JP2016123948A - Solid material recovery system of drum type concentrator - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a solid material recovery system of a drum type concentrator which recovers solid material in dehydrated separation liquid discharged from a dehydrator and improves concentration efficiency.SOLUTION: A solid material recovery system of a drum type concentrator includes: the drum type concentrator 1 for concentrating liquid to be treated mixed with coagulant; a dehydrator 103 for dehydrating and squeezing the solid material which is concentrated by the drum type concentrator 1; and a return pipe 104 for returning dehydrated separation liquid discharged from the dehydrator 103 to the drum type concentrator 1. Therein, the drum type concentrator 1 has a drum 3 which is rotated and driven while stretching a screen 2 on the surrounding and a ribbon screw 4 fixed to an inner circumferential surface of the drum 3, allows a supply pipe 5 for supplying liquid to be treated to be inserted from one side of the drum 3, at the same time, allows a feed liquid pipe 8 which is connected with the return pipe 104 from the other side of the drum 3 and adds the dehydrated separation liquid to be inserted along a rotation shaft of the ribbon screw 4 and, thereby, solid material in the dehydrated separation liquid can be recovered and, therefore, the recovery of the solid material is improved.SELECTED DRAWING: Figure 1

Description

The present invention relates to a concentrator for separating and removing moisture from a large amount of liquid to be treated containing solids and moisture such as sludge generated from wastewater treatment facilities such as sewage, human waste, village drainage, and industrial waste. In particular, the present invention relates to a drum type concentrator that supplies a liquid to be processed into a rotating drum type screen and performs concentration while conveying the liquid to be processed with a screw.

Conventionally, a technology that dehydrates solids after concentration treatment to remove more water, and also supplies a dehydration separation liquid recovered during dehydration to the former concentrator. It is disclosed in Document 1.

In addition, a spiral solid discharge blade (hereinafter referred to as a ribbon screw) is arranged in a drum with a screen stretched, and the liquid to be treated is supplied to a filtration chamber formed in the screen, and concentrated while rotating the drum. A rotary concentrator for carrying is conveyed in Patent Document 2.

In addition, a drum on which a screen is stretched and a screw shaft around which screw blades are wound are arranged concentrically, and the liquid to be treated is fed from a supply hole of a supply path provided on the screw shaft to a filtration chamber constituted by the drum and the screw shaft. Patent Document 3 discloses a rotary concentrator that supplies, concentrates and conveys a liquid to be processed while rotating a drum and a screw shaft in reverse, and discharges a concentrated solid from a terminal end of a filtration chamber.

JP 2010-000436 JP-A-10-165723 JP 2004-17014 A

Patent Document 1 discloses that the dehydrated separation liquid obtained by the screw press is returned to the concentrator before the screw press, but it cannot be specified how it is added to the concentrator.

In the concentrator described in Patent Document 2, the liquid to be processed is supplied to a filtration chamber partitioned by a ribbon screw below the drum, and the ribbon liquid rotates with the drum while conveying the liquid to be processed in the discharge direction. Concentrate.

However, when the amount of liquid to be treated is large, the liquid to be treated is supplied at a height higher than that of the lower ribbon screw that defines the filtration chamber, and the liquid to be treated that exceeds the height of the ribbon screw Into the discharge side. (See FIG. 5) Thus, since the liquid level of the supplied liquid to be processed does not become higher than the height of the lower ribbon screw when the ribbon screw is used, the liquid to be processed is concentrated only below the drum, and the efficiency is improved. It was not good. In addition, since the liquid to be treated flows to the discharge side due to oversupply and may be discharged without being concentrated, it is difficult to perform a large-capacity treatment. Furthermore, if a dehydration separation liquid is added like patent document 1, concentration will become more difficult.

Since the concentrator described in Patent Document 3 includes a screw shaft, even if the liquid level of the liquid to be treated supplied to the drum exceeds the height of the lower screw blade, it does not flow into the discharge side compartment, The liquid level of the liquid to be processed rises to the height of the screw shaft.

