CA1302302C - Apparatus for separation of solid from liquid - Google Patents
Apparatus for separation of solid from liquidInfo
- Publication number
- CA1302302C CA1302302C CA000522514A CA522514A CA1302302C CA 1302302 C CA1302302 C CA 1302302C CA 000522514 A CA000522514 A CA 000522514A CA 522514 A CA522514 A CA 522514A CA 1302302 C CA1302302 C CA 1302302C
- Authority
- CA
- Canada
- Prior art keywords
- screen
- disc screen
- liquid
- vessel
- solid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 35
- 239000007787 solid Substances 0.000 title abstract description 43
- 238000000926 separation method Methods 0.000 title abstract description 7
- 239000000706 filtrate Substances 0.000 claims abstract description 20
- 239000012530 fluid Substances 0.000 claims abstract description 18
- 239000002826 coolant Substances 0.000 claims abstract description 15
- 238000005406 washing Methods 0.000 abstract description 14
- 238000011001 backwashing Methods 0.000 description 7
- 238000001914 filtration Methods 0.000 description 7
- 238000003754 machining Methods 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 206010000369 Accident Diseases 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000001154 acute effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000010705 motor oil Substances 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/15—Filters with filtering elements which move during the filtering operation with rotary plane filtering surfaces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/44—Regenerating the filter material in the filter
- B01D33/46—Regenerating the filter material in the filter by scrapers, brushes nozzles or the like acting on the cake-side of the filtering element
- B01D33/463—Regenerating the filter material in the filter by scrapers, brushes nozzles or the like acting on the cake-side of the filtering element nozzles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/44—Regenerating the filter material in the filter
- B01D33/48—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
- B01D33/50—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps with backwash arms, shoes or nozzles
Abstract
AN APPARATUS FOR SEPARATION OF SOLID FROM LIQUID
ABSTRACT
An apparatus for separating solids from various types of liquid is disclosed, which includes a vessel for a filtrate arranged adjacent to one side wall of receiving vessel for a solid-containing liquid, and a disc screen arranged at an opening of the side wall using a liquid seal, the disc screen being connected to a rotary shaft which in turn is connected to a driving source, while the disc screen at its surface of the filtrate vessel side being opposed with an ejecting nozzle for a washing fluid thereby to back-wash the disc screen during its rotation, resulting in an excellent solid/liquid separator having capability of preventing the clogging of the solids in the screen and continuous operation, as well as the compactness and high capacity of the apparatus.
The apparatus according to the invention may be applied effectively to the separation of, for example, chips from a coolant for various machines.
ABSTRACT
An apparatus for separating solids from various types of liquid is disclosed, which includes a vessel for a filtrate arranged adjacent to one side wall of receiving vessel for a solid-containing liquid, and a disc screen arranged at an opening of the side wall using a liquid seal, the disc screen being connected to a rotary shaft which in turn is connected to a driving source, while the disc screen at its surface of the filtrate vessel side being opposed with an ejecting nozzle for a washing fluid thereby to back-wash the disc screen during its rotation, resulting in an excellent solid/liquid separator having capability of preventing the clogging of the solids in the screen and continuous operation, as well as the compactness and high capacity of the apparatus.
The apparatus according to the invention may be applied effectively to the separation of, for example, chips from a coolant for various machines.
Description
~3~Z3~
_ ELD OF THE INVENTION
This invention relates to an apparatus for filtering solids from a solid-containing liquid through a screen and transporting the separated solids.
BACKGROUND OF THE INVENTION
Heretofore, various apparatus for removing relatively large machined chips have been proposed and utilized for treating these chips produced by machine tools. However, these apparatus cannot remove fine chips, which in turn are collected together with a machining fluid in a coolant tank and precipitated therein. Thus, if a large amount of the fine chips precipitates in the coolant tank, a capacity of the tank is insufficient for the coolant, which overflows from the tank. As a result, a fire accident may occur due to oily property of the coolant. Further, circulation of the unremoved chips together with the coolant may bloc~ an e~ecting nozzle for the coolant, thereby to cause damage of the tools and worse quality of machined works. Furthermore, a setting disorder may arise in a machining center upon replacement of automatic tools, thereby to adversely affect a machining accuracy.
