CA2034502A1 - Viscous fluid pressure-feed apparatus - Google Patents
Viscous fluid pressure-feed apparatusInfo
- Publication number
- CA2034502A1 CA2034502A1 CA 2034502 CA2034502A CA2034502A1 CA 2034502 A1 CA2034502 A1 CA 2034502A1 CA 2034502 CA2034502 CA 2034502 CA 2034502 A CA2034502 A CA 2034502A CA 2034502 A1 CA2034502 A1 CA 2034502A1
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- Canada
- Prior art keywords
- casing
- viscous fluid
- flexible film
- feed
- pressure
- Prior art date
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Abstract
Abstract of the Disclosure:
This invention relates to a viscous fluid pressure-feed apparatus which feeds and drains a slurry of a highly viscous fluid in a casing to a filter press, or the like inside, or outside, a flexible film by pressurizing the swellable flexible film through the feed/drain operation by an oil pressure generation apparatus outside, or inside, the flexible film which is supported by the casing.
Particularly, a mechanical press-in apparatus such as a screw feeder is disposed at a suction port of the viscous fluid into the flexible film disposed in the casing so as to operate in synchronism with expansion and contraction of the flexible film and to supply compulsively the slurry having a high viscosity from a slurry tank. Furthermore, a gas reservoir chamber is added to the casing and a gas exhaust valve is disposed in the gas reservoir chamber. The interior of the casing is sealed through a valve disposed at an outflow port of the press-in apparatus and separation and exhaust of the gas existing in mixture in the slurry of the viscous fluid can be made freely through the opening or closing operation of the exhaust valve.
This, the pressure-feed apparatus of a viscous fluid of the invention can make high pressure pressure-feed of the viscous fluid.
This invention relates to a viscous fluid pressure-feed apparatus which feeds and drains a slurry of a highly viscous fluid in a casing to a filter press, or the like inside, or outside, a flexible film by pressurizing the swellable flexible film through the feed/drain operation by an oil pressure generation apparatus outside, or inside, the flexible film which is supported by the casing.
Particularly, a mechanical press-in apparatus such as a screw feeder is disposed at a suction port of the viscous fluid into the flexible film disposed in the casing so as to operate in synchronism with expansion and contraction of the flexible film and to supply compulsively the slurry having a high viscosity from a slurry tank. Furthermore, a gas reservoir chamber is added to the casing and a gas exhaust valve is disposed in the gas reservoir chamber. The interior of the casing is sealed through a valve disposed at an outflow port of the press-in apparatus and separation and exhaust of the gas existing in mixture in the slurry of the viscous fluid can be made freely through the opening or closing operation of the exhaust valve.
This, the pressure-feed apparatus of a viscous fluid of the invention can make high pressure pressure-feed of the viscous fluid.
Description
~3~
-- 1 .
SPECIFICATION
Title of the Invention:
VISCOUS FLUID PRESSURE-FE:ED APPARATUS
Background of the Invention:
Field of the Invention:
This invention pertains to the technical field of the structure of a pressure feed apparatus used for disposing highly viscous fluids such as factory waste fluids, sludges, cement milk, and so forth.
Description of the Prior Art:
Large quantities of waste matters, waste oils, sludges, and the like, are discharged from production factories of various industrial plants as is well known in the art and disposal of these wastes has hecome very important as a measure to be taken against environmental pollution which occurs unavoidably with the development of industry. As to disposal of highly viscous fluids such as muddy slurry and sludge among them, technology which provides solid-liquid separation, disposes the resulting solid matter by incineration and reclamation and reutilizes the liquid in an appropriate way has been employed widely.
Various pressure-feed apparatuses having a large-capacity, a high-output and high-durability ~3~
disposing capacity have been used for such disposal purposes.
As the pressure-feed apparatus of this kind, a pressure-feed apparatus such as the one 1 shown in Fig. 3 o the accompanying drawings, for example, has been used widely. An operation oil 5 is supplied by an oil pressure generation apparatus 4 to a swellable type flexible film 3 which is stored in a drum-shaped casing 2 and is made of a rubber and the flexible film 3 is pressurized from inside for expansion and contraction in a cycle operation so that a solution 6 to be disposed such as a slurry is sucked from a slurry tank 7 into the casing 2 and is pressure-fed to a processing apparatus 8 of the next stage such as a filter press.
The solid component of the slurry 6 is taken out as a cake by predetermined sol:id-liquid separation treatment whLle the llquid component is clarified and is discharged appropriately or reutilized effectively.
