US2220676A - Method and apparatus fob refining - Google Patents
Method and apparatus fob refining Download PDFInfo
- Publication number
- US2220676A US2220676A US2220676DA US2220676A US 2220676 A US2220676 A US 2220676A US 2220676D A US2220676D A US 2220676DA US 2220676 A US2220676 A US 2220676A
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- US
- United States
- Prior art keywords
- chamber
- screen
- impeller
- stock
- refining
- Prior art date
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- Expired - Lifetime
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- 238000007670 refining Methods 0.000 title description 22
- 239000000463 material Substances 0.000 description 60
- 230000005484 gravity Effects 0.000 description 12
- 238000009987 spinning Methods 0.000 description 8
- 239000000203 mixture Substances 0.000 description 6
- 239000002699 waste material Substances 0.000 description 6
- 239000010813 municipal solid waste Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 229920000298 Cellophane Polymers 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000002657 fibrous material Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000010893 paper waste Substances 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
Images
Definitions
- Figure 1 is a front elevation of the apparatus, partly in section, in order to better illustrate the interior thereof.
- Figure 2 is an end elevation.
- Figure 3 is a section on the line 3-3 of Fig- 28 ure 1.
- the outlet opening for discharge of material which falls to pass through the screens is located at the periphery of the impeller chamber.
- the apparatus comprises a casing having opposed end plates I and 2 45 which are spaced by an annular ring 3 located therebetween and forming a substantially cylindrical chamber 4 for purposes hereinafter described.
- the end plate I is provided with an opening 5 constituting an outlet opening from the 50 casing and the chamber 4 and the end plate 2 is provided with a bearing member 6 supporting a shaft 1 carrying an impeller 8 which rotates within the chamber 4.
- the outlet opening 5 is arranged coaxially with the shaft 1.
- plate I is also provided with an outlet opening 9 and the end plate 2 is provided with a similar outletopening I0, the said openings being connected with similar outlet conduits I I.
- the ring 3 is provided with an inlet opening I! which as previously stated, and as illustrated in 5 Figure 3, is arranged substantially tangentially to the periphery of the ring. That is, the inlet opening is. so arranged that the incoming flow of material enters the chamber 4- in a tangential direction, and moves in the same direction that 10 the impeller is moving (clockwise as shown in Figure 3).
- the said ring is also provided with an outlet opening I5 connected by a conduit It to a trap I! for purposes hereinafter described.
- the end plate I is provided with an annular l5 chamber or trough 24 and the end plate 2 is provided with a similar annular chamber or trough 25, which said chambers communicate with the outlet openings 9 and I0 respectively.
- Covering the said annular chambers so as to form one wall thereof are perforated screens 26 and 21 which are thus interposed between the inlet opening I4 and outlet openings 9 and I0 in such manner that material supplied to the apparatus through the inlet opening cannot leave the apparatus through 25 outlet openings 9 and I 0 without passing through screens 25 and 21.
- the said screens which are in the form of annular disks, are supported from behind by grids or frames 28 and 29 having large openings 30 therein so as not to interfere with the flow of material through the screens.
- the screens 26 and 27 are held rigidly in place, being clamped at their outer peripheries between the annular ring 3 and .the supporting frames 28 and 29, which in turn are clamped between the end plates I and 2.
- the inner peripheries of the screens are fastened between the supporting frames 28 and 29 and screen retaining plates 3I and 32 by screws 33.
- the material to be treated be introduced through the inlet opening under pressure, and at suitable velocity, i. e. in the region of 2,000 lineal ft. per minute or more.
- the material may be pumped to the inlet opening by any suitable type of hydraulic pump, as for example a centrifugal pump. Therefore, the impeller 3 need not be relied upon, as before, to circulate the material, but merely keeps the material in circulation and carries the scrapers 40 iii) which perform the functions described in my previous application. Accordingly, it is necessary to supply very little power to the shaft 1, it being sufiicient merely to overcome the friction of the scrapers against the screens.
- the impeller comprises a plurality of radial vanes 35 reinforced by web members 35 and carrying scrapers M of any suitable construction such, for example, as those disclosed in said application.
- the trash and undefibered material which it is desired to separate from the useful fibrous material which passes through the screens may be of various types, depending on the kind of material being treated.
