JP4522932B2 - Solid-liquid separation method - Google Patents

Description

  The present invention relates to a solid-liquid separation method for separating a liquid substance and a solid substance from a mixture.

As an apparatus for carrying out this type of solid-liquid separation method, for example, as shown in the following Patent Document 1, the filtration unit in which the mixture is supplied to the surface, and the above-mentioned supply to the surface of the filtration unit There is known a configuration including a pressurizing unit that pressurizes the mixture, and a recovery unit that is provided on the back side of the filtration unit and is connected to a vacuum suction device. Furthermore, the pressurizing means of this document 1 includes a pressurizing plate in which a plurality of through-holes are formed, and a surface on which the through-holes open contacts and pressurizes the mixture. In a state where the mixture is pressurized, a pressure fluid is passed through the through hole, and the mixture is pressurized with the pressure fluid.
As described above, the mixture is pressurized by both the pressure plate and the pressure fluid, and the liquid substance is squeezed out from the mixture, and at the same time, the mixture is recovered by the recovery means, so that the mixture is liquid. The substance and the solid substance are separated.
Japanese Patent No. 3311417

By the way, in the conventional solid-liquid separation method, since the mixture in the initial stage to be pressurized by the pressurizing means contains a large amount of liquid substance, the mixture is scattered around in the initial stage of the pressurization. Or in the direction along the surface of the filtration part, from the outer peripheral edge of the surface (hereinafter referred to as “pressurizing region”) of the pressure plate where the through-hole opens and contacts and pressurizes the mixture. There was also a risk of being extruded outward.
The mixture extruded in this way has a larger amount of residual liquid material than that located in the pressurizing region, resulting in variations in the purity of the obtained solid material, and improving this purity. There was a problem that was difficult. Further, due to the extrusion or the like, the amount of the mixture located in the pressurizing region becomes small, and there is a possibility that the solid-liquid separation efficiency is lowered.

  The present invention has been made under such a background, and in the initial stage of pressurization, the mixture is extruded outward from the pressurization region in the direction along the surface of the filtration part, or Solid-liquid that can prevent scattering, suppress variation in the purity of the obtained solid substance, improve the purity of the solid substance, and improve the solid-liquid separation efficiency An object is to provide a separation method.

In order to solve such problems and achieve the above object, the solid-liquid separation method of the present invention comprises a guide roll rotatably provided on the main body of the solid-liquid separator, and an endless shape on the guide roll. The tensioning filter cloth, and the pressurization for pressurizing the mixture supplied to the surface of the filtration part, provided on the surface side of the filtration part that is positioned on the upper side of the filter cloth and can run substantially horizontally Means and a recovery means provided on the back side of the filtration part and connected to a vacuum suction device, and the mixture supplied to the surface of the filtration part is vacuumed by the recovery means. A solid-liquid separation method in which a liquid substance and a solid substance are separated by pressurizing with a pressurizing means while sucking, and supported by the solid-liquid separation apparatus so as to be able to advance and retreat toward the surface of the filtration unit. In addition, it has a frame-like or annular seal part That sealing means are provided, to travel the filtration unit, the in the mixture supplied to the surface of the filtration portion is opposed to said pressurizing means and sealing means at the time of stopping the running of the filtration unit, wherein The vacuum suction is started while supplying the mixture to the portion located on the rear side of the filtration unit in the running direction of the filtration unit on the surface of the filtration unit , and then the vacuum suction is continued. In addition, the pressurization is started in a state where the seal portion is moved toward the surface of the filtration portion and the pressurizing means and the mixture facing the seal means are surrounded by the seal portion and sealed. It is characterized by.

According to this invention, after the vacuum suction is started, the pressurization is started in a state where the vacuum suction is continued, so that the amount of the liquid material contained in the mixture is reduced in advance prior to the pressurization. This makes it possible to keep this mixture hard. Therefore, when this mixture is pressurized by the pressurizing means, the mixture is scattered around or the area is pressurized by the pressurizing means in the direction along the surface of the filtration part. It is possible to prevent the material from being extruded outward (hereinafter referred to as “pressurizing region”). As a result, it is possible to suppress the amount of the mixture located in the pressurizing region from becoming small during pressurization by the pressurizing means, and it is possible to improve the solid-liquid separation efficiency. In addition, the purity of the obtained solid substance can be suppressed and the purity can be improved.
Moreover, since the sealing means is provided, the occurrence of the scattering and the like can be reliably suppressed.
Further, while the mixture is intermittently run by the filter cloth, it is possible to perform solid-liquid separation by stopping the pressurization and vacuum suction when the mixture is stopped, and the solid-liquid separation in which the purity of the obtained solid substance is improved. Processing can be performed with high efficiency.

Here, when pressurizing the mixture by the pressurizing means, the pressure applied to the mixture may be gradually increased over time.
In this case, since the pressure is gradually increased with time, it is possible to prevent the mixture from being scattered around during the pressurization. In particular, the mixture in the initial stage of pressurization has a large amount of liquid substance, so that the applied pressure in the initial stage is applied to the liquid substance in spite of the occurrence of the scattering. By making the pressure smaller than the pressure applied to the mixture at the later stage when the content of is reduced, it is possible to suppress the occurrence of such scattering.
Further, in the process of solid-liquid separation by pressurization, the amount of liquid substance contained in the mixture is gradually reduced without causing the scattering, etc. While increasing the thickness, it is possible to apply to the mixture always or each time a maximum pressure suitable for its hardness, that is, a maximum pressure that does not cause the scattering or the like. Therefore, efficient solid-liquid separation can be performed without causing the scattering and the like.