If the solution to be disposed is a waste liquid containing chemical agents and microorganisms, however, fermentation occurs in the solution if it is stored in the tank for a long period and bubbles come to be mixed in the solution. If this solution to disposed is highly viscous, natural deaeration becomes ~3~
very difficult. If the pressure-feed operation of such a solution is carried out by use of the pressure-feed apparatus 1 described above, the bubbles 10, 10, ... mix during the suction process because the inside of the casing 2 is closed or opened by a check valve 9 interposed between the casing 2 and the slurry tank 7. Since the bubbles 10 are compressible, they gather and stay inside the casing and cavities are formed locally. Accordingly, even when the flexible film 3 effects a sufficient expansion/contraction operation, the capacity of these cavities changes and the pressure is not transmitted sufficiently, thereby causing so-called "damping". For this reason, the slurry 6 cannot be discharged completely from inside the casing 2 to the processing apparatus 8 of the next stage.
Even if the casing 2 is installed in a vertical arrangement to position suction and discharge ports atop, natural suetion of the slurry 6 occurs sometimes and if the slurry 6 is highly viscous, the bubbles 10 are ruptured at the time of suction and a substantial suction quantity of the slurry 6 into the casing 2 becomes insufficient, so that a smooth feed/drain operation o the pressure-feed apparatus 1 cannot be made.
-- 1 .
SPECIFICATION
Title of the Invention:
VISCOUS FLUID PRESSURE-FE:ED APPARATUS
Background of the Invention:
Field of the Invention:
This invention pertains to the technical field of the structure of a pressure feed apparatus used for disposing highly viscous fluids such as factory waste fluids, sludges, cement milk, and so forth.
Description of the Prior Art:
Large quantities of waste matters, waste oils, sludges, and the like, are discharged from production factories of various industrial plants as is well known in the art and disposal of these wastes has hecome very important as a measure to be taken against environmental pollution which occurs unavoidably with the development of industry. As to disposal of highly viscous fluids such as muddy slurry and sludge among them, technology which provides solid-liquid separation, disposes the resulting solid matter by incineration and reclamation and reutilizes the liquid in an appropriate way has been employed widely.
Various pressure-feed apparatuses having a large-capacity, a high-output and high-durability ~3~
disposing capacity have been used for such disposal purposes.
As the pressure-feed apparatus of this kind, a pressure-feed apparatus such as the one 1 shown in Fig. 3 o the accompanying drawings, for example, has been used widely. An operation oil 5 is supplied by an oil pressure generation apparatus 4 to a swellable type flexible film 3 which is stored in a drum-shaped casing 2 and is made of a rubber and the flexible film 3 is pressurized from inside for expansion and contraction in a cycle operation so that a solution 6 to be disposed such as a slurry is sucked from a slurry tank 7 into the casing 2 and is pressure-fed to a processing apparatus 8 of the next stage such as a filter press.
The solid component of the slurry 6 is taken out as a cake by predetermined sol:id-liquid separation treatment whLle the llquid component is clarified and is discharged appropriately or reutilized effectively.
If the solution to be disposed is a waste liquid containing chemical agents and microorganisms, however, fermentation occurs in the solution if it is stored in the tank for a long period and bubbles come to be mixed in the solution. If this solution to disposed is highly viscous, natural deaeration becomes ~3~
very difficult. If the pressure-feed operation of such a solution is carried out by use of the pressure-feed apparatus 1 described above, the bubbles 10, 10, ... mix during the suction process because the inside of the casing 2 is closed or opened by a check valve 9 interposed between the casing 2 and the slurry tank 7. Since the bubbles 10 are compressible, they gather and stay inside the casing and cavities are formed locally. Accordingly, even when the flexible film 3 effects a sufficient expansion/contraction operation, the capacity of these cavities changes and the pressure is not transmitted sufficiently, thereby causing so-called "damping". For this reason, the slurry 6 cannot be discharged completely from inside the casing 2 to the processing apparatus 8 of the next stage.
Even if the casing 2 is installed in a vertical arrangement to position suction and discharge ports atop, natural suetion of the slurry 6 occurs sometimes and if the slurry 6 is highly viscous, the bubbles 10 are ruptured at the time of suction and a substantial suction quantity of the slurry 6 into the casing 2 becomes insufficient, so that a smooth feed/drain operation o the pressure-feed apparatus 1 cannot be made.
