US2980350A - Fibre disintegrating apparatus - Google Patents
Fibre disintegrating apparatus Download PDFInfo
- Publication number
- US2980350A US2980350A US737929A US73792958A US2980350A US 2980350 A US2980350 A US 2980350A US 737929 A US737929 A US 737929A US 73792958 A US73792958 A US 73792958A US 2980350 A US2980350 A US 2980350A
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- stator
- rotor
- chamber
- disintegrating apparatus
- pressure
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- 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
- D21D1/22—Jordans
Definitions
- This invention relates to grinding and/or disintegrating apparatus of the type used Vparticularly in connection with cellulosicmaterials such as paper pulp, and similar fibrous materials.
- 5 Grinding apparatus of this type generally comprises coaxial stator and rotor members respectively provided with similar grinding elements, such as projecting teeth or ribs which project inwardly into the gap between the stator and rotor to disintegrate and grind the fibrous materials introduced into said gap.
- a slightly frustoconical shape is imparted to both stator and rotor members for gradually varying the gap between the operating elements by imparting a limited relative am'al reciprocation between the stator and rotor members.
- Another object is t'o provide such apparatus including means for gradually separating the ground pulp or disintegrated material progressively as it is formed, from the incompletely ground stock.
- part of the stator specitically the lower part thereof, be provided in the form of a perforate wall through which the disintegrated libre material is adapted to drop into a collector chamber.
- the perforate wall is provided in the form of arcuate perforate sheet elements positioned beneaththe rotor periphery and extending arcuately over the lower half of the stator periphery.
- the disintegrated material is allowed to drop by gravity into a sorting chamber provided in the base of the apparatus, and the ground pulp collected in this chamber is desirably maintained under a predetedmined pressure.
- the ground pulp in the chamber is caused to remain in contact with the underside of the perforate wall thereby to exert upon the material being processed au upward back-pressure through the perforations, opposing the passage of incompletely ground material therethrough.
- means are preferably provided for establishing at the outlet of the apparatus a hydraulic back-pressure for thus maintaining the ground material in contact with the perforations.
- a hydraulic back-pressure may for example be provided by providing a riser pipe or tank connected with the collecting chamber and wherein the ground pulp is allowed to rise to a predetermined height for establishing the desired back pressure.
- Adjustable overow means may be provided in said riser pipe or tank for maintaining the controllable head of pulp in it.
- the inlet pressure of raw stock supplied to the apparatus is made higher than the outlet back-pressure thus created.
- the pressure differential between inlet and outlet pressures is adjusted in accordance with the desired degree of a iineness in the iinal pulp product, and in accordance with the operating characteristics of the apparatus including velocity of rotor rotation, cross sectional area of the perforations and the like.
- the back pressure provided at the outlet should be in- Patented Apr. 18, 1961 rice creased when the rotation velocity is decreased and vice versa.
- the frusto-conical shape imparted to the stator and rotor makes it easier to separate materials that are relatively difficult to grind, from the ground material, in the apparatus of the invention. This is because as a result of the tapering gap the raw stock fed into the operating gap or chamber at the smallerdiameter end of the apparatus isgradually separated into the bottom collector chamber, while the material that has not yet been disintegrated and cannot pass through the perforations is forced to revolve round and round in the operating chamber and is thereby gradually forced over a helical path towards the larger-diameter end of the apparatus.
- a further chamber be provided at the large-diameter end of the apparatus in which the coarser portions of the material will tend to collect as a result of the action just described, whence such coarse portions may be withdrawn for recycling or for rejection as the case may be.
- the above mentioned screening wall is left imperforate at the large-diameter area of the apparatus thereby to deline a reject chamber and a discharge conduit is connected with said chamber for disposing of the coarse material fractions collecting therein and/ or recycling such fractions back to the inlet of the apparatus.
