Known coated printing papers which contain mechanical pulp and whose opacity is at least 89 %, brightness at least 65 % and surface roughness not more than 4.5 jAm, include for example machine finished coated (MFC), film coated offset (FCO), light weight coated (LWC) and heavy weight coated (HWC) papers.

MFC papers refer to coated papers whose coating content varies from 5 to 10 g/m2 per paper side and which are used for magazines, cata- logues, books, and commercial printed matter. The grammage of MFC papers varies from 48 to 80 g/m2. Of the fibre content of the paper, 60 to 80 % is mechanical pulp and 15 to 40 % is chemical pulp. The total filler content of the coated paper is 20 to 30 weight-%. In some cases, MFC papers also include MFP papers whose coating content is nor- mally from 2 to 5 g/m2 per paper side.

LWC papers refer to coated papers whose coating content varies from 5 to 12 g/m2 per paper side and which are used for magazines, cata- logues, inserts, and commercial printed matter. The grammage of LWC papers varies from 35 to 80 g/m2. Of the fibre content of the paper, 50 to 70 % is mechanical pulp and 30 to 50 % is chemical pulp. In un- coated base paper, the filler content is 4 to 10 % of the total mass of the base paper. The total filler content of coated paper is 24 to 36 weight-%.

HWC papers refer to coated papers with a considerably high coating content. FCO papers refer to coated papers with a film coating.

The above-mentioned paper grades have the problem of high chemical pulp content which the papers must have to achieve the desired prop- erties. The printing paper according to the invention provides an

alternative to replace coated papers of prior art, and an improvement in certain properties of the paper.

The coated printing paper according to the invention is characterized in that it contains mechanical pulp at least 90 weight-% of the total fibre content of the paper. The coated printing paper according to the inven- tion has good opacity which is achieved when chemical pulp is used little or not at all. The printing paper according to the invention is stiffer than other printing papers used for the same purposes. The printing paper has a relatively high bulk. The desired bulk can be influenced by calendering, wherein it is possible to achieve very good printability of the paper. It is inexpensive to manufacture, because the quantity of chemical pulp is low or non-existent.

The coated printing paper according to the invention is intended to replace the above-mentioned paper grades, particularly LWC and MFC papers, which have an opacity of at least 89 %, a brightness of at least 65 %, preferably at least 70 %, and a surface roughness of not more than 4.5 Zm, preferably not more than 3.0 um. Normally, the bright- ness value required is at least 70 % and the surface roughness value is not more than 3.0, um, but for some insert grades, the allowed bright- ness and surface roughness values are at least 65 % and not more than 4.5 Fm, respectively. Inserts refer to for example special news- papers, newspaper supplements and handouts. The numerical values referred to have been obtained by the following testing methods: - opacity SCAN-P 8: 93 - brightness SCAN-P 3: 93 - surface roughness SCAN-P 76: 95 Paper with a high content of mechanical pulp will have a poorer tear resistance than corresponding papers containing more chemical pulp.

The tear resistance will be further decreased by coating of the paper. Surprisingly, this did not affect the runnability of the paper in the machine, although this should, according to a common assumption, correlate better with the runnability of the paper.

In the printing paper according to the invention, the mechanical pulp used is advantageously special thermomechanical pulp (TMP) whose production will be discussed below in this application. By using the special thermomechanical pulp, good values are achieved for the paper in, for example, breaking energy, tensile strength and elongation.

In the paper manufacturing process, the aim is to replace such parts which cause impairing of the properties of the paper, with new con- structions. For example, in the press section of the paper machine, the paper web is arranged to be supported during the running, wherein the elongation properties of the paper remain good, because it is not nec- essary to use such a high running tension for the web as would be necessary if the web were unsupported during the running.

Very good properties are achieved for the coated printing paper according to the invention, even though the content of chemical pulp in the paper is very low or non-existent. The coated printing paper may contain chemical pulp not more than 10 wt-% of the total fibre content of the paper; advantageously, it contains chemical pulp not more than 5 weight-% of the total fibre content of the paper; and preferably, the total fibre content of the printing paper is mechanical pulp.

