AU636059B2 - Soft paper of high strength and method for production thereof - Google Patents

Soft paper of high strength and method for production thereof Download PDF

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Publication number
AU636059B2
AU636059B2 AU83775/91A AU8377591A AU636059B2 AU 636059 B2 AU636059 B2 AU 636059B2 AU 83775/91 A AU83775/91 A AU 83775/91A AU 8377591 A AU8377591 A AU 8377591A AU 636059 B2 AU636059 B2 AU 636059B2
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pulp
paper
cellulosic
fibre
weight
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AU8377591A (en
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Leif Elsby
Margareta Oijerfeldt
Anette Thyberg
Marie Turunen
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Nouryon Pulp and Performance Chemicals AB
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Eka Nobel AB
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H11/00Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/10Mixtures of chemical and mechanical pulp

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  • Making Paper Articles (AREA)
  • Sanitary Thin Papers (AREA)

Abstract

A paper having an advantageous combination of softness and strength is disclosed, which is based on a mixture of cellulosic pulps and in which a) 55-90% by weight, of the total amount of cellulose fibres consists of a hardwood pulp, a waste paper pulp or a mechanical or semi-mechanical cellulosic pulp, or a mixture thereof, having a drainage resistance below 25<0>SR, and b) 10-45% by weight, of the total amount of cellulose fibres consists of a sulphite pulp and/or sulphate pulp based on softwood and having a drainage resistance exceeding 30<0>SR. The paper can be produced by preparing a stock from the cellulosic pulps a) and b) in the above amounts, whereupon the stock is taken up on a wire, and is drained and dried in per se known manner.

