[go: up one dir, main page]

AU700129B2 - Improving the quality of coated paper - Google Patents

Improving the quality of coated paper Download PDF

Info

Publication number
AU700129B2
AU700129B2 AU32986/95A AU3298695A AU700129B2 AU 700129 B2 AU700129 B2 AU 700129B2 AU 32986/95 A AU32986/95 A AU 32986/95A AU 3298695 A AU3298695 A AU 3298695A AU 700129 B2 AU700129 B2 AU 700129B2
Authority
AU
Australia
Prior art keywords
weight
coating
inorganic pigment
preliminary
paper
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.)
Ceased
Application number
AU32986/95A
Other versions
AU3298695A (en
Inventor
David Frederick Bailey
Ulrika Elofsson
John Claude Husband
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.)
Imerys Minerals Ltd
Original Assignee
ECC International Ltd
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 ECC International Ltd filed Critical ECC International Ltd
Publication of AU3298695A publication Critical patent/AU3298695A/en
Application granted granted Critical
Publication of AU700129B2 publication Critical patent/AU700129B2/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • 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
    • D21H19/80Paper comprising more than one coating
    • D21H19/82Paper comprising more than one coating superposed
    • D21H19/822Paper comprising more than one coating superposed two superposed coatings, both being pigmented
    • 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
    • D21H19/36Coatings with pigments
    • D21H19/44Coatings with pigments characterised by the other ingredients, e.g. the binder or dispersing agent
    • 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
    • D21H19/36Coatings with pigments
    • D21H19/44Coatings with pigments characterised by the other ingredients, e.g. the binder or dispersing agent
    • D21H19/46Non-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
    • 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

Landscapes

  • Paper (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Laminated Bodies (AREA)