In view of the foregoing, an apparatus of such a type has been proposed that a conventional coolant tank is provided at its inner bottom with a screw conveyor for removing the precipitated chips therefrom. In such type of apparatus, however, the conveyor was generally arranged horizontally in consideration of its conveying capacity and ~3~J2302 was impossible to be arranged obliquely for the purpose of reducing a setting area.
Since most of the machined chips are generally magnetic in nature, an apparatus provided at its bottom with a magnetic plate has also been proposed to aggregate the magnetic chips at the bottom within the tank, from which they are scraped and removed by a scraper. Such apparatus, however, necessitates also enlargement of a setting area for the magnetic plate in order to increase the aggregation, thereby to require a large size of the scraper. Thus, the apparatus has a further disadvantage in that only very limited amount of non-magnetic chips may be removed.
For solving the foregoing problems, there has been proposed an apparatus for filtering the chips from chip-containing liquid, such as a coolant, by use of a filtering means, such as a screen, and transporting the chips on a screw conveyor, a~ disclosed in U.S Patent 3,585,924. How-ever, the apparatus of such type often becomes impossible to filter the chips due to adhesion and clogging of the chips to the screw conveyor for cleaning the filtering means, resulting in a time-consuming, troublesome and ineEficient operation.
Accordingly, it has long been needed to provide an apparatus for treating chips, which is compact and achieves efficient recovery and removal of the chips, as well as reduction of the equipment cost.
It has now been found out that suspending and precipi-tating solids in liquid may be surely filtered by arranging ~3(J~;~3~
a filtrate vessel adjacent to one side of a receiving vessel for a solid-containing liquid, providing rota~ably a disc screen between the receiving vessel and the filtrate vessel for communicating these vessels with each other, and arrang-ing an ejecting nozzle for ejecting a washing fluid which isdirected against the screen from its filtrate vessel side, resulting in the effective cleaning of the screen and thus efficient operation of the apparatus.
Due to its ability of the effective and continuous filtration of the solids through the screen, the apparatus may be compact in construction and have an ability of treat-ing a large quantity of the liquid containing chips.
Further, the compactness of the apparatus requires less volume and thus less space of its placement.
Accordingly, an object of the invention is to provide an apparatus for separation of solids from a liquid, which has several advantages of compactness, efficient filtration, convenient maintenance, small space for placement, and reduced cost for equipment.
SVMMARY OF THE INVENT_ON
In order to achieve the above object, the invention provides a solid/liquid separator, which comprises a vessel for a Eiltrate arranged adjacent to one side wall of a receiving vessel for a solid-containing liquid, and a disc screen arranged at an opening of the side wall using a liquid seal, said disc screen being connected to a rotary shaft which in turn is connected to a driving source, said 13(~23~:
disc screen at its surface of the filtrate vessel side being opposed with an ejecting nozzle for a washing fluid, thereby to back-wash the disc screen during its rotation.
The invention will be described hereinbelow in more detail for better understanding with reference to preferred embodiments of the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
Figure 1 is a schematic side sectional view of one embodiment of the solid/liquid separator according to the invention;
Figure 2 is a sectional view taken along the line II-II
in Fig. l; and Figure 3 is a sectional side view of main portions of another embodiment according to the invention.
PREFERRED EMBODIMENTS OF THE INVENTION
Figures 1 and 2 illustrate one embodiment of the apparatus for solid/liquid separation according to the in-vention. In Fig. 1, reference 10 represents a receivng vessel for rèceiving a solid-containing liquid, while refer-ence 12 represents a filtrate vessel arranged adjacent to one side wall 14 of the receiving vessel 10. The side wall 14 is provided with a disc screen 16 by means of a peripher-al sealing material 18, through which screen the receiving vessel 10 and the filtrate vessel 12 are communicated with each other. The disc screen 16 at its center is connected to one end of a rotary shaft 20, one end of which in turn is ~3~3~
rotatably connected to a driving source 22, such as an electric motor. From the filtrate vessel 12 is extended a pipe 24 which is communicated with a storage tank 26 for collecting a filtrate. The separated solids 28 may be deposited from the solid-containing li~uid onto a bottom of the receiving vessel 10.
Especially in accordance with the invention, the disc screen 16 may be made not only of a wedge wire or mesh screen in the range of 60 to 200 mesh size but also of a punched plate with or without a nylon or teflon net. In order to mount the disc screen 16 rotatably to the rotary shaft 20, as shown in Fig. 2, there is provided with a supporting element 36 comprising a boss 30 mounted to a front end of the rotary shaft 20, a plurality of arms 32 protruded radially outward from the boss 30, and a ring element 34 attached peripherally to the arm 32, while the screen material is extended over the supporting element 36.
