CN213407983U - Integrated filtering separation pry - Google Patents

Integrated filtering separation pry Download PDF

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Publication number
CN213407983U
CN213407983U CN202022069419.6U CN202022069419U CN213407983U CN 213407983 U CN213407983 U CN 213407983U CN 202022069419 U CN202022069419 U CN 202022069419U CN 213407983 U CN213407983 U CN 213407983U
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tank body
layer
mud
sewage
sludge
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CN202022069419.6U
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Chinese (zh)
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仇国锋
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Yangzhou Xinya Environmental Engineering Co ltd
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Yangzhou Xinya Environmental Engineering Co ltd
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Abstract

The integrated filtration separation sled. Relate to sewage treatment technical field, concretely relates to integrated filtration separation sled. The integrated filtering separation pry of the utility model separates the tapered cyclone barrel from the tank body, so that an annular gap is formed between the tank body and the cyclone barrel; the fast separation of the suspended matters with large particle size and the sewage is realized through the 'abrupt change' of the sewage flow speed; the full separation of suspended matters with large particle size is realized, thereby ensuring that the water quality of the purified water reliably reaches the standard. The utility model discloses still hinder and revolve the board through setting up on the mud collection fill, to mud that the mud collection fill top converges the flow down disperse the buffering, reduce its velocity of flow, reduce the disturbance to mud in the mud collection fill, and then reduce bubble content in the mud collection fill, be favorable to improving pressure filter efficiency. Additionally, the utility model discloses intensive filtering mechanism and the pressure filter that sets up has saved the construction of traditional mud ground, and equipment fixing is quick and economy, still practices thrift the land used simultaneously, arranges beautifully.

