out of the impregnation tank 4 and transfers it to a transfer roller 2, wherein on the transfer roller 2 a layer of the fatty acid chloride composition with one forms certain layer thickness.
  • This layer of the fatty acid chloride composition is transferred from the transfer roller 2 as a coated film 6 to the cellulose-based fibrous substrate web 7, whereby the cellulose-based fibrous substrate web 7 is passed around a fibrous substrate support roller 3. Excess fatty acid chloride composition is collected in a sump 8 and passed into a waste container 9. Examples
  • This fatty acid chloride composition consists of 50% by weight of palmitoyl chloride (CAS number: 112-67-4) and 50% by weight of stearoyl chloride (CAS number: 1 12-76-5).
  • the base paper used in the examples was a brown, unsized testliner from Thurpapier Model Management AG in Weinfelden and had a basis weight of 130 g / m 2 and a Cobbßo value of 159 g / m 2 .
  • palmitoyl chloride (CAS number: 1 12-67-4) from BASF SE was used.
  • a fatty acid chloride composition consisting of 50% by weight of palmitoyl chloride and 50% by weight of steroaryl chloride (CAS number: 1 12-76-5) can also be used.
  • the base paper used in the examples was a brown, unsized testliner from Thurpapier Model Management AG in Weinfelden and had a basis weight of 130 g / m 2 and a Cobbßo value of 159 g / m 2 .
  • the raw paper was pre-dried by means of contact drying at 60 ° C. and about 5% RH to a dry content of> 96% (according to EN ISO 638: 2008).
  • the dried base paper was coated with Fetiklareehlorld at a speed of 5 m / min using a roller applicator (ZIL2140 Zehntner-ink-Lox).
  • the gravure roller had 180 rasters per cm at an angle of 45 ° and a specific cell volumes of 3.8 cm 3 / m 2 .
  • the contact pressure of the engraving machine on the transfer roller was 56 N / m.
  • the rubber transfer roller had a Shore A hardness of 40 and was pressed against the paper substrate with a line force of 152 N / m.
  • the coating weight was 1 to 3 g / m 2 .
  • the coated paper substrate was then thermally treated with two Krelus IR emitters (G7-50-2.5) for 12 seconds at 42 kW / m 2 .
  • the treatment of the raw paper was carried out analogously to experimental design 1 with the difference that the base paper was pre-dried by contact drying at 1 10 ° C and ca, 5% RH to a residual moisture content of 1, 7% (according to EN ISO 638: 2008).
  • the paper thus treated had a Cobb ⁇ o value of 19 g / m 2 on the coated front side and a Cobb ⁇ o value of 72 g / m 2 on the back side.
  • Example 2 comparativative example
  • the treatment of the base paper with the fatty acid chloride was carried out analogously to experimental setup 1 with the difference that the base paper was not dried and had a moisture content of 5.9%.
  • the paper thus treated had a Cobbßo value of 20 g / m 2 on the coated front side and a Cobbßo value of 86 g / m 2 on the back side.
  • the higher moisture content in the base paper leads to a poorer penetration of the fatty acid chloride into the paper and thus to a poorer product quality.
  • the treatment of the base paper with the fatty acid chloride was carried out analogously to experimental setup 1 with the difference that the paper was pre-dried for 1 min at 105 ° C. in a forced-air drying oven.
  • the paper thus treated had on the coated front side of a Cobbßo value of 18 g / m 2 and on the back on a Cobbßo- value of 18 g / m 2.
  • the base paper was coated with a 20% aqueous Polyvinyalkohol solution (Mowiol 4-98, degree of hydrolysis> 98%) by coating on a spreading table of Eilensen GmbH with a Rakei Nr, 2 and a coating speed of 5 ° at 25 ° C with a one-ply surface application of 5 g / m 2 coated.
  • the resulting paper was dried at 105 ° C for 24 hours.
  • the treatment of the coated base paper with the fatty acid chloride was carried out on the polyvinyl alcohol-coated side in analogy to Example 3.
  • the paper thus treated had a Cobb ⁇ o value of 4 g / m 2 on the coated front side and a Cobb ⁇ o value on the back side of 58 g / m 2 .

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Biochemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Paper (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
  • Coating Apparatus (AREA)
  • Materials Applied To Surfaces To Minimize Adherence Of Mist Or Water (AREA)

Abstract

La présente invention concerne un procédé de revêtement en continu d'une bande de substrat fibreux à base de cellulose avec du chlorure d'acide gras, le procédé comprenant les étapes suivantes a) effectuer un pré-séchage d'une bande de substrat fibreux à base de cellulose pour atteindre une siccité selon la norme EN ISO 638:2008 inférieure à 10%; b) revêtir la bande de substrat fibreux à base de cellulose, pré-séchée à l'étape a), avec une composition de chlorure d'acide gras liquide à une humidité relative de l'air selon la norme DIN EN 20187 de moins de 20% HR et à une température inférieure au point d'ébullition de la composition de chlorure d'acide gras liquide; c) traiter thermiquement la bande de substrat fibreux à base de cellulose munie du revêtement obtenu à l'étape b).
EP15829002.3A 2014-08-06 2015-08-06 Procédé de revêtement en continu d'une bande de substrat fibreux à base de cellulose avec du chlorure d'acide gras Active EP3177408B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL15829002T PL3177408T3 (pl) 2014-08-06 2015-08-06 Sposób ciągłego powlekania chlorkiem kwasu tłuszczowego wstęgi podłoży włóknistych na bazie celulozy