- waste paper there are certain waste materials of high specific gravity such as sand, bits of glass, metal, etc., which must be separated out, and there are also certain waste materials of low specific gravity such as strings, rubber bands, Cellophane, wood, etc., which must be separated out.
- the present apparatus is particularly well adapted to the separation of both types of waste materials, for the relatively high velocity of the material in the casing produces a centrifugal action which throws the heavy materials outwardly toward the periphery where they can enter the outlet opening it, and permits the light materials to move toward .the axis where they can enter the outlet opening 5.
- the heavy materials which enter the outlet opening i5 fall into the trap ill from which they may be removed through valve iii.
- the trap may be provided with a pipe connection i9 having a valve through which water may be introduced to the trap at a rate sufficient to cause a slow fiow from the trap to the chamber i. If the rate is properly adjusted, the flow will not interfere with the entrance of heavy materials, but will prevent entrance and loss of good fibers.
- the ight materials which enter the outlet opening 5 may be removed by permitting continuous flow through said opening or by causing intermittent fiow therethrough by periodically opening and closing a valve controlling said openmg.
- Method of refining paper stock which comprises spinning said stock at relatively high velocity in a substantially cylindrical chamber having a perforated screen therein and forming one wall thereof, introducing said stock tangentially through the cylindrical wall of said chamber in a direction parallel to said screen, withdrawing screened stock through said screen, and with drawing rejected material axially through the end wall of said chamber in a direction at right angles to said screen.
- Method of refining paper stock which comprises spinning said stock at relatively high velocity in a substantially cylindrical chamber having a perforated screen therein and forming one wall thereof, introducing said stock tangentially through the cylindrical wall of said chamber in a direction parallel to said screen, working said stock against said screen by means of rotatable scrapers engaging said screen, withdrawing screened stock through said screen, and withdrawing rejected material axially through the end wall of said chamber in a direction at right angles to said screen.
- Method of refining paper stock which comprises spinning said stock at relatively high velocity in a substantially cylindrical chamber having a perforated screen therein and forming one wall thereof, introducing said stock tangentially through the cylindrical wall of said chamber in a direction parallel to said screen, withdrawing screened stock through said screen, withdrawing rejected material of low specific gravity axially through the end wall of said chamber in a direction at right angles to said screen, and withdrawing rejected material of high specific gravity through the cylindrical wall of said cham ber.
- Method of refining paper stock which comprises spinning said stock at relatively high velocity in a substantially cylindrical chamber having a perforated screen therein and forming onewall thereof, introducing said stock tangentially through the cylindrical wall of said chamher in a direction parallel to said screen, working said stock against said screen by means of rotatable scrapers engaging said screen, withdrawing screened stock through said screen, withdrawing rejected material of low specific gravity axially through the end wall of said chamber in a direction at right angles to said screen, and withdrawing rejected material of high specific gravity through the cylindrical wall of said chamber.
- Apparatus for refining paper stock comprising, in combination, a casing having opposed end plates and an annular member therebetween spacing said plates to form an impeller chamber, an impeller mounted for rotation in said chamber on an axis coinciding with the axis of said annular member, a screen in said chamber, said screen being fiat and lying in a plane perpendicular to the axis of said impeller, said casing being provided with inlet and outlet openings to and from said chamber on opposite sides of said screen, said inlet opening being located in said annular member, a conduit connected to said inlet opening, said conduit being arranged to direct the incoming fiow of material substantially tangentially to the inner wall of said annular member, and said casing being provided with an additional outlet opening located coaxially with the axis of said impeller.
- Apparatus for refining paper stock comprising, in combination, a casing having opposed end plates and an annular member therebetween spacing said plates to form an impeller chamber, an impeller mounted for rotation in said chamber on an axis coinciding with the axis of said annular member, a screen in said chamber, said screen being fiat and lying in a plane perpendicular to the axis of said impeller, said casing being provided with inlet and outlet openings to and from said chamber on opposite sides of said screen, said inlet opening being located in said annular member, a conduit connected to said inlet opening, said conduit being arranged to direct the incoming fiow of material substantially tangentially to the inner wall of said annular member, said casing being provided with an additional outlet opening located coaxially with the axis of said impeller, and said annular bit , member being provided with a second additional being provided with inlet and outlet openings to outlet opening spaced from said inlet opening.