Description

1 I P/00/011 Regulation 3.2
AUSTRALIA
Patents Act 1990
ORIGINAL
COMPLETE SPECIFICATION STANDARD PATENT Invention Title: "IMPROVING THE QUALITY OF COATED PAPER" The following statement is a full description of this invention, I .r including the best method of performing it known to the Applicant:- S**t o 0 too: at *4 f -1A- IMPROVING THE QUALITY OF COATED PAPER This invention relates to the improvement of the quality of a coated cellulosic sheet material which is prepared by applying, to a cellulosic sheet material base, two or more mineral pigment-containing coating compositions.
If a high quality printed image is to be applied to a cellulosic sheet material such as paper or cardboard it is generally necessary to apply to the surface at least one coating composition containing one or more mineral pigments such as kaolin clay, calcium carbonate, calcium sulphate, titanium dioxide, barium sulphate, satin white and the like. The application of such a coating composition improves the smoothness, gloss, whiteness and opacity of the surface to which o the printed image is to be applied. In many cases, in order to obtain a final coated surface of the desired quality, it is necessary to apply two or more layers of o 0pigment-containing coating compositions.
20 Generally, in order to receive the maximum return from capital invested in paper coating machinery, it is desirable to run the coating machine at the highest practicable web speed. Also, since the coating compositions consist of pigment, adhesives, and 25 possibly other solid ingredients in suspension in water, it is necessary to remove the water content of the composition by thermal evaporation in order to dry the coating. In order to minimise the consumption of energy for thermal evaporation it is desirable to operate with coating compositions having the highest possible solids concentrations. However, it is found that when a final coating composition of relatively high solids concentration is applied to a base sheet of relatively high water absorbency, there is a tendency, when a doctor blade is used to remove excess coating composition and smooth the coating, for this final
C--
M
coating to be marred by scratches and other defects.
An object of this invention is to provide a method in which two or more coatings are applied to a cellulosic sheet base, and in which it is possible to achieve a final surface of good quality at a relatively high web speed in the coating machine and with a final coating composition of high solids concentration.
It is well known to use water-repellant chemical reagents in the production of cellulosic sheet products. The absorption of water into the sheet product may be controlled by a process known as "sizing". There are generally two main types of sizing process, internal sizing and surface sizing. In internal sizing a water-repellant reagent is mixed with 15 the pulp of cellulosic fibres prior to the formation of 00 the sheet. In surface sizing, the reagent, which is usually starch in this case, is applied to a web of ready formed sheet material, by passing the web through a coating trough known as a "size press". Generally, in surface sizing, both sides of the web are coated with a film of the reagent.
The most commonly used sizing reagent for internal sizing is rosin which is precipitated in a suspension 1 of cellulosic fibres by the addition of aluminium 25 sulphate. However, this treatment reduces the pH of the suspension of fibres to about 4-6 which renders it unsuitable for use when an alkaline filler, such as calcium carbonate, is incorporated into the suspension.
In order to size a cellulosic sheet material containing an alkaline filler, sizing agents have been developed which confer water-repellant properties to the cellulosic fibres at neutral or alkaline pH values.
Examples of these sizing agents include those of the alkyl ketene dimer type which are described in United States Patent Specification No. 2627477, and those of the alkenyl succinic anhydride type which are described -3in United States Patent Specification No. 3102064.
The present invention provides a method of coating a cellulosic sheet material, which method comprises coating the cellulosic sheet material with at least one preliminary inorganic pigment-containing coating composition and then with a final inorganic pigmentcontaining coating composition, wherein there is present in the preliminary coating composition, or in at least one of the preliminary coating compositions, from 0.01 to 0.30% by weight, based upon the weight of the inorganic pigment, of a sizing reagent selected from an alkyl ketene dimer, an alkenyl succinic anhydride or an anionic polyurethane.
The sizing reagent is conveniently an alkyl ketene 15 dimer of the type which is used as an internal size for o paper under alkaline or neutral conditions. Such an o alkyl ketene dimer has the general formula:- t 0
R-CH-C=O
O=C-CH-R
l o where R is an alkyl group having from 8 to 20 carbon •atoms.
The sizing reagent may also be an alkenyl succinic anhydride or an anionic polyurethane.
The inorganic pigment in both the preliminary and the final coating compositions may be chosen from the group consisting of kaolin clay, calcium carbonate, titanium dioxide, calcium sulphate, barium sulphate and satin white. In addition to the inorganic pigment, both the final and the preliminary coating compositions may also include an adhesive for the pigment, preferably from 4% to 20% by weight, based on the weight of the inorganic pigment, of an adhesive for the pigment, which pigment is generally chosen from the group consisting of starches, proteinaceous adhesives such as casein, and latices of, for example, styrene 1 o 7 l EI 04 4-I I I I 1 *o
SO
*r S
S
5* C S S C C S 55
S.
Ce *s S 9* C
S
S -4butadiene rubber or an acrylic polymer. The coating compositions will also generally contain from 0.02% to 1% by weight, based on the weight of the pigment, of a dispersing agent for the inorganic pigment.