The mechanical pulp to be used in the manufacture of coated printing paper is preferably refiner mechanical pulp, for example thermome- chanical pulp (TMP). The thermomechanical pulp is refined and screened to make it very bondable and strong pulp. Typically, it has a relatively high content of long fibres and fines but a lower content of medium-size fibres than normally. However, the fibre distribution may differ from the typical distribution presented above, and strong and bondable pulp can still be achieved by the fibre manufacturing method.

The method for manufacturing fibrous pulp can be used to produce mechanical fibre pulp with a high proportion of long fibres. In this appli- cation, mechanical pulp refers to fibre pulp made of wood material, such as wood chips, by beating. In connection with the beating, the wood material and/or the fibre pulp is subjected to thermal treatment, wherein it is a process for producing thermomechanical pulp. In addi- tion to the thermal treatment, the wood raw material may also have

been treated with chemicals before the beating, wherein it is a process for producing chemi-thermomechanical pulp.

By the method, it is possible to achieve an average fibre length of about 10 % higher than by methods used before, if desired. It is typical of the method that the content of short fibres in the fibre pulp remains approximately the same as before, but the content of medium-size fibres is reduced and the relative content of long fibres is increased.

However, it is not necessarily the fibre length and its distribution that is the determining factor but, by controlling the process, the method can be used to produce various fibre distributions which are each charac- terized in high strength and bondability. Surprisingly, such fibre pulp can be used to make paper which has a good formation and whose properties meet the high demands set for printing paper. Convention- ally, long average fibre length and fibre pulp with a good formation have been difficult to achieve in the same product, because it has not been known to refine fibres to fines, simultaneously retaining a rela- tively long fibre length. Furthermore, in the method for producing fibre pulp according to the invention, the energy consumption is lower than in methods of prior art aiming at the same freeness level. The freeness value of the finished fibre pulp is from 30 to 70 mi CSF. In this applica- tion, the freeness value refers to the Canadian Standard Freeness value with the unit of ml CSF. The freeness value can be used to indi- cate the degree of beating of the pulp. According to prior art, the fol- lowing correlation is present between the freeness value and the spe- cific surface area of the fibres: A =-3,03 In (CSF) + 21,3, in which A = total specific surface area of the pulp (unit m2/g).

According to the above-mentioned formula, the total specific surface area of the pulp is increased as the freeness value is decreased; in other words, the freeness value gives a clear indication of the beating degree, because as the content of fines is increased, the specific sur- face area of the fibres will increase.

The wood species which are presented as suitable raw materials used in this application, are spruce (genus Picea, several different species), silver fir (genus Abies, several different species), pine (Pinus sylves- tris), and Southern pine (genus Pinus, several different species). It is also possible that the fibre pulp made of wood raw material contains fibre pulp obtained from at least two different wood species and/or fibre pulp made in at least two different ways, which are mixed together at a suitable production step.

The production of fibre pulp comprises the primary beating of a suitable wood material and subsequent beating and screening steps. The so- called primary beating, or the first step of the beating process, is per- formed at a high temperature of 165 to 175°C and at a high pressure of 600 to 700 kPa (6 to 7 bar) for a short time, wherein most of the fibre pulp remains relatively rough. The average retention time of the raw material to be supplied in a high-pressure refiner is only 5 to 10 sec- onds. The temperature during the beating is determined by the pres- sure of saturated steam.

In the first beating step, preferably one-step beating is only used. How- ever, there can be several refiners in parallel at the same step. After the first beating step, the freeness value of the fibre pulp is 250 to 700 mi CSF. After the first beating step, the fibre pulp is screened to a first accepted fibre pulp grade and a first rejected fibre pulp grade. After the fibre pulp has been screened to the first accepted fibre pulp grade and the first rejected fibre pulp grade, there are different ways to con- tinue the process, for example - 1-step processing of the first rejected fibre pulp grade, in which the rejected fibre pulp is refined and screened in one step. Accepted fibre pulp grades are removed from the process after each screening step and/or accepted fibre pulp grades are re- screened, or - 2-step processing of the first rejected fibre pulp grade, in which the rejected fibre pulp is refined and screened in two steps. Accepted fibre pulp grades are removed from the process after

each screening step and/or accepted fibre pulp grades are re- screened, or 3-step processing of the first rejected fibre pulp grade, in which the rejected fibre pulp is refined and screened in three steps, and accepted fibre pulp grades are removed from the process after each screening step, or forward coupled processing of rejected fibre pulp in two or three steps, which refers to the processing of rejected fibre pulp in first two or three steps and and the removal of accepted fibre pulp grades from the process after each screening step, followed by the beating of the last remaining rejected fibre pulp grade in, for example, a low-consistency refiner and the removal of all the fibre pulp processed in the low-consistency refiner from the process.