Description

P/001011 2815191 Regulation 3.2(2)
AUSTRALIA
Patents Act 1990 63605
ORIGINAL
COMPLETE SPECIFICATION STANDARD PATENT Application Number: Lodged: 00 a Invention Title: SOFT PAPER OF HIGH STRENGTH AND METHOD FOR PRODUCTION THEREOF The follow,.ing statement is a full description of this invention, including the best method of performing it known to :-us 0 5505S S
S
*.SS 6.
S
1 SOFT PAPER OF HIGH STRENGTH AND METHOD FOR PRODUCTION THEREOF The present invention concerns a soft but also strong paper which is based on a mixture of a hardwood pulp, a waste paper pulp or a mechanical or semi-mechanical cellulosic pulp, or a mixture thereof, and a sulphate pulp and/or sulphite pulp based on softwood; as well as a method for the production thereof.
Usually, it is required that a soft paper, e.g. tissue paper, should be not only soft, but also strong. To achieve a satisfactory compromise between qualitative properties, such as softness and strength, on the one hand, and financial considerations, on the other hand, one has mixed different cellulosic pulps of differing origins and properties when producing soft paper, for example tissue paper. Generally, one main component is long-fibred S**l to impart strength to the paper, while the other main component is short-fibred to give the paper its softness and the desired absorption qualities.
The long-fibred pulp is usually based on softwood, such as pine wood or spruce wood, which has been chemically delignified by a sulphate or sulphite process. The 6g short-fibred pulp is generally based on hardwood, such as birch wood, eucalyptus wood, aspen wood or oak wood, which has been delignified by a sulphate process. At times, the cellulosic raw material may to a certain extent be based also on mechanical and semi-mechanical pulp, such as groundwood pulp, TMP and CTMP pulp and waste paper pulp.
30 The long-fibred pulps, for example chemical pulp from spruce wood or pine wood, has a fibre length of about 3mm and a fibre width of about 0.04 mm. A short-fibred pulp based on birch sulphate has an average fibre length of 1.3 mm and a fibre thickness which is about half of thlit of conifer fibres. The proportion of short fibres, so-called fines, is high. Mechanical, semi-mechanical and waste fibre pulp have a fibre length which usually is shorter than that of chemical pulp from spruce wood or pine wood. The proportion of fines may be high. When producing soft paper, it is desirable that the proportion of fines be kept as low as possible in order to reduce dusting.
To impart suitable paper-forming properties to the pulp, the latter is usually ground, e.g. in a beater or a refiner, which results in a paper of higher tensile strength. The degree of grinding is generally measured as the drainage resistance of the pulp according to Schopper-Riegler (SCAN C 19:65) which is the definition of the term °SR as used herein. The °SR value increases with increasing grinding of the pulp. Already during the production of cellulosic pulp for paper, the pulp usually is refined to 10-20 0
SR.
When making tissue paper, the different pulps can be refined separately or in mixture. Grinding not only results in a higher tensile strength, but also in a higher tensile stiffness of the paper. Table 1 below illustrates this fact in connection with hand-made sheets of a mixture of 70% birch sulphate and 30% pine sulphate pulp. In TAPPI Journal 66 1983, pp 97-99, H.
Hollmark states that the tensile stiffness of a paper correlates extremely well with softness determined by means of panel tests. The lower the "3nsile stiffness, the softer the paper, according to the test panel.
i US Patent 2,706,155 discloses a method for producing soft paper, S 20 the starting material being a mixture of 25-70% oak wood pulp, the remainder being softwood pulp. The oak wood pulp is essentially unground, whereas the softwood pulp is refined. In an example, the softwood sulphate pulp was ground to 500 ml CSF, which corresponds to 25 0 SR, and was then mixed with equal parts of essentially unrefined oak wood sulphate pulp to achieve the desired combination of tensile strength, tearing strength, softness and adsorption q o t .qualities of the paper.
o•i 3 Soviet Patent 779,483 discloses the production of a paper from 40-60% bleached softwood sulphate pulp, 30-54% chemically refined aspen wood pulp and 5-15% birch wood sulphate pulp which has been further chemically refined to increase the strength of the paper.