5 The invention will now be illustrated by the following Examples, wherein reference is made to Figures 1 to 4 of the accompanying drawings.
EXAMPLE 1 Three coating compositions were prepared for use in providing the first of two coatings applied to a base paper to form a double coated paper. Each composition was prepared according to the general recipe:- Ingredient Parts by Weight Calcium carbonate pigment 100 Adhesive The calcium carbonate pigment was a comminuted natural marble which had a particle size distribution such that 60% by weight consisted of particles having an equivalent spherical diameter smaller than 2pm.
The adhesive used in each of the three compositions was: A 15 parts by weight of starch B 12 parts by weight of starch and 3 parts by weight of latex solids C 10 parts by weight of starch and 5 parts by weight of latex solids The starch was an oxidised corn starch which is marketed by Cerestar under the trade name "AMISOL 05591". The latex contained 50% by weight of styrene butadiene rubber polymer and is marketed by The Dow Chemical Company under the trade name "DOW 950". The amounts of latex used in the recipes given above are 44 4 expressed in terms of the weight of dry polymer solids.
44 S" Each composition was divided into two portions, 1 and 2. To Portion 1 there was added 0.25 parts by weight, on a dry weight basis, per hundred parts by weight of calcium carbonate pigment, of a weakly 20 cationic alkyl ketene dimer which is marketed by the Hercules Corporation under the trade name "AQUAPEL C519". No alkyl ketene dimer was added to Portion 2.
Y*4 Each composition was applied to an unsized, absorbent, woodfree base paper by means of a laboratory paper coating machine of the type described in British Patent Specification No. 1032536 at a paper speed of 400m.min-1. In each case the coating was dried by blowing air over it for 2 minutes.
Each sample of paper coated with a first coating composition was then coated by means of a laboratory bench blade coating apparatus with a second composition having the general formula:- Ingredient Parts by Weight Fine calcium carbonate pigment 100 Latex adhesive 12 Sodium carboxymethyl cellulose 1
I
1 P -6- The fine calcium carbonate pigment was a comminuted natural marble having a particle size distribution such that 95% by weight consisted of particles having an equivalent spherical diameter smaller than 2pm. The latex adhesive was the same as that used for the first coat, and the sodium carboxymethyl cellulose was that marketed by Metsa Serla under the trade name "FINNFIX Each sample of paper coated with each of the six different first coating compositions was divided into a number of portions and the blade pressure in the coating apparatus was varied to give a series of different weights per unit area of the second composition in the range from 8 to 20g.m 2 a £t 15 The coating apparatus was provided with a device f which monitored the rate of drying of the second coating composition by measuring the intensity of light reflected from the surface of the coated paper. The coating immediately after passing beneath the blade was 20 uniformly wet and was therefore highly reflective to light. However, as the coating dried it became duller :0:9 in appearance. An adjustable light source and a detector were mounted above the coating apparatus to give an incident light beam and a measured beam both at an angle of 750 to the normal to the paper. The signal from the detector was applied by way of a voltage measurement interface to an input of a personal computer. The computer was capable of recording up to 15,000 measurements of light intensity per second, so, in order to provide 150 data points per second, the average of 100 such measurements was calculated to give each data point.
For each sample of paper to be coated, measurements of reflected light intensity were made for about 2 seconds on dry paper. The coating apparatus was then started and a drying curve of light intensity I t i against time was recorded by the computer. A typical drying curve takes the form of an initial drop in light intensity to near zero as the blade passes beneath the source and detector, followed by a rapid increase in intensity as the wet coating film is exposed. The intensity will then begin to decrease as the coating dries and will eventually become constant to give a measure of the reflectance of light from the dry coated paper. For each sample of paper, the rate of drying was expressed as a drying parameter, 6. The value of 6 was determined precisely by plotting the rate of change of light intensity with time and reading as 6 the time interval between the maximum positive gradient of the 4.
light intensity/time curve, when the wet coating is 15 first sensed, and the greatest negative gradient of this curve, when the rate of change of light intensity o* is at a maximum and the coating is in a partially dried i state.
Foi each of the six first coating compositions a 20 graph was plotted of drying parameter, 6, against coat weight and the results are shown in Figures 1-3.
Figure 1 gives the results for first coating compositions Al and A2, with and without the alkyl ketene dimer, respectively; Figure 2 gives the results 25 for first coating compositions B1 and B2 and Figure 3 gives the results for first coating compositions Cl and C2.
It will be noted that in every case the drying parameter, 6, and hence the drying time, increases with coat weight, but that, for each adhesive system used in the first coating composition, the second coat dries more slowly when the alkyl ketene dimer is added to the first coating composition.
EXAMPLE 2 Batches of an absorbent woodfree base paper of weight 83g.m-2 were precoated with four different first weight 83g.m were precoated with four different first -8coating compositions, each of which was prepared to the general recipe:- Ingredient Parts by weight Calcium carbonate pigment 100 Oxidised starch adhesive 18 Sodium hydroxide to pH Alkyl ketene dimer see below Water to 62% solids The calcium carbonate pigment was the same as that used in the first coating composition in Example 1.