In the above-mentioned alternatives, each step comprises a refiner and a screen, one after the other. Said embodiments will be presented in detail hereinbelow. The accepted fibre pulp grades obtained from dif- ferent steps in the process are combined and mixed with each other, bleached preferably by peroxide bleaching, and used as raw material for papermaking in a paper machine. The apparatus for producing fibre pulp may comprise several production lines in parallel, the resulting accepted fibre pulp grades being combined with each other.

The fibre pulp obtained from the process for producing fibre pulp is led for use in a paper machine. The principle of the papermaking process is known as such. However, the papermaking line is provided with such modifications that wet paper with a poor strength can be made without affecting the runnability ; in other words, the aim of the new arrange- ments is to avoid web breaks. The running speed used in the paper machine during papermaking is higher than 1300m/min, advanta- geously higher than 1500 m/min and preferably higher than 2000 m/min.

In the press section of the paper machine, the web has a closed transfer, which means that the web is supported when running in the

press section. This has an advantageous effect on, for example, the elongation properties of the web. Thus, the tension of the web does not need to be as high as if the web were unsupported during the running.

The press section of the paper machine can be, for example, Opti- Press@ (Metso Paper, Inc., Finland).

The paper is coated with a suitable coating method, such as film coat- ing. The coating preferably contains kaolin and/or calcium carbonate.

The coating content used is preferably 3 to 9 g/m2 per paper side.

The paper is calendered at a suitable nip pressure in a multi-nip calen- der, which can be, for example, OptiLoad (Metso Paper, Inc., Finland).

The production of the fibre pulp will be described in more detail with reference to Figures 1 to 5 which show principle process charts for the production of fibre pulp.

Before the feeding of wood chips into the process of Fig. 1, the wood chips are pretreated in hot steam under pressure, wherein the wood chips are softened. The pressure in the pretreatment is preferably 50 to 800 kPa. For the pretreatment of the wood chips, it is also possible to use chemicals, for example, alkali peroxide or sulphite treatments, such as sodium sulphite treatments. Before the refiners, there are nor- mally also devices intended for steam separation, such as cyclones.

In the process of Fig. 1, the wood chips are fed at a consistency of 40 to 60 %, for example about 50 %, to a refiner 1, which yields fibre pulp with a freeness value of 250 to 700 mi CSF. When spruce (Picea abies) is used as the raw material, the average fibre length after the refiner 1 is at least 2.0 mm. The pressure used at the refiner 1 is high, an overpressure of more than 400 kPa (an overpressure of more than 4 bar), preferably 600 to 700 kPa. Overpressure refers to overpressure compared to normal atmospheric pressure. The refiner 1 can be a conical or disc refiner, preferably it is a conical refiner. A longer fibre can be obtained with a conical refiner than with a disc refiner. The energy consumption at the refiner 1 is 0.4 to 1.2 MWh/t.

The fibre pulp is fed via a latency container 2 to a screen 3. In the latency container 2, fibres curled during the beating are straightened out, when they are held in hot water for about one hour. The consis- tency in the latency container 2 is 1 to 5 %.

The screen 3 yields a first accepted fibre pulp grade A1 with a freeness value of 20 to 50 mi CSF. Of the total fibre pulp, 60 to 90 %, preferably about 80% is passed to a first rejected fibre pulp grade R1. After dewatering, the first rejected fibre pulp grade R1 is fed at a consistency of 30 to 60 %, preferably about 50 %, to a refiner 4 and further at a consistency of 1 to 5 % to a screen 5. The energy consumption at the refiner 4 is 0.5 to 1.8 MWh/t.