- Fig. l is an axial sectional view of the stator and rotor of the grinder apparatus
- Fig. 2 is a transverse sectional view showing the same apparatus together with hydraulic back pressure means therefor;
- Fig. 3 is a smaller-scale View in side elevation of the apparatus showing the axial reciprocating means used therewith.
- the apparatus shown includes a rotor member 1 and a stator member 2 coaxially arranged and having a frusto-conical shape.
- the rotor I. is secured on a shaft 3 journalled at its ends in bearings 4 and 5, see Fig. 3.
- the stator 2 is comprised of an upper shell member 6 and a lower shell member 7 which are assembled together on horizontal plane X-X by means of suitable anges as shown.
- Secured in the upper stator shell 6 is a grinding element or set of elements 8 in the form of axially extending ribs and grooves, or serrations.
- the grinding means 8 are omitted in an area adjacent the inlet feed aperture 13 provided at the top -of the apparatus, as shown.
- Serrationssimilar to the-serrations 8 are provided all around the rotor circumference by forming spaced apart, axially extending grooves in the rotor surface, as shown in Fig. 2.
- a collecting chamber 15 Deiined by the frame 15 of the apparatus beneath the perforate wall 9 is a collecting chamber 15.). An outlet is formed in a side of this chamber which connects by way of a conduit 11 with the base of a riser pipe or tank 18 provided with a separating Wall 19 and adjustable overflow means 20 at the top of the wall for maintaining a predetermined head of liquid pulp in the tank and thus establishing the desired back pressure within chamber 16 as previously described.
- the perforate Wall 9 includes a solid i.e. imperforate end portion adjacent the large diameter end of the stator and rotor thus defining a chamber in which the Coarser portions of the material tend to collect for the reasons previously stated.
- topof thisfreject chamber is connected with amconduit 14 connected at one end by wayY of a shut-0E- valvewithY the supply inlet 13 for recycling the rejects back into the grinder, and connected at its other end by way of another shut-o: valve to any suitable meansof disposal foriinally 'rejected material.
- Y a shut-0E- valvewithY the supply inlet 13 for recycling the rejects back into the grinder, and connected at its other end by way of another shut-o: valve to any suitable meansof disposal foriinally 'rejected material.
- Meansy are provided for axially reciprocating the stator 6-*7V axially of the rotor and forrthis purpose the frame j axial portion thereof extending from said small diameter Yendv a distance corresponding to the length of said grooves of the rotor, the lower portiony of said stator being in the form of a smooth wall having perforations in an axial portion thereof extending fromfs'aid small diameter end to form asieve for the disintegratedmaterial, a substantial 15"is bodily reciprocable 'on slideways 16 relatively to a i
- the desired axialreciprocation may be mparted tothe frame by way of a linkage 17, see Fig. 3, driven through suitable conventional means from the same power source as that serving to rotate the rotor.
- Apparatus for dsintegrating andY reining 'cellulosicz material comprising a frustoconical stator arranged with its axis extending substantially horizontally, affrustoconical rotor rotatably mountedpin said stator vcoraxially with the latterand having disintegrating grooves in the surface of the rotor, Vsaid stator having an inlet opening .for'the ma- Y tenal to be treated in its upper portion adjacent the relaaxial llength of sa'idrstator adjacent therelativ'ely large diameter' endY thereof ⁇ being smooth andiimperforate at least in said lower portion there'of', and said stator fur ther having an outlet orifice .for in'completelyV disintegrated material opening ,from saidV upper portion adjacent said large diameter end; f 'i UNITED STATESV PATENTS References Cited in the tile of this patent V1,939,747 wiener l r l Dee 1.9,-*
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Description
April 1s, 1961 E. J. A. LEJEUNE 2,980,350
FIBRE DISINTEGRTING APPARATUS Filed May 26, 1958 United States atent O FIBRE DISlNTEGRATING APPARATUS Emile Jean Albert Lejeune, 44 Rue la Botie, Paris, France Filed May 26, 1958, Ser. No. 737,929
Claims priority, application France May 24, 1957 1 Claim. (Cl. 241-73) This invention relates to grinding and/or disintegrating apparatus of the type used Vparticularly in connection with cellulosicmaterials such as paper pulp, and similar fibrous materials. 5 Grinding apparatus of this type generally comprises coaxial stator and rotor members respectively provided with similar grinding elements, such as projecting teeth or ribs which project inwardly into the gap between the stator and rotor to disintegrate and grind the fibrous materials introduced into said gap. Frequently a slightly frustoconical shape is imparted to both stator and rotor members for gradually varying the gap between the operating elements by imparting a limited relative am'al reciprocation between the stator and rotor members. It is an object of this invention to provide improved grinding apparatus of this kind. Another object is t'o provide such apparatus including means for gradually separating the ground pulp or disintegrated material progressively as it is formed, from the incompletely ground stock.