An article in the Soviet periodial Sb. Tr. TsNIIB No. 15: 72-77 (1978) deals with hand-made sheets produced from softwood sulphite pulp, softwood sulphate pulp and hardwood sulphate pulp ground to 13-300SR, said sheets being tested as to absorption, compressibility, softness, tensile strength, bulk and strain. According to the article, a three-component mixture consisting of 50% softwood sulphate pulp (<25SR), 30% hardwood sulphate pulp (20-21°SR) and 20% softwood sulphite pulp (20-21 0
SR)
resulted in the tissue paper with the best properties.
Soviet Patent 775,212 states that tissue paper produced from a mixture of softwood sulphate pulp, hardwood sulphate pulp and softwood sulphite pulp ground to 23- 0 SR becomes softer if the softwood sulphate pulp has 20 first been ground to 18-20SR.
SV 1,008,324 discloses the production of typographic paper of good opacity and ink absorbency from a papermaking pulp containing 30-40% by weight of bleached softa* wood sulphate pulp ground to 50-55 0 SR and 60-70% by weight of hardwood sulphate pulp ground to 30-35 0
SR.
One method of imparting increased softness to the paper is to treat the paper or the paper stock with a fibre-fibre-bond-reducing agent, often called debonding agent. A fibre-fibre-bond-reducing agent usually comprises 30 a primary, secondary, tertiary or quaternary ammonium compound containing a hydrocarbon group having 8-30 carbon atoms and, optionally, nonionic hydrophilic chains. It is common to combine the cationic ammonium compound with a nonionic surface-active compound. Such fibre-fibre-bondreducing agents are inter alia described in US Patent Specifications 3,554,862, 3,554,863 and 4,144,122, as well as in GB Patent Specification 2,121,449. The fibre-fibre- 4 bond-reducing agent markedly reduces the strength of the bonds between the fibres in the paper, while the softness increases. This is apparent from Table 1 bearing upon hand-made sheets from a mixture of 70% birch wood sulphate pulp and 30% pine wood sulphate pulp. US Patent Specification 4,795,530 tries to solve the inconvenience of strength reduction by applying the fibre-fibre-bondreducing agent only to part of the thickness of the tissue paper, thereby to obtain an untreated part of paper maintaining its original strength. As is apparent from Table 1 below, the changes in tensile stiffness and tensile strength of the paper owing to a conventional increased grinding of a pulp mixture and the addition of a fibre-fibre-bond-reducing agent to the ground fibre mixture cancel each other out. When grinding is increased, the strength and the stiffness increase proportionally.
When the amount of fibre-fibre-bond-reducing agent added is increased, the tensile stiffness as well as the tensile 2 strength are proportionally reduced. Thus, the gain in 20 strength is cancelled out by the loss in softness, and vice versa. There is, therefore, a generally expressed desire to improve the softness of a paper while maintaining a satisfactory strength.
It has now suprisingly been found that a paper advantageously combining softness and strength is obtained if based on a mixture of a) a hardwood pulp, a waste paper pulp or a mecha- 0 nical or semi-mechanical cellulosic pulp, or a mixture thereof, constituting 55-90% by weight, of the total 30 amount of cellulose fibres and having a drainage resistance below 25 0 SR, and b) a sulphate pulp and/or sulphite pulp based on softwood and constituting 10-45% by weight, of the total amount of cellulose fibres and having a drainage resist- 35 ance exceeding 30 0 SR. The difference in drainage resistance between 'he cellulosic pulps b) and a) is preferably at least 10SR. The paper can be produced by preparing a stock from the above cellulosic pulps a) and b) in the given amounts, whereupon the stock mixture is taken up on a wire, and is drained and dried in per se known manner.
In a preferred embodiment, the soft paper also contains a fibre-fibre-bond-reducing agent in an amount of 0.05-2.5% by weight, as based on the amount of cellulose fibres. As mentioned earlier, a soft paper according to the invention has a surprisingly advantageous ratio of softness to strength. To achieve this effect, the cellulosic pulp b) shoul be ground to above 30 0 SR, but preferably not above 80 0 SR, since pulps of so high grinding degrees require comparatively large amounts of fibrefibre-bond-reducing agents to give the paper a satisfactory softness. The cellulosic pulp b) preferably has 60"SR. The cellulosic pulp a) should be essentially unground or ground to less than 25 0 SR, preferably less than 200SR.
