Classifications

• • 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
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
  • D21D1/00—Methods of beating or refining; Beaters of the Hollander type
  • D21D1/20—Methods of refining
  • D21D1/30—Disc mills

Definitions

• This invention relates to a method and apparatus for producing fibre pulp from fibrous T-ignocellulose containing raw materials, in which the material is preheated in a preheater by means of steam, and in which the preheated material thereafter is ground at an increased pres- sure of steam or gas, between grinding discs which rotate relatively to one another in a grinding apparatus into a fibrous pulp, which is pro ⁇ pelled from the apparatus housing by means of the steam or gas to a separation device which is similarly maintained under steam pressure and in which the steam is separated from the pulp.
• the raw material consists of chips from softwood or hardwood, bamboo, straw, bagasse, etc., which while undergoing fragmentation in the grinding apparatus may be either chemically treated or untreated.
• the grinding apparatus comprises at least two grinding units, such as of the disc type having flat or con ⁇ ical grinding surfaces or a combination thereof, which rotate relatively to one another.
• OMPI • v_V WlrO % Enclosing the grinding unit in a pressure-proof housing enables the fragmentation or grinding of the material .suppl ied in an already-heated condition to take place while the conditions o ' f increased pressure and temperature which are favourable to the process are maintained.
• the fibrous material produced from the fragmentation process is discharged from the pressurized grinding housing into a receiving device which is similarly maintained at overpressure which is equal to or somewhat lower than that maintained in the discharge zone of the grinding housing.
• the receiving device in which the fibre pulp is separated from the -steam accompanying it f om "the grinding device, is provided with an arrange- ment for discharging the fibrous material from the receiving device while maintaining the pressure of steam in the said receiving device, and without any major simultaneous discharge of steam with the fibrous material .
• the steam separated in ' the receiving device has previously been used to preheat the material under atmospheric conditions to about 100 -.0 U .C before being fed under pressure-proof conditions into the preheater, which operates under pressure and which is connected directly to the grinding device.
• the heating of the material is achieved by supplying live pressurized steam to the preheater, or, for fragmentation processes requiring greater amounts of electrical energy, by reintroducing steam from the inlet zone of the grinding device.
• the purpose of the invention is, with application of a grinding process of a known nature (cf. for example, Swedish Patent 413.601), to • enable the grinding to take pl.ace at a- favourably high pressure and temperature, and, at the same time, to enable re-cycling of the elec ⁇ trical or steam energy supplied for this purpose for preheating to the highest possible temperature of the material in the preheater.
• a grinding process of a known nature cf. for example, Swedish Patent 413.601
• the invention also comprises an arrangement suitably-designed for applic ⁇ ation of the method.
• the grinding process according to the invention can be carried out under the most favourable conditions of temperature and pressure, the steam energy generated " during the grinding process or supplied as live steam is re-cycled in the preheater, reducing consid- erably the energy consumption required for carrying out the process.
• the invention is particularly suitable for the manufacture of porous and hard fibreboards, in which the requirements are less exacting as regards whiteness in the fibre pulp.
• fragmentation of the fibres, which results in the exposure of fibrils- in such products is not required to be performed to such an extent, and the overall process becomes less energy-consuming in the grinding app ⁇ aratus.
• the pressure obtained from the outlet zone of the grinding device with or without the addition of a lesser volume of fresh steam at the inlet zone of the separate grinding device, can ' , by virtue of the turbo effect of the grinding device and the electrical energy supplied for the fragmentation, despite resistance and pressure losses in pipes, valves and regulating devices, be brought to a level such that the temperature and degree of processing for the material conveyed to the grinding device from the separate preheater is equal to, or deviates only to a negligible extent from that which has been at- tained previously by the addition of live steam at the preheating device directly (openly) connected to the grinding device.