Description

Integrated filtering separation pry
Technical Field
The utility model relates to a sewage treatment technical field, concretely relates to integrated filtration separation sled.
Background
With the general promotion of environmental protection consciousness, people put forward higher requirements on the treatment of sewage. How to carry out effectual processing to sewage, can discharge safely after making sewage purification, avoid causing the pollution to the surrounding environment, become the key point that people paid attention to.
In the prior art, the sewage purification is usually carried out by adopting the matching of a filter tank and a filter press, the sludge in the filter tank is discharged to a sludge tank, and the filter press pumps the sludge from the sludge tank for filter pressing. The water inlet of sewage sets up on filtering the jar wall of jar, and sewage lets in jar body back, and the uniform velocity of following cylindric jar body is rotatory earlier, sinks to the whirl bucket with jar body coupling again, and under the effect of vortex field, the large particle size suspended particles in the sewage sinks (collects and forms mud) along the whirl bucket separation, and the sewage rises and passes through the filter layer after discharging.
The disadvantage of this method of purification of sewage is that the large-particle-size suspended particles to be separated form a large interference with the rising sewage. If the sewage flow rate is too large, on the one hand: sewage is not fully filtered and quickly penetrates through the filter layer to be discharged; on the other hand, the large suspended particles separated and thrown to the tank wall in the ascending process are driven upwards again by newly introduced sewage, so that the quality of the purified water does not reach the standard. If the sewage flow speed is too small, the sewage lifting force is insufficient, and part of sewage flows to the sludge tank along the cyclone barrel, so that the sludge water content is too large, and the filter pressing workload and the treatment cost of the sludge are increased.
SUMMERY OF THE UTILITY MODEL
The utility model provides an above problem, it is reliable to provide a purification performance, filters the intensive integrated filtration separation sled that sets up of filter-pressing.
The technical scheme of the utility model is that:
the integrated filtering and separating pry comprises a filtering mechanism and a filter press which are connected,
the filtering mechanism comprises a tank body, the top of the tank body is provided with a water outlet, the bottom of the tank body is provided with a mud collecting hopper, and a filtering layer, a shallow pond sedimentation layer and a rotational flow barrel are sequentially arranged in the tank body from top to bottom;
at least one layer of filter medium is arranged in the filter layer, and a plurality of inclined channels are arranged in the shallow pool settling layer;
the cyclone barrel is in a conical shape with a large upper part and a small lower part, the upper part and the lower part of the cyclone barrel are provided with openings, an annular gap is arranged between the cyclone barrel and the tank body, the upper part of the cyclone barrel is provided with a water inlet, sewage enters the cyclone barrel from the water inlet, and is discharged from a water outlet after passing through a shallow pool sedimentation layer and a filter layer in sequence;
and a sludge discharge port is arranged at the bottom of the sludge collecting hopper and is connected with the filter press.
Furthermore, a rotation resisting plate is arranged between the mud collecting hopper and the rotational flow barrel, and the rotation resisting plate is a plate provided with a plurality of through holes.
Furthermore, the bottom of the rotation resisting plate is provided with a protruding part extending along the through hole.
Further, the inclined channel is formed by a plurality of inclined plates and/or inclined pipes which are arranged in an inclined mode.
Furthermore, a sludge concentration detector is arranged on the sludge collecting hopper.
The integrated filtering separation pry of the utility model separates the tapered cyclone barrel from the tank body, so that an annular gap is formed between the tank body and the cyclone barrel; on one hand, the flowing section of the sewage introduced into the conical rotational flow barrel is smaller and smaller, the newly flowed-in outer layer sewage shrinks and presses the inner layer sewage, the sewage is pressed to spirally go upwards, and the large-particle-size suspended matters are forced to separate from the sewage to spirally sink due to slow speed change, namely, the large-particle-size suspended matters are quickly separated from the sewage through the 'abrupt change' of the flow speed of the sewage; on the other hand, in the rising process after the sewage is separated from the cyclone barrel, part of large-particle-size suspended matters which are not separated in the barrel are thrown to the wall of the tank under the action of centrifugal force and then flow into the mud collecting hopper along the annular gap between the tank body and the cyclone barrel, so that the large-particle-size suspended matters are fully separated, and the water quality of the purified water is ensured to be up to the standard reliably.
The utility model discloses still hinder and revolve the board through setting up on the mud collection fill, to mud that the mud collection fill top converges the flow down disperse the buffering, reduce its velocity of flow, reduce the disturbance to mud in the mud collection fill, and then reduce bubble content in the mud collection fill, be favorable to improving pressure filter efficiency. Additionally, the utility model discloses intensive filtering mechanism and the pressure filter that sets up has saved the construction of traditional mud ground, and equipment fixing is quick and economy, still practices thrift the land used simultaneously, arranges beautifully.
Drawings
Figure 1 is a schematic structural view of the present invention,
figure 2 is a cross-sectional view a-a of figure 1,
FIG. 3 is a schematic structural view of the rotation-resisting plate of the present invention,
figure 4 is a schematic structural view of another embodiment of the rotation-resisting plate of the present invention,
figure 5 is a front view of figure 4,
fig. 6 is a working principle diagram of the present invention.
In the figure: 1-a filtering mechanism, 10-a tank body, 11-a rotational flow barrel, 110-a water inlet, 12-a shallow pool sedimentation layer, 13-a filtering layer, 130-a manhole, 14-a mud collecting hopper, 141-a mud discharging port, 15-a water outlet, 16-a rotation blocking plate, 160-a through hole and 161-a bulge; 2-filter press, 21-feed pump; 31-an upper sludge concentration detector and 32-a lower sludge concentration detector; 4-ring gap.
Detailed Description
The present invention will be described in further detail with reference to the accompanying fig. 1 to 6. The integrated filtering and separating pry of the utility model comprises a filtering mechanism 1 and a filter press 2 which are connected,
the filtering mechanism 1 comprises a tank body 10, a water outlet 15 is arranged at the top of the tank body 10, a mud collecting hopper 14 is arranged at the bottom of the tank body 10, and a filtering layer 13, a shallow pond sedimentation layer 12 and a rotational flow barrel 11 are sequentially arranged in the tank body 10 from top to bottom;
at least one layer of filter medium is arranged in the filter layer 13, for example, a polymeric foam bead filter layer can be used for rough filtration, and a polyester fiber ball filter layer can be used for fine filtration, and a manhole 130 can be arranged at the corresponding position of the filter layer 13 of the tank body 10, so as to facilitate the replacement of the filter medium; a plurality of inclined channels are arranged in the shallow pool sedimentation layer 12, and according to the shallow pool sedimentation theory, medium-particle-size suspended matters in the sewage are settled in the inclined channels and separated from the sewage;
the cyclone barrel 11 is in a conical shape with a large upper part and a small lower part and is provided with an upper opening and a lower opening, an annular gap 4 is arranged between the cyclone barrel 11 and the tank body 10, and the annular gap 4 is used for collecting sludge which is centrifugally thrown to the tank wall in the sewage rising process and flowing into the sludge collecting hopper 14; the upper part of the cyclone barrel 11 is provided with a water inlet 110, and the water inlet 110 is preferably arranged along the tangent of the cyclone barrel 11, so that the cyclone effect of sewage can be enhanced, and the separation of water and mud can be accelerated; sewage enters the cyclone barrel 11 from the water inlet 110 and then starts to be pressed and swirled, the sewage at the outer layer extrudes the sewage at the inner layer, so that the sewage is passively turned and spirally flows upwards out of the cyclone barrel 11, large-particle-size suspended matters in the sewage are separated from the sewage due to slow speed change and spirally flow downwards into the sludge collecting hopper 14, the raised sewage is purified through the shallow pool sedimentation layer 12 and the filter layer 13 in sequence, and purified water is discharged from the water outlet 15 and is recovered;
the bottom of the sludge collecting hopper 14 is provided with a sludge discharge port 141, the sludge discharge port 141 is connected with the inlet of the filter press 2, the sludge in the sludge collecting hopper 14 is pumped into the filter press 2 by the feeding pump 21 for filter pressing, after filter pressing, sludge cakes are discharged, and the clear liquid is introduced into the filtering mechanism 1 for purification treatment again.
A rotation resisting plate 16 is arranged between the mud collecting hopper 14 and the rotational flow barrel 11, and the rotation resisting plate 16 is a plate provided with a plurality of through holes 160; the through holes 160 may be formed by laying a plurality of grids, or by inserting a tube into the rotation blocking plate 16; the rotation resisting plate 16 is used for reducing disturbance of the sludge which is converged upwards on the existing sludge in the sludge collecting hopper 14, and further reducing bubble generation.
The bottom of the rotation resisting plate 16 is provided with a protrusion 161 extending along the through hole 160 to further guide the sludge to move vertically downwards, so as to reduce the rotational flow effect.
The inclined channel is formed by a plurality of inclined plates and/or inclined pipes which are arranged in an inclined way, and the shape or the combination of the shapes can be selected according to the processing convenience.
The sludge collecting hopper 14 is provided with a sludge concentration detector, and an upper sludge concentration detector 31 and a lower sludge concentration detector 32 are conventionally and selectively arranged on the upper part and the lower part of the sludge collecting hopper 14 respectively, so that the upper limit and the lower limit of sludge in the sludge collecting hopper 14 can be conveniently measured.
And the automatic control of the filtering/filter pressing treatment can be realized through a PLC (programmable logic controller) system, so that the labor cost is reduced, and the equipment operation and maintenance cost is reduced.
The disclosure of the present application also includes the following points:
(1) the drawings of the embodiments disclosed herein only relate to the structures related to the embodiments disclosed herein, and other structures can refer to general designs;
(2) in case of conflict, the embodiments and features of the embodiments disclosed in this application can be combined with each other to arrive at new embodiments;
the above embodiments are only examples disclosed in the present application, but the scope of the present disclosure is not limited thereto, and those skilled in the art should be able to change some of the technical features of the present disclosure within the scope of the present application.