Whether the long-fibred pulp b) has been obtained by S* a sulphate process or by a sulphite process is of no 20 decisive importance. Also, whether it originates from pine wood, spruce wood or another conifer is of no vital impor- *tance either. It is, however, desirable that it has been ground in such a manner that the fibres have been shortened as little as possible. The grinding results in a fibre of higher flexibility. To benefit from this increased flexibility of the long-fibred ground cellulosic pulp, there is preferably an addition of a fibre-fibre-bondreducing agent serving to reduce the increase in strength 0* resulting from the grinding, when the pulp forms a sheet 30 of paper. The agent is added in such a manner as to be able to act on the bonds between the fibres. Preferably, the addition takes place at a staga during the preparation of the stock, but the fibre-fibre-bond-reducing agent may O also be added to the cellulosic pulp a) and/or the cellu- 35 losic pulp b) or to the wet, formed or dried paper web.
6 Preparation of Hand-made Sheets and Measuring Techniques The cellulosic pulps were ground in a beater according to SCAN C 25:67 to the desired drainage resistance determined in a Schopper-Riegler apparatus according to SCAN Standard C 19:65. In those cases when one did not want to noticeably change the drainage resistance of the cellulosic pulp, the latter was wet-defibrated according to SCAN C 18:65.
Before the formation of sheets, the cellulosic pulp, alternatively the mixture of cellulosic pulp, was stirred, optionally in the presence of a fibre-fibre-bond-reducing agent, at a pulp concentration of about 2% by weight for min. In the production of sheets, use was made of tap water of 30 0 C whose pH had been adjusted to 6-7. The sheets were dried and conditioned according to SCAN P 2:75, whereupon the basis weight of the sheets was determined according to SCAN P 6:63. When measuring tensile strength and tensile stiffness according to SCAN P 44:81, but with 15 mm broad straps, one used a tensile-strength 20 tester of the mark Alwetron THI, made by Lorentzen Wettre, Stockholm. The indices of tensile strength and o* tensile stiffness, respectively, were determined by division by the basis weight of the sheet, in order to eliminate the influence thereof.
Comparison In the comparative study, pine wood sulphate pulp and birch wood sulphate pulp were mixed. The pulps, ground as below, were mixed in such a manner that 70% by weight consisted of birch wood sulphate pulp and 30% by weight con- 30 sisted of pine wood sulphate pulp. Hand-made sheets were formed in accordance with the above-described method. The following results were obtained.
.ee*.e Table 1 Birch Pine Ten- Stiff- Strength/ wood wood sile ness Stiffness pulp pulp index index (oSR) (Nm/g) (Nm/g) *1000 Without debonder 12 12 19.3 2780 6.9 Without debonder 18.5 18.5 35.6 5250 6.8 With, 2 kg ptp*) 18.5 18.5 32.3 4680 6.9 With, 4 kg ptp 18.5 18.5 28.0 3960 7.1 With, 16 kg ptp 18.5 18.5 19.9 2740 7.3 Without deborder 26 26 55.0 7950 6.9 With, 2 kg ptp 26 26 38.3 5600 6.8 With, 4 kg ptp 26 26 30.6 4400 With, 16 kg ptp 26 26 22.3 3140 7.1 q
QS
S.
S.
SS
ptp per ton pulp As is apparent from these results, an increased grinding of a pulp mixture combined with an addition of fibre-fibre-bond-reducing agent to the ground fibre mixture does not noticeably affect the ratio of strength to stiffness (see the last column of the Table). When grinding is increased, the strength as well as the tensile stiffness are proportionally increased. When more of the fibre-fibre-bond-reducing agent is added, the tensile stiffness is reduced proportionally, as is the strength.
Thus, the gain in tensile strength is cancelled out by a reduced softness, and vice versa.
Example 1 A long-fibred pine wood sulphate pulp was ground to 13, 16.5, 20, 27 and 45 0 SR. Then, 30 parts by weight of the long-fibred pulp was mixed with 70 parts by weight of shortfibred wet-defibrated birch wood sulphate pulp, whereupon hand-made sheets were produced. The following results were obtained.
Table 2 Birch Pine Ten- Stiff- Strength/ wood wood sile ness Stiffness pulp pulp index index (OSR) (Nm/g) (Nm/g) *1000 Without debonder 14 13 15.5 2240 6.9 Without debonder 14 16.5 18.7 2750 6.8 With, 4 kg ptp 14 16.5 12.2 1770 6.9 Without debonder 14 20 21.5 3110 6.9 With, 4 kg ptp 14 20 14.8 2110 Without debonder 14 27 26.1 3640 7.2 With, 4 kg ptp 14 27 15.3 2120 7.2 Without debonder 14 45 32.8 4050 8.1 With, 4 kg ptp 14 45 16.0 1750
S
*55 0
S.
*r
S.
.9 *5
S
S .0 o
S.
As is apparent from these results, the ratio strength/stiffness of the paper drainage resistance of 13-27 0
SR
is roughly constant at of the pine wood pulp, a but is considerably improved when pine wood pulp of 450SR is used.
5 Further, it can be seen that a stock containing pine wood pulp ground to a drainage resistance of 45 0 SR and with an addition of a fibre-fibre-bond-reducing agent results in an even better ratio.