The amounts of the alkyl ketene dimer in the four compositions were, respectively, 0, 0.02, 0.05 and 0.1 *oao parts by weight of active alkyl ketene dimer per 100 go, 15 parts by weight of the pigment. The alkyl ketene dimer was the same as that used in Example 1. The alkyl I ketene dimer, when used, was added into the composition 0 4 after the starch adhesive at a temperature below 40 0
C.
The first coating composition was applied to the 20 base paper in each case by means of a pilot-scale paper S" coating machine fitted with a roll applicator and a odoctor blade at a web speed of 600m.min-1 and a blade angle of 490. The blade pressure was adjusted to give a coat weight of 10g.m 2 In order to minimise curl of 25 the paper during the second coating step, a first 9 coating composition was also applied to the reverse 2 side of the paper web at a coat weight of 8.5g.m 2 After the first coating composition had been applied to each batch of paper, the surface of the coated paper was calendered by passing it through two nips of a supercalender at a line pressure of 50kN.m-1 at 60 0 C and at a speed of 600m.min-1.
Each sample of paper coated with a first coating composition was then coated with a second coating composition having the general formula:- A i -9- Ingredient Parts by Weight Fine calcium carbonate pigment 100 Styrene butadiene latex 12 Sodium carboxymethyl cellulose 1 Optical brightening agent The fine calcium carbonate pigment, the latex and the sodium carboxymethyl cellulose were the same as those used in Example 1.
The second coat was applied to each batch of precoated paper by means of a pilot-scale paper coating machine fitted with a roll applicator and a doctor blade. The blade pressure was kept constant at a of, suitable value which would give a coat weight of the second coating of 9g.m 2 I O The runnability, or resistance to scratching, of I the second coat was investigated by the following procedure:- A second coat was applied first to a batch of base 20 paper which had been precoated with a first coating composition containing no alkyl ketene dimer. The second coating composition was applied at a web speed of 300m.min I at the highest solids concentration which would permit the application of a coat weight of 9g.m~ 2 The web speed was then increased until scratching was observed at the blade. When scratching was observed, the base paper was changed to a base paper which had been precoated with a first coating composition which contained some alkyl ketene dimer, and a second coat was applied to this paper keeping the second coating composition and the coating machine settings unchanged. If an improvement in the resistance to scratching was observed, the web speed was increased until scratching was observed, or until a web speed of 800m.min-1 was reached.
The second coating composition was then dil' ted t with water by about 1-2% by weight of solids and coated on to the base paper which had been precoated with a first coating containing no alkyl ketene dimer. The procedure was then repeated until no scratching could be detected during the application of a second coat to the base paper which had been precoated with the first coating which contained no alkyl ketene dimer.
The whole procedure was then repeated using the base papers which had been precoated with the first coating compositions which contained different amounts of the alkyl ketene dimer.
The results are set forth in Table 1 below:
DO
4O90 I00 *o to o soee 0 *s 0 *0 0
A~
IN -11- Table 1 Amount of alkyl by weight web speed Observations ketene dimer in solids in (m.min--) first coat (pph) second coat 0 69.0 300 Frequent scratching 0 67.4 300 Slight scratching 0 65.7 300 Slight scratching 0 63.9 300 No scratching 0.02 68.4 300 Slight scratching 0.02 66.8 300 No scratching 0.02 66.8 800 No scratching 0.05 66.6 800 No scratching 0.10 68.6 300 No scratching 0.10 68.6 600 Scratching reappeared 0.10 66.9 600 No ___scratching a *9 9 *9l 9 a.
9 .L.
99 9 9 9o a a 9 90 a 9 a i *9 99.9 9 99c *9 9 9999 9 0 *99 9*9 a 9 99 9 *9 a 9 9* 9 9* Note:- "pph" means parts by weight per weight of pigment.
100 parts by These results show that scratching was most pronounced when a second coating composition was being applied at a high solids concentration (68-69% by weight) on to a base paper which had been precoated with a first coating composition containing no alkyl ketene dimer. The inclusion of only 0.02 parts by weight of alkyl ketene dimer into the first coating composition was sufficient to reduce scratching markedly when a second coating composition was applied at a solids concentration of 68-69% by weight. When a i, -12first coating containing 0.1 parts by weight of alkyl ketene dimer was applied, scratching during the application of a second coating composition was completely eliminated under the same conditions.
EXAMPLE 3 Batches of an absorbent woodfree base paper of 2 weight 94g.m- 2 were precoated with three different first coating compositions having the following recipes:- 1. 100 parts by weight calcium carbonate pigment A; parts by weight oxidised corn starch.
2. 100 parts by weight calcium carbonate pigment B; parts by weight oxidised corn starch; 0.6 part by weight sodium salt of styrene-maleic acid copolymer.
0 15 3. 100 parts by weight calcium carbonate pigment A; parts by weight oxidised corn starch; 0.25 part by weight alkenyl succinic anhydride.
Calcium carbonate pigment A was the same as that used in the first coating composition in Example 1.
20 Calcium carbonate pigment B was a natural marble which was comminuted to a similar particle size distribution as that of calcium carbonate pigment A, but in an aqueous suspension of lower solids concentration and in the absence of a dispersing agent.