The refiner 5 yields a second accepted fibre pulp grade A2 and a sec- ond rejected fibre pulp grade R2, which contains 60 to 80 % of the rejected fibre pulp grade R1 of the preceding step screened in screen 5. The second rejected fibre pulp grade R2 is led at a consis- tency of 30 to 60 %, preferably 50 %, to a refiner 6 and further at a consistency of 1 to 5 % to a screen 7, which yields a third accepted fibre pulp grade A3 and a third rejected fibre pulp grade R3, which is returned to the feeding of the refiner 6. The energy consumption at the refiner is 0.5 to 1.8 MWh/t. The total fibre pulp, which is obtained by combining the accepted fibre pulp grades A1, A2 and A3, has a free- ness value of 30 to 70 ml CSF.

The above-presented energy consumption values relating to the proc- ess of Fig. 1 correspond to the energy consumption when the wood chips are not treated with chemicals, that is, the pulp is thermome- chanical pulp.

The pressure at the refiners 4 and 6 may be high, at least more than 400 kPa (more than 4 bar), preferably 600 to 700 kPa (6 to 7 bar), or it can be on the normal level, at a maximum of 400 kPa, preferably 300 to 400 kPa.

Dewatering before the refiners, to achieve a consistency of 30 to 60 %, preferably about 50 %, is performed by screw presses or correspond- ing devices which can be used to remove so much water from the process that said high consistency is achieved. The dilution of the fibre pulp before the screening, in turn, is performed by pumping water into the process, by pumps suitable for the purpose.

The fibre pulp is screened by known methods. In the screens, it is pos- sible to use, for example, a slotted screen with a slot size of 0.10 to 0.20 mm and a profile height suitably selected in view of the screening situation and the desired final result. In a process including several screening steps, the slot size of the screens is normally increased towards the end of the process. The properties of the screens must be selected, for example, in such a way that they are not blocked in abnormal running situations, for example when the process is started.

The consistency is normally 1 to 5 % when slotted screens are used.

One possibility to screen the fibre pulp is a vortex cleaner ; when it is used, the consistency must be adjusted lower than in the use of a slotted screen. The consistency is preferably about 0.5 % when a vortex cleaner is used.

Measured by the Bauer-McNett method, the fibre distribution of the finished fibre pulp, obtained by combining and mixing the acceptable fibre pulp grades A1, A2 and A3, is typically the following: 40-50 % of the fibres will not pass screens with a slot size of 16 mesh and 28 mesh, 15-20 % of the fibres will pass screens of 16 and 28 mesh but will not pass screens with a slot size of 48 mesh and 200 mesh, and 35-40 % of the fibres will pass screens of 48 and 200 mesh; that is, these fibres pass through all the screens used (up to 200 mesh).

The average fibre length of the fibres left on the 16 mesh screen is 2.75 mm, the average fibre length of the fibres left on the 28 mesh screen is 2.0 mm, the average fibre length of the fibres left of the 48 mesh screen is 1.23 mm, and the average fibre length of the fibres

left on the 200 mesh screen is 0.35 mm. (Source: J. Tasman: The Fiber Length of Bauer-McNett Screen Fractions, TAPPI, Vol. 55, No. 1 (January 1972)) Thus, the resulting fibre pulp contains 40 to 50 % of fibres with an average fibre length of more than 2.0 mm, 15 to 20 % of fibres with an average fibre length of more than 0.35 mm, and 35 to 40 % of fibres with an average fibre length of less than 0.35 mm. However, the fibre distribution may differ from that presented above.

Figure 2 shows a second embodiment of the invention. The beginning of the process is similar to that shown in Fig. 1, but the third rejected fibre pulp grade R3 is led to a refiner 8 and further to a screen 9. The fourth accepted fibre pulp grade A4 obtained from the screen 9 is led to be combined with the other accepted fibre pulp grades A1, A2 and A3.

The fourth rejected fibre pulp grade R4 is led back to the input of the refiner 8. This kind of an arrangement may be necessary when the aim is to achieve a low freeness level, for example the level of 30 ml CSF.