Claims (5)

1. The integrated filtering and separating pry is characterized by comprising a filtering mechanism and a filter press which are connected,
the filtering mechanism comprises a tank body, the top of the tank body is provided with a water outlet, the bottom of the tank body is provided with a mud collecting hopper, and a filtering layer, a shallow pond sedimentation layer and a rotational flow barrel are sequentially arranged in the tank body from top to bottom;
at least one layer of filter medium is arranged in the filter layer, and a plurality of inclined channels are arranged in the shallow pool settling layer;
the cyclone barrel is in a conical shape with a large upper part and a small lower part, the upper part and the lower part of the cyclone barrel are provided with openings, an annular gap is arranged between the cyclone barrel and the tank body, the upper part of the cyclone barrel is provided with a water inlet, sewage enters the cyclone barrel from the water inlet, and is discharged from a water outlet after passing through a shallow pool sedimentation layer and a filter layer in sequence;
and a sludge discharge port is arranged at the bottom of the sludge collecting hopper and is connected with the filter press.
2. The integrated filtering and separating pry of claim 1, wherein a rotation resisting plate is arranged between the sludge collecting hopper and the rotational flow barrel, and the rotation resisting plate is a plate provided with a plurality of through holes.
3. The integrated filter separator sled of claim 2 wherein said rotation-resisting plate bottom is provided with a projection extending along said through hole.
4. The integrated filter separator skid of claim 1, wherein the diagonal channel is formed by a plurality of diagonally arranged diagonal plates and/or tubes.
5. The integrated filtering and separating sled as claimed in claim 1, wherein a sludge concentration detector is arranged on the sludge hopper.
CN202022069419.6U 2020-09-18 2020-09-18 Integrated filtering separation pry Active CN213407983U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202022069419.6U CN213407983U (en) 2020-09-18 2020-09-18 Integrated filtering separation pry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202022069419.6U CN213407983U (en) 2020-09-18 2020-09-18 Integrated filtering separation pry

Publications (1)

Publication Number Publication Date
CN213407983U true CN213407983U (en) 2021-06-11

Family

ID=76262779

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202022069419.6U Active CN213407983U (en) 2020-09-18 2020-09-18 Integrated filtering separation pry

Country Status (1)

Country Link
CN (1) CN213407983U (en)

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