In attaining these objects, it is contemplated according to a feature of the invention that part of the stator, specitically the lower part thereof, be provided in the form of a perforate wall through which the disintegrated libre material is adapted to drop into a collector chamber. In a preferred construction, the perforate wall is provided in the form of arcuate perforate sheet elements positioned beneaththe rotor periphery and extending arcuately over the lower half of the stator periphery.
With this arrangement the disintegrated material is allowed to drop by gravity into a sorting chamber provided in the base of the apparatus, and the ground pulp collected in this chamber is desirably maintained under a predetedmined pressure. Thus the ground pulp in the chamber is caused to remain in contact with the underside of the perforate wall thereby to exert upon the material being processed au upward back-pressure through the perforations, opposing the passage of incompletely ground material therethrough.
According to a further feature of the invention, means are preferably provided for establishing at the outlet of the apparatus a hydraulic back-pressure for thus maintaining the ground material in contact with the perforations. Such hydraulic back-pressure may for example be provided by providing a riser pipe or tank connected with the collecting chamber and wherein the ground pulp is allowed to rise to a predetermined height for establishing the desired back pressure. Adjustable overow means may be provided in said riser pipe or tank for maintaining the controllable head of pulp in it.
The inlet pressure of raw stock supplied to the apparatus is made higher than the outlet back-pressure thus created. The pressure differential between inlet and outlet pressures is adjusted in accordance with the desired degree of a iineness in the iinal pulp product, and in accordance with the operating characteristics of the apparatus including velocity of rotor rotation, cross sectional area of the perforations and the like. Thus, it has been found that the back pressure provided at the outlet should be in- Patented Apr. 18, 1961 rice creased when the rotation velocity is decreased and vice versa.
It has further been found that the frusto-conical shape imparted to the stator and rotor makes it easier to separate materials that are relatively difficult to grind, from the ground material, in the apparatus of the invention. This is because as a result of the tapering gap the raw stock fed into the operating gap or chamber at the smallerdiameter end of the apparatus isgradually separated into the bottom collector chamber, while the material that has not yet been disintegrated and cannot pass through the perforations is forced to revolve round and round in the operating chamber and is thereby gradually forced over a helical path towards the larger-diameter end of the apparatus. In this connection, it is contemplated according to the invention that a further chamber be provided at the large-diameter end of the apparatus in which the coarser portions of the material will tend to collect as a result of the action just described, whence such coarse portions may be withdrawn for recycling or for rejection as the case may be. For this purpose, the above mentioned screening wall is left imperforate at the large-diameter area of the apparatus thereby to deline a reject chamber and a discharge conduit is connected with said chamber for disposing of the coarse material fractions collecting therein and/ or recycling such fractions back to the inlet of the apparatus.
An exemplary embodiment of the invention will now be described for purposes of illustration but not of limitation with reference to the accompanying drawings, wherein:
Fig. l is an axial sectional view of the stator and rotor of the grinder apparatus;
Fig. 2 is a transverse sectional view showing the same apparatus together with hydraulic back pressure means therefor; and
Fig. 3 is a smaller-scale View in side elevation of the apparatus showing the axial reciprocating means used therewith.