• the invention can also be said to be distinguished in that the raw material, before being conveyed by means of an, in principle, pressure-sensitive feeding device to a grinding device operating at increased pressure and temperature, is exposed to preheating to a temperature in excess of 100°C, but not in excess of the temperature maintained in the outlet zone of the grinding device, whereby the volume of steam required for such preheating is mainly conveyed from the outlet zone of the
• the device will be described in greater detail hereinafter, with reference to a preferred embodiment shown as an example in the attached drawings.
• Figure 1 is a more or less schematic side view, partly in section, showing equipment for carrying out the process according to the inven ⁇ tion.
• Figure 2 shows the grinding apparatus which forms part of the equipment and a pressure-sensitive conveyor connected with it, drawn to an enlarged scale and in a vertical section,. - . . . ' '
• the reference numeral J_0_ designates a feed hopper for the raw material, for example wood chips, which are conveyed by a screw conveyor J _ into a preheater _15_.
• the material is compressed by the conveyor's screw Y__ which is driven by a rotor J_9, forming a steam-tight plug of the material.
• the degree of compression is • regulated by means of a pneumatically-operated counterpressure device _13_ working in conjunction with a conical valve piece _14- which rests against the material plug being fed in.
• the material plug With the passage of the conical valve piece, the material plug is broken up and the material drops down into the vertical preheater _15_, in which a level of material is maintained which results in the desired dwell-ti e in the preheater vessel.
• This material level is maintained in that a level regulator __ acts upon the speed of the feed screw Y__ by means of the driving device ⁇ 9_.
• the material heated in the preheater vessel __5_ is discharged at the bottom of the preheater by means of a conveyor J_8 via a sealed conveyor ___ to the intake section of conveyor 22 which compresses the material, in order to bring about a fundament ⁇ ally steam-tight conveying of the material from the preheater _1_5 to the grinding apparatus or disc refiner 24.
• the conveyor 22_ comprises, in the same way as the feed conveyor 11 in the. embodiment example, a conical tube v/hich tapers internally in the direction of the material flow, in which tube a screw 26 ⁇ of the same shape operates.
• a counterpressure device Z7_ Connected to the discharge side of the tube, if required for performing the process, is a counterpressure device Z7_, which may
• the degree of compression of the preheated material supplied to the grinding device 24 can be varied to the required extent, while the liquid (water) accompanying the material is simultaneously pressed out through perforations 3_1_ in the compression tube into a funnel 35 connected by pressure-proof means to this tube, from which funnel the expelled water is removed via a pipe 9 into a tank 92_, the overpressure in which is equal to or in the vicinity of the pressure of steam maintained in the supply tube 2 in that a conduit 9__ connects the tank 9 ⁇ with the supply tube 2__.
• the level of liquid in the tank S2_ is monitored by a level-sensor 100 and a regulating device 9__ controlled therefrom for a valve 97 provided in the discharge pipe 96_ from the tank.
• the grinding device or defibrator 24 comprises grinding discs which are disposed in a housing 36_, in the embodiment example a stationary grinding disc 38 which is secured rigidly to the housing, and a grinding disc ___ which is mounted on a drive shaft 44, which is driven by a motor 42.
• the primary material_ has been compressed by conveyor 7__ and the counterpressure device _U_, it advances further through a pipe 7__, suitably-having a cylindrical bore, the free end of which is located closely adjacent to the rotating grinding disc 4O.
• the pipe 70 is arranged eccentrically relative to the axis of rotation of the grinding disk in order to enhance the breaking-up of the highly com ⁇ pressed plug before the pulp material is introduced into the grinding space ___ between the grinding discs.
• the plug may suitably be broken up by one or more vanes 7 ⁇ on the disc 4TJ directly in front of the mouth of the pipe 70.
• v/ater may be added to the material when it is introduced into the grinding space 48, to compensate for the water expelled in the conveyor.
• a conveyor of the type described here is known by virtue of Swedish Letters Patent 419.659.
• a drain pipe 5 is connected to grinding disc housing 36_, through which pipe the fibrous material produced in .the grinding apparatus is conveyed or propelled, at no loss of pressure, into a receiving tank 80, preferably of the cyclone type, in which fibre and steam are separ ⁇ ated from one another.