Further, the pressurizing means includes a ventilation plate that is supported so as to be able to advance and retreat with respect to the surface of the filtration part, and has a plurality of through holes, and allows a pressure fluid to pass through these through holes, The rear surface of the vent plate is maintained in a state in which the ventilation plate is moved toward the surface of the filtration part, and the surface of the vent plate in which the through hole is opened is brought into contact with the mixture, and the contact is maintained. The pressure fluid may be passed through the through hole from the side, and pressurization of the mixture with the pressure fluid may be started.

In this case, after the airflow plate is brought into contact with the mixture, pressurization with the pressure fluid is started in a state where the contact is maintained, so that the mixture is scattered around when pressurized with the pressure fluid. It can be surely suppressed. That is, in the pressurization with the pressure fluid, the liquid substance is squeezed out by spraying the pressure fluid onto the mixture, and thus the mixture is likely to be scattered around by the spraying. By causing the ventilation plate to contact the mixture, that is, by sandwiching and restraining the mixture between the ventilation plate and the surface of the filtration part, it is possible to prevent the occurrence of such scattering. As described above, since the amount of liquid material contained in the mixture is large in the initial stage of pressurization, the scattering is particularly likely to occur in this initial stage. Can be suppressed.
Here, bringing the vent plate into contact with the mixture includes pressurizing the mixture with the vent plate. That is, the pressurizing means may pressurize the mixture by both the vent plate and the pressure fluid.

Further, after the pressurization by the pressure fluid is stopped, the ventilation plate may be separated from the obtained solid substance, and in this case, the occurrence of the scattering can be reliably suppressed.

Furthermore, after pressurizing the mixture, a pressure fluid may be passed through the through-hole when the vent plate is separated from the obtained solid substance. It becomes possible to remove the mixture, etc., adhering to the vent plate including the surface by the pressure fluid, and when the next mixture is pressurized and solid-liquid separated, the previous mixture, etc. It is possible to avoid adhering to and mixing in the mixture. Therefore, it can suppress that the purity of the solid substance obtained by solid-liquid separation varies for every solid-liquid separation process. In addition, in order to pass this pressure fluid through a through-hole, it may be from any of the surface side of a ventilation board, and a back surface side.

  In the case where the seal portion and the ventilation plate can be driven independently by providing the drive means for driving the seal portion forward and backward and the drive means for driving the ventilation plate forward and backward, respectively. The forward drive force of the seal part toward the surface of the filtration part and the pressure applied to the mixture by the ventilation plate can be appropriately changed according to, for example, the properties of the mixture. It is possible to prevent the mixture from being pushed outward or scattered regardless of the type of the mixture when the mixture is pressurized by the pressure means. As a result, even when various types of mixtures are squeezed and ventilated, stable filtration can be performed without scattering the mixture, and solid-liquid separation efficiency can be improved. It becomes possible to improve the handleability of this solid-liquid separator.

  Further, the form of the seal portion is not particularly limited. For example, the seal portion is provided in a frame shape or an annular shape, and the opening surface is supplied to the surface of the filtration portion or the surface over the entire circumference. It is also possible to employ a sealing material supported so as to be intimately pressed by the mixture. Alternatively, at least a part of the seal portion in the circumferential direction is a wall portion that pierces the mixture supplied to the surface of the filtration portion in its thickness direction, and the mixture supplied to the surface of the filtration portion It is also possible to employ a configuration in which the seal is surrounded by the seal portion while being pierced by the wall portion. Furthermore, you may make it comprise the said seal part only by the said wall part.

  Not only can the solid-liquid separation efficiency be improved, but also the purity of the obtained solid substance can be suppressed and the purity of the solid substance can be improved.

Hereinafter, an embodiment of the present invention will be described with reference to FIGS.
In the solid-liquid separation device 10 according to the present embodiment, the filtration unit 11a to which the mixture is supplied to the surface, the sealing means 12 having a frame-like or annular seal part, and the mixture supplied to the surface of the filtration unit 11a A pressurizing means 13 for pressurizing and a recovery means 14 provided on the back side of the filtration part 11a and connected to a vacuum suction device (not shown) are provided. The seal portion of the present embodiment is configured only by a seal material 12a described later.

  The filtration part 11a of this embodiment is comprised by a part of filter cloth 11 provided in the apparatus main body 10a so that it can drive | work substantially horizontally. That is, as shown in FIG. 4, the filter cloth 11 is stretched endlessly on a number of guide rolls 15 rotatably provided on the apparatus main body 10a, and is horizontally stretched on the upper side of the apparatus main body 10a. A portion (hereinafter referred to as “horizontal portion”) 11a constitutes the filtering portion (hereinafter, the horizontal portion 11a is referred to as “filtering portion 11a”).

  A plurality of (four in the illustrated example) recovery means 14 is provided on the back surface side of the filtration unit 11a along the traveling direction F of the filtration unit 11a, and is connected to a vacuum suction device (not shown). Consists of trays A1 to A4. The mixture is a so-called slurry S containing a solid substance in a liquid substance.