Referring to the drawings, the apparatus shown includes a rotor member 1 and a stator member 2 coaxially arranged and having a frusto-conical shape. The rotor I. is secured on a shaft 3 journalled at its ends in bearings 4 and 5, see Fig. 3. The stator 2 is comprised of an upper shell member 6 and a lower shell member 7 which are assembled together on horizontal plane X-X by means of suitable anges as shown. Secured in the upper stator shell 6 is a grinding element or set of elements 8 in the form of axially extending ribs and grooves, or serrations. The grinding means 8 are omitted in an area adjacent the inlet feed aperture 13 provided at the top -of the apparatus, as shown. The lower stator shell 7, instead of receiving similar serrated elements as is generally the case in conventional grinders supports an arcuate perforate sheet metal wall 9., Serrationssimilar to the-serrations 8 are provided all around the rotor circumference by forming spaced apart, axially extending grooves in the rotor surface, as shown in Fig. 2.
Deiined by the frame 15 of the apparatus beneath the perforate wall 9 is a collecting chamber 15.). An outlet is formed in a side of this chamber which connects by way of a conduit 11 with the base of a riser pipe or tank 18 provided with a separating Wall 19 and adjustable overflow means 20 at the top of the wall for maintaining a predetermined head of liquid pulp in the tank and thus establishing the desired back pressure within chamber 16 as previously described.
As shown in Fig. l, the perforate Wall 9 includes a solid i.e. imperforate end portion adjacent the large diameter end of the stator and rotor thus defining a chamber in which the Coarser portions of the material tend to collect for the reasons previously stated. An outlet at the xed base.
topof thisfreject chamber is connected with amconduit 14 connected at one end by wayY of a shut-0E- valvewithY the supply inlet 13 for recycling the rejects back into the grinder, and connected at its other end by way of another shut-o: valve to any suitable meansof disposal foriinally 'rejected material. Y
Meansy are provided for axially reciprocating the stator 6-*7V axially of the rotor and forrthis purpose the frame j axial portion thereof extending from said small diameter Yendv a distance corresponding to the length of said grooves of the rotor, the lower portiony of said stator being in the form of a smooth wall having perforations in an axial portion thereof extending fromfs'aid small diameter end to form asieve for the disintegratedmaterial, a substantial 15"is bodily reciprocable 'on slideways 16 relatively to a i The desired axialreciprocation may be mparted tothe frame by way of a linkage 17, see Fig. 3, driven through suitable conventional means from the same power source as that serving to rotate the rotor.
VWhat I claim is: Y Y
Apparatus for dsintegrating andY reining 'cellulosicz material comprising a frustoconical stator arranged with its axis extending substantially horizontally, affrustoconical rotor rotatably mountedpin said stator vcoraxially with the latterand having disintegrating grooves in the surface of the rotor, Vsaid stator having an inlet opening .for'the ma- Y tenal to be treated in its upper portion adjacent the relaaxial llength of sa'idrstator adjacent therelativ'ely large diameter' endY thereof` being smooth andiimperforate at least in said lower portion there'of', and said stator fur ther having an outlet orifice .for in'completelyV disintegrated material opening ,from saidV upper portion adjacent said large diameter end; f 'i UNITED STATESV PATENTS References Cited in the tile of this patent V1,939,747 wiener l r l Dee 1.9,-*1933 2,180,080 Cowles` 4 L' Nov. 14, 1939 2,207,194 Gruendler Y. luly'9,j1940 2,741,954
Allibe a Y lApr. 17; 1956
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR2980350X | 1957-05-24 |
Publications (1)