The oxidised corn starch was the same as that used in Example 1.
The sodium salt of the styrene-maleic acid copolymer was supplied by Atochem under the trade name "SMA 3000".
The alkenyl succinic anhydride was supplied by Claymore Chemicals Limited under the trade name "CLAYSIZE PR4'.
In each case the oxidised corn starch was added to the coating coposition in the form of a 30% by weight solution which was cooked at 90 0 C for 20 minutes before addition.
-13- In the case of compositions 1 and 3, the cooked starch solution was added to an aqueous suspension containing 78% by weight of calcium carbonate pigment A and a sodium polyacrylate dispersing agent. In the case of composition 3, the alkenyl succinic anhydride was mixed in to the composition immediately before coating.
Composition 2 was prepared by mixing 1333g of a cake containing 75% by weight of the dry calcium carbonate pigment B with 6g of the sodium salt of the styrene-maleic acid copolymer. A deflocculated suspension of the calcium carbonate pigment at a solids concentration of 74.4% by weight was obtained.
Each first coating composition was applied to the 15 base paper by means of the laboratory paper coating machine described in Example 1 at a paper speed of 400m.min and a blade angle of 35°. The blade angle aa 00 SI was adjusted, if necessary, to give a coat weight of 8.0±0.5g.m 2 for each first composition. The coatings 20 were dried by infrared heating for 25 seconds with a *t current of hot air followed by 25 seconds during which cold air was blown over the coated surface.
t" a Each sample of paper coated with a first coating composition was then coated by means of the laboratory bench blade coating apparatus with a second coating S composition having the general formula:- *0 Ingredient Parts by Weight Fine calcium carbonate pigment 100 Latex adhesive 12 Sodium carboxymethyl cellulose 1 The fine calcium carbonate pigment, the latex adhesive and the sodium carboxymethyl cellulose were the same as those used in Example 1. Each sample of paper coated with each of the three different first coating compositions was divided into a number of -14portions and the blade pressure in the bench coating apparatus was varied to give a series of different weights per unit area of the second coating composition in the range from 8 to 20g.m" 2 For each first coating composition a graph was drawn of drying parameter, 6, against coat weight, and the results are shown in Figure 4. It will be seen that for the control first coating composition 1 the drying parameter remains virtually constant with second composition coat weight, while in the case of first compositions 2 and 3 the drying parameter increases steeply with second composition coat weight, indicating that the second coat dries more slowly when a sizing reagent is added to the first composition.
EXAMPLE 4 o. Batches of an absorbent woodfree base paper of a. weight 83g.m 2 were precoated with three different first coating compositions, each of which was prepared .according to the general recipe:-
Q
20 Ingredient Parts by weight Calcium carbonate pigment 100 Oxidised starch adhesive 18 Sodium hydroxide to pH Sizing reagent see below Water to 62% solids The calcium carbonate pigment was the same as that used in the first coating composition in Example 1.
The sizing reagent was an anionic polyurethane marketed by Eka Nobel under the trade name "CYCLOPAL (RTM) A" and the amounts used in the three compositions were, respectively, 0, 0.1 and 0.2 parts by weight of active anionic polyurethane per 100 parts by weight of the pigment. The anionic polyurethane was added into the composition before the starch adhesive.
The first coating composition was applied to the
I
base paper in each case by means of a pilot-scale paper coating machine fitted with a roll applicator and a doctor blade at a web speed of 600m.min-1 and a blade angle of 490. The blade pressure was adjusted to give a coat weight of 10g.m 2 It was not necessary in this case to apply a first coating to the reverse side of the paper web, as the paper coated on one side only was found, after calendering, to have sufficient resistance to curling.
After the first coating had been applied to each batch of paper, the surface of the coated paper was calendered by passing it through two nips of a supercalender at a line pressure of 50kN.m at 60 0
C
S" and at a speed of 600m.min a 15 Each sample of paper coated with a first coating S"r composition was then coated with a second coating Scomposition having the general formula:- Ingredient Parts by Weight Fine calcium carbonate pigment 100 Styrene butadiene latex 12 Sodium carboxymethyl cellulose 1 tea. Optical brightening agent The fine calcium carbonate pigment, the latex and the sodium carboxymethyl cellulose were the same as 25 those used in Example 1.
The second coat was applied to each batch of precoated paper by means of a pilot-scale paper coating machine fitted with a roll applicator and a doctor blade. The blade pressure was kept constant at a suitable value which would give a coat weight of the second coating of 9g.m 2 The runnability, or resistance to scratching, of the second coating was irvestigated by the procedure described in Example 2. The results are set forth in Table 2 below: C- I Y a *a al aI a o a -16- Table 2 Amount of by web speed Observations anionic weight (m.min-) polyurethane in solids in first coat second (pph) coat 0 69.2 500 Frequent scratching 0 69.2 1000 Frequent scratching 0 67.2 500 No scratching 0.1 69.0 500 Slight scratching 0.1 69.0 1000 No scratching 0.2 69,1 300 No scratching 0.2 69.1 1000 No scratching These results show that the inclusion of the anionic polyurethane into the first coating composition at a level of 0.1 part by weight per 100 parts by weight of pigment greatly reduces scratching when the second coating composition is applied at a solids concentration of about 69% by weight.