2~33~2 As compression inside the casing 2 is repeated by the operation of the pressure-feed apparatus 1, the temperature of the staying bubbles 10 rises, causing the problem in that the pressure-feed apparatus 1 reaches a high temperature and packings and the like interposed in the connection portions of pipings get fatigued or their service life is reducedO
For the reasons described above, in a so-called "plunger type" pressure-feed apparatus, the solution to be disposed is limited to those which do not contain modifying matters nor bubbles and the pressure-feed apparatus cannot dispose all kinds of waste liquids inclusive of a highly viscous liquid.
Since the slurry 6 is sucked and discharged between the flexible film 3 and the casing 2 outside the flexible film 3, the highly viscous liquid cannot be sucked sufficiently by the negative pressure in the con.raction process of the flexible film 3 at the time of suction and there exists another problem that the occurrence of folding of the flexible film 3 is likely to cause its fatigue.
Summary of the Invention:
In order to solve those various problems which are encountered during the pressure-feed operation of 7~
viscous fluids by use of the pressure-feed apparatus in accordance with the prior art technique described above, it is a first object of the present invention to make it possible to feed reliably under a high pressure not only waste liquids and sludges discharged from various factories and construction sites but also those highly viscous fluids which contain bubble formation components when they are stored for a long period in an underground tank of factoxies or the like and cannot be deaerated easily, to a next processing - stage.
A second object of the present invention is to make it possible to feed and drain liquid efficiently ir by a plunger or flexible film inside a casing.
A third object of the preslent invention is to provide an excellent viscous fluid pressure~feed apparatus which will be useful in the field of environmental pollution prevention technology.
Brief Description of the Drawings:
Fig. 1 is an overall schematic sectional view of an embodiment of the present invention;
Fig. 2 is an overall schematic sectional view of another embodiment of the present invention; and Fig. 3 is an overall schematic sectional view of a prior art.
2 ~
Description of the Preferred Embodiments:
Hereinafter, preferred embodiments of the present invention will be described with reference to Figs. 1 and 2.
Incidentally, like reference numerals will be used to identify like constituents as in Fig. 3.
In the embodiment shown in Fig. 1, reference numeral 1' represents a pressure-feed apparatus which constitutes one of the gists of the presently claimed invention. An oil feed/drain port ll of an operation oil S is disposed on one (2') of the sides of a drum-shaped casing 2 of this pressure-feed apparatus, and is connected to a predetermined oil pressure generation apparatus 4 through :its output port 12~
~ he base portion of the casing 2 has the shape of a bottomed cylinder and a flange 13 is disposed integrally with it. A swelling type flexible film 3 made of a rubber is clamped to and supported by the casing at its skirt portion through rings with its swell portion facing inside the casing 2.
Reference numeral 14 represents an outside support net for the retreating posture of the flexible film 3 and the base portion of this support net is fixed to the casing 2 so as to retain the shape of the flexible film 3 at the time of swelling.
~ ~ 3 ~
A faed port 15 and a drain port 16 of a viscous fluid as a solution to be disposed are disposed at predetermined positions of the bottom of the casing 2 on the other side and a solenoid valve 17 is interposed between the feed pcrt 15 through an appropriate packing and a press-in device 18 connected to and supported by the feed port.
The press-in device 18 is equipped with a screw eeder 20 inside its gun type case 19 and a hopper 21 is formed integrally with the upper portion of the case 19. A highly viscous slurry 6 such as cement milk, for example, is always charged into this hopper 21 in such a manner as to supply the highly viscous slurry 6 between the inside of the casing 2 and the flexible film 3 with the tip portion of the screw feeder 20 facing the feed port 15.
Incidentally, the highly viscous slurry 6 inside the casing 2 is discharged to a processing apparatus 8 of the next stage such as a filter press via the drain port 16.
Accordingly, the highly viscous liquid 6 is supplied and discharged inside the flexible ~ilm 3 in the casing 2 whereas the operation oil 5 is supplied and discharged outside the flexible film 3.
The screw feeder 20 is connected to a motor 23 ~3~
through a reduction device 22 and a control design may be selected arbitrarily so that the motor 23 may be always rotated or driven under the open state of the solenoid valva 17.
A gas exhaust port 24 is formed at the top of the casing 2 in the proximity of the feed port 15 and a solenoid valve 25 as a gas exhaust valve is fitted through a suitable packing. A gas exhaust device 26 operating as a gas reservoir is connected to communicate with the gas exhaust port 24~
The gas exhaust device 26 is connected to the casing 2 at the lower end of a chamber 27 which serves as the gas reservoir chamber and has a predetermined capacity. A gas exhaust pipe 28 is formed at the upper end of the gas exhaust device 26 and a solenoid valve 29 is fitted to this gas exhaust valve 28.
