Classifications

• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
  • D21D5/00—Purification of the pulp suspension by mechanical means; Apparatus therefor
  • D21D5/18—Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force
  • D21D5/24—Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force in cyclones
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
  • D21B1/00—Fibrous raw materials or their mechanical treatment
  • D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
  • D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam

Definitions

• the present invention is concerned with a method of manufacturing cellulose pulp from ligno-cellulose material wherein the material is ground in a mill which is subjected to internal steam pressure.
• the invention is further concerned with means for the implementation of the method.
• the main object of the invention is to provide a method of the above-mentioned type whereby the pulp as manufactured can be cleaned and the shives or bundles of fibres removed in the cleaning process can be subjected to further treatment, without the addition of substantial quantities of water which must subsequently be removed by various de- watering methods.
• a further object of the invention is to provide such a method, economical of energy and water, which can be implemented in combination with the mechanical separation of lig ' nocellulose material at temperatures in excess of .100 C and/or at pressures exceeding normal atmospheric pressure.
• Figure 1 is a schematic diagram of a plant implementing the method.
• Figure 2 is a section through a type of mechanical separator that can be used in the plant of Figure 1.
• Figure 3 is a section thorugh another embodiment of mechani ⁇ cal separator.
• Figure 4 is a longitudinal section through yet another type of separator.
• the number 10 indicates a feed hopper for a lignocellulose fibre material, such as wood chips.
• a lignocellulose fibre material such as wood chips.
• the material is fed by a screw 12 to a pre-heater 14 and from there by a screw . 16 to a first defibrator 18, such as a disc defibrator, wherein the lignocellulose material, such as wood chips, is comminuted to single fibres or bundles of fibres.
• this treatment which may or may- not b.e preceded by chemical treatment and/or heating in the pre-heater 14, most of the energy supplied to the material in the defibrator 18 is converted into heat.
• the natural moisture present in the material and/or wat ⁇ r added to prevent overheating of the fibre material during defibration in the defibrator 18 is thereby converted into steam.
• the steam thus generated, together with steam, compressed air, or other gases added during or after the defibration process in the defi- brator 18, is now used according to the invention for the very effective removal of large, unwanted bundles of fibres or shives without the addition of water.
• This separation is effected by using the gas or steam so generated to carry the fibre material at high velocity via a pipeline 20 from the defibrator 18 to at least one separating vessel 22.
• fibres and/or fibre bundles of various sizes are separated by imparting to the cellulose suspension a motion such that a sorting of the fibres takes place according to certain distinguishing properties such as weight, size, or other similar feature.
• the accepted fibres pass on via pipeline 24 to a cyclone steam separator 26, while the reject fibres or bundles are fed by a screw 28 to an outlet pipe 30.
• the accepted fibres are fed from the cyclone steam separator 26 to a refiner 32 for a second refining step.
• the cellulose suspension is carried via a pipeline 34 to a further separating step, which in the embodiment illustrated consists of three units 36, 38, and 40. These units are in the form of cleaning cyclones whose reject outlets are connected to a discharge means 42 whose outlet is connected to a pipeline 44 leading to a collector 46.
• the reject line 30 from the first cyclone separator 22 is also connected to the collector 46, so that all reject fibres and fibre bundles are collected therein.
• the contents of the collector 46 are fed to a defi ⁇ brator 48 * where the reject fibres or fibre bundles are re-treated and * comminuted and the outlet of the defibrator 48 is connected via a pipe- line 50 to the cyclone steam separator 26, i.e. the cellulose suspension discharged from the defibrator 48 is fed to the second refining step 32.
• the outlet from the cyclone 36 in the second cleaning step is connected to the cyclone 38, whose outlet is in turn connected to cy ⁇ clone 40.