• the separated fibre is discharged from a rotating valve &2, in principle pressure-proof, to a receiver/conveyor device ES4, wherein the moisture accompanying the fibrous material is vaporized and drawn off via a collecting hood 89_ for possible re-use in any other part of the units in the installation which operates -at atmospheric pressure.
• the pressure level in the receiving tank ⁇ 5 is regulated to the desired value by means of a differential regulator 815, which senses, by means of the sensor devices 54 and 55_, via the pipes 8J_ and 83 ⁇ the pressure both in.the housing 3t_ for the grinding apparatus and in the receiving vessel 8__, and automatically maintains a pressure differential
• steam pressure in the grinding housing may rise to 7 - 12 kg/cm .
• the temperature • of the steam in the- outlet from the grinding housing may be - in the range of 11-5 - 125, to J50 - 170°C, to which temperature the material is therefore heated in the preheater, regardless of the inevit ⁇ able pressure and temperature losses on the way to the preheater. . . .
• a valve 5_2_ may be disposed in the pipe 5 between the grinding device 24_ and the receiving vessel 8CL By this valve, it is possible to regulate the speed of discharge of the fibrous material from the grind ⁇ ing housing, with regard to the overall length of the pipe 5__.
• the material supplied to the preheater J_5 is heated by means of steam drawn off from the receiving vessel 8 via a pipe 8__, which steam is at a level of pressure less than that maintained in the grinding housing, only with such loss of pressure required for conveying the treated fibrous material from the grinding housing 3t_, via the receiving
• the grinding disc housing 36 ⁇ is supplied with live steam via pipes 120, 124 and 122 before, and, where required, " after the passage of the ground material through the grinding space £8 between the grinding discs.
• the purpose of the live steam is to maintain a pressure which is required for the process. This pressure is balanced by means of a reg ⁇ ulating device 110 which actuates a valve 112 located in the pipe 122 and which senses the pressure at the outlet to the grinding housing via a pipe 114.
• the live steam supplied is conveyed, together with the steam generated by electrical energy supplied during the grinding process, to the preheater _15_ with only a minimal, loss of pressure and temperature-.
• Pipe 122 is only required to be switched in at extremely low levels of steam generation between the grinding discs in order then to be able to maintain the required pres ⁇ sure and preheating temperature in the vessel J_5. In many cases, the pipe 122 may be dispensed with.
• the turbo effect_of the grinding device 4TJ together with the electrical energy supplied during the fragmentation process, it is possible to increase the pressure which is maintained at the outlet for . the grinding housing 36_ to a level enabling the steam re-cycled to the preheater j_5_ to be maintained at a pressure which is higher than the steam pressure maintained in the preheater.
• the material supplied to the grinding device 24 can, given this arrangement, be maintained at the same temperature as could be achieved in previous designs only by supplying live steam to the preheater, a fact implying substantial (40 - 80%) savings in heat energy for heat- processing the material.
• a valve ___ is disposed in the pipe 8, the setting of which valve can be monitored by the regulating device 85.
• the invention is not limited to the disclosed embodi ⁇ ments, but may find a variety of expressions within the scope of the inventive concept.
• a gas for example air, to be introduced into the steam atmosphere in order to bring about the envisaged levels of pressure and temperature in the enclosed system.

Landscapes

• Engineering & Computer Science (AREA)
• Life Sciences & Earth Sciences (AREA)
• Wood Science & Technology (AREA)
• Mechanical Engineering (AREA)
• Paper (AREA)
• Disintegrating Or Milling (AREA)
• Chemical Or Physical Treatment Of Fibers (AREA)

Priority Applications (4)

Applications Claiming Priority (2)

Publications (1)

Family

ID=20346021

Family Applications (1)

Country Status (7)

Cited By (14)

Families Citing this family (4)

Citations (5)

• 1982
  • 1982-02-16 SE SE8200943A patent/SE429874B/sv unknown
• 1983
  • 1983-02-15 WO PCT/SE1983/000048 patent/WO1983002788A1/en active IP Right Grant
  • 1983-02-15 JP JP83500775A patent/JPS59500175A/ja active Pending
  • 1983-02-15 DE DE8383900743T patent/DE3364587D1/de not_active Expired
  • 1983-02-15 EP EP83900743A patent/EP0113353B1/de not_active Expired
  • 1983-10-11 NO NO833688A patent/NO833688L/no unknown
• 1984
  • 1984-03-14 FI FI841041A patent/FI75610C/fi not_active IP Right Cessation

Patent Citations (5)

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