A solenoid valve 30 is fitted to the drain port 16 of the casing 2 and the process.ing apparatus 8 of the next stage such as a filter press is connected to it through a predetermined piping.
The solenoid valves 17, 25, 29, 30 are connected electrically to a predetermined controller 31, which controls also the operation of the oil pressure generation apparatus 4.
The hydraulic pressure generation apparatus 4 is ~3l~0~
- 9 ~-a redoubling device of a piston type. Namely, the operation oil 5 supplied from an oil tank 32 through a pump 33 is supplied to inflow-outflow ports 36, 37 of a cylinder 35 through the operation of a direction control solenoid valve 34 controlled by the operation controller 31 and as the pistons 38, 38' are moved back and forth at a predetermined speed, the pressure oil 5 is supplied into the casing 2 of the pressure-feed apparatus 1'. Its timing control is mada by transmitting the signals which are detected by the operation of limit switche~ 41, 41' for the dog 40 disposed at the rear end of a piston rod 39 to the controller 31.
In the construction described above, it will be assumed hereby that the highly viscous slurry ~
containing bubbles in mixture as the solution to be disposed is pressure-fed into the filter press 8 by use of the pressure-feed apparatus 1'. When thP
switch of the controller 31 is turned on, the o~l pressure generation apparatus 4 is actuated to start the pump 33, the direction control solenoid valve 34 is reset to the initial state, the operation oil 5 is pressure-fed to the inflow port 37 of the cylinder 35 and the pistons 38, 38' are moved back and forth.
When the dog 40 of the piston rod 39 strikes the ~ ~ 3 '~
limit switch 41, the controller 31 changes over next the direction control solenoid valve 34 so as to move back the pistons 38, 38'.
The pis~on 38' sucks the operation oil 5 into the large capacity cylinder 35 and applies the negative pressure to the feed/drain port 11 on one (2') side of the casing 2 connected thereto through the port 12, reduces the pressure of the pressurizing chamber defined outside the flexible film 3 and increases the capacity of the flurry chamber inside the flexible film 3 by the retreat expansion of the flexible film 3 to prepare for the suction of the slurry 6.
The highly viscous liquid slurry 6 is extruded to the feed port 15 of the casing 2 by the rotation of the screw feeder 20 of the press-in apparatus 18.
The controller 31 opens the solenoid valve 17 fitted to the feed port 15, ope:rates the oil pressure generation apparatus 4 so as to move back the pistons 38, 38' and to discharge the operation oil 5 ~rom inside the casing 2 and expands the ~lexible film 3 so as to increase the capacity of the slurry chamber.
Incidentally, at this point, the controller 31 makes control so as to open the solenoid valve 30 disposed in the slurry drain port 16 of the casing 2, the solenoid valve 29 of the gas exhaust apparatus 26 2~3~
and the solenoid valve 25.
In the suction process of the highly viscous slurry 6 by the pressure-feed apparatus 1', the highly viscous slurry 6 is supplied into the slurry chamber by a kind of push-pull operation by the pressu.re reduction of the slurry chamber due to the retreat of the flexible film 3 and extrusion of the highly viscous slurry 6 by the press-in apparatus 18 and the bubbles 10, lOj ... existing in mixture in the highly viscous slurry 6 are not ruptured but are caused to flow smoothly into the casing 2 of the pressure-feed apparatus l' by the retreat of the flexible film 3 and the feed operation of the press-in apparatus 18 which is synchronous with the former.
Part of the bubbles 10, 10, ..~ staying inside the casing 2 is raised during the feed process into the casing 2 and move near to the gas exhaust port 24.
Then, the controller 31 opens the solenoid valve 25 of the gas exhaust apparatus 26 so as to introduce the bubbles 10, 10, ... into the chamber 27, the highly viscous slurry 6 is packed into the casing 2 and the retreating motion of the flexible film 3 is completed. The dog 40 of the piston rod 39 o~ the oil pressure generation apparatus 4 strikes the limit switch 41' and its signal is transmitted to the , ~33~2 - 12 ~
controller 31.
The controller 31 controls the oil pressure generation apparatus 4 to move forth the pistons 38, 38' and to supply the operation oil 5 into the pressurizing chamber defined by the flexible film 3 outside it inside the casing 2 and at the same time, opens the solenoid valve 25 disposed in the gas exhaust apparatus 26. Accordingly, the gas inside the casing 2 is compressed and sealed into the chamber 27 of the gas exhaust apparatus 26.