  As shown in FIGS. 1 and 2, the upper surfaces of the plurality of vacuum trays A1 to A4 each have a horizontal portion 14b at the center of the cross section when viewed from the running direction F of the filtration portion 11a, and both ends of the horizontal portion 14b. It is made into the substantially V shape by which the inclination part 14c which stands | starts up diagonally upward toward the part was provided in a row. Here, the filtration part 11a is arranged on the upper surface of the vacuum trays A1 to A4, so that the filtration part 11a is also substantially V-shaped along the upper surface of the vacuum trays A1 to A4. A plurality of through holes are formed on the horizontal part 14b and the horizontal part 14b side of the inclined part 14c in the upper surface of the vacuum trays A1 to A4, and the filtering part 11a is formed through the through holes. A vacuum suction force acts on the slurry S supplied to the surface, and the liquid material from the slurry S flows into the vacuum trays A1 to A4.

  The plurality of vacuum trays A1 to A4 are independently connected to a control valve (not shown) and a filtrate tank, and each filtrate tank is connected to a vacuum pump and a filtrate pump (not shown). And each vacuum tray A1-A4 can perform required vacuum pressure and air release operation independently. In addition, the filter cloth 11 on each vacuum tray A1 to A4, that is, the filtration unit 11a, is divided into a cake forming section, a first and second washing section, and a dewatering section.

  Above the filtering unit 11a, the slurry supply device 16 supported by the moving frame 10b and the first and second cleaning devices 17a and 17b are reciprocated along the traveling direction F of the filtering unit 11a in a state where they are connected to each other. It is provided movably. The slurry supply device 16 supplies the slurry S to the cake forming section, and the cleaning devices 17a and 17b respectively supply a second cleaning filtrate (second cleaning section to the first and second cleaning sections). Permeated recovered liquid) and fresh cleaning liquid (for example, tap water) are supplied.

Further, as shown in FIG. 4, a support member 19 is attached to the lower part of the apparatus main body 10a, and a traveling carriage 18 is disposed on the support member 19 so as to be able to travel along the traveling direction F of the filter portion 11a. Has been. The traveling carriage 18 is provided with a clamping cylinder (not shown) that holds the filter cloth 11 located below the vacuum trays A1 to A4 from the thickness direction.
Furthermore, a moving cylinder 20 is suspended from the lower part of the apparatus main body 10a so that the axis extends in the traveling direction F, and one end portion (rear end portion in the traveling direction F) 20a of the moving cylinder 20 is provided. It is connected to the traveling carriage 18.

As described above, the one end side 20a of the moving cylinder 20 is moved in the direction opposite to the traveling direction F in a state where the holding cylinder holds the filter cloth 11 located below the vacuum trays A1 to A4. Then, the traveling carriage 18 and the filter cloth 11 positioned below the vacuum trays A1 to A4 are caused to travel toward the side opposite to the traveling direction F, and the filtering unit 11a is traveled toward the traveling direction F. It has become so.
A cleaning pipe 21 is connected to the other end portion (front end portion in the traveling direction F) 20b of the moving cylinder 20, and is obtained at the tip of the cleaning pipe 21 (front end portion in the traveling direction F). A cleaning nozzle 22 for cleaning the filter cloth 11 after the solid material is peeled off is provided surrounded by a cover 23 for preventing scattering of the cleaning water.

  In the solid-liquid separation device 10 of the present embodiment, above the filtration unit 11a, the second cleaning liquid supply means 17b is located in front of the traveling direction F (in the illustrated example, at the front end in the traveling direction F). The pressurizing means 13 and the sealing means 12 are arranged at the arrangement position of the vacuum tray A4. Note that the pressurizing means 13 and the sealing means 12 are disposed at the same position in the traveling direction F of the filtration part 11a, and can simultaneously act on the same slurry S on the surface of the filtration part 11a. ing.

  As shown in FIGS. 1 to 3, the pressurizing means 13 includes a main body portion 13a having a rectangular shape in plan view, and a flat vent plate disposed on the lower surface side of the main body portion 13a facing the surface of the filtration portion 11a. 13b, a pressurizing means driving portion 13c that supports the main body portion 13a and the ventilation plate 13b so as to be able to advance and retreat toward the surface of the filtration portion 11a, and a pressure fluid supply means (not shown) that supplies the main body portion 13a with a pressure fluid. It has been.

  As shown in FIG. 2, openings 13e and 13f that open to the surface of the filtration part 11a are provided on the lower surface of the main body part 13a. A plurality of openings 13e and 13f of the present embodiment are provided, and a main opening 13e that opens at the center in the width direction on the surface of the filtration part 11a and a sub-opening 13f that opens at both ends in the width direction on the surface of the filtration part 11a. , 13f. The insides of these openings 13e and 13f are communicated with the pressure fluid supply means via a pressure fluid supply hole 13h so that the pressure fluid can be supplied. In this embodiment, air is used as the pressure fluid.

  Further, a pressurizing means driving unit 13c is connected to the upper surface of the main body part 13a, and by driving the driving part 13c, the main body part 13a can move forward and backward with respect to the surface of the filtering part 11a together with the ventilation plate 13b. It is like that.

  The ventilation plate 13b is attached to the lower surface of the main body 13a so as to close the openings 13e and 13f. The ventilation plate 13b has a plurality of through holes 13g penetrating in the thickness direction, so that the pressure fluid supplied to the openings 13e and 13f through the pressure fluid supply hole 13h passes therethrough. The slurry S that passes through the hole 13g and contacts the surface of the filtration part 11a is supplied and can be pressurized.