However, unlike Patent Document 1, the screw shaft is rotated for transporting the liquid to be processed, and thus a rotary drive machine and a bearing are required. In addition, since the load is concentrated below the screen, the drum is rotated to prevent clogging. However, when the drum is rotated, a separate drive mechanism is required and the apparatus becomes complicated.

The present invention provides a solids recovery system for a drum-type concentrator that improves the recovery rate of solids by returning the dehydrated separation liquid discharged from the dehydrator to a concentrator capable of processing a large volume.

A drum-type concentrator that concentrates the liquid to be treated mixed with the flocculant, a dehydrator that dehydrates and squeezes the solids concentrated in the drum-type concentrator, and a drum-type concentrator that removes the dehydrated separation liquid discharged from the dehydrator The drum-type concentrator has a drum that is driven to rotate with a screen stretched around it, and a ribbon screw that is fixed to the inner peripheral surface of the drum. Insert a supply pipe for supplying the treatment liquid and a supply pipe for adding the dehydrated separation liquid connected to the return pipe from the other side of the drum along the rotation axis of the ribbon screw. Since solids can be collected, the solids recovery rate is improved.

Insert the supply pipe of the liquid to be treated along the rotation axis of the ribbon screw, approximate the outer diameter of the supply pipe to the inner diameter of the ribbon screw, and provide the supply pipe with a supply hole on the drum start end side. By closing on the downstream side of the hole, the liquid level rises at the portion where the supply pipe is inserted, and the concentration efficiency is improved. Therefore, sufficient concentration can be achieved even if a dehydrated separation liquid is added.

(Proposal 1 only)
The liquid supply pipe is inserted from the end of the drum, the supply pipe is inserted from the start end of the drum, and the supply pipe is extended from the start end by one pitch or more of the ribbon screw, so that the liquid level can be stabilized. It can be raised above the supply pipe.

By disposing the supply pipe and the ribbon screw slidably and sealing the sliding surface, the liquid to be treated does not leak from the gap between the supply pipe and the ribbon screw.

By gradually decreasing the pitch of the ribbon screw from the starting end portion to the terminating end of the drum, the filtration surface is large at the starting end portion, and the conveying speed is gentle at the terminating end portion, so that the concentration time can be increased.

By connecting the liquid supply pipe and the supply pipe inside the drum, the liquid supply pipe and the supply pipe can be handled as an integrated object.

By returning the dehydrated separation liquid discharged from the dehydrator downstream of the concentrator and adding it again to the concentrator, the solids recovery rate is improved. When the dehydrating separation liquid is added through the liquid supply pipe inserted from the drum end portion opened in the concentrator, the insertion position of the liquid supplying pipe can be adjusted to easily set the dehydrating separation liquid addition position.

In order to approximate the outer diameter of the supply pipe to the inner diameter of the ribbon screw, the liquid level of the supplied liquid to be processed rises to the upper part of the supply pipe in the part where the supply pipe is extended, and concentration can be performed even above the drum. Since the effective filtration area is increased, the concentration efficiency is improved. Therefore, sufficient concentration can be achieved even if a dehydrated separation liquid is added. Further, since the concentration operation is performed only by the drum rotation mechanism, the structure of the apparatus is simplified, maintenance is easy, and the manufacturing cost can be reduced.

It is a figure which shows the flow of the dehydration process which concerns on this invention. Similarly, it is sectional drawing of a drum type concentrator. Similarly, it is a schematic sectional view of a drum type concentrator. It is sectional drawing of the drum type concentrator which concerns on the Example of this invention. It is a schematic sectional drawing of the conventional drum type concentrator.