- Apparatus for refining paper stock, comscreen said inlet opening being located in said prising, in combination, a casing having opposed annular member, a conduit connected to said end plates and an annular member therebetween inlet opening, said conduit being arranged to 5 spacing said plates to form an impeller chamber, direct the incoming flow of material substantial- Van impeller mounted for rotation in said cham- 1y tangentially to the inner wall of said annular her on an axis coinciding with the axis of said member, and said casing being provided with an annular member, a screen in said chamber, said additional outlet opening located coaxially with screen being flat and lying in a plane perpenthe axis of said impeller. 10 dicular to the axis or said impeller, scrapers on EDWIN COWLES.
Description
NOV. 5, CQWLES 2,220,676
METHOD AND APPARATUS FOR REFINING PAPER STOCK Filed July 29, 1957 2 Sheets-Sheet 1 2 5 2 [NiNTOR ATTORNEY Nov. 5, 1940.
E. COWLES METHOD AND APPARATUS FOR REFINING PAPER STOCK Filed July 29, 1937 2 Sheets-Sheet 2 I 2 {N ViNfole Patented Nov. 5, 1940 UNITED STATES lMETHOD AND APPARATUS FOR REFINING PAPER STOCK Edwin Cowles, Hopewell, N. J., assignor to The I Cowles Company, Princeton, N. J a corporation of New Jersey Application July 29, 1937, Serial No. 156,268
7 Claims.
It is an object of the invention to improve the hydraulic efiiciency of such apparatus, and thereby to effect a saving in the amount of power rejo quired: and it is a further object of the invention to improve the performance of the apparatus,
particularly with respect to the separation and discharge of trash and undefibered material which falls to pass through the screens.
15 Other objects and advantages of the invention will appear hereinafter.
A preferred embodiment of the invention selected for purposes of illustration is shown in the accompanying drawings, in which,
20 Figure 1 is a front elevation of the apparatus, partly in section, in order to better illustrate the interior thereof.
Figure 2 is an end elevation.
Figure 3 is a section on the line 3-3 of Fig- 28 ure 1.
In the apparatus disclosed in my prior patent and application the inlet opening, through which material is introduced to the impeller chamber, is arranged coaxially with the impeller shaft, and
30 the outlet opening for discharge of material which falls to pass through the screens is located at the periphery of the impeller chamber.
According to the present invention I propose to introduce material to the impeller chamber 35 through an inlet opening located at the periphery of the impeller chamber, and preferably in a direction substantially tangential to the periphery. I also propose to discharge material which fails to pass through the screens through a plurality of outlet openings, one of which is coaxial with the impeller shaft, and another of which is located at the periphery of the impeller chamber.
Referring to the drawings, the apparatus comprises a casing having opposed end plates I and 2 45 which are spaced by an annular ring 3 located therebetween and forming a substantially cylindrical chamber 4 for purposes hereinafter described. The end plate I is provided with an opening 5 constituting an outlet opening from the 50 casing and the chamber 4 and the end plate 2 is provided with a bearing member 6 supporting a shaft 1 carrying an impeller 8 which rotates within the chamber 4. As shown, the outlet opening 5 is arranged coaxially with the shaft 1. The
55 plate I is also provided with an outlet opening 9 and the end plate 2 is provided with a similar outletopening I0, the said openings being connected with similar outlet conduits I I.
The ring 3 is provided with an inlet opening I! which as previously stated, and as illustrated in 5 Figure 3, is arranged substantially tangentially to the periphery of the ring. That is, the inlet opening is. so arranged that the incoming flow of material enters the chamber 4- in a tangential direction, and moves in the same direction that 10 the impeller is moving (clockwise as shown in Figure 3).. The said ring is also provided with an outlet opening I5 connected by a conduit It to a trap I! for purposes hereinafter described.
The end plate I is provided with an annular l5 chamber or trough 24 and the end plate 2 is provided with a similar annular chamber or trough 25, which said chambers communicate with the outlet openings 9 and I0 respectively. Covering the said annular chambers so as to form one wall thereof are perforated screens 26 and 21 which are thus interposed between the inlet opening I4 and outlet openings 9 and I0 in such manner that material supplied to the apparatus through the inlet opening cannot leave the apparatus through 25 outlet openings 9 and I 0 without passing through screens 25 and 21.