The solenoid valve 25 of the gas exhaust apparatus 26 is opened at a predetermined timing and the oil pressure generation apparatus 4 diminishes strongly the ~lexible film 3 so as to press the highly viscous slu~ry 6 inside the slurry chamber~ The solenoid valve 30 disposed at the drain port 16 is opened and the highly viscous slurry 6 is pressure-fed into the filter presses 8 while the gas inside the chambar 27 is discharged as the solenoid valve ~9 disposed in the exhaust pipe 28 is opened.
Here, those bubbles 10, 10, ... which rise in~ide the casing 2 without passing through the exhaust port 16 during the contraction process of the flexible ilm 3 stay at the upper portion inside the casing 2 but are discharged when the exhaust valve 25 is opened at 2 ~ 2 the initial stage of the next feed/drain process because the gas exhaust apparatus 26 is disposed.
Since the bubbles 10, 10, ... are removed from the highly viscous slurry 6 in the interim, the press/discharge operation for the highly viscous slurry 6 can be carried out reliably.
The bubbles 10, 10, .~. existing in mixture in the highly viscous slurry 6 are removed from the slurry 6 and discharged outside the casing 2 during the pressure-feed operation of the highly viscous slurry 6 to the filter press 8, and a predetermined quantity of slurry 6 is pressure-fed at a high pressure in each cycle.
As the process described above is repeated, solid-liquid separation of the highly viscous slurry 6 is oonducted.
In comparison with th~ embodiment shown in Fig.
1, the embodiment shown in Fig. 2 has the structure wherein the direction of the flexible film 3' and the support net 14l inside the casing 2" and their arrangement direction are opposite and the support net 14' retains the shape of the flexible film 3 at the time of contraction of the latter.
The bubble-removing operation at the time of feed and drain of the highly viscous slurr~ 6' to and from 2 ~
the casing 2" due to expansion and contraction of the flexible film 3' is the same as in the embodiment described above.
Incidentally, the mode of practising the present invention is not naturally limited to the embodiments described above and various other modes such as the one wherein the gas reservoir chamber discharges the viscous fluid can be employed, for example.
The apparatus of the present invention can naturally pressure-feed sufficiently an ordinary slurry, cement milk, and the like.
The apparatus in accordance with the present invention has basically the construction wherein the gas reservoir chamber is added to a pressure feed apparatus used for disposing various sludges and waste liquid so as to pressure-feed compulsively the highly viscous slurry into the casing and the exhaust valve of the gag reservoir chamber is opened or closed in synchronization wikh the feed/drain operation of the highly viscous slurry. Accordingly, those bubbles which receive repeatedly the compression and suction of the highly viscous slurry due tv expansion and contraction of the flexible film inside the casing, move upward and stay at the upper portion of the casing, are separated as the gas component from the ~3~
solution to be processed and the highly viscous slurry can be pressure-fed to the separation apparatus such as a filter press.
The highly viscous slurry is supplied into the casing by the press-in apparatus and the bubble component existing in mixture in the solution to be processed at the time of suction into tha casing risa inside the casing during the discharge process of the flexible film, are collected and discharged into the gas reservoir chamber and are thareafter dischaxged outside the casing by the exhaust apparatus.
Accordingly, the gas does not exist any longer in the solution to be processed, the high pressure pressure-feed operation due to expansion and contraction of the flexible film can be conducted efficiently and working efficiency of the feed/drain operation can be improved.
Even when expansion and contraction of the flexible film is conducted repeatedly, the bubbles are not compressed during the high pressure pressure-feed operation and exothermy does not occur inside the casing, so that degradation of accessorial components such as packings can be prevented.
For the reasons described above, in a so-called "plunger type" pressure-feed apparatus, the solution to be disposed is limited to those which do not contain modifying matters nor bubbles and the pressure-feed apparatus cannot dispose all kinds of waste liquids inclusive of a highly viscous liquid.
Since the slurry 6 is sucked and discharged between the flexible film 3 and the casing 2 outside the flexible film 3, the highly viscous liquid cannot be sucked sufficiently by the negative pressure in the con.raction process of the flexible film 3 at the time of suction and there exists another problem that the occurrence of folding of the flexible film 3 is likely to cause its fatigue.