FIG. 1 is a diagram showing a flow of dehydration processing according to the present invention.
As shown in FIG. 1, the dehydration treatment of the present invention is performed in a coagulation mixing tank 101 in which a polymer flocculant is added and mixed with a liquid to be treated (sludge etc.) flowing into a wastewater treatment facility and the like. Concentrate the produced agglomerated sludge to obtain a separated liquid and concentrated sludge, a dehydrator 103 to obtain a dehydrated cake and a dehydrated separated liquid by squeezing and dewatering the obtained concentrated sludge, and a dehydrated separated liquid. A return pipe 104 and a return pump 105 for returning to the concentrator are provided. Instead of providing the transfer pump 105, the dehydrated separation liquid may be supplied from above the concentrator 102. Moreover, the storage tank 106 which stores temporarily the concentrated sludge discharged | emitted from the concentrator as needed, and the transfer pump 107 which supplies the stored concentrated sludge to a dehydrator are arrange | positioned. As the dehydrator 103, a known dehydrator such as a screw press can be used.

FIG. 2 is a sectional view of a drum type concentrator according to the present invention.
The concentrator 102 according to the present invention employs a drum type concentrator 1, and the drum type concentrator 1 includes a drum 3 having a screen 2 stretched around it, a ribbon screw 4 fixed to the inner peripheral surface of the drum 3, and a drum. A fixed supply pipe 5 for supplying the liquid to be treated into the interior 3, a rotary drive 6 for rotating the drum 3, and a liquid supply pipe 8 connected to the return pipe 104 for adding the dehydrated separation liquid to the drum 3. Prepare.

The starting end portion of the drum 3 provided with the ribbon screw 4 is closed and the terminal end portion is opened. The liquid to be treated supplied from the start end side of the drum 3 is conveyed toward the end of the drum 3 by the ribbon screw 4 that rotates together with the drum 3. While the liquid to be treated is conveyed, only the water is separated by the screen 2 stretched on the drum 3, and the separated water is discharged from below the drum 3. And the concentrated solid substance is discharged | emitted from the open | released drum 3 terminal part.

The outer diameter of the supply pipe 5 for supplying the liquid to be treated into the drum 3 has the same size as the inner diameter of the ribbon screw 4, and the drum extends along the rotation axis of the ribbon screw 4 from the start end of the drum 3. 3 is inserted into the interior. The supply pipe 5 inserted into the drum 3 extends to the inside of the drum 3. Specifically, the effect of the present invention described later is obtained by extending the length of one pitch of the ribbon screw 4 or more.

A supply hole 7 for supplying the liquid to be processed from the supply pipe 5 into the drum 3 is provided on the start end side of the drum 3 of the supply pipe 5. The supply pipe 5 is closed on the downstream side of the supply hole 7. The outer diameter of the supply pipe 5 is close to the inner diameter of the ribbon screw 4 and has a minute gap. Since the supply pipe 5 is fixed, the supply pipe 5 does not rotate together with the rotation of the drum 3.

The liquid supply pipe 8 for adding the dehydrated separation liquid into the drum 3 is inserted into the drum 3 from the end portion of the drum 3 along the rotation axis of the ribbon screw 4. The supply pipe 8 is provided with a supply hole 9 in the drum 3 and is closed on the downstream side of the supply hole 9. The addition position of the dehydrated separation liquid is set as appropriate.
The outer diameter of the liquid supply pipe 8 may be approximated to the inner diameter of the ribbon screw 4 and provided with a minute gap. The supply pipe 5 and the liquid supply pipe 8 may be connected.

In addition, by always keeping the liquid level in the supply pipe 5 above the screen 2, the liquid level of the liquid to be processed supplied to the drum 3 rises above the screen 2. The supply pipe 5 may be provided with a supply device for press-fitting the liquid to be processed into the drum 3. Similarly to the supply pipe 5, the dehydration separation liquid is added to the supply pipe 8.