The said screens, which are in the form of annular disks, are supported from behind by grids or frames 28 and 29 having large openings 30 therein so as not to interfere with the flow of material through the screens. The screens 26 and 27 are held rigidly in place, being clamped at their outer peripheries between the annular ring 3 and .the supporting frames 28 and 29, which in turn are clamped between the end plates I and 2. The inner peripheries of the screens are fastened between the supporting frames 28 and 29 and screen retaining plates 3I and 32 by screws 33.
Any suitable type of perforated screen may be employed, but I prefer to use the type of screen disclosed in my said Patent No. 2,180,080 to which reference may be had for a more complete description.
According to the present invention it is proposed that the material to be treated be introduced through the inlet opening under pressure, and at suitable velocity, i. e. in the region of 2,000 lineal ft. per minute or more. For this purpose the material may be pumped to the inlet opening by any suitable type of hydraulic pump, as for example a centrifugal pump. Therefore, the impeller 3 need not be relied upon, as before, to circulate the material, but merely keeps the material in circulation and carries the scrapers 40 iii) which perform the functions described in my previous application. Accordingly, it is necessary to supply very little power to the shaft 1, it being sufiicient merely to overcome the friction of the scrapers against the screens. Consequently there is an important gain in efliclency, for since pumps of high efiiciency are readily obtainable, the total power iniput to pump and impeller is considerably less than that required to drive the impeller alone when said impeller is used to circulate the material.
The impeller comprises a plurality of radial vanes 35 reinforced by web members 35 and carrying scrapers M of any suitable construction such, for example, as those disclosed in said application.
It will be understood that the trash and undefibered material which it is desired to separate from the useful fibrous material which passes through the screens may be of various types, depending on the kind of material being treated. In the case of waste paper, there are certain waste materials of high specific gravity such as sand, bits of glass, metal, etc., which must be separated out, and there are also certain waste materials of low specific gravity such as strings, rubber bands, Cellophane, wood, etc., which must be separated out. From the foregoing descrip- .tion, it will be seen that the present apparatus is particularly well adapted to the separation of both types of waste materials, for the relatively high velocity of the material in the casing produces a centrifugal action which throws the heavy materials outwardly toward the periphery where they can enter the outlet opening it, and permits the light materials to move toward .the axis where they can enter the outlet opening 5.
The heavy materials which enter the outlet opening i5 fall into the trap ill from which they may be removed through valve iii. If desired the trap may be provided with a pipe connection i9 having a valve through which water may be introduced to the trap at a rate sufficient to cause a slow fiow from the trap to the chamber i. If the rate is properly adjusted, the flow will not interfere with the entrance of heavy materials, but will prevent entrance and loss of good fibers.
The ight materials which enter the outlet opening 5 may be removed by permitting continuous flow through said opening or by causing intermittent fiow therethrough by periodically opening and closing a valve controlling said openmg.
It will be understood that the invention may be variously modified and embodied within the scope of the subjoined claims.
I claim as my invention:
1. Method of refining paper stock which comprises spinning said stock at relatively high velocity in a substantially cylindrical chamber having a perforated screen therein and forming one wall thereof, introducing said stock tangentially through the cylindrical wall of said chamber in a direction parallel to said screen, withdrawing screened stock through said screen, and with drawing rejected material axially through the end wall of said chamber in a direction at right angles to said screen.
2. Method of refining paper stock which comprises spinning said stock at relatively high velocity in a substantially cylindrical chamber having a perforated screen therein and forming one wall thereof, introducing said stock tangentially through the cylindrical wall of said chamber in a direction parallel to said screen, working said stock against said screen by means of rotatable scrapers engaging said screen, withdrawing screened stock through said screen, and withdrawing rejected material axially through the end wall of said chamber in a direction at right angles to said screen.
3. Method of refining paper stock which comprises spinning said stock at relatively high velocity in a substantially cylindrical chamber having a perforated screen therein and forming one wall thereof, introducing said stock tangentially through the cylindrical wall of said chamber in a direction parallel to said screen, withdrawing screened stock through said screen, withdrawing rejected material of low specific gravity axially through the end wall of said chamber in a direction at right angles to said screen, and withdrawing rejected material of high specific gravity through the cylindrical wall of said cham ber.