As shown in FIGS. 1 to 3, the sealing means 12 includes a frame-shaped sealing material 12a, a backup plate 12b bonded to the upper surface of the sealing material 12a, and an upper surface of the backup plate 12b. And a seal portion driving means 12c such as a cylinder device that supports the seal member 12a together with the seal member 12a so as to be able to advance and retreat. The vacuum tray A4 extends over the entire circumference of the opening surface of the seal member 12a. The surface of the filtration part 11a located in a part corresponding to the inclined part 14c of the material and the slurry S supplied to the surface can be pressed and brought into close contact with each other.
The seal portion drive means 12c is constituted by another component different from the pressurizing means drive portion 13c, and the seal material 12a corresponds to the inclined portion 14c of the vacuum tray A4 independently of the ventilation plate 13b. It is possible to press the surface of the filtration part 11a located in the portion to be pressed and the slurry S supplied to the surface.

  The sealing means 12 is provided on the outer peripheral edge of the main body portion 13a of the pressurizing means 13, the sealing material 12a is disposed so that the lower surface side thereof protrudes from the lower surface of the main body portion 13a, and the backup plate 12b is The seal portion driving means 12c is disposed inside the main body portion 13a, and is configured to be disposed on the upper surface of the main body portion 13a.

  As shown in FIG. 1, the backup plate 12b is disposed so as to cover substantially the entire upper surface of the sealing material 12a, and is divided into a plurality of parts in the circumferential direction. That is, the backup plate 12b presses the portion of the sealing material 12a that presses the surface of the filtration portion 11a that is located in the portion corresponding to the inclined portion 14c of the vacuum tray A4, and the slurry S that is supplied to the surface. It is set as the structure divided | segmented into the part.

  A plurality of seal portion driving means 12c are provided corresponding to the plurality of divided backup plates 12b, and each of the divided backup plates 12b is separated from the surface of the filtration portion 11a by a plurality of seal portion driving means 12c. They are advanced and retracted independently of each other. Thus, the integrally formed sealing material 12a presses the portion that presses the surface of the filtration portion 11a located at the portion corresponding to the inclined portion 14c of the vacuum tray A4 and the slurry S supplied to the surface. The close contact force is made different between the portions to be made, and these close contact states can be made uniform over the entire circumference of the sealing material 12a. The sealing material 12a of the present embodiment is formed of, for example, foamed rubber, single foam sponge, or urethane, and is supplied to the surface of the filtration unit 11a that is located at a portion corresponding to the inclined portion 14c of the vacuum tray A4 and the surface. When it is pressed and brought into close contact with the slurry S, it is elastically deformed.

  Here, in a plan view of the sealing means 12 and the pressurizing means 13, the inner peripheral edge shape of the sealing material 12a is substantially the same as the outer peripheral edge shape of the vent plate 13b of the pressurizing means 13, and these inner peripheral edges are the same. There is almost no gap between the outer peripheral edge and the outer peripheral edge. That is, the ventilation plate 13b and the sealing material 12a of the present embodiment are configured such that a part of the outer peripheral edge of the ventilation plate 13b bites into the inner peripheral edge of the sealing material 12a.

  Further, when the sealing material 12a is moved forward, as shown in FIG. 2, the outer peripheral edge side in the width direction of the filtration part 11a is on the upper surface of the inclined part 14c of the vacuum tray A4, as shown in FIG. The inner peripheral edge in the width direction of the filtration part 11a is in close contact with the outer peripheral edge of the slurry S in the width direction. Further, both ends of the lower surface of the sealing material 12a in the traveling direction F are in close contact with the slurry S as shown in FIG.

Next, a method for separating the slurry S into a liquid substance and a solid substance by the solid-liquid separation apparatus 10 configured as described above will be described.
First, after stopping the vacuum suction to each of the vacuum trays A1 to A4, the one end portion 20a of the moving cylinder 20 is placed in a state where the filter cloth 11 located below the vacuum trays A1 to A4 is sandwiched by the sandwiching cylinder. It is moved by a predetermined distance in the direction opposite to the traveling direction F. Accordingly, the filter cloth 11 positioned below the vacuum trays A1 to A4 is moved toward the opposite side of the traveling direction F, and the filtering unit 11a is moved by a predetermined distance toward the traveling direction F.

  Next, vacuum suction of the vacuum trays A1 to A4 is started. At this time, the slurry S is uniformly supplied to the cake forming section on the upper surface of the vacuum tray A1 by the slurry supply device 16, and the first and second cleaning devices 17a and 17b are used to supply the first and second surfaces on the upper surfaces of the vacuum trays A2 and A3. The second washing filtrate and fresh washing liquid are uniformly sprayed in the second washing section, respectively, and the cake-like slurry S formed in the first and second washing sections is washed, while the washing nozzle 22 Washing water is supplied to the filter cloth 11 to wash the filter cloth 11. In the dehydration section on the upper surface of the vacuum tray A4, dehydration and drying are performed by vacuum suction of the washed slurry S.

  As described above, the filter unit 11a is intermittently moved by a predetermined distance in the traveling direction F by the sandwiching cylinder and the moving cylinder 20, and the slurry S is supplied to the surface of the filter unit 11a by the slurry supply device 16 and vacuumed. After the cake-like slurry S is obtained, the slurry S is supplied to the slurry S by the first and second cleaning devices 17a and 17b and sucked in vacuum, and further washed. The slurry S is dehydrated and dried by vacuum suction, and the solid material is peeled off and collected from the filter cloth 11 by a scraper (not shown).