FIG. 3 is a schematic cross-sectional view of a drum type concentrator according to the present invention.
On the starting end side of the drum type concentrator 1 of the present invention, a supply pipe 5 extending inside the drum 3 is disposed with a small gap from the ribbon screw 4. A liquid supply pipe 8 is inserted along the rotating shaft of the ribbon screw 4 from the opened end of the drum 3. The dehydrated separation liquid is added from the liquid supply pipe 8 into the drum 3, and is combined with the liquid to be treated supplied from the supply pipe 5 to separate the solid matter contained in the dehydrated separation liquid from the water. Since most of the dehydrated separation liquid is water, the liquid load on the screen 2 is small.

FIG. 3A is a schematic cross-sectional view of the drum-type concentrator 1 at the initial stage of supplying the liquid to be processed. The liquid to be processed supplied from the supply hole 7 of the supply pipe 5 is a drum 3 partitioned by a ribbon screw 4. It is supplied to the filtration chamber on the start end side and accumulates while being concentrated.
In addition, the dehydrated separation liquid added from the liquid supply pipe 8 is agglomerated as the solid matter mixed in the dehydrated separation liquid is combined with the concentrated sludge in the drum 3, and the water in the dehydrated separation liquid is discharged from the screen 2.

The liquid level of the deposited liquid to be processed rises to above the supply pipe 5 because the supply pipe 5 is extended to block the hollow portion of the ribbon screw 4. Since the supply pipe 5 and the ribbon screw 4 have a minute gap, a very small amount of the liquid to be processed flows out of the gap. However, if the supply amount of the liquid to be processed is set so as to exceed the outflow amount. The liquid level of the liquid to be processed rises. In this embodiment, a gap of about 1 mm is provided.

By extending the supply pipe 5 by the pitch length of the ribbon screw 4, the hollow portion of the ribbon screw 4 can be closed and the liquid level of the liquid to be treated can be raised above the supply pipe 5. In consideration of the rotation of the ribbon screw 4, it is more preferable to extend the length more than twice the pitch. In addition, by increasing the outer diameter of the supply pipe 5, the liquid amount load per unit area of the filtration surface is reduced, so that the concentration efficiency is improved.

FIG. 3B is a schematic cross-sectional view of the drum type concentrator 1 during the concentration operation, and the liquid level of the liquid to be processed accumulated on the drum 3 starting end side exceeds the height of the supply pipe 5, and the discharge direction is increased. It flows into the filtration chamber. When the supply pipe 5 extends to the previous filtration chamber that has flowed in, the liquid to be treated is deposited again, and the liquid level rises to the height of the supply pipe 5.

Further, on the discharge side from the end portion of the supply pipe 5, concentration is performed while the dehydrated separation liquid and the liquid to be processed added from the supply pipe 8 are conveyed to the end side of the drum 3 by the ribbon screw 4 that rotates together with the drum 3. . In addition, since concentration progresses toward the drum 3 termination | terminus side, a liquid level falls. The concentrated solid is discharged from the end of the drum 3.

In the drum type concentrator 1 as in the present invention, as the liquid level of the supplied liquid to be processed increases, the area where the liquid to be processed contacts the screen 2 (filtration surface) of the drum 3 increases, and the concentration efficiency increases. Become. In particular, since the liquid to be treated immediately after the supply contains a large amount of moisture, the improvement in the concentration efficiency due to the increase in the filtration surface appears remarkably.

By configuring the supply pipe 5 and the ribbon screw 4 as in the present invention, the unconcentrated liquid to be treated immediately after the supply can be supplied up to the height of the supply pipe 5, and the cylindrical filtration surface can be used effectively. Thus, the concentration efficiency can be improved.

Further, if the pitch of the ribbon screw 4 is large on the starting end side of the drum 3 and gradually decreases toward the terminal end side, the filtration area on the starting end side increases, and the residence time of the concentrated solid matter increases on the terminal end side. Therefore, the concentration concentration can be further reduced.

In this embodiment, a minute gap is provided between the supply pipe 5 and the ribbon screw 4. However, the same effect can be obtained by arranging the supply pipe 5 and the ribbon screw 4 to be slidable. At this time, the sliding surface of the supply pipe 5 and the ribbon screw 4 may be sealed by a known technique such as a seal rubber so that the supplied liquid to be processed does not flow out between the supply pipe 5 and the ribbon screw 4.