4. Method of refining paper stock which comprises spinning said stock at relatively high velocity in a substantially cylindrical chamber having a perforated screen therein and forming onewall thereof, introducing said stock tangentially through the cylindrical wall of said chamher in a direction parallel to said screen, working said stock against said screen by means of rotatable scrapers engaging said screen, withdrawing screened stock through said screen, withdrawing rejected material of low specific gravity axially through the end wall of said chamber in a direction at right angles to said screen, and withdrawing rejected material of high specific gravity through the cylindrical wall of said chamber.
5. Apparatus for refining paper stock, comprising, in combination, a casing having opposed end plates and an annular member therebetween spacing said plates to form an impeller chamber, an impeller mounted for rotation in said chamber on an axis coinciding with the axis of said annular member, a screen in said chamber, said screen being fiat and lying in a plane perpendicular to the axis of said impeller, said casing being provided with inlet and outlet openings to and from said chamber on opposite sides of said screen, said inlet opening being located in said annular member, a conduit connected to said inlet opening, said conduit being arranged to direct the incoming fiow of material substantially tangentially to the inner wall of said annular member, and said casing being provided with an additional outlet opening located coaxially with the axis of said impeller.
6. Apparatus for refining paper stock, comprising, in combination, a casing having opposed end plates and an annular member therebetween spacing said plates to form an impeller chamber, an impeller mounted for rotation in said chamber on an axis coinciding with the axis of said annular member, a screen in said chamber, said screen being fiat and lying in a plane perpendicular to the axis of said impeller, said casing being provided with inlet and outlet openings to and from said chamber on opposite sides of said screen, said inlet opening being located in said annular member, a conduit connected to said inlet opening, said conduit being arranged to direct the incoming fiow of material substantially tangentially to the inner wall of said annular member, said casing being provided with an additional outlet opening located coaxially with the axis of said impeller, and said annular bit , member being provided with a second additional being provided with inlet and outlet openings to outlet opening spaced from said inlet opening. and from said chamber on opposite sides of said 7. Apparatus for refining paper stock, comscreen, said inlet opening being located in said prising, in combination, a casing having opposed annular member, a conduit connected to said end plates and an annular member therebetween inlet opening, said conduit being arranged to 5 spacing said plates to form an impeller chamber, direct the incoming flow of material substantial- Van impeller mounted for rotation in said cham- 1y tangentially to the inner wall of said annular her on an axis coinciding with the axis of said member, and said casing being provided with an annular member, a screen in said chamber, said additional outlet opening located coaxially with screen being flat and lying in a plane perpenthe axis of said impeller. 10 dicular to the axis or said impeller, scrapers on EDWIN COWLES.
said impeller engaging said screen, said casing v
Publications (1)
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US2220676A true US2220676A (en) | 1940-11-05 |
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US2220676D Expired - Lifetime US2220676A (en) | Method and apparatus fob refining |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2452135A (en) * | 1944-10-26 | 1948-10-26 | Harmer R Lutz | Paper pulp machine |
US2581143A (en) * | 1947-04-02 | 1952-01-01 | Noble & Wood Machine Company | Stuff treatment apparatus |
US4136018A (en) * | 1977-11-10 | 1979-01-23 | Beloit Corporation | Vortex separator with coaxial inlet and lightweight reject pipelines |
US4222817A (en) * | 1978-06-26 | 1980-09-16 | Beloit Corporation | Method and apparatus for pulping and grading waste material |
-
0
- US US2220676D patent/US2220676A/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2452135A (en) * | 1944-10-26 | 1948-10-26 | Harmer R Lutz | Paper pulp machine |
US2581143A (en) * | 1947-04-02 | 1952-01-01 | Noble & Wood Machine Company | Stuff treatment apparatus |
US4136018A (en) * | 1977-11-10 | 1979-01-23 | Beloit Corporation | Vortex separator with coaxial inlet and lightweight reject pipelines |
US4222817A (en) * | 1978-06-26 | 1980-09-16 | Beloit Corporation | Method and apparatus for pulping and grading waste material |
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