Summary of the Invention:
In order to solve those various problems which are encountered during the pressure-feed operation of 7~
viscous fluids by use of the pressure-feed apparatus in accordance with the prior art technique described above, it is a first object of the present invention to make it possible to feed reliably under a high pressure not only waste liquids and sludges discharged from various factories and construction sites but also those highly viscous fluids which contain bubble formation components when they are stored for a long period in an underground tank of factoxies or the like and cannot be deaerated easily, to a next processing - stage.
A second object of the present invention is to make it possible to feed and drain liquid efficiently ir by a plunger or flexible film inside a casing.
A third object of the preslent invention is to provide an excellent viscous fluid pressure~feed apparatus which will be useful in the field of environmental pollution prevention technology.
Brief Description of the Drawings:
Fig. 1 is an overall schematic sectional view of an embodiment of the present invention;
Fig. 2 is an overall schematic sectional view of another embodiment of the present invention; and Fig. 3 is an overall schematic sectional view of a prior art.
2 ~
Description of the Preferred Embodiments:
Hereinafter, preferred embodiments of the present invention will be described with reference to Figs. 1 and 2.
Incidentally, like reference numerals will be used to identify like constituents as in Fig. 3.
In the embodiment shown in Fig. 1, reference numeral 1' represents a pressure-feed apparatus which constitutes one of the gists of the presently claimed invention. An oil feed/drain port ll of an operation oil S is disposed on one (2') of the sides of a drum-shaped casing 2 of this pressure-feed apparatus, and is connected to a predetermined oil pressure generation apparatus 4 through :its output port 12~
~ he base portion of the casing 2 has the shape of a bottomed cylinder and a flange 13 is disposed integrally with it. A swelling type flexible film 3 made of a rubber is clamped to and supported by the casing at its skirt portion through rings with its swell portion facing inside the casing 2.
Reference numeral 14 represents an outside support net for the retreating posture of the flexible film 3 and the base portion of this support net is fixed to the casing 2 so as to retain the shape of the flexible film 3 at the time of swelling.
~ ~ 3 ~
A faed port 15 and a drain port 16 of a viscous fluid as a solution to be disposed are disposed at predetermined positions of the bottom of the casing 2 on the other side and a solenoid valve 17 is interposed between the feed pcrt 15 through an appropriate packing and a press-in device 18 connected to and supported by the feed port.
The press-in device 18 is equipped with a screw eeder 20 inside its gun type case 19 and a hopper 21 is formed integrally with the upper portion of the case 19. A highly viscous slurry 6 such as cement milk, for example, is always charged into this hopper 21 in such a manner as to supply the highly viscous slurry 6 between the inside of the casing 2 and the flexible film 3 with the tip portion of the screw feeder 20 facing the feed port 15.
Incidentally, the highly viscous slurry 6 inside the casing 2 is discharged to a processing apparatus 8 of the next stage such as a filter press via the drain port 16.
Accordingly, the highly viscous liquid 6 is supplied and discharged inside the flexible ~ilm 3 in the casing 2 whereas the operation oil 5 is supplied and discharged outside the flexible film 3.
The screw feeder 20 is connected to a motor 23 ~3~
through a reduction device 22 and a control design may be selected arbitrarily so that the motor 23 may be always rotated or driven under the open state of the solenoid valva 17.
A gas exhaust port 24 is formed at the top of the casing 2 in the proximity of the feed port 15 and a solenoid valve 25 as a gas exhaust valve is fitted through a suitable packing. A gas exhaust device 26 operating as a gas reservoir is connected to communicate with the gas exhaust port 24~
The gas exhaust device 26 is connected to the casing 2 at the lower end of a chamber 27 which serves as the gas reservoir chamber and has a predetermined capacity. A gas exhaust pipe 28 is formed at the upper end of the gas exhaust device 26 and a solenoid valve 29 is fitted to this gas exhaust valve 28.
A solenoid valve 30 is fitted to the drain port 16 of the casing 2 and the process.ing apparatus 8 of the next stage such as a filter press is connected to it through a predetermined piping.
The solenoid valves 17, 25, 29, 30 are connected electrically to a predetermined controller 31, which controls also the operation of the oil pressure generation apparatus 4.
The hydraulic pressure generation apparatus 4 is ~3l~0~
- 9 ~-a redoubling device of a piston type. Namely, the operation oil 5 supplied from an oil tank 32 through a pump 33 is supplied to inflow-outflow ports 36, 37 of a cylinder 35 through the operation of a direction control solenoid valve 34 controlled by the operation controller 31 and as the pistons 38, 38' are moved back and forth at a predetermined speed, the pressure oil 5 is supplied into the casing 2 of the pressure-feed apparatus 1'. Its timing control is mada by transmitting the signals which are detected by the operation of limit switche~ 41, 41' for the dog 40 disposed at the rear end of a piston rod 39 to the controller 31.