The disc screen 16 thus constructed may Eilter the solids deposited thereon when the receiving vessel 10 receives the solid-containing liquid, and may feed the filtrate appropriately to the filtrate vessel 12. The deposited solids on the screen 16 cannot be readily removed, however, merely by rotation of the disc screen 16. Accord-ing to the invention, therefore, the filtrate vessel 12 at its inner portion is arranged an ejecting nozzle 38 for a washing fluid which is directed against the rotating screen surface in order to achieve back-washing. For this purpose, the washinq fluid may be either a clean gas or liquid when 131~}Z3C~Z
the nozzle 38 is located above a filtrate level in the vessel 12. Preferably, however, the storage tank 26 and the ejecting nozzle 38 may be connected by means of a pipe 40, as shown in Fig. 1, which pipe at its portion is provided with a pump 42 for utilizing the filtrate as the washing liquid.
The most effective back-washing of the disc screen 16 may be varied depending on an outer diameter and a mesh size of the screen 16, a rotation rate and others. Preferably, the outer diameter of 100 to 500 mm, the mesh size of 60 to 200, the rotation rate of 1 to 50 r.p.m., the washing fluid pressure of about 1 to 3 kg/cm2 and the ejecting flow rate of 20 to 50 l/min may be usually effective for the back-washing.
Further, the back-washing by the washing fluid against the disc screen 16 may be carried out either continuously or batchwise. In addition or alternate to the nozzle 38, the screen surface on the receiving vessel side is contacted with a scraper (not shown) when the deposited solids are difficut to be eliminated, thereby to forcibly scrape off the deposited solids from the surface for improving the washing effect.
In operation of the solid/liquid separator of the above embodiment, the disc screen 16 is rotated by the electric motor 22 while the coolant containing the solids 28, such as chips, is introduced into the receiving vessel 10. Thus, the disc screen may filter the solids 28 and pass the coolant through the screen to the storage tank 26 via the 13~23(~Z
filtrate vessel 12. A portion of the filtered solids remains deposited on the screen surface but is subjected to the back-washing action of the washing fluid from the nozzle 38, thereby to fall on its own gravity onto the bottom of the receiving vessel 10 for deposition. The deposited por-tion of the solids 28 may be optionally removed automatical-ly or intermittently from the bottom of the receving vessel 10 by a conveyor which is optionally arranged under the receiving vessel 10.
Figure 3 illustrates another embodiment of the appara-tus according to the invention, wherein the same references are used for the same elements of the previous embodiment for omitting the detailed description therefor. According to this embodiment, the ejecting nozzle 38 for the washing fluid is dipped in the filtrate, while the receiving vessel 10 at its upper portion is provided wlth another nozzle 44 for a surface washing fluid so as to be directed against the surface of the screen 16 with a certain degree of inclina-tion (an acute angle). Otherwise, the construction is sub-stantially same as in the apparatus shown in Fig. 1. As the driving source 22 connected to the rotary shaft 20 for rotating the disc screen 16, there may be employed a direct connection of the rotary shaft 20 with a driving shaft of the electric motor, a gear connection system or a transmis-sion system utilizing an endless chain or belt connected with a remote electric motor.
In operation of the solid/liquid separator according to this embodiment, the electric motor is driven to rotate the ~3~~ 23~Z
disc screen 16 for filtering the solid~containing coolant introduced into the receiving vessel 10, as described for the previous embodiment. The screen 16 may filter the solids 28 and pass the filtrate therethrough. In this embodiment, however, the ejecting nozzle 38 dipped in the filtrate may eject the washing liquid for back-washing the deposited solids on the screen 16 and subsequently the other nozzle 44 may eject the washing fluid against the surface of the disc screen 16, thereby to ensure removal of the solids remaining unseparated after the back-washing.
As apparent from the embodiments described herein-above, in accordance with the invention the solid/liquid separation may be achieved by the rotating disc screen, and the disc screen may be back-wahsed continuously or intermit-tently by the washing fluid, thereby to prevent clogging dueto adhesion of the solids, to maintain the effective solid/
liquid separation and to enhance the treating capacity considerably.
Further, the separated solids may be automatically collected and removed by an optional conveyor system.