Example 2 A pine wood sulphate pulp according to Example 1 and ground as below was mixed with a short-fibred pulp consisting of a wet-defibrated eucalyptus wood sulphate pulp.
For the sheet formation, use was made of a pulp mixture of 70% eucalyptus wood sulphate pulp and 30% ground pine wood pulp. The following results were obtained.
sulphate pulp. The following results were obtained.
5 Sir~ Table 3 Euca- Pine Ten- S+iff- Strength/ lyp- wood sile ness Stiffness tus pulp index index wood pulp (OSR) (Nm/g) (Nm/g) *1000 Without debonder 16 12 19.0 2740 6.9 Without debonder 16 45 29.6 3620 8.2 With, 4 kg ptp 16 45 18.9 2100 From the above Table, it can be gathered that the ratio of tensile strength to tensile stiffness is advantageous for the paper according to the invention.
Example 3 A spruce wood sulphite pulp ground as below was mixed with a short-fibred wet-defibrated birch wood sulphate pulp. For the sheet formation, use was made of a pulp mix- 20 ture of 70% birch wood sulphate pulp and 30% ground spruce wood sulphite pulp. The following results were obtained.
Table 4
S.
S
a
S.
a 0@.
6o *5O
YS
S
S.
*r S
S.
4 U 4 a. S Birch Spruce Ten- Stiff- Strength/ wood wood sion ness Stiffness pulp pulp index index (OSR) (OSR) (Nm/g) (Nm/g) *1000 Without debonder 13 12 18.0 2790 Without debonder 13 39 30.9 4510 6.9 With, 4 kg ptp 13 39 15.5 1990 7.8 Without debonder 13 47 33.2 4660 7.1 With, 2 kg ptp 13 47 25.7 3420 With, 4 kg ptp 13 47 19.9 2520 7.9 From ;hie above Table, it can be gathered that the ratio of tensile strength to tensile stiffness also in this case is advantageous for the paper according to the invention.
Example 4 A long-fibred pine wood sulphate pulp ground as below was mixed with a short-fibred wet-defibrated birch wood sulphate pulp. For the sheet formation, use was made of a pulp mixture of 80% birch wood sulphate pulp and ground pine wood sulphate pulp. The following results were obtained.
Table BB 20 *i B
C
Birch Pine Ten- Stiff- Strength/ wood wood sile ness Stiffness pulp pulp index index (OSR) (Nm/g) (Nm/g) *1000 Without debonder 14 1i 18.1 2830 6.4 Without debonder 14 28 22.3 3410 With, 4 kg ptp 14 28 11.4 1630 6.7 Without debonder 14 46 27.4 3530 7.8 With, 4 kg ptp 14 46 14.7 2030 7.9 It is apparent from these results that the ratio of tensile strength to tensile stiffness is advantageous when the paper has a composition according to the invention.
Example A pine wood sulphate pulp ground as below was mixed with a short-fibred wet-defibrated birch wood sulphate pulp.
For the sheet formation, use was made of a pulp mixture of birch wood sulphate pulp and 40% ground pine wood sulphate pulp. The following results were obtained.
Table 6 Birch Pine Ten- Stiff- Strength/ wood wood sile ness Stiffness pulp pulp index index (OSR) (oSR) (Nm/g) (Nm/g) *1000 Without debonder 14 12 19.1 2750 6.9 Without debonder 14 28 25.5 3640 With, 4 kg ptp 14 28 16.7 2350 7.1 Without debonder 14 46 34.5 3970 8.7 With, 4 kg ptp 14 46 24.3 2620 9.3 As is apparent from to tensile sile strength to tensile these results, the ratio of tenstiffness is advantageous when the 0* a
-I.
*a *0 paper has a composition according to the invention.
Example 6 A pine wood sulphate pulp ground as below was mixed with a deinked waste-paper-based pulp. The pulp had been produced in a deinking plant, the waste paper consisting of computer printouts, books, brochures and the like. For the sheet formation, use was made of a pulp mixture of 70% waste paper pulp and 30% ground pine wood sulphate pulp. The following results were obtained.
Table 7 Waste Pine Ten- Stiff- Strength/ paper wood sile ness Stiffness pulp pulp index index J0 (Nm/g) (Nm/g) *1000 Without debonder 24 12 32.0 4100 7.8 Without debonder 24 45 39.6 4660 With, 4 kg ptp 24 45 33.8 4020 8.4 With, 8 kg ptp 24 45 32.4 3700 8.8 With, 16 kg ptp 24 45 24.6 2660 9.2 a It is apparent from these results that the ratio of tensile strength to tensile stiffness is advantageous when the paper has a composition according to the invention.
Example 7 A pine wood sulphate pulp ground as below was mixed with a wet-defibrated CTMP pulp. For the sheet formation, use was made of a pulp mixture of 70% CTMP and 30% ground pine wood sulphate pulp. The following results were obtained.
Table 8 CTMP Pine Ten- Stiff- Strength/ pulp wood sile ness Stiffness pulp index index (oSR) (Nm/g) (Nm/g) *1000 Without debonder 11 12 18.2 2200 8.3 Without debonder 11 45 31.6 2900 10.9 With, 4 kg ptp 11 45 21.6 2090 10.3 2 With, 6 kg ptp 11 45 17.5 1650 10.6 It is apparent from these results that the ratio of tensile strength to tensile stiffness is advantageous when the paper has a composition according to the invention.
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Claims (12)

