NZ199947A - Manufacturing pulp from wood chips:wood chips compressed into body and fed to grinding zone having converging wall surfaces formed by grinder - Google Patents

Description

T # . << 199947 Priority Date(s): Complete Specification Filed: ^.7?."^?. Class: XlW.J!!^.l/t...

Publication DatsJ MMm P.O. Journal, No: IP~~? 7 Patents Form No.5 NEW ZEALAND PATENTS ACT 1953 COMPLETE SPECIFICATION "METHOD AND GRINDER FOR THE MANUFACTURE OF PULP" v\ u --I-,WE SUNDS DEFIBRATOR AB, a Swedish company, & '^> J/5 Z& of -3.fi.?,L 5J Stockholm, Sweden, \ hereby declare the invention, for which -t/we pray that a patent may be granted to me/us, ,and the method by which it is to be performed, to be particularly described in and by the following statement:— (followed by page I A/N /« 1999 47 Our Case: Def 165 Method and Grinder for the Manufacture o.f Pulp This invention is concerned with a method and a grinder for the manufacture of pulp from ligno-cellulosic material, such as wood chips or the like, the fibres being detached from the material by means of grinding to.ols or members.

Mechanical pulp is manufactured since long ago from round timber in grinders and from wood chips in disc-crushers, so-called refiners. During the last decade the refiner method has been developed so that is now is possible to manufacture a stronger pulp than that which is obtained in conventional grinding mills. However, the refiner method requires about 50 % more energy than the grinding, mill method. Due to the increased energy costs, the interest has anew become directed towards the grinding mill method. Thus, a grinding mill has become known which is operated under pressure, whereby a pulp is obtained which is equally strong as refiner pulp, but with an energy consumption as in conventional grinding mills. However, grinding mills operated under pressure are expensive to be made and require high-priced round timber.

To all methods now in use applies that the produced grist requires extensive subsequent treatment such as screening and milling, which operations are expensive both with regard to investment costs and to energy consumption. Known grinders are imperfect in their most important portion, the.grinding zone, due to insufficient control possibilities i a regarding maintenance of the temperature in the grinding zone, supply of liquid to the grinding zone, the pressure in the grinding zone, removal of released fibres, formation of sticks and shives, and orientation of the wood. 199947 2 Regarding the orientation of the wood it has been established by both experiments and practical experience that the consumption of power for manufacture of mechanical wood pulp is at its minimum when the wood 5 is orientated in the plane of the grinding tool and with the grain transverse to the direction of movement of the surface of the tool.

The main object of the invention is to reduce the drawbacks inherent to today's grinding apparatus and 10 refiners and relating to the possibility in the grinding zone to control temperature, pressure, liquid supply and liquid removal. In addition, the invention renders possible optimal orientation of the wood in grinding zone, elimination of formation of sticks and shives, 15 reduction of wear of the grinding members, reduction of energy consumption and improvement of the brightness and bonding properties of the ground pulp.

This and other objects of the invention are achieved thereby that it has been imparted with the character-20 istic features set forth in the subsequent claims.

The invention will hereinafter be described in more detail in conduction with embodiments illustrated in the attached drawings.

Figure 1 shows a longitudinal section through a 25 grinder for implementation of the method of the in-venti on.

Figure 2 shows a section along the line 11 -11 in Figure 1 .

Figure 3 shows a section along the line 111 -111 in 3 0 F igu re 1 .

Figure 4 shows a top view from a section following the line IV-1V in Figure 5 of another e m b odiment of the grinder according to the invention. 1999 4 7 3 Figure 5 shows a section along- the line V-V in Figure 4.

Figures 6 and 6a show sections' along the line VI-VI in the Figures 4 and 5, respectively, of two different 5 embodiments.