Figure 3 shows a third embodiment of the invention. The beginning of the process is similar to that shown in Fig. 2, but the fourth rejected fibre pulp grade R4 is led to a low-consistency refiner LC. The consis- tency of the fibre pulp grade R4 to be fed into the low-consistency refiner LC is 3 to 5 %. The resulting accepted fibre pulp grades A1, A2, A3, A4, and A5 are combined and mixed to finished fibre pulp.

Figure 4 shows a fourth embodiment of the invention. The rejected fibre pulp grade R1 obtained from the screen 3 is led to a refiner 4 and further to a screen 5. The rejected fibre pulp grade obtained from the screen 5 is led back to the inlet of the refiner 4. The accepted fibre pulp grade A2 obtained from the screen 5 is removed from the process.

The accepted fibre pulp grade A1 obtained from the screen 3 is led to be re-screened in a screen 10. The accepted fibre pulp grade A11 obtained from the screen 10 is removed from the process. The rejected fibre pulp grade R11 obtained from the screen 10 is led to a refiner 11 and further to a screen 12. The rejected fibre pulp grade R12 obtained

from the screen 12 is led back to the inlet of the refiner 11. The accepted fibre pulp grade A12 obtained from the screen 12 is removed from the process, to be combined with the other accepted fibre pulp grades A11 and A2.

Figure 5 shows a fifth embodiment of the invention. The process is, in other respects, similar to that shown in Fig. 1, but the accepted fibre pulp grade A1 obtained from the screen 3 is led to be re-screened in a screen 13. The accepted fibre pulp grade A13 obtained from the screen 13, the accepted fibre pulp grade A2 obtained from the screen 5, and the accepted fibre pulp grade A3 obtained from the screen 7 are combined and mixed and led to be used in the paper- making process. The rejected fibre pulp grade R13 obtained from the screen 13 is combined with the rejected fibre pulp grades R2 and R3, and the combined fibre pulp is led to the refiner 6.

The wood raw material used in the process may be any kind of wood, but normally it is softwood, preferably spruce, but also for example pine or Southern pine are suitable wood raw materials for the use. When spruce is used as the wood raw material and the wood chips are not treated with chemicals, the energy consumption is about 2.8 MWh/t, of which about 0.3 MWh/t is consumed to adjust the consistency to be suitable for each process step. In the process according to Fig. 1, the energy consumption is 0.4 to 1.2 MWh/t in the first step of the beating, 0.5 to 1.8 MWh/t in the second step of the beating, and 0.5 to 1.8 MWh/t in the third step of the beating. The required processing energy is greater for pines than for spruce; for example, the processing of Southern pine requires about 1 MWh/t more energy than spruce.

Also the change in the wood chip size will affect the energy consump- tion. The above-mentioned energy consumption values result from tests in which the wood chips had an average size of 21.4 mm and an average thickness of 4.6 mm according to a test screening.

It is also possible to implement the above-described processes for the production of fibre pulp by using a screen which performs the screen- ing at substantially the same consistency as that of the beating. In this

case, the energy consumption will be lower, because the amount of energy taken for the adjustment of the consistency will be saved.

In the following, the invention will be described in more detail by means of examples. The test results presented in the examples have been obtained by using test methods listed below.

Grammage SCAN-C28 : 76/SCAN-M8: 76 Thickness SCAN-P 7: 96 Bulk SCAN-P 7: 96 Filler content SCAN-P 5: 63 Tensile strength SCAN-P 38: 80 Elongation SCAN-P 38: 80 Tear resistance SCAN-P 11: 96 Bending strength SCAN-P 29: 95 Bending length mod. ASTM: D 1388-96 Bonding strength TAPPI Useful Method 403 (instructions for RD device) ISO brightness SCAN-P 3: 93 D65 brightness SCAN-P 66: 93 Opacity SCAN-P 8: 93 Airpermeance SCAN-P 19: 78 PPS roughness SCAN-P 76: 95 Gloss (%) 75° T 480 Example 1.