1. Paper having an advantageous combination of softness and strength and based on a mixture of cellulosic pulps, characterised in that a) 55-90% by weight of the total amount of cellulose fibres consists of a pulp selected from the group consisting of a hardwood pulp, a waste paper pulp, a mechanical cellulosic pulp, a semi-mechanical cellulosic pulp or mixture of the foregoing pulps having a drainage resistance below 25 0 SR as hereinbefore defined, and b) 10-45% by weight, of the total amount of cellulose fibres consists of a pulp selected from the group consisting of sulphite pulp and sulphate pulp, each said pulp being based on softwood and having a drainage resistance exceeding 30 0 SR as hereinbefore defined.
2. Paper as claimed in claim 1, characterised in that the cellulosic pulp b) has a drainage resistance not exceeding 80 0 SR as hereinbefore defined.
3. Paper as claimed in claim 1 or 2, characterised in that the cellulosic pulp b) has a drainage resistance of 35-60°SR as hereinbefore defined.
4. Paper as claimed in any one of claims 1-3, characterised in that the cellulosic pulp a) has a drainage resistance below 20 0 SR as hereinbefore S defined.
5. Paper as claimed in any one of claims 1-4, characterised in that it contains a fibre-fibre-bond-reducing agent. 14
6. Paper as claimed in claim 5, characterised in that the fibre-fibre- bond-reducing agent contains a compound with ammonium ions.
7. Paper as claimed in claim 5 or 6, characterised in that it contains 0.05-2.5% by weight of said fibre-fibre-bond-reducing agent.
8. A method of producing paper according to any one of claims 1-7, characterised in that a stock is prepared from a) a cellulosic pulp selected from the group consisting of a hardwood pulp, a waste paper pulp, a mechanical cellulosic pulp, a semi-mechanical cellulosic pulp, or a mixture of the foregoing pulps, having a drainage resistance below 25 0 SR as hereinbefore defined, and is mixed with b) a pulp selected from the group consisting of sulphite pulp and sulphate pulp, each said pulp being based on softwood and having a drainage resistance exceeding 30 0 SR as hereinbefore defined, the cellulosic pulp a) constituting 55-90% by weight of the total amount of cellulose fibres, and the cellulosic pulp b) constituting 10-45% by weight of the total amount of cellulose fibres, whereupon the stock mixture is taken up on a wire, and is drained and dried.
9. A method as claimed in claim 8, characterised in that the cellulosic puip a) has a drainage resistance below 20 0 SR as hereinbefore defined, and that the cellulosic pulp b) has a drainage resistance of 35-60° SR as hereinbefore defined.
10. A method as claimed in claim 8 or 9, characterised by the addition, at some stage, of a fibre-fibre-bond-reducing agent.
11. A method as claimed in claim 10 wherein said fibre-fibre-bond- reducing agent contains a compound with ammonium ions. llil t
12. A method as claimed in claim 11 wherein said compound with ammonium ions is present in an amount of 0.05-2.5% by weight, based on the amount of cellulose fibres. DATED this 25th day of January, 1993. EKA NOBEL AB WATERMARK PATENT TRADEMARK ATTORNEYS THE ATRIUM 290 BURWOOD ROAD HAWTHORN VICTORIA 3122 AUSTRALIA .t 9 9 99 *oo o* 4 e ABSTRACT A paper having an advantageous combination of soft- ness and strength is disclosed, which is based on a mix- ture of cellulosic pulps and in which a) 55-90% by weight, of the total amount of cellulose fibres consists of a hardwood pulp, a waste paper pulp or a mechanical or semi-mechanical cellulosic pulp, or a mixture thereof, having a drainage resistance below 25 0 SR, and b) 10-45% by weight, of the total amount of cellulose fibres consists of a sulphite pulp and/or sulphate pulp based on softwood and having a drainage resistance 6A 015 exceeding 30 0 SR. The paper can be produced by preparing a stock from the cellulosic pulps a) and b) in the above amounts, 0, whereupon the stock is taken up on a wire, and is drained and dried in per se known manner. o 3
AU83775/91A 1990-09-12 1991-09-11 Soft paper of high strength and method for production thereof Ceased AU636059B2 (en)