In the embodiment shown in Figures 1 to 3 of a grinder for implementation of the method according to the invention, wood chips are fed into the grinder by means of a slotted sieve plate 1, which is used for orientating the 10 wood chips into a predetermined direction. It is advantageous to use relatively long chips. The chip bits orientated in this way enter now a space or chamber 2 which is formed between a core stationarily mounted in the grinder and an outer tube or casing 7. The orien-15 tated and loosely packed chip bits in the chamber 2 are thereafter fed by means of a reciprocating piston device 3 to the right in Figure 1 towards a tapered portion of the chamber 2, within which portion the wood chips are compressed against the stationary core 4 and form a 20 continuous cylindrical or tubular body of chips on the stationary core 4. Annexed to the right end, according the figure, of the core 4 is a rotatable grinding member 6, the diameter of which increases conically in the direction towards the right-hand end of the casing 7. 25 In this way, a converging grinding zone 5 is formed, which zone is confined by the inner wall surface of the casing 7 and the outer circumference of the grinding member 6. Obviously, the converging grinding zone 5 can be formed also by the walls of the casing having 30 decreasing inner diameter and the grinding member 6 being cylindrical, or by both the casing 7 and the grinding member 6 having conical surfaces.

The casing 7 must have a length permitting formation of a plug having sufficient extent for not becoming 199947 4 forced back by the steam pressure generated within the -' grinding zone. The plug is retained in the grinding zone 5 by friction against the wall of the casing 7. The grinding member 6 may be manufactured as a tubular 5 body and its grinding surface may be formed out on the member proper or be procured by means of grinding segments rigidly secured onto the grinding member.

The body or plug of chips which is compressed additionally during the continued advancement in the grinding 10 zone 5 along the surface of the rotating grinding member 6 constitutes in the grinding zone 5 a compressed.plug which is stationary and from which the fibres are detached by the grinding member 6. This plug is forced into contact with the grinding member by the pressure 15 from the piston device 3. The grinding member 6 has a surface with projections, preferably in a pattern which produces pressure impacts causing the plug of chips to be worked internally during its advance within the converging grinding zone 5. The pattern on the surface may 20 be coherant or consist of separate punctiform "burls". In both cases the pattern may have spiral shape with positive or negative course, i e to the left or to the right in the figure, even in a sine-shaped spiral form, but may also extend in parallel to the axis. The pro-25 jections of the pattern may also have a recess or "cavity" at the top. In a punctiform pattern the projections should overlap each other seen in the direction of movement of the grinding member. The pattern may also have projections resembling sawteeth, at least one of the 30 edges being curved or rounded and the pattern being arranged so that the rounded edge is turned in the direction of movement (direction of rotation) of the grinding member. The projections should have a height up to 1.2 mm, preferably between 0.03 and 1.0 mm. 199 9 47 The grinding member may be of a material v/hich has pores in the surface, i e is permeable to water, which permits penetration downwards into the surface of the grinding member, so that a thin layer of water is formed 5 adjacent said surface. This layer of water creates a hydraulic pressure which results in that the grinding member does not come into direct contact with the fibrous material, the thin water layer instead transferring the pulsations from the surface pattern to the fibrous material. 10 The thin water layer also contributes to keep the surface of the grinding member free from material which otherwise could stick fast on the surface. The grinding member or its grinding segments are preferably made of cemented pulverulent material of steel, hard metal or 15 the like or granules of ceramic material which are compressed and joined together in a manner known in this s p e c i f i c . a r t.

Through channels 9 in the grinding member 6 liquid, such as water, but also chemicals, alkali or the like, 20 is supplied at desired places distributed over the grinding zone. The released fibres are carried away by the added liquid via one or several channels 8 in the grinding member 6. Said grinding member, which in the embodiment illustrated in Figure 1 is conical, has a 25 greatest diameter which comes near the inner diameter of casing 7 at the right-hand discharge end thereof. Thereby, the wood residues form a seal towards the grinding zone 5, when they pass through the gap existing between saidcasing and the grinding member 6. These wood resi-30 dues can be taken care of and returned to the incoming chips material. The grinding operation in the grinding zone 5 can also be performed under pressure above atmospheric (steam pressure) which is built up by generating a counter-pressure in the outlet channel 8, the body of 35 chips precompressed in the chamber 2 forming a plug which seals against the inlet for the chips from the 19 9 9 4 7 feeding device 1. Obviously, a sluicing device can be used also for feeding the chips into the chamber 2 and/ or discharging the grist from the outlet channel 8. In this latter case the grist passes from the channel 5 8 into a vessel 10, wherein the grist and the steam are separated from each other and in pressure-tight-manner led away from the vessel.

