CN210150858U - Novel water regeneration treatment system - Google Patents
Novel water regeneration treatment system Download PDFInfo
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- CN210150858U CN210150858U CN201920726169.3U CN201920726169U CN210150858U CN 210150858 U CN210150858 U CN 210150858U CN 201920726169 U CN201920726169 U CN 201920726169U CN 210150858 U CN210150858 U CN 210150858U
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Abstract
The utility model provides a novel water regeneration treatment system, which comprises a wastewater tank, an adjusting tank, a flocculating agent box, a coagulating sedimentation tank, a vertical flow sedimentation tank, an adsorption tank, a sludge concentration tank, a dehydrator, a mud cake external transport vehicle, a high temperature deamination box, a liquid ammonia storage tank, a transmission pump and a sludge pump, the flocculating agent box, the dehydrator and an active carbon layer are arranged, tiny colloid particles and suspended particles in wastewater are adsorbed under the action of colloid substances, large particles in the wastewater are adsorbed, the subsequent efficiency of adsorbing ammonia nitrogen molecules is improved, the adsorbed and plump active carbon layer evaporates the ammonia nitrogen through high temperature steam, the utilization rate of the active carbon layer is improved, the cost of the water regeneration system is reduced, a motor drives an auger roller to rotate, the volume of a spiral cavity is continuously shrunk, the internal pressure is continuously increased under the action of a back pressing plate, and the moisture content of the mud cake is controlled by adjusting the back pressing plate, the sludge is dewatered and discharged, the water content in the sludge is reduced, and the secondary pollution of the sludge to the environment is avoided.
Description
Technical Field
The utility model belongs to the technical field of water regeneration processing system, especially, relate to a novel water regeneration processing system.
Background
Water is an important natural resource, an economic resource, a social resource and an ecological basic factor for urban development, the water shuttles back and forth and flows in cities, and the system has an important function for maintaining urban ecological functions and safety and stability, and high-concentration ammonia nitrogen wastewater belongs to industrial wastewater which is difficult to treat.
The invention discloses a reclaimed water treatment system which is called CN 207659259U and comprises a microorganism aeration tank and a wetland ecological filter tank, wherein the microorganism aeration tank is connected with the wetland ecological filter tank through a connecting pipeline, an aeration area and a buffer area are arranged in the microorganism aeration tank, filler attached by a biological membrane is filled in the microorganism aeration tank, the wetland ecological filter tank is provided with a water inlet and a water outlet, the connecting pipeline is connected with the water inlet, and a wetland ecological system is arranged in the wetland ecological filter tank. But the existing water regeneration treatment system has the problems that large particles doped in the wastewater enter the adsorption tank together, the ammonia nitrogen molecule adsorption efficiency is reduced, the sludge is directly discharged without treatment, the secondary pollution is caused to the environment, the adsorption process is unreasonable, and the system cost is improved.
Therefore, it is necessary to develop a new water regeneration treatment system.
SUMMERY OF THE UTILITY MODEL
In order to solve the technical problem, the utility model provides a novel water regeneration treatment system to solve present water regeneration treatment system and having the large granule thing of adulteration in the waste water and get into the adsorption tank together, reduce the absorptive efficiency of ammonia nitrogen molecule, mud is not directly discharged through handling, causes secondary pollution to the environment, and adsorption process is unreasonable, improves the problem of system cost. A novel water regeneration treatment system comprises a wastewater tank, an adjusting tank, a flocculating agent box, a coagulating sedimentation tank, a vertical sedimentation tank, an adsorption tank, a sludge concentration tank, a dehydrator, a mud cake external transport vehicle, a high-temperature deamination tank, a liquid ammonia storage tank, a transmission pump and a sludge pump, wherein the adjusting tank is arranged on the right side of the wastewater tank and is connected with the wastewater tank through a pipeline, and the transmission pump is arranged on the pipeline; the flocculant box is positioned above the regulating tank and connected with the regulating tank through a pipeline, and a transmission pump is arranged on the pipeline; the coagulating sedimentation tank is positioned on the right side of the regulating tank and is connected with the regulating tank through a pipeline, and a transmission pump is arranged on the pipeline; the vertical flow sedimentation tank is positioned on the right side of the coagulating sedimentation tank and is connected with the coagulating sedimentation tank through a pipeline, and a transmission pump is arranged on the pipeline; the adsorption tank is positioned on the right side of the vertical flow sedimentation tank and is connected with the vertical flow sedimentation tank through a pipeline, and a transfer pump is arranged on the pipeline; the sludge concentration tank is positioned below the coagulating sedimentation tank and is respectively connected with the coagulating sedimentation tank and the regulating tank through pipelines, and a sludge pump and a transmission pump are arranged on the pipelines; the dehydrator is positioned below the sludge concentration tank and connected with the sludge concentration tank through a pipeline, and a sludge pump is arranged on the pipeline; the high-temperature deamination tank is positioned at the lower side of the adsorption tank, is connected with the adsorption tank through a pipeline, and is provided with a transmission pump; the liquid ammonia storage tank is positioned below the high-temperature deamination tank and is connected with the high-temperature deamination tank through a pipeline; 8 transmission pumps are adopted; the number of the sludge pumps is 3.