FIG. 4 is a cross-sectional view of a drum type concentrator according to an embodiment of the present invention.
The drum 3 on which the screen 2 is stretched closes the start end and opens the end. The supply pipe 5 passes through the drum 3 and is pivotally supported at both ends. The outer diameter of the supply pipe 5 is approximated to the inner diameter of the ribbon screw 4 fixed to the drum 3.

The liquid to be treated flows into the supply pipe 5 from the terminal end side of the drum 3 and is supplied into the drum 3 through the supply hole 7 opened on the drum 3 start end side. Then, the return pipe is connected to the supply pipe 5 on the drum 3 starting end side, and the dehydrated separation liquid is added from the supply hole 9 provided on the drum 3 starting end side of the supply pipe 5.
The pipe may be closed on the downstream side of the supply hole 7 of the supply pipe 5, and the supply position of the liquid to be processed and the addition position of the dehydrated separation liquid may be separated.
The liquid to be processed and the dehydrated separation liquid supplied into the drum 3 are transported by the ribbon screw 4 of the drum 3 that is rotated by the rotary drive 6, and the concentrated solid matter is discharged from the terminal portion.

The drum-type concentrator according to the present invention can recover the fine solid contained in the dehydrated separation liquid by returning the dehydrated separation liquid to the concentrator from the dehydrator downstream of the concentrator.
Further, a flocculant can be added to the concentrator instead of the dehydrated separation liquid, and various utilization methods are conceivable.

DESCRIPTION OF SYMBOLS 1 Drum type concentrator 2 Screen 3 Drum 4 Ribbon screw 5 Supply pipe 7 Supply hole 8 Liquid supply pipe 103 Dehydrator 104 Return pipe

Claims (6)

A drum-type concentrator (1) for concentrating the liquid to be treated mixed with the flocculant, a dehydrator (103) for dehydrating / squeezing solids concentrated by the drum-type concentrator (1), and a dehydrator (103) A return pipe (104) for returning the dehydrated separation liquid discharged from the drum type concentrator (1),
The drum type concentrator (1)
A drum (3) that is rotatably driven with a screen (2) stretched around it,
A ribbon screw (4) fixed to the inner peripheral surface of the drum (3),
While inserting the supply pipe (5) for supplying the liquid to be treated from one of the drums (3),
Drum-type concentration characterized by inserting a liquid supply pipe (8) connected to a return pipe (104) from the other side of the drum (3) and adding a dehydrated separation liquid along the rotational axis of the ribbon screw (4). Machine solids collection system. Insert the liquid supply pipe (5) along the rotational axis of the ribbon screw (4),
While approximating the outer diameter of the supply pipe (5) to the inner diameter of the ribbon screw (4),
A supply hole (7) is provided on the start end side of the drum (3) of the supply pipe (5),
The solids recovery system for a drum type concentrator according to claim 1, wherein the supply pipe (5) is closed downstream of the supply hole (7). The liquid supply pipe (8) is inserted from the end of the drum (3), the supply pipe (5) is inserted from the start end of the drum (3), and the supply pipe (5) is inserted from the start end to the ribbon screw ( 4. The solids recovery system for a drum type concentrator according to claim 2, wherein the system is extended by one pitch or more of 4). The solid material recovery system for a drum type concentrator according to claim 2 or 3, wherein the supply pipe (5) and the ribbon screw (4) are slidably disposed, and the sliding surface is sealed. . The solid recovery of a drum type concentrator according to any one of claims 1 to 4, wherein the pitch of the ribbon screw (4) is gradually reduced from the start end to the end of the drum (3). system. The solids collection system for a drum type concentrator according to any one of claims 1 to 5, wherein the liquid supply pipe (8) and the supply pipe (5) are connected inside the drum (3).

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