Claims (8)

1. A method of coating a cellulosic sheet material, which method comprises coating the cellulosic sheet material with at least one preliminary inorganic pigment-containing coating composition and then with a final inorganic pigment-containing coating composition, wherein there is present in the preliminary coating composition, or in at least one of the preliminary coating compositions, from 0.01 to 0.30% by weight, based upon the weight of the inorganic pigment, of a sizing reagent selected from an alkyl ketene dimer, an alkenyl succinic anhydride or an anionic polyurethane.
2. A method according to claim 1, wherein the S; inorganic pigment is kaolin clay, calcium carbonate, 15 titanium dioxide, calcium sulphate, barium sulphate or satin white.
3. 'A method according to claim 1 or 2, wherein the preliminary and/or final coating compositions additionally contain an adhesive.
4. A method according to claim 3, wherein the adhesive is a starch, a proteinaceous adhesive or a polymer latex.. A method according to claim 3 or 4, wherein the adhesive is present in an amount of from 4 to by weight, based on the weight of the inorganic pigment.
6. A method according to any of claims 1 to wherein the preliminary and/or final coating compositions additionally contain a dispersing agent.
7. A method according to claim 6, wherein the dispersing agent is present in an amount of from 0.02 to i% by weight, based on the weight of the inorganic pigment.
8. A method according to claim 1, substantially as described in any of the foregoing Examples.
9. A cellulosic sheet material which has been I 1A coated by a method according to any of claims 1 to 8. Dated this 25th day of May 1998 ECC INTERNATIONAL~ LIMITED BY ITS PATENT ATTORNEYS CARTER SMITH BEADLE 9 9 00 99 9 0 4 09 0.99 9. 0* 9 09 9* 0 9 9 *4 00 4 4 9 9*99 99 49 99 0 *9 9 0009 *9 4 9. C IMPROVING THE QUALITY OF COATED PAPER ABSTRACT There is disclosed a method for improving the ease of application of a final inorganic pigment-containing coating to a cellulosic sheet material which has been coated with at least one preliminary inorganic pigment- containing coating. The method comprises incorporating into the preliminary coating or into at least one of the preliminary coatings, up to 2% by weight, based upon the weight of the inorganic pigment, of a sizing reagent, such as an alkyl ketene dimer. A composition for use in the method is also disclosed. Oti Otte S:" I reli
AU32986/95A 1994-10-14 1995-09-29 Improving the quality of coated paper Ceased AU700129B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9420777 1994-10-14
GB9420777A GB2293991B (en) 1994-10-14 1994-10-14 Improving the quality of coated paper