During the manufacture of coated printing paper according to the invention, calender tests were made with an OptiLoad calender. The nip pressure was 500 kN/m. A 6-roll calender was used for sample 1, an 8-roll calender for samples 2 to 4. The temperature of the calender was adjusted so that it was 110°C during the calendering of the sample 2,125°C during the calendering of sample 3, and 140°C during the calendering of sample 3. The properties measured of the samples are given in Table 1. Table 1. Properties of some coated printing papers according to the invention.

Sample 1 2 3 4 Grammage (g/m2) 52,8 52,2 52,9 52,3 Thickness (m) 58 57 58 52 Density (kg/m 3) 951 966 972 999 Bulk (cm3/g) 1,06 1,03 1,02 1 Filler content 560°C (%) 20, 8 20, 8 20,4 20, 8 Mechanical pulp (%) 100 100 100 100 Chemical pulp (%) 0 0 0 0 Tensile strength in machine 3,13 3, 09 3,18 3,22 direction (kN/m) Elongation (%) - machine direction 1 1 1 1 - cross-machine direction 1, 6 1, 4 1,7 1,4 Tear resistance (mN) - cross-machine direction 155 151 149 155 Bending strength (mN) - machine direction 31 29 29 27 - cross-machine direction 16 14 15 14 Bending length (mm) - machine direction 115 116 117 115 - cross-machine direction 89 86 92 85 Bonding strength SB Low J/m2) * 308 293 260 304 Brightness ISO ts 71 71, 2 70,8 70,3 Brightness D65 ts 71,1 71, 1 70,9 70,2 Opacity (%) 3 93, 1 93,3 92,5 Air permeance (s/100 ml) 970 760 800 1020 Roughness PPS (pu) 1,76 1,79 1,63 1,55 Gloss (%) - machine direction 48 45 49 54 *) In the measurement of the bonding strength, the scale SB Low (0 to 525 J/m2) has been used.

Example 2.

A comparison was made between the properties of the coated printing paper according to the invention and coated printing papers of prior art.

The grammages of the samples to be compared in the same table are substantially the same. The properties are presented in tables 2 to 4.

Table 2. Properties of coated printing papers The coated printing paper according to the invention is sample 5, samples of prior art are samples 6 to 8.

Sample 5 6 7 8 Grammage (g/M2) 52 51, 6 51,6 50,6 Thickness m) 57 47 47 48 Density kg/m3 954 1092 1100 1061 Bulk (cm3/g) 1,048 0, 92 0,91 0,94 Filler content 560°C (%) 28,2 25,5 30,5 29,7 Mechanical ulp (%) 100 56 65 70 Chemical pulp (% 0 44 35 30 Tensile strength in machine direction 2,96 4,01 2,78 2,82 (kN/m) Elongation (%) 1, 25 1,2 1,1 - machine direction 0, 9 Tear resistance (mN) 132 373 - 242 - cross-machine direction Bending strength (mN) - machine direction 28 18, 9 20 17 - cross-machine direction 13 9,6 11 9, 5 Bending length (mm) - machine direction 106 96 97 - cross-machine direction 84 71 - 76 Bonding strength SB High (J/m2) ** 202 286 294 318 Brihgtness ISO ts 72, 1 69,4 72,1 69,7 Brightness D65 ts 72, 4 69,5 7371, 7 Opacity (%) 92,4 90,1 92,6 92,4 Air permeance (s/100 ml) 1700 2207 1030 1918 Roughness PPS (pm) 1,97 1,51 1,26 1,66 Gloss (%) 44 51 57 52,8 - machine direction **) In the measurement of the bonding strength, the scale SB High (210 to 1051 J/m2) has been used.

Table 3. Properties of coated printing papers The coated printing paper according to the invention is sample 9, samples of prior art are samples 10 to 13.