  Here, in this embodiment, in the vacuum tray A4 (the dehydration section) located at the most distal portion in the traveling direction F, the slurry S to which the second cleaning filtrate and the cleaning liquid are supplied is traveled by the filter cloth 11. In the stopped state, first, vacuum suction by the vacuum tray A4 is started. And in the state which continued this vacuum suction, the pressurization means drive part 13c of the pressurization means 13 drives forward toward the surface of the filtration part 11a, and the main-body part 13c is put on the surface of the said filtration part 11a with the ventilation plate 13b. And moving forward until the lower surface of the vent plate 13b contacts the slurry S.

At this time, the seal portion drive means 12c of the seal means 12 is driven forward toward the surface of the filtration portion 11a, and the seal material 12a is moved forward toward the surface of the filtration portion 11a via the backup plate 12b. The lower surface of 12a is pressed and brought into close contact with the surface of the filtration unit 11a located at a portion corresponding to the inclined portion 14c of the vacuum tray A4 and the slurry S supplied to the surface. At this time, the sealing material 12a is elastically deformed in the thickness direction.
As described above, the lower surface of the ventilation plate 13b is surrounded by the sealing material 12a at substantially the same time that the lower surface of the sealing material 12a is pressed and brought into close contact with the surface of the filtration part 11a and the slurry S supplied to the surface. Contact the sealed slurry S.

  Then, the pressure fluid supply means is operated in a state where the surrounding of the slurry S by the sealing material 12a, the contact by the lower surface of the vent plate 13b, and the vacuum suction by the vacuum tray A4 are maintained, and is formed in the main body portion 13a. The pressure fluid starts to be supplied to the openings 13e and 13f through the pressure fluid supply hole 13h. As a result, the inside of the openings 13e and 13f of the main body 13a is blocked by the ventilation plate 13b and the slurry S, and the internal pressure increases. Then, the increased internal pressure and the pressure fluid supplied to the openings 13e and 13f act on the slurry S through the through holes 13g formed in the ventilation plate 13b.

As described above, the slurry S located in contact with the lower surface of the ventilation plate 13b on the inner side of the opening surface of the sealing material 12a is vacuum-sucked from the lower surface side of the filtration unit 11a by the vacuum tray A4, and the openings 13e and 13f. The slurry S is separated into a solid substance and a liquid substance by being pressurized by the pressure fluid supplied therein.
Here, in this embodiment, in the process of pressurizing with the pressure fluid, the pressure applied to the slurry S is gradually increased over time. For example, the pressurizing force is increased continuously or stepwise as the pressurization time elapses.

  As described above, when the solid-liquid separation is completed, first, the supply of the pressure fluid is stopped, and then the vent plate 13b is moved backward to be separated from the surface of the obtained solid substance. Then, when the lower surface of the vent plate 13b and the solid substance are not in contact with each other, the pressure fluid is supplied to the openings 13e and 13f through the pressure fluid supply hole 13h. Spray from the upper surface side of 13b. By passing through the through hole 13g, the pressure fluid is sprayed also on the lower surface side of the vent plate 13b, thereby removing the slurry S and the like adhering to the vent plate 13b. The flow rate of the pressure fluid at this time may be the same as the flow rate when the slurry S is pressurized. Further, the sealing material 12a was moved backward after the supply of the pressure fluid was stopped, and the surface of the filtration part 11a located at the part corresponding to the inclined part 14c of the vacuum tray A4, and the obtained on the surface were obtained. Separated from solid material.

  As described above, according to the solid-liquid separation method according to the present embodiment, after the vacuum suction is started, the pressurization is started in a state where the vacuum suction is continued. Therefore, prior to the pressurization, It becomes possible to reduce the amount of the liquid substance contained in the slurry S and keep the slurry S hard. Therefore, when this slurry S is pressurized by the pressurizing means 13, the slurry S is scattered to the surroundings, or the area that is pressurized by the pressurizing means 13 in the direction along the surface of the filtration part 11 a. It is possible to prevent the material from being extruded outward (hereinafter referred to as “pressurizing region”). As a result, it is possible to suppress the amount of the slurry S located in the pressurizing region from becoming small at the time of pressurization by the pressurizing means 13, and it is possible to improve the solid-liquid separation efficiency. In addition, the purity of the obtained solid substance can be suppressed and the purity can be improved.

Further, since the pressure applied to the slurry S by the pressurizing means 13 is gradually increased with time, it is possible to prevent the slurry S from being scattered during the pressurization. In particular, the slurry S in the initial stage of pressurization by the pressurizing means 13 has a large amount of liquid substance, so that the applied pressure in the initial stage is increased even though the scattering is likely to occur. Thus, by reducing the pressure compared to the pressure applied to the slurry S at the later stage when the content of the liquid substance is reduced, it is possible to suppress the occurrence of such scattering.
Further, in the process of solid-liquid separation by pressurization, the amount of liquid substance contained in the slurry S is gradually decreased without causing the scattering, etc. While increasing the thickness, it is possible to apply to the slurry S always or each time a maximum pressing force suitable for the hardness, that is, a maximum pressing force that does not cause the scattering or the like. Therefore, efficient solid-liquid separation can be performed without causing the scattering and the like.