Thus, the apparatus according to the invention may be constructed in a compact type, requires less space for placement, and is convenient in maintenance of the disc screen with its separating function, thereby to significant-ly reduce the production and maintenance cost of the appara-tus. In particular, the solid/liquid separator according to the invention may be conveniently and readily attached to the conventional existing solid/liquid separating tank.
_ - 8 -13~Z3~2 Further, any number of such apparatus may be arranged for selectively setting or improving the treating capacity of the solid-containing liquid.
Although the invention has been described herein-above with the preferred embodiments, it will be appreciated that the apparatus according to the invention may be widely applied to various machine tools, such as a cutter, a grinder, a rolling mill, a scrubber, a honing machine and others, for separating inorganic suspended matters (such as iron chips) from a machining oily fluid or an engine oil, or to a solid/liquid separator for a liquid containing sands or activated carbons t and that many variations and modifica-tions may be made without departing from the true spirit and scope of the invention.
_ ELD OF THE INVENTION
This invention relates to an apparatus for filtering solids from a solid-containing liquid through a screen and transporting the separated solids.
BACKGROUND OF THE INVENTION
Heretofore, various apparatus for removing relatively large machined chips have been proposed and utilized for treating these chips produced by machine tools. However, these apparatus cannot remove fine chips, which in turn are collected together with a machining fluid in a coolant tank and precipitated therein. Thus, if a large amount of the fine chips precipitates in the coolant tank, a capacity of the tank is insufficient for the coolant, which overflows from the tank. As a result, a fire accident may occur due to oily property of the coolant. Further, circulation of the unremoved chips together with the coolant may bloc~ an e~ecting nozzle for the coolant, thereby to cause damage of the tools and worse quality of machined works. Furthermore, a setting disorder may arise in a machining center upon replacement of automatic tools, thereby to adversely affect a machining accuracy.
In view of the foregoing, an apparatus of such a type has been proposed that a conventional coolant tank is provided at its inner bottom with a screw conveyor for removing the precipitated chips therefrom. In such type of apparatus, however, the conveyor was generally arranged horizontally in consideration of its conveying capacity and ~3~J2302 was impossible to be arranged obliquely for the purpose of reducing a setting area.
Since most of the machined chips are generally magnetic in nature, an apparatus provided at its bottom with a magnetic plate has also been proposed to aggregate the magnetic chips at the bottom within the tank, from which they are scraped and removed by a scraper. Such apparatus, however, necessitates also enlargement of a setting area for the magnetic plate in order to increase the aggregation, thereby to require a large size of the scraper. Thus, the apparatus has a further disadvantage in that only very limited amount of non-magnetic chips may be removed.
For solving the foregoing problems, there has been proposed an apparatus for filtering the chips from chip-containing liquid, such as a coolant, by use of a filtering means, such as a screen, and transporting the chips on a screw conveyor, a~ disclosed in U.S Patent 3,585,924. How-ever, the apparatus of such type often becomes impossible to filter the chips due to adhesion and clogging of the chips to the screw conveyor for cleaning the filtering means, resulting in a time-consuming, troublesome and ineEficient operation.
Accordingly, it has long been needed to provide an apparatus for treating chips, which is compact and achieves efficient recovery and removal of the chips, as well as reduction of the equipment cost.
It has now been found out that suspending and precipi-tating solids in liquid may be surely filtered by arranging ~3(J~;~3~
a filtrate vessel adjacent to one side of a receiving vessel for a solid-containing liquid, providing rota~ably a disc screen between the receiving vessel and the filtrate vessel for communicating these vessels with each other, and arrang-ing an ejecting nozzle for ejecting a washing fluid which isdirected against the screen from its filtrate vessel side, resulting in the effective cleaning of the screen and thus efficient operation of the apparatus.
Due to its ability of the effective and continuous filtration of the solids through the screen, the apparatus may be compact in construction and have an ability of treat-ing a large quantity of the liquid containing chips.
Further, the compactness of the apparatus requires less volume and thus less space of its placement.
Accordingly, an object of the invention is to provide an apparatus for separation of solids from a liquid, which has several advantages of compactness, efficient filtration, convenient maintenance, small space for placement, and reduced cost for equipment.