Publication Number | Publication Date |
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US2980350A true US2980350A (en) | 1961-04-18 |
Family
ID=9690546
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US737929A Expired - Lifetime US2980350A (en) | 1957-05-24 | 1958-05-26 | Fibre disintegrating apparatus |
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US (1) | US2980350A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3138336A (en) * | 1960-07-13 | 1964-06-23 | Lejeune Emile | Pulping machine |
US4500040A (en) * | 1982-04-19 | 1985-02-19 | Bert Steffens | Method and apparatus for separating the components of cellulose sanitary articles |
US4664320A (en) * | 1982-04-19 | 1987-05-12 | Bert Steffens | Apparatus for separating the components of cellulose sanitary articles |
US4955549A (en) * | 1986-08-07 | 1990-09-11 | Sunds Defibrator Aktiebolag | Apparatus for treatment of fibre suspensions |
US5047118A (en) * | 1986-04-10 | 1991-09-10 | Kamyr Ab | Method for decreasing energy consumption during refining of fiber material at a reduced grinding frequency while maintaining capacity |
US5326038A (en) * | 1991-04-12 | 1994-07-05 | Harry Nilsson | Beating apparatus for fiber suspensions |
US20110024539A1 (en) * | 2002-10-24 | 2011-02-03 | Graham Strauss | Distributor Plate |
US20110095113A1 (en) * | 2007-04-05 | 2011-04-28 | Lehigh Technologies, Inc. | Conical-shaped impact mill |
US20150352601A1 (en) * | 2013-01-16 | 2015-12-10 | Cvp Clean Value Plastics Gmbh | Device and method for removing impurities from shredded plastic |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1939747A (en) * | 1933-06-29 | 1933-12-19 | John A Wiener | Fiber-stock refiner |
US2180080A (en) * | 1939-11-14 | Appabatus fob befdhng papeb stock | ||
US2207194A (en) * | 1937-09-07 | 1940-07-09 | Charles D Altick | Means for the manufacture and refining of pulp |
US2741954A (en) * | 1954-01-20 | 1956-04-17 | Black Clawson Co | Refining paper pulp |
-
1958
- 1958-05-26 US US737929A patent/US2980350A/en not_active Expired - Lifetime
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2180080A (en) * | 1939-11-14 | Appabatus fob befdhng papeb stock | ||
US1939747A (en) * | 1933-06-29 | 1933-12-19 | John A Wiener | Fiber-stock refiner |
US2207194A (en) * | 1937-09-07 | 1940-07-09 | Charles D Altick | Means for the manufacture and refining of pulp |
US2741954A (en) * | 1954-01-20 | 1956-04-17 | Black Clawson Co | Refining paper pulp |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3138336A (en) * | 1960-07-13 | 1964-06-23 | Lejeune Emile | Pulping machine |
US4500040A (en) * | 1982-04-19 | 1985-02-19 | Bert Steffens | Method and apparatus for separating the components of cellulose sanitary articles |
US4664320A (en) * | 1982-04-19 | 1987-05-12 | Bert Steffens | Apparatus for separating the components of cellulose sanitary articles |
US5047118A (en) * | 1986-04-10 | 1991-09-10 | Kamyr Ab | Method for decreasing energy consumption during refining of fiber material at a reduced grinding frequency while maintaining capacity |
US4955549A (en) * | 1986-08-07 | 1990-09-11 | Sunds Defibrator Aktiebolag | Apparatus for treatment of fibre suspensions |
US5326038A (en) * | 1991-04-12 | 1994-07-05 | Harry Nilsson | Beating apparatus for fiber suspensions |
US20110024539A1 (en) * | 2002-10-24 | 2011-02-03 | Graham Strauss | Distributor Plate |
US20110095113A1 (en) * | 2007-04-05 | 2011-04-28 | Lehigh Technologies, Inc. | Conical-shaped impact mill |
US8132751B2 (en) * | 2007-04-05 | 2012-03-13 | Lehigh Technologies, Inc. | Conical-shaped impact mill |
US20150352601A1 (en) * | 2013-01-16 | 2015-12-10 | Cvp Clean Value Plastics Gmbh | Device and method for removing impurities from shredded plastic |
US10058898B2 (en) * | 2013-01-16 | 2018-08-28 | Cvp Clean Value Plastics Gmbh | Device and method for removing impurities from shredded plastic |
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