  In addition, after the ventilation plate 13b is brought into contact with the slurry S, pressurization with the pressure fluid is started in a state in which the contact is maintained, so that it is ensured that the slurry S scatters around the pressurization with the pressure fluid. Can be suppressed. That is, in the pressurization with the pressure fluid, the liquid substance is squeezed out by spraying the pressure fluid onto the slurry S. Therefore, the slurry S is likely to be scattered around by the spraying, but before pressurization with the pressure fluid, By causing the ventilation plate 13b to come into contact with the slurry S, that is, holding the slurry S between the ventilation plate 13b and the surface of the filtration part 11a and restraining it, it is possible to prevent such scattering. As described above, in the initial stage of pressurization, the amount of the liquid substance contained in the slurry S is large, so that the scattering is particularly likely to occur. However, even in this initial stage, the occurrence of the scattering can be suppressed.

Furthermore, after the pressurization by the pressure fluid is stopped, the ventilation plate 13b is moved backward and separated from the obtained solid substance, so that the occurrence of the scattering can be reliably suppressed.
Furthermore, since the pressure fluid is allowed to pass through the through hole 13g when the vent plate 13b is separated, the slurry S or the like adhering to the vent plate 13b including the inner peripheral surface of the through hole 13g is removed from the pressure hole. It is possible to remove by the fluid, and when the next slurry S is pressurized and solid-liquid separated, it is possible to avoid the previous slurry S and the like from adhering to and mixing with the next slurry S become. Therefore, it can suppress that the purity of the solid substance obtained by solid-liquid separation varies for every process of solid-liquid separation.

Further, in this embodiment, the sealing means 12 is provided, and in a state where the slurry S is surrounded and sealed by the sealing material 12a, the enclosed slurry S is pressurized while the vacuum is sucked to solidify the liquid substance. Since it is separated from the substance, the occurrence of the scattering and the like can be reliably suppressed.
Further, after the pressurization by the pressure fluid is stopped, the sealing material 12a is moved backward, and the surrounding by the sealing material 12a is released. Therefore, the slurry S is continuously surrounded by the sealing material 12a in the pressurizing process. Therefore, the occurrence of the scattering and the like can be suppressed more reliably.

  Further, since the sealing material 12a is formed of the elastically deformable material, the sealing material 12a is elastically deformed and brought into close contact with the surface of the filtration portion 11a and the slurry S supplied to the surface. It becomes possible to pressurize the slurry S located inside the opening surface of the material 12a and separate it into solid and liquid, and at the time of pressing, the slurry S is extruded from the inside of the opening surface of the sealing material 12a to the outside. Can be reliably suppressed, and solid-liquid separation efficiency can be improved and variations in the purity of the solid substance can be further suppressed.

  Since the sealing material 12a is supported by the sealing portion driving means 12c via the backup plate 12b so as to be able to move forward and backward, the sealing material 12a is formed of the material and has high flexibility. Therefore, the seal member 12a can be moved forward and backward easily and reliably by the seal portion driving means 12c.

  Furthermore, since the sealing material 12a can be pressed against the surface of the filtration part 11a and the slurry S supplied to the surface independently of each other in a region divided into a plurality in the circumferential direction. For each circumferential position of the material 12a, that is, in this embodiment, the portion that presses the surface of the filtration portion 11a located in the portion corresponding to the inclined portion 14c of the vacuum tray A4, and the slurry S supplied to the surface is pressed. It becomes possible to make the close force different from the part that does. For example, the pressing force in the portion that presses the slurry S can be made smaller than the pressing force in the portion that presses the surface of the filtration part 11a. This makes it possible to make the intimate state uniform over the entire circumference of the sealing material 12a, and to ensure that the slurry S is pushed outward from the inside of the opening surface of the sealing material 12a. Can be suppressed.

  Furthermore, the surface of the filtration part 11a is constituted by a filter cloth 11 provided on the apparatus main body 10a so as to be able to run substantially horizontally, and a plurality of recovery means 14 are provided below the filter cloth 11 in the running direction F of the filter cloth 11. In addition to being provided and configured by vacuum trays A1 to A4 connected to a vacuum suction device (not shown) (hereinafter referred to as “the configuration of the horizontal vacuum filter”), the traveling of the surface of the filtration unit 11a is stopped, After starting the vacuum suction, pressurization by the pressurizing means 13 is started while continuing the vacuum suction, so that the slurry S is intermittently run by the filter cloth 11 and the pressurization and vacuum suction are stopped when the slurry S is stopped. Thus, the solid-liquid separation can be performed, and the solid-liquid separation process in which the purity of the obtained solid substance is improved can be performed with high efficiency.

  Further, the seal portion driving means 12c is constituted by another component different from the pressurizing means driving portion 13c, and the sealing material 12a corresponds to the inclined portion 14c of the vacuum tray A4 independently of the ventilation plate 13b. Since the surface of the filtration part 11a located in the part to be pressed and the slurry S supplied to the surface can be pressed, for example, according to the properties of the slurry S supplied to the surface of the filtration part 11a It is possible to appropriately change the load of the pressing of the plate 13b and the sealing material 12a toward the surface of the filtration part 11a. Thereby, when the slurry S is pressurized by the pressurizing means 13, the slurry S can be prevented from being pushed out or scattered regardless of the type of the slurry S. As a result, even when various types of slurry S are squeezed and ventilated, stable filtration can be performed without scattering the slurry S, and the solid-liquid separation efficiency can be improved. The handling property of the solid-liquid separator 10 can be improved.