Sample 9 10 11 12 13 Grammage (g/M2) 60,5 60,5 59,4 59,2 59,6 Thickness (m) 55 52 56 65 Density (kg/m3) 966 1108 1152 1050 907 Bulk (cm3/g) 1, 035 0,9 0,87 0,95 1, 11 Filler content 560°C %) 25, 8 30,3 32,9 32 25, 8 Mechanical pulp 100 66 52 73 84 Chemical pu p 0 34 48 27 16 Tensile strength in machine 3,8 4,01 3,42 3,41 3,02 direction (kN/m) Elongation (%) -machine direction 1 1, 35 1,17 1,2 1,27 Tear resistance (mN) - cross-machine direction 190 365 301 Bending strength (mN) - machine direction 44 26 20 26 38 - cross-machine direction 21 12 9 12 22 Bending length (mm) - machine direction 128 106 99 101 118 - cross-machine direction 100 80 62 83 89 Bonding strength SB High (J/m2) ** 244 282 326 291 245 Brightness ISO ts 73, 5 71,9 71,4 71 76, 8 Brightness D65 ts 73, 9 71,9 72,6 72,25 77,6 Opacity (%) 93 92 92, 8 95 93 Air permeance s/100 ml 2200 3166 797 1812 710 Roughness PPS (pm) 2,23 1,41 1,82 1,66 2, 08 Gloss (%) -machine direction 47 58 54 57 32 **) In the measurement of the bonding strength, the scale SB High (210 to 1051 J/m2) has been used.

Table 4. Properties of coated printing papers The coated printing paper according to the invention is sample 14, samples of prior art are samples 15 to 17.

Sample 14 15 16 17 Grammage (g/m) 54,9 54,2 54,5 53,4 Thickness m 62 57 52 56 Density kg/m3 887 950 1054 960 Bulk (cm3/g) 1, 12 1,05 0,95 1,04 Filler content 560°C %) 24, 1 28,9 28,1 30,5 Mechanical ulp (%) 100 54 54 71 Chemical pulp (%) 0 46 46 29 Tensile strength in machine direction (kN/m) 3,54 3,09 2,66- Elongation (%) 1, 2 1,25 1,5 - machine direction Tear resistance (mN) 198 306 302 258 - cross-machine direction Bending strength (mN) - machine direction 33 23,5 21 - cross-machine direction 14 12,5 - 12 Bending length (mm) - machine direction 113 111 101 -cross-machine direction 79 85 76 Bonding strength SB Hiah (J/m2) ** 296 411 560 297 Brightness ISO ts 73, 5 75 72, 1 71,4 Brightness D65 ts 73, 6 75, 2 75 72 Opacity (%) 93 92 89, 9 94,3 Air ermeance s/100 ml 260 1310 220 860 Roughness PPS (pm) 2,39 2,52 2,97 2,18 Gloss (%) 21 30 23 32 - machine direction **) In the measurement of the bonding strength, the scale SB High (210 to 1051 J/m2) has been used.

Example 3.

In the following, one fibre pulp grade will be presented, of which it is possible to make printing paper according to the invention. Of the fibre pulp grade, whose properties are shown in Table 5, unoriented sheets, whose properties are shown in Table 6, were made in a laboratory.

Table 5. Properties of fibre pulp.

Freeness Fibre distribution by Bauer-Average fibre (ml CSF) McNett method length (mm) *** +16 +28 +48 +200-200 (%) (%) (%) (%) (%) 61 34, 0 10,6 17,9 16,9 20,6 1,67

***) The average fibre length is the average of the length-weighted average fibre length measured with a Kajaani FS-200 device.

Table 6. Properties of unoriented sheets made of fibre pulp. Grammage (g/m2) 60, 2 Thickness (um) 121 Density (kg/m) 497 Bulk (m3/kg) 2,01 Tensile index (Nm/a) 55, 7 Elongation (%) 2,46 Breaking energy index (J/kg) 920, 6 Tear index (mNm2/g) 7, 48

As seen from the properties in Tables 5 and 6, good strength values are achieved for the fibre pulp. The fibre distribution differs slightly from the typical fibre distribution obtained from the method, wherein it can be stated that the fibre production method provides strong and

bondable pulp, even though the fibre distribution did not match the typical fibre distribution obtained by the method.

The invention is not restricted to the description above, but it may vary within the scope of the claims. It is possible to use pulp grades with varying fibre distribution for the manufacture of printed paper, as long as they are refined so that they have good strength values and bond- ability. The main idea in this invention is that certain printing paper grades can be replaced by using printing paper containing mechanical pulp at least 90 weight-% of the total fibre content of the paper.