SVMMARY OF THE INVENT_ON
In order to achieve the above object, the invention provides a solid/liquid separator, which comprises a vessel for a Eiltrate arranged adjacent to one side wall of a receiving vessel for a solid-containing liquid, and a disc screen arranged at an opening of the side wall using a liquid seal, said disc screen being connected to a rotary shaft which in turn is connected to a driving source, said 13(~23~:
disc screen at its surface of the filtrate vessel side being opposed with an ejecting nozzle for a washing fluid, thereby to back-wash the disc screen during its rotation.
The invention will be described hereinbelow in more detail for better understanding with reference to preferred embodiments of the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
Figure 1 is a schematic side sectional view of one embodiment of the solid/liquid separator according to the invention;
Figure 2 is a sectional view taken along the line II-II
in Fig. l; and Figure 3 is a sectional side view of main portions of another embodiment according to the invention.
PREFERRED EMBODIMENTS OF THE INVENTION
Figures 1 and 2 illustrate one embodiment of the apparatus for solid/liquid separation according to the in-vention. In Fig. 1, reference 10 represents a receivng vessel for rèceiving a solid-containing liquid, while refer-ence 12 represents a filtrate vessel arranged adjacent to one side wall 14 of the receiving vessel 10. The side wall 14 is provided with a disc screen 16 by means of a peripher-al sealing material 18, through which screen the receiving vessel 10 and the filtrate vessel 12 are communicated with each other. The disc screen 16 at its center is connected to one end of a rotary shaft 20, one end of which in turn is ~3~3~
rotatably connected to a driving source 22, such as an electric motor. From the filtrate vessel 12 is extended a pipe 24 which is communicated with a storage tank 26 for collecting a filtrate. The separated solids 28 may be deposited from the solid-containing li~uid onto a bottom of the receiving vessel 10.
Especially in accordance with the invention, the disc screen 16 may be made not only of a wedge wire or mesh screen in the range of 60 to 200 mesh size but also of a punched plate with or without a nylon or teflon net. In order to mount the disc screen 16 rotatably to the rotary shaft 20, as shown in Fig. 2, there is provided with a supporting element 36 comprising a boss 30 mounted to a front end of the rotary shaft 20, a plurality of arms 32 protruded radially outward from the boss 30, and a ring element 34 attached peripherally to the arm 32, while the screen material is extended over the supporting element 36.
The disc screen 16 thus constructed may Eilter the solids deposited thereon when the receiving vessel 10 receives the solid-containing liquid, and may feed the filtrate appropriately to the filtrate vessel 12. The deposited solids on the screen 16 cannot be readily removed, however, merely by rotation of the disc screen 16. Accord-ing to the invention, therefore, the filtrate vessel 12 at its inner portion is arranged an ejecting nozzle 38 for a washing fluid which is directed against the rotating screen surface in order to achieve back-washing. For this purpose, the washinq fluid may be either a clean gas or liquid when 131~}Z3C~Z
the nozzle 38 is located above a filtrate level in the vessel 12. Preferably, however, the storage tank 26 and the ejecting nozzle 38 may be connected by means of a pipe 40, as shown in Fig. 1, which pipe at its portion is provided with a pump 42 for utilizing the filtrate as the washing liquid.
The most effective back-washing of the disc screen 16 may be varied depending on an outer diameter and a mesh size of the screen 16, a rotation rate and others. Preferably, the outer diameter of 100 to 500 mm, the mesh size of 60 to 200, the rotation rate of 1 to 50 r.p.m., the washing fluid pressure of about 1 to 3 kg/cm2 and the ejecting flow rate of 20 to 50 l/min may be usually effective for the back-washing.
Further, the back-washing by the washing fluid against the disc screen 16 may be carried out either continuously or batchwise. In addition or alternate to the nozzle 38, the screen surface on the receiving vessel side is contacted with a scraper (not shown) when the deposited solids are difficut to be eliminated, thereby to forcibly scrape off the deposited solids from the surface for improving the washing effect.
In operation of the solid/liquid separator of the above embodiment, the disc screen 16 is rotated by the electric motor 22 while the coolant containing the solids 28, such as chips, is introduced into the receiving vessel 10. Thus, the disc screen may filter the solids 28 and pass the coolant through the screen to the storage tank 26 via the 13~23(~Z
filtrate vessel 12. A portion of the filtered solids remains deposited on the screen surface but is subjected to the back-washing action of the washing fluid from the nozzle 38, thereby to fall on its own gravity onto the bottom of the receiving vessel 10 for deposition. The deposited por-tion of the solids 28 may be optionally removed automatical-ly or intermittently from the bottom of the receving vessel 10 by a conveyor which is optionally arranged under the receiving vessel 10.