Next, a second embodiment according to the present invention will be described with reference to FIG. 5. The same parts as those in the first embodiment will be denoted by the same reference numerals, the description thereof will be omitted, and only different points will be described.
The sealing means 40 includes a sealing portion driving means 41 made of a diaphragm instead of the sealing portion driving means 12c made of a cylinder device or the like of the sealing means 12. That is, when the pressure fluid is supplied to the pressure fluid supply hole 42 formed in the main body portion 13 a of the pressurizing means 13 and the pressure fluid is supplied into the seal portion driving means 41, the seal portion driving means 41 is Elastically expanding and deforming, and the deformation causes the sealing material 12a to move forward toward the surface side of the filtration part 11a, and the surface of the filtration part 11a located at a part corresponding to the inclined part 14c of the vacuum tray A4; and The slurry S supplied to the surface can be pressed.

  In the present embodiment, a plurality of seal portion drive means 41 are provided, and a plurality of pressure fluid supply holes 42 are formed in the main body portion 13a according to the number of the seal portion drive means 41, and each pressure fluid supply hole is formed. The pressure fluid can be supplied from 42 to the inside of each seal portion driving means 41 independently of each other. Thereby, in the sealing material 12a, the pressing force can be made different between a portion that presses the surface of the filtering portion 11a and a portion that presses the slurry S supplied to the surface of the filtering portion 11a. Yes.

  Also in the present embodiment, it is possible to carry out the same solid-liquid separation method as in the first embodiment, and it is possible to achieve substantially the same operational effects as in the first embodiment. In particular, as compared with the sealing means 12 of the first embodiment, it is possible to reduce the number of components of the sealing means 40, improve handling, and increase the cost of the apparatus. Can be suppressed.

Next, a third embodiment according to the present invention will be described with reference to FIG. 6, but only differences from the first embodiment will be described.
The sealing means 30 of the present embodiment is provided with a sealing material 31 formed of a diaphragm instead of the sealing material 12a and the backup plate 12b of the first embodiment, and the main body 13a of the pressurizing means 13 is provided with a sealing material. A pressure fluid supply hole 32 is provided to connect the inside of 31 and a pressure fluid supply means (not shown). Then, the pressure fluid is supplied into the seal material 31 through the pressure fluid supply hole 32, whereby the seal material 31 expands and deforms, whereby the lower surface of the seal material 31 becomes the surface of the filtration part 11a. In close contact with the elastically deformed state.
Also in the present embodiment, it is possible to carry out the same solid-liquid separation method as in the first embodiment, and not only the effects similar to those in the first embodiment can be achieved, but also the second embodiment. Compared with the embodiment, it is possible to further reduce the components of the sealing means 30.

The technical scope of the present invention is not limited to the above-described embodiments, and various modifications can be made without departing from the spirit of the present invention.
For example, in the above-described embodiment, the configuration including only the sealing material 12a is shown as the sealing portion of the sealing means 12, but instead, at least a part of the sealing portion in the circumferential direction is used as shown in FIG. The slurry S supplied to the surface of the filtration part 11a can be a wall part 12d that pierces in the thickness direction, and the slurry S can be surrounded by the seal part while being pierced by the wall part 12d. . In this case, the seal portion is configured by the seal material 12a over the entire circumference, and both end portions of the seal portion in the traveling direction F are configured by both the wall portion 12d and the seal material 12a. May be. Furthermore, as shown in FIG. 8, the seal portion may be configured by only the wall portion 12d.

Moreover, in the said embodiment, although the structure which employ | adopted air as a pressure fluid was shown, you may employ | adopt liquids, such as water and a washing | cleaning liquid, for example. Moreover, you may employ | adopt the solid-liquid separation apparatus 10 which does not have the ventilation board 13b.
Furthermore, you may use the ventilation board 13b as a pressurization board which pressurizes the slurry S supplied to the surface of the filtration part 11a. For example, when the pressurizing means driving unit 13c is driven forward relative to the surface of the filtration unit 11a, the slurry S on the surface of the filtration unit 11a is pressurized by the lower surface of the ventilation plate 13b, and the pressure applied by the ventilation plate 13b is increased. You may make it pressurize the slurry S with the said pressure fluid in the state which maintained the pressure. Alternatively, the slurry S may be pressurized only by the vent plate 13b without using the pressure fluid.

  As modes of pressurizing the slurry S by the pressurizing means 13, there are three modes, one using only one of the pressure fluid and the vent plate 13b and one using both the pressure fluid and the vent plate 13b. In each of the above aspects, the slurry S may not be surrounded by the sealing means 12, 40, 30 during the pressurization.

  Moreover, it may replace with the sealing means 30 shown in FIG. 6, and the structure which divided | segmented the sealing material 31 into plurality in the circumferential direction may be employ | adopted. In other words, in the sealing means 40 shown in FIG. 5, the sealing material 12a may be removed, and a plurality of sealing portion driving means 41 formed of a diaphragm may be used as the sealing material. In this case, when the pressure fluid is separately supplied to the inside of the plurality of sealing materials (seal portion driving means 41) via the pressure fluid supply holes 42 and the respective sealing materials are expanded and deformed, the lower surfaces thereof are The peripheral end of the seal portion drive means 41 that is in close contact with the surface of the filtration portion 11a located in the portion corresponding to the inclined portion 14c of the vacuum tray A4 and the slurry S supplied to the surface and adjacent in the circumferential direction. It is desirable that the parts be in close contact with each other in an elastically deformed state.