In the construction described above, it will be assumed hereby that the highly viscous slurry ~
containing bubbles in mixture as the solution to be disposed is pressure-fed into the filter press 8 by use of the pressure-feed apparatus 1'. When thP
switch of the controller 31 is turned on, the o~l pressure generation apparatus 4 is actuated to start the pump 33, the direction control solenoid valve 34 is reset to the initial state, the operation oil 5 is pressure-fed to the inflow port 37 of the cylinder 35 and the pistons 38, 38' are moved back and forth.
When the dog 40 of the piston rod 39 strikes the ~ ~ 3 '~
limit switch 41, the controller 31 changes over next the direction control solenoid valve 34 so as to move back the pistons 38, 38'.
The pis~on 38' sucks the operation oil 5 into the large capacity cylinder 35 and applies the negative pressure to the feed/drain port 11 on one (2') side of the casing 2 connected thereto through the port 12, reduces the pressure of the pressurizing chamber defined outside the flexible film 3 and increases the capacity of the flurry chamber inside the flexible film 3 by the retreat expansion of the flexible film 3 to prepare for the suction of the slurry 6.
The highly viscous liquid slurry 6 is extruded to the feed port 15 of the casing 2 by the rotation of the screw feeder 20 of the press-in apparatus 18.
The controller 31 opens the solenoid valve 17 fitted to the feed port 15, ope:rates the oil pressure generation apparatus 4 so as to move back the pistons 38, 38' and to discharge the operation oil 5 ~rom inside the casing 2 and expands the ~lexible film 3 so as to increase the capacity of the slurry chamber.
Incidentally, at this point, the controller 31 makes control so as to open the solenoid valve 30 disposed in the slurry drain port 16 of the casing 2, the solenoid valve 29 of the gas exhaust apparatus 26 2~3~
and the solenoid valve 25.
In the suction process of the highly viscous slurry 6 by the pressure-feed apparatus 1', the highly viscous slurry 6 is supplied into the slurry chamber by a kind of push-pull operation by the pressu.re reduction of the slurry chamber due to the retreat of the flexible film 3 and extrusion of the highly viscous slurry 6 by the press-in apparatus 18 and the bubbles 10, lOj ... existing in mixture in the highly viscous slurry 6 are not ruptured but are caused to flow smoothly into the casing 2 of the pressure-feed apparatus l' by the retreat of the flexible film 3 and the feed operation of the press-in apparatus 18 which is synchronous with the former.
Part of the bubbles 10, 10, ..~ staying inside the casing 2 is raised during the feed process into the casing 2 and move near to the gas exhaust port 24.
Then, the controller 31 opens the solenoid valve 25 of the gas exhaust apparatus 26 so as to introduce the bubbles 10, 10, ... into the chamber 27, the highly viscous slurry 6 is packed into the casing 2 and the retreating motion of the flexible film 3 is completed. The dog 40 of the piston rod 39 o~ the oil pressure generation apparatus 4 strikes the limit switch 41' and its signal is transmitted to the , ~33~2 - 12 ~
controller 31.
The controller 31 controls the oil pressure generation apparatus 4 to move forth the pistons 38, 38' and to supply the operation oil 5 into the pressurizing chamber defined by the flexible film 3 outside it inside the casing 2 and at the same time, opens the solenoid valve 25 disposed in the gas exhaust apparatus 26. Accordingly, the gas inside the casing 2 is compressed and sealed into the chamber 27 of the gas exhaust apparatus 26.
The solenoid valve 25 of the gas exhaust apparatus 26 is opened at a predetermined timing and the oil pressure generation apparatus 4 diminishes strongly the ~lexible film 3 so as to press the highly viscous slu~ry 6 inside the slurry chamber~ The solenoid valve 30 disposed at the drain port 16 is opened and the highly viscous slurry 6 is pressure-fed into the filter presses 8 while the gas inside the chambar 27 is discharged as the solenoid valve ~9 disposed in the exhaust pipe 28 is opened.
Here, those bubbles 10, 10, ... which rise in~ide the casing 2 without passing through the exhaust port 16 during the contraction process of the flexible ilm 3 stay at the upper portion inside the casing 2 but are discharged when the exhaust valve 25 is opened at 2 ~ 2 the initial stage of the next feed/drain process because the gas exhaust apparatus 26 is disposed.