Figure 3 illustrates another embodiment of the appara-tus according to the invention, wherein the same references are used for the same elements of the previous embodiment for omitting the detailed description therefor. According to this embodiment, the ejecting nozzle 38 for the washing fluid is dipped in the filtrate, while the receiving vessel 10 at its upper portion is provided wlth another nozzle 44 for a surface washing fluid so as to be directed against the surface of the screen 16 with a certain degree of inclina-tion (an acute angle). Otherwise, the construction is sub-stantially same as in the apparatus shown in Fig. 1. As the driving source 22 connected to the rotary shaft 20 for rotating the disc screen 16, there may be employed a direct connection of the rotary shaft 20 with a driving shaft of the electric motor, a gear connection system or a transmis-sion system utilizing an endless chain or belt connected with a remote electric motor.
In operation of the solid/liquid separator according to this embodiment, the electric motor is driven to rotate the ~3~~ 23~Z
disc screen 16 for filtering the solid~containing coolant introduced into the receiving vessel 10, as described for the previous embodiment. The screen 16 may filter the solids 28 and pass the filtrate therethrough. In this embodiment, however, the ejecting nozzle 38 dipped in the filtrate may eject the washing liquid for back-washing the deposited solids on the screen 16 and subsequently the other nozzle 44 may eject the washing fluid against the surface of the disc screen 16, thereby to ensure removal of the solids remaining unseparated after the back-washing.
As apparent from the embodiments described herein-above, in accordance with the invention the solid/liquid separation may be achieved by the rotating disc screen, and the disc screen may be back-wahsed continuously or intermit-tently by the washing fluid, thereby to prevent clogging dueto adhesion of the solids, to maintain the effective solid/
liquid separation and to enhance the treating capacity considerably.
Further, the separated solids may be automatically collected and removed by an optional conveyor system.
Thus, the apparatus according to the invention may be constructed in a compact type, requires less space for placement, and is convenient in maintenance of the disc screen with its separating function, thereby to significant-ly reduce the production and maintenance cost of the appara-tus. In particular, the solid/liquid separator according to the invention may be conveniently and readily attached to the conventional existing solid/liquid separating tank.
_ - 8 -13~Z3~2 Further, any number of such apparatus may be arranged for selectively setting or improving the treating capacity of the solid-containing liquid.
Although the invention has been described herein-above with the preferred embodiments, it will be appreciated that the apparatus according to the invention may be widely applied to various machine tools, such as a cutter, a grinder, a rolling mill, a scrubber, a honing machine and others, for separating inorganic suspended matters (such as iron chips) from a machining oily fluid or an engine oil, or to a solid/liquid separator for a liquid containing sands or activated carbons t and that many variations and modifica-tions may be made without departing from the true spirit and scope of the invention.
Claims
1. A separator for separating machine chips from a coolant, which comprises a receiving vessel for chip-containing coolant, a vessel for filtered coolant disposed next to the receiving vessel, a disc screen through which said vessels communicate with each other, a rotary shaft for rotating said disc screen, means for rotating said rotary shaft thereby to rotate the disc screen, a submerged ejecting nozzle in the filtrate vessel for propelling a fluid against the disc screen thereby to back-wash the disc screen during its rotation, and another ejecting nozzle for ejecting a fluid against the disc screen within the receiving vessel thereby readily to release and remove chips deposited on the surface of the disc screen within the receiving vessel, there being liquid in said receiving vessel having a liquid level, the first-mentioned nozzle being so disposed as to direct fluid against the screen below said liquid level and the second-mentioned nozzle being so disposed as to direct fluid against the screen above said liquid level.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1985170456U JPS6279509U (en) | 1985-11-07 | 1985-11-07 | |