  Further, in the first embodiment shown in FIGS. 1 to 3, the second embodiment shown in FIG. 5, the fourth embodiment shown in FIG. 7, and the fifth embodiment shown in FIG. , The seal portion driving means 12c and 41 for moving the wall portion 12d) back and forth toward the surface of the filtration portion 11a, and the pressurization for supporting the main body portion 13a and the ventilation plate 13b toward the surface of the filtration portion 11a so as to advance and retreat. Although constituted by a component different from the means driving unit 13c, instead of this, the seal part may be moved forward and backward toward the surface of the filtering part 11a by the pressurizing means driving unit 13c. That is, in the first, second, fourth, and fifth embodiments, a solid-liquid separation device that does not include the seal portion driving means 12c and 41 and the backup plate 12b may be employed. Even in such a configuration, the sealing portion is moved forward and backward toward the surface of the filtering portion 11a together with the main body portion 13a and the ventilation plate 13b by the pressurizing means driving portion 13c, and is supplied to the surface of the filtering portion 11a. When the applied slurry S is pressurized by the pressurizing means 13, the slurry S can be surrounded by the seal portion.

  Further, in each of the above embodiments, the configuration of the horizontal vacuum filter is shown as the solid-liquid separation device 10, but instead, the filtration unit 11a which has a fixed surface and is not supported so as to be able to travel is added. You may employ | adopt the structure which has the pressure means 13 and the collection | recovery means 14 connected with the said vacuum suction apparatus. Furthermore, in each said embodiment, although the vacuum trays A1-A4 were shown as the collection | recovery means 14, it is not restricted to this structure.

  At the time of pressurization, it becomes possible to prevent the mixture from being extruded or scattered outside the pressurization region in the direction along the surface of the filtration part, and the purity of the obtained solid substance is It is possible to suppress variation and improve the purity of the solid substance.

It is the principal part schematic of the solid-liquid separator shown as 1st Embodiment of this invention. In the solid-liquid separator of FIG. 1, it is the cross-sectional top view seen from the running direction of the filter cloth. In the solid-liquid separator of FIG. 1, it is the cross-sectional top view seen from the direction orthogonal to the running direction of a filter cloth. It is the whole solid-liquid separator shown as one embodiment of the present invention. It is the principal part schematic of the solid-liquid separator shown as 2nd Embodiment of this invention. It is a principal part schematic of the solid-liquid separator shown as 3rd Embodiment of this invention. In the solid-liquid separator shown as 4th Embodiment of this invention, it is the cross-sectional top view seen from the direction orthogonal to the running direction of a filter cloth. It is the principal part schematic of the solid-liquid separator shown as 5th Embodiment of this invention, Comprising: (a) The cross-sectional top view seen from the running direction of the filter cloth, (b) The direction orthogonal to the running direction of the filter cloth It is the cross-sectional top view seen from.

Explanation of symbols

DESCRIPTION OF SYMBOLS 10 Solid-liquid separation apparatus 10a Apparatus main body 11 Filter cloth 11a Filtration part 12 Sealing means 12a Sealing material (seal part)
13 Pressurizing means 13b Ventilation plate 13g Through hole 14 Recovery means A1 to A4 Vacuum tray F Running direction S Slurry (mixture)

Claims (5)

A guide roll rotatably provided on the main body of the solid-liquid separator;
A filter cloth stretched endlessly on a guide roll;
Of the filter cloth, a pressurizing means provided on the surface side of the filtration unit located on the upper side and capable of running substantially horizontally, and pressurizing the mixture supplied to the surface of the filtration unit;
Using a solid-liquid separation device provided on the back side of the filtration unit and connected to a vacuum suction device,
Said mixture supplied to the surface of the filtration unit, by pressurizing by the pressurizing means with vacuum suction by the recovery means, a solid-liquid separation method for separating the liquid material and solid material,
The solid-liquid separator is provided with a sealing means that is supported so as to be able to advance and retract toward the surface of the filtration part, and has a seal part provided in a frame shape or in an annular shape,
When the filtration unit is run , the mixture supplied to the surface of the filtration unit is opposed to the pressurizing unit and the sealing unit, and the running of the filtration unit is stopped.
The vacuum suction is started while supplying the mixture to a portion of the surface of the filtration unit that is located on the rear side in the running direction of the filtration unit with respect to the pressurizing unit and the sealing unit, and then the vacuum suction is continued. In addition, the pressurization is started in a state where the seal portion is moved toward the surface of the filtration portion and the pressurizing means and the mixture opposed to the seal means are surrounded and sealed by the seal portion. The solid-liquid separation method characterized by the above-mentioned. The solid-liquid separation method according to claim 1,
A solid-liquid separation method characterized by gradually increasing the pressure applied to the mixture over time when the mixture is pressurized by the pressurizing means. The solid-liquid separation method according to claim 1 or 2,
The pressurizing means includes a vent plate that is supported so as to be able to advance and retreat with respect to the surface of the filtration unit, has a plurality of through holes, and allows pressure fluid to pass through the through holes.
The rear surface of the vent plate is maintained in a state in which the ventilation plate is moved toward the surface of the filtration part, and the surface of the vent plate in which the through hole is opened is brought into contact with the mixture, and the contact is maintained. A solid-liquid separation method, wherein the pressure fluid is passed through the through-hole from the side, and pressurization of the mixture with the pressure fluid is started. The solid-liquid separation method according to claim 3,
A solid-liquid separation method, wherein after the pressurization by the pressure fluid is stopped, the vent plate is separated from the obtained solid substance. In the solid-liquid separation method according to claim 3 or 4,
After pressurizing the mixture, when the vent plate is separated from the obtained solid substance, a pressure fluid is allowed to pass through the through hole.

Images