In the embodiment shown in Figures 4 to 6a of the grinder according to the invention, corresponding 10 details of the grinder have been given the same reference numerals as in the embodiment of Figure 1 with the number 1 additionally ahead of said reference numeral. Thus, the grinding member shown in Figures 5, 6 and 6a, consists of a disc 16 which rotates towards the feed 15 chamber 12 in the casing or housing 17. The chips are fed from the slotted sieve plate 11 by means of a piston device 13 into the chips chamber 12. The chips bits are orientated with the grain radially in the plane of the disc 16 so that the grinding surface of the grinding 20 member or grinding disc 16 in the same manner as previously is moved transversally to the fibre grain. The converging grinding zone is formed by the bottom of the chips chamber 12 having upward slope in the direction of feed, whereby the chips are forced by the piston device 25' 13 into contact with the grinding disc 16. Water is added to the grinding zone through water inlets 19 provided either in the disc 16, see Figure 6, the water then suitably being supplied through a bore in the shaft or, as an alternative, in the casing 17, as illustrated. 30 in Figure 6a. Released fibres and water are drawn off through grooves 18 in the disc 16 adjacent the outer wal1 of the cas i ng 17.

The grinding operation may be effected under super-atmospheric pressure by the whole grinding mill being 35 enclosed in a pressurized housing. The wood chips are sluiced into the housing by the piston device 13 whereby 1999 47 they become compressed to a continuous, sealing plug of chips. In order to attain uniform load around the grinding disc 16, the chips suitably are fed in at several places into the chips chamber 12, eg at three 5 places as is shown in the embodiment of Figure 4.

Obviously, the shown embodiments can be varied within the scope of the invention. Thus, the feeding devices, for example, may in known manner be devised as continuous one, such as screw feeders. The invention 10 may also be applied to the grinding of round timber, in which case the core 4 in the centre is dispensed with and the grinding member 6 is formed as a cone.

Realized experiments show that the invention can be utilized for manufacturing a brighter pulp having i m -15 proved bonding properties over pulp manufactured by known methods and,additiona11y , with low energy consumption. The probable explanation is that the wood in the grinding zone by the rotating member is compressed both axially and radially and forced into contact with the 20 casing. The member produces vibrations which by the thin layer of water are transferred to the wood, whereby fibres are released.

Owing to the defined processing in the grinding zone a pulp can be manufactured with very low coarse fraction 25 which is important for the printability of paper made from said pulp.

The invention has the following advantages over previously known grinders and refiners: 1. The grinding zone is stuffed with compressed and 30 orientated wood. Therefore, energy can be trans ferred from the grinding member to the wood with out appreciable shock'losses, without air admission and without excess of water. 2. Each wood element is subjected to a defined pro-35 cessing, i e every surface element of the wood in the grinding zone receives at a definite 199947 8 grinding pressure a predetermined number of pressure shocks from the grinding member, which has a settled pattern and is homogenuous, whereby a pulp practical ly free from shives is obtained. 5 Usual inhomogeneous grindstones with their grains of various sizes mixed at random produce in the same manner as refiner discs varying frequencies which suppress each other. In known grinders and refiners, the wood is subjected to highly varying 10 surface loading in contrast to the present in vention. 3. The pattern of the grinding member transfers vibrations to the wood material via a thin layer of water, for which reason the friction is low and, 15 therefore, the wear of the member slight. In known refiners the wear is great because of the direct contact between grinding disc and wood. The costs for .replacement of grinding discs is a great item of expenditure for refiners. 20 4. The grinding is effected almost perpendicularly to the grain, which results in the smallest energy consumption. In known refiners the treatment is at random with respect to the grain and, therefore, unfavourable. 5. Detached fibres leave the grinding zone quickly via a channel in the grinding member due to the fact that the grinding zone is relatively small. In known grinders and refiners, the fibres have to pass through a larger grinding zone and are 30 subjected there to an uncontrolled treatment. 6. The grinding operation is effected in the absence of air, which prevents the pulp from oxidization. 7. The grinding is made in a sealed room where the 35 grinding pressure can be adjusted, whereby the pulp quality can be acted upon. 1999 47 9 The term "grinding" in the preceding description is primarily understood to define all kinds of treatment of the fibrous material where the fibres are torn off from the material by means of pressure shocks from the pat-5 terned surface of the grinding member.