• the accepted flow from cyclone 40 is fed via a pipeline 52 to a cyclone steam separator 54 from which the stock is fed to a stock chest 56. From the stock chest 56 the stock is drawn off via a pipeline 58 for further treatment or use.
• the pulp after being dried in a drying plant 60 which may be served by steam from the cyclone steam separators 26, 54, is conveyed via a pipe- line loop 62 and pump 64 to a baling station 66.
• the separator 22 used in the first separation step may, as shown in more detail in Figure 2, include a steam-collecting and/or gas-collect-' ing shell into which the pipeline 20 from the first defibration step discharges ' and into which the cellulose suspension is blown at high velocity by the energy supplied in the fibre separation step in the form of electricity and/or steam or compressed gas.
• the pulp On entering the cyclone 22 the pulp is thus given a rapid spiralling motion while at the same time the gas or stea ' fed to the cyclone causes the cellulose suspension to pass, against the action of centrifugal force, . to an outlet pipe 68 located at the centre of the cyclone 22, to which pipe the pipeline 24 is connected.
• the sorting of the fibres or fibre bundles present in the gas or steam suspension is easily controlled by varying the quantity of steam or gas passed through the cyclone.
• the pipe 68 may be arranged to be raised and lowered in the cyclone 22 so that by varying the vertical position of the outlet pipe 68 in relation to the conical lower part of the cyclone one can likewise control the separa ⁇ tion of the fibres or fibre bundles.
• the larger, heavier fibres and fibre bundles will offer greater resistance to the change of direction inwards towards the centre pipe 68 of the cyclone 22, ith the result that the heavier particles will be entrained towards the bottom of the cyclone, where they are discharged by means of e.g. the discharge screw 28 shown in Figure 1 to the dis ⁇ charge l ne 30.
• the separator consists of a shell 70 having a centre pipe 72 to which is connected a feed line for the cellulose suspension such as the feed line 20 in Fig. 1.
• the cellulose suspension enters the centre pipe and is set in rapid spiralling motion therein while simultaneously flowing downwards in the pipe 72.
• a conical dish 74 on which the cellulose suspension impinges.
• the lighter, ac- - ceptable fibres will then be entrained with the gas or steam upwards inside the shell 70 to the outlet 76 which is connected to the pipeline 24 in Figure 1, while heavier fibres and fibre bundles drop down inside the shell 72 to the conical bottom thereof, where they are discharged by the screw 28 to the reject line 30.
• the sorting of * fibres and fibre bundles can also be effected by gravity, as illustrated in Figure 4.
• the cellulose suspen ⁇ sion is introduced via a pipeline 78 at one end of an elongated shell 80 ' arid blown at high velocity into the interior thereof.
• the heavier fibres and. fibre bundles fall more rapidly to the bottom of the shell 80, while lighter, acceptable fibres follow a flatter trajectory inside the shell.
• feed screws 82 and 84 for the respective stock fractions, which screws are separated by a partition 86.
• the screw 82 carries the rejected fibre bundles and shives to an outlet 88 which discharges to vessel 46 in Figure 1.
• the screw 84 carries the acceptable fibres to an outlet 90 which is connect ⁇ ed to the second refining stage 32 in Figure 1.
• the steam is discharged via an outlet 92 from the shell 80 to a steam cyclone 94.

Landscapes

• Engineering & Computer Science (AREA)
• Mechanical Engineering (AREA)
• Life Sciences & Earth Sciences (AREA)
• Wood Science & Technology (AREA)
• Paper (AREA)

Priority Applications (2)

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Publications (1)

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Country Status (6)

Cited By (3)

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Citations (3)

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• 1982
  • 1982-05-04 SE SE8202790A patent/SE435849B/sv not_active IP Right Cessation
• 1983
  • 1983-05-03 EP EP83901432A patent/EP0109409A1/en not_active Withdrawn
  • 1983-05-03 WO PCT/SE1983/000177 patent/WO1983003856A1/en active IP Right Grant
  • 1983-05-03 US US06/574,153 patent/US4606789A/en not_active Expired - Fee Related
  • 1983-05-03 JP JP58501558A patent/JPS59500725A/ja active Pending
• 1984
  • 1984-01-02 FI FI840006A patent/FI72353C/fi not_active IP Right Cessation

Patent Citations (3)

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