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SE9002900A SE500524C2 (en) 1990-09-12 1990-09-12 Soft paper with high strength and process for its preparation
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SE504030C2 (en) * 1995-02-17 1996-10-21 Moelnlycke Ab High bulk spun lace material and absorbency as well as process for its preparation
SE505388C2 (en) * 1995-11-24 1997-08-18 Sca Hygiene Paper Ab Soft, bulky, absorbent paper containing chemitermomechanical pulp
FI119562B (en) * 2000-02-07 2008-12-31 Upm Kymmene Corp Fluff, process for making fluff, using fluff, and product made from fluff
CN100427680C (en) * 2006-04-15 2008-10-22 永州湘江纸业有限责任公司 High-temp. hot-pressing type bedding paper and its prodn. method
PT115562B (en) 2019-06-03 2021-12-24 Raiz Instituto De Investig Da Floresta E Papel EUCALYPTUS GLOBULUS PEEL PULP AND ITS PRODUCTION PROCESS FOR TISSUE PAPER PRODUCTS

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2706155A (en) * 1951-10-24 1955-04-12 Camp Mfg Company Inc Absorbent paper
GB1117731A (en) * 1963-09-17 1968-06-26 Wycombe Marsh Paper Mills Ltd Two-layer paper
US4120747A (en) * 1975-03-03 1978-10-17 The Procter & Gamble Company Use of ozone treated chemithermomechanical pulp in a high bulk tissue papermaking process

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2706155A (en) * 1951-10-24 1955-04-12 Camp Mfg Company Inc Absorbent paper
GB1117731A (en) * 1963-09-17 1968-06-26 Wycombe Marsh Paper Mills Ltd Two-layer paper
US4120747A (en) * 1975-03-03 1978-10-17 The Procter & Gamble Company Use of ozone treated chemithermomechanical pulp in a high bulk tissue papermaking process

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DE69107940D1 (en) 1995-04-13
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ATE119595T1 (en) 1995-03-15
NO177938C (en) 1995-12-20
SE500524C2 (en) 1994-07-11
EP0478045A1 (en) 1992-04-01
NZ239562A (en) 1992-11-25
DE69107940T2 (en) 1995-07-13
ES2069819T3 (en) 1995-05-16
NO177938B (en) 1995-09-11
NO913436L (en) 1992-03-13
SE9002900D0 (en) 1990-09-12
CA2051218A1 (en) 1992-03-13
FI914269A0 (en) 1991-09-10
EP0478045B1 (en) 1995-03-08
SE9002900L (en) 1992-03-13
NO913436D0 (en) 1991-09-02
FI96335B (en) 1996-02-29
FI96335C (en) 1996-06-10

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