Since the bubbles 10, 10, ... are removed from the highly viscous slurry 6 in the interim, the press/discharge operation for the highly viscous slurry 6 can be carried out reliably.
The bubbles 10, 10, .~. existing in mixture in the highly viscous slurry 6 are removed from the slurry 6 and discharged outside the casing 2 during the pressure-feed operation of the highly viscous slurry 6 to the filter press 8, and a predetermined quantity of slurry 6 is pressure-fed at a high pressure in each cycle.
As the process described above is repeated, solid-liquid separation of the highly viscous slurry 6 is oonducted.
In comparison with th~ embodiment shown in Fig.
1, the embodiment shown in Fig. 2 has the structure wherein the direction of the flexible film 3' and the support net 14l inside the casing 2" and their arrangement direction are opposite and the support net 14' retains the shape of the flexible film 3 at the time of contraction of the latter.
The bubble-removing operation at the time of feed and drain of the highly viscous slurr~ 6' to and from 2 ~
the casing 2" due to expansion and contraction of the flexible film 3' is the same as in the embodiment described above.
Incidentally, the mode of practising the present invention is not naturally limited to the embodiments described above and various other modes such as the one wherein the gas reservoir chamber discharges the viscous fluid can be employed, for example.
The apparatus of the present invention can naturally pressure-feed sufficiently an ordinary slurry, cement milk, and the like.
The apparatus in accordance with the present invention has basically the construction wherein the gas reservoir chamber is added to a pressure feed apparatus used for disposing various sludges and waste liquid so as to pressure-feed compulsively the highly viscous slurry into the casing and the exhaust valve of the gag reservoir chamber is opened or closed in synchronization wikh the feed/drain operation of the highly viscous slurry. Accordingly, those bubbles which receive repeatedly the compression and suction of the highly viscous slurry due tv expansion and contraction of the flexible film inside the casing, move upward and stay at the upper portion of the casing, are separated as the gas component from the ~3~
solution to be processed and the highly viscous slurry can be pressure-fed to the separation apparatus such as a filter press.
The highly viscous slurry is supplied into the casing by the press-in apparatus and the bubble component existing in mixture in the solution to be processed at the time of suction into tha casing risa inside the casing during the discharge process of the flexible film, are collected and discharged into the gas reservoir chamber and are thareafter dischaxged outside the casing by the exhaust apparatus.
Accordingly, the gas does not exist any longer in the solution to be processed, the high pressure pressure-feed operation due to expansion and contraction of the flexible film can be conducted efficiently and working efficiency of the feed/drain operation can be improved.
Even when expansion and contraction of the flexible film is conducted repeatedly, the bubbles are not compressed during the high pressure pressure-feed operation and exothermy does not occur inside the casing, so that degradation of accessorial components such as packings can be prevented.
Claims (6)
1. A viscous fluid pressure-feed apparatus of the type in which a swellable flexible film is interposed between one of the sides of a casing communicating with an output port of an oil pressure generation apparatus and the other side of said casing communicating with a viscous slurry tank and with a piping of a separation apparatus, wherein a press-in apparatus is disposed between said slurry tank and said casing in such a manner as to face inside of said flexible film, and a gas reservoir chamber is disposed in said casing.
2. A viscous fluid pressure-feed apparatus according to claim 1, wherein an exhaust valve of said gas reservoir chamber is connected electrically to a valve disposed at an outflow port of said press-in apparatus through a controller.
3. A viscous fluid pressure-feed apparatus according to claim 2, wherein said gas reservoir chamber functions also as a viscous fluid reservoir.
4. A viscous fluid pressure-feed apparatus according to claim 1, wherein said press-in apparatus is a screw feeder.
5. A viscous fluid pressure-feed apparatus according to claim 1, wherein said flexible film is disposed inside a support net fixed to said casing.
6. A viscous fluid pressure-feed apparatus according to claim 1, wherein said flexible film is disposed outside a support net fixed to said casing.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2013607A JPH03222875A (en) | 1991-02-06 | 1990-01-25 | Viscous fluid pressure feed device |
| JPH2-13607 | 1990-01-25 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2034502A1 true CA2034502A1 (en) | 1991-07-26 |
Family
ID=11837920
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA 2034502 Abandoned CA2034502A1 (en) | 1990-01-25 | 1991-01-21 | Viscous fluid pressure-feed apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA2034502A1 (en) |
-
1991
- 1991-01-21 CA CA 2034502 patent/CA2034502A1/en not_active Abandoned
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