Claims (14)

WHAT WE CLAIM IS: 10

1. A method for the manufacture of pulp from ligno-cellulosic material, such as wood chips wherein the fibres are detached from the material by grinding members, characterized in that the fibrous material is formed into a body, that said body without rotational movement is fed, while being compressed, into a grinding zone which has converging wall surfaces, that the body of fibrous material in the grinding zone is worked upon by at least one grinding member which is rotatable relatively to the body of fibrous material and delimits at least one of the converging wall surfaces of the grinding zone, and that detached fibres are removed continuously from the grinding zone. 15 20

2. The method according to claim 1, characterized in that the fibrous material prior to the feeding into the grinding zone is orientated with the fibres into a desired direction, preferably into parallel to the plane of the grinding surface and perpendicularly to the direction of rotation of the grinding member. 25 30

3. The method according to claim 1 or 2, characterized in that liquid and/or chemicals are supplied to the grinding zone during the grinding operation.

4. The method according to any of claims 1 to 3, characterized in that the feeding of the fibrous material into, and/or the discharge of the detached fibres from, the grinding zone are effected in a pressure-tight manner for generating superatmospheric pressure in the grinding zone.

5. The method according to claim 3 or 4, character i z e d in that the pressure and the temperature in the grinding zone are adjusted totally or partially by the quantity, pressure and temperature of the supplied liquid. - 11 - m«M7

6. A grinder for implementation of the method as claimed in any of the claims 1 to 5, for manufacture of pulp from ligno-celulosic material, such as wood pulp, and comprising grinding members for detaching fibres from the fibrous material, characterized by a feeding and grinding zone having converging wall surfaces, within which zone the fibrous material is formed into a coherent body which during the feeding into the grinding zone is worked upon by at least one grinding member, the surface of which forms at least one of the converging wall surfaces, and an outlet for discharge of detached fibres from the grinding zone.

7. A grinder according to claim 6, characterized by a tubular casing, a grinding member rotatable within said casing, the casing and the grinding member having converging wall surfaces, and a gap formed at the narrowest part of the converging grinding zone, in which gap the fibrous material forms a seal against the grinding zone.

8. A grinder according to claim 6 or 7, characterized in that the grinding members are provided with at least one supply channel for liquid or solution of chemicals and at least one discharge channel for the produced suspension of fibres.

9. A grinder according to any one of claims 6 to 8, characterized by a solid body or core disposed in - 12 - 199S47 the feeding direction for the fibrous material ahead of the grinding zone and arranged at a distance from the surrounding casing so as to form a space adapted to receive a tubular body of fibrous material to be formed for advancement into said grinding zone.

10- A grinder according to any one of claims 6 to 9 characterized by a disc-shaped grinding member and feeding and grinding zones having converging wall surfaces arranged adjacent one face of said disc and following a peripheral path and radially extending channels for supply of liquid to said zones.

11. A grinder according to any one of claims 6 to 10, characterized in that the grinding member has a patterned surface comprising small projections which follow a continuous or interrupted course and which have a height of up to 1.2 mm, preferably between 0.01 and 1.0 mm.

12. A grinder according to any one of claims 6 to 11, characterized by a vessel connected to the outlet and within which grist and steam are separated from each other and from which the grist is removed in a pressure-tight manner for generating a desired counters-pressure in the vessel and the outlet.

13. A method for the manufacture of pulp from lignocellulosic material, such as wood chips , wherein the fibres are detached from the 199947 material by means of grinding members, substantially as herein described with reference to any one of the embodiments shown in the accompanying drawings.

14 . A grinder for manufacture of pulp from ligno-cellulosic material such as wood pulp substantially as herein described with reference to any one of the embodiments shown in the accompanying drawings.