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP14180103 2014-08-06
PCT/IB2015/055961 WO2016020866A1 (fr) 2014-08-06 2015-08-06 Procédé de revêtement en continu d'une bande de substrat fibreux à base de cellulose avec du chlorure d'acide gras

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EP3177408A1 true EP3177408A1 (fr) 2017-06-14
EP3177408A4 EP3177408A4 (fr) 2018-04-11
EP3177408B1 EP3177408B1 (fr) 2020-04-29

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US (1) US20170241080A1 (fr)
EP (1) EP3177408B1 (fr)
JP (1) JP6636501B2 (fr)
KR (1) KR102193503B1 (fr)
CN (1) CN106573268B (fr)
BR (1) BR112017002040B1 (fr)
ES (1) ES2808674T3 (fr)
MX (1) MX2017001636A (fr)
PH (1) PH12017500194A1 (fr)
PL (1) PL3177408T3 (fr)
PT (1) PT3177408T (fr)
WO (1) WO2016020866A1 (fr)

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CN107709666B (zh) * 2015-06-29 2021-03-12 斯道拉恩索公司 用于使纤维素基底疏水化的方法
KR102035571B1 (ko) * 2017-12-21 2019-11-26 한국기초과학지원연구원 친수성 표면의 방수화 처리 방법 및 친수성 표면의 방수처리용액
KR101974895B1 (ko) * 2018-10-04 2019-05-07 강원대학교산학협력단 압착 가열 기상 그라프팅 소수화 장치 및 이를 이용하여 제조한 내열수성 종이 및 유흡착 종이
SE543029C2 (en) * 2018-11-16 2020-09-29 Stora Enso Oyj Method for hydrophobizing a cellulose substrate by utilizing a fatty acid halide
SE543479C2 (en) * 2019-07-09 2021-03-02 Stora Enso Oyj Bio-barrier coated paperboard and laminates thereof
SE1951393A1 (en) * 2019-12-04 2021-06-05 Stora Enso Oyj Water-resistant cellulose-based substrate with improved repulpability
SE544899C2 (en) * 2020-02-21 2022-12-27 Stora Enso Oyj Water-resistant multilayered cellulose-based substrate
SE544101C2 (en) * 2020-05-13 2021-12-21 Stora Enso Oyj Water-resistant mineral-coated cellulose-based substrate grafted with fatty acid halide and method for its manufacturing
SE544175C2 (en) * 2020-06-24 2022-02-22 Stora Enso Oyj Water-resistant paper or paperboard
US20230265613A1 (en) * 2020-08-13 2023-08-24 Cellulotech Inc Process for acylation of a hydroxylated solid material
AU2020480101A1 (en) * 2020-12-01 2023-07-13 Cellulotech Inc Method and device for acylating a moving hydroxylated material
FR3135980A1 (fr) * 2022-05-31 2023-12-01 Cellulotech Inc. Procédé d’acylation d’un matériau solide hydroxylé

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JP2937658B2 (ja) * 1992-10-02 1999-08-23 日華化学 株式会社 故紙の再生処理方法
FR2767270B1 (fr) * 1997-08-14 2000-02-11 Daniel Gamain Procede de traitement en phase gazeuse d'un materiau solide pour le rendre hydrophobe, materiau obtenu et applications
DE19841767A1 (de) * 1998-09-11 2000-03-16 Voith Sulzer Papiertech Patent Trockenpartie sowie Konvektionstrockner für eine solche Trockenpartie
PT1976817E (pt) * 2006-01-03 2011-07-25 Hercules Inc Preparação de dímeros de alquil-ceteno
FR2912427B1 (fr) * 2007-02-14 2009-12-11 Soprema Procede de fabrication d'une armature de renfort et d'une membrane d'etancheite comprenant une telle armature et produits obtenus.
DE202008018404U1 (de) * 2007-10-11 2013-09-20 manroland sheetfed GmbH Thermoluft-Trocknungseinrichtung zur Bewerkstelligung der Trocknung eines Bedruckstoffes
FR2925910B1 (fr) * 2007-12-26 2010-02-12 Centre Nat Rech Scient Film aux proprietes barrieres a l'eau, aux graisses, au gaz et a la vapeur d'eau
JP4676564B1 (ja) * 2009-12-28 2011-04-27 大王製紙株式会社 ティシュペーパー製品の製造方法及び製造設備
FR2967363B1 (fr) * 2010-11-16 2012-11-30 Centre Nat Rech Scient Machine et procede de traitement par greffage chromatogenique d'un substrat hydroxyle
FR2990694B1 (fr) * 2012-05-15 2014-05-30 Centre Nat Rech Scient Procede d'enduction de supports solides
US9139661B2 (en) * 2012-06-25 2015-09-22 Yagna Limited Methods for biocompatible derivitization of cellulosic surfaces

Also Published As

Publication number Publication date
PT3177408T (pt) 2020-07-24
BR112017002040A2 (pt) 2017-12-26
ES2808674T3 (es) 2021-03-01
PH12017500194B1 (en) 2017-06-28
KR20170039179A (ko) 2017-04-10
US20170241080A1 (en) 2017-08-24
EP3177408A4 (fr) 2018-04-11
PH12017500194A1 (en) 2017-06-28
MX2017001636A (es) 2017-09-01
JP2017530855A (ja) 2017-10-19
BR112017002040B1 (pt) 2022-04-05
WO2016020866A1 (fr) 2016-02-11
EP3177408B1 (fr) 2020-04-29
KR102193503B1 (ko) 2020-12-22
CN106573268A (zh) 2017-04-19
PL3177408T3 (pl) 2020-11-02
JP6636501B2 (ja) 2020-01-29
CN106573268B (zh) 2019-11-19

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