Publications (2)

Publication Number Publication Date
AU3298695A AU3298695A (en) 1996-04-26
AU700129B2 true AU700129B2 (en) 1998-12-24

Family

ID=10762881

Family Applications (1)

Application Number Title Priority Date Filing Date
AU32986/95A Ceased AU700129B2 (en) 1994-10-14 1995-09-29 Improving the quality of coated paper

Country Status (9)

Country Link
EP (1) EP0707112A1 (en)
JP (1) JPH08183145A (en)
AU (1) AU700129B2 (en)
BR (1) BR9504397A (en)
CA (1) CA2159130A1 (en)
FI (1) FI954803L (en)
GB (1) GB2293991B (en)
NO (1) NO953841L (en)
TW (1) TW305900B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3270104A (en) * 1959-05-21 1966-08-30 Grace W R & Co Vacuum forming of plastic material

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI20022046A0 (en) * 2002-11-18 2002-11-18 Raisio Chem Oy Improvement of paper or cardboard
CN1860270A (en) * 2004-01-26 2006-11-08 王子制纸株式会社 Coated paper for printing
CN101148847B (en) * 2006-09-19 2012-06-27 珠海经济特区红塔仁恒纸业有限公司 Liquid and food packing paper and method for producing the same

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4962072A (en) * 1986-12-18 1990-10-09 The Wiggins Teape Group Limited Pressure sensitive record material
JPH0625999A (en) * 1992-07-06 1994-02-01 New Oji Paper Co Ltd Production of multilayer coated paper

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2627477A (en) 1949-10-06 1953-02-03 Hercules Powder Co Ltd Higher alkyl ketene dimer emulsion
NL282997A (en) 1961-09-08
GB1032536A (en) 1964-05-04 1966-06-08 English Clays Lovering Pochin Improvements in or relating to the coating of paper and the like
SE441457C (en) * 1978-10-30 1990-06-18 Supra Ab MAKE SUBSTITUTE SLAM FOR PREPARING FOR PAPER, CARTON AND LIKE, CONTAINING CALCIUM SULPHATE AS PIGMENT
CA1316957C (en) * 1986-12-18 1993-04-27 John Brian Cooper Pressure sensitive record material
AR244372A1 (en) * 1990-04-11 1993-10-20 Hercules Inc Pretreatment of filler with cationic ketene dimer
HU213655B (en) * 1990-11-19 1997-09-29 Patria Papier & Zellstoff Method for reduction vapour-transmissing capability of paper and paper made by such method
JP2521896B2 (en) * 1991-01-18 1996-08-07 日本製紙株式会社 Inkjet recording sheet
US5270076A (en) * 1991-04-11 1993-12-14 E. I. Du Pont De Nemours And Company Process for coating alkyl ketene dimer on titanium dioxide

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4962072A (en) * 1986-12-18 1990-10-09 The Wiggins Teape Group Limited Pressure sensitive record material
JPH0625999A (en) * 1992-07-06 1994-02-01 New Oji Paper Co Ltd Production of multilayer coated paper

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3270104A (en) * 1959-05-21 1966-08-30 Grace W R & Co Vacuum forming of plastic material

Also Published As

Publication number Publication date
GB2293991A (en) 1996-04-17
JPH08183145A (en) 1996-07-16
NO953841L (en) 1996-04-15
FI954803A7 (en) 1996-04-15
GB9420777D0 (en) 1994-11-30
FI954803A0 (en) 1995-10-09
TW305900B (en) 1997-05-21
FI954803L (en) 1996-04-15
AU3298695A (en) 1996-04-26
CA2159130A1 (en) 1996-04-15
EP0707112A1 (en) 1996-04-17
NO953841D0 (en) 1995-09-28
GB2293991B (en) 1998-06-10
BR9504397A (en) 1997-05-27

Similar Documents

Publication Publication Date Title
US5885340A (en) Quality of multiple coated paper
US3714107A (en) High solids coating composition
US4012543A (en) Coated paper and method of making same
US6284034B1 (en) Pigment materials and their use in coating compositions
US4317849A (en) Process for producing high-gloss coated paper
US4241143A (en) Process for producing highly glossy coated paper
US3578493A (en) High solids coating composition
US4102845A (en) Spread-coating compositions for paper comprising an aqueous dispersion of styrene/butadiene polymer and polyethylene oxide
EP0430391A1 (en) Coated printing material and process for producing the same
WO2000066510A1 (en) Pigment composition for employment in paper coating and coating composition and method employing the same
US3963843A (en) Production of coated paper
US3573236A (en) Paper coating compositions and method of their application
CA2269648A1 (en) Coated printing paper and method of manufacture
AU700129B2 (en) Improving the quality of coated paper
EP0860547A2 (en) Producing gloss papers
US7300509B2 (en) Aqueous pigmented coating formulation providing for improved opacity
US5314753A (en) Printing paper and a process for its manufacture
US20040200593A1 (en) Printing paper and a method for manufacturing the same
CA1145211A (en) Method of producing medium-grade coated paper containing high yield pulps for web offset printing
CA2153182C (en) Coated printing paper
FI98235C (en) Printing paper, method of making it and its use
JPH07119085A (en) Double-sided coated paper manufacturing method
US3546066A (en) Size press coating paper with tio2-starch paste to improve opacity
WO2000066509A1 (en) Pigment composition for paper coating, paper coating using the same and method of coating paper
JP2004091997A (en) Coated paper for printing