JP60-170456 | 1985-11-07 |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1302302C true CA1302302C (en) | 1992-06-02 |
Family
ID=15905271
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA000522514A Expired - Lifetime CA1302302C (en) | 1985-11-07 | 1986-11-07 | Apparatus for separation of solid from liquid |
Country Status (7)
Country | Link |
---|---|
US (1) | US4765894A (en) |
EP (1) | EP0221565B1 (en) |
JP (1) | JPS6279509U (en) |
KR (1) | KR870004720A (en) |
CA (1) | CA1302302C (en) |
DE (1) | DE3672563D1 (en) |
ES (1) | ES2017461B3 (en) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5361683A (en) * | 1992-05-04 | 1994-11-08 | Imdec Sa | Apparatus for batch cooking and packing fruit and vegetable pieces |
JPH0755439B2 (en) * | 1993-02-15 | 1995-06-14 | 株式会社サンテクノ | Coolant separation device |
DE19623644A1 (en) * | 1996-06-13 | 1997-12-18 | Brueckner Apparatebau Gmbh | filter |
FR2770578B1 (en) * | 1997-10-30 | 2000-03-31 | Joseph Fedesin | DRILLING SLUDGE RECYCLING UNIT |
JP4786232B2 (en) * | 2005-06-30 | 2011-10-05 | 榎本ビーエー株式会社 | Filtration device for chip conveyor |
JP5325008B2 (en) * | 2009-04-23 | 2013-10-23 | コマツNtc株式会社 | Coolant processing equipment |
ES2372074B1 (en) * | 2010-05-27 | 2013-02-11 | Equipos Técnicos Para El Agua, S.L. | ADVANCED WATER PRE-TREATMENT UNIT. |
JP6082536B2 (en) * | 2012-06-29 | 2017-02-15 | ヌオーヴェ エネルジエ エッセ.エッレ.エッレ. | Water treatment apparatus and water treatment method |
NL2012621B1 (en) * | 2014-04-15 | 2016-05-09 | Van Den Berg Bart | Drum filter for water filtration and method thereof. |
CN103933774B (en) * | 2014-04-29 | 2015-08-19 | 蒋顺 | Two vacuum filter |
NO20160570A1 (en) | 2015-04-09 | 2016-10-10 | Joy Mm Delaware Inc | System and method of detecting dull and worn cutter bits |
EP3412864B1 (en) | 2017-06-05 | 2020-09-30 | Joy Global Underground Mining LLC | System and method for determining efficiency of an industrial machine |
WO2020152834A1 (en) * | 2019-01-24 | 2020-07-30 | 株式会社Fuji | Machine tool |
CN112973242B (en) * | 2021-02-05 | 2022-07-15 | 九江市骏昇纺织科技有限公司 | Weaving sewage treatment plant |
CN114131424B (en) * | 2022-01-11 | 2022-07-26 | 江苏益铨数控科技有限公司 | Cutting fluid recovery unit for digit control machine tool |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA591659A (en) * | 1960-02-02 | Cousins Thomas | Rotatable disc filter | |
CA590916A (en) * | 1960-01-19 | Ajem Laboratories | Fluid filter apparatus | |
FR602884A (en) * | 1925-09-02 | 1926-04-02 | Self-releasing rotating grid for loading chamber | |
US1804934A (en) * | 1927-09-09 | 1931-05-12 | Oliver United Filters Inc | Fluid pressure discharge for continuous filters |
US2458139A (en) * | 1946-10-15 | 1949-01-04 | Glenfield And Kennedy Ltd | Filter or strainer for liquids |
NL281849A (en) * | 1961-08-12 | |||
US3585924A (en) * | 1969-03-10 | 1971-06-22 | William J Nolan | Apparatus for the removal of liquids from fibrous materials |
US4431541A (en) * | 1982-08-25 | 1984-02-14 | Arleigh Lee | Circular filter device |
-
1985
- 1985-11-07 JP JP1985170456U patent/JPS6279509U/ja active Pending
-
1986
- 1986-11-06 US US06/927,495 patent/US4765894A/en not_active Expired - Fee Related
- 1986-11-06 KR KR860009377A patent/KR870004720A/en not_active Application Discontinuation
- 1986-11-07 EP EP86115447A patent/EP0221565B1/en not_active Expired - Lifetime
- 1986-11-07 ES ES86115447T patent/ES2017461B3/en not_active Expired - Lifetime
- 1986-11-07 CA CA000522514A patent/CA1302302C/en not_active Expired - Lifetime
- 1986-11-07 DE DE8686115447T patent/DE3672563D1/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
EP0221565A3 (en) | 1987-07-29 |
KR870004720A (en) | 1987-06-01 |
EP0221565B1 (en) | 1990-07-11 |
JPS6279509U (en) | 1987-05-21 |
ES2017461B3 (en) | 1991-02-16 |
DE3672563D1 (en) | 1990-08-16 |
US4765894A (en) | 1988-08-23 |
EP0221565A2 (en) | 1987-05-13 |
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