A stirrer is arranged in the regulating tank; the vertical flow sedimentation tank is connected with the sludge concentration tank through a pipeline, and a sludge pump is arranged on the pipeline; the dehydrator is connected with the regulating tank through a pipeline, and a transmission pump is arranged on the pipeline.
A discharge pipeline is arranged above the coagulating sedimentation tank; 20 activated carbon layers are arranged in the adsorption tank, and are connected with the regulating tank through pipelines, and a discharge pipeline is arranged above the adsorption tank; the connection part of the flocculating agent box and the regulating tank is connected through a screw conveyor.
The transmission pump is of an MPH-423 type and is connected with a power supply through a lead; the sludge pump is G135-2 type and is connected with a power supply through a lead; the coagulating sedimentation tank and the adsorption tank discharge pipe are both provided with a purification detector; the auger conveyor is 001 type and is connected with a power supply through a lead.
The dehydrator comprises a base, an electric control cabinet, a motor, a feeding hopper, a filtrate storage box, a packing auger roller, a roller and a back pressure plate, wherein the electric control cabinet is fixed on the left side above the base through a bolt; the motor is fixed in the middle position above the base through a bolt and is connected with the electric control cabinet through a wire, and the output shaft penetrates into the feeding hopper; the feeding hopper is welded on the left side above the base; the filtrate storage tank is fixed on the right side of the base through bolts and is connected with the pipeline; the auger roller is fixed on the left side of the feeding hopper through a bearing, penetrates into the feeding hopper and is connected with an output shaft of the motor through a coupler; the drum is sleeved on the outer side of the auger roller, the right side of the drum is fixed on the left side of the feeding hopper through bolts, and a plurality of through holes are formed in the drum; the back pressure plate is fixed at the left end of the roller through bolts and penetrates into the roller.
Compared with the prior art, the utility model discloses following beneficial effect has:
1. the utility model discloses a setting of flocculating agent, through auger conveyor with flocculating agent conveying to the equalizing basin in, fuse with waste water, stir through the mixer and make the flocculating agent fully react, with tiny colloidal particle and suspended solid granule under colloidal substance's effect in the waste water, the granule combines together, adsorbs big particulate matter in the waste water, carries out the preliminary treatment to waste water, improves follow-up to the absorbent efficiency of ammonia nitrogen molecule.
2. The utility model discloses a setting of hydroextractor, the motor switch on, when the motor drives the auger roller and rotates, it rotates to drive mud, make the interior filtrating of mud flow at the through-hole of cylinder, utilize constantly dwindling of volume between auger roller ring piece and ring piece simultaneously, the long-pending shrink of spiral cavity, the pressure constantly increases under the effect of backpressure board, and through adjusting the backpressure board, the moisture degree of control mud cake, make the filtrating continuous separation outflow, convey to the equalizing basin through the pipeline, sludge dewatering discharges, reduce moisture in the mud, avoid mud to cause secondary pollution to the environment.
3. The utility model discloses a setting on activated carbon layer will adsorb full activated carbon layer and transport to high temperature deamination case, evaporates out the ammonia nitrogen through high temperature steam, and the activated carbon layer can carry out regeneration, improves the utilization ratio on activated carbon layer, reduces water regeneration system's running cost.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a schematic structural view of the dehydrator of the present invention.
In the figure:
1-a wastewater pond, 2-a regulating pond, 3-a flocculating agent box, 4-a coagulating sedimentation tank, 5-a vertical flow sedimentation tank, 6-an adsorption tank, 7-a sludge concentration tank, 8-a dehydrator, 81-a base, 82-an electric control cabinet, 83-a motor, 84-a feeding funnel, 85-a filtrate storage tank, 86-a packing auger roller, 87-a roller, 88-a back pressing plate, 9-a mud cake external transport vehicle, 10-a high temperature deamination box, 11-a liquid ammonia storage tank, 12-a transfer pump and 13-a sludge pump.
Detailed Description
The invention is further described below with reference to the accompanying drawings:
example (b):
as shown in figures 1-2
The utility model provides a novel water regeneration treatment system, which comprises a wastewater disposal basin 1, an adjusting tank 2, a flocculating agent box 3, a coagulating sedimentation tank 4, a vertical flow sedimentation tank 5, an adsorption tank 6, a sludge thickening tank 7, a dehydrator 8, a mud cake external transport vehicle 9, a high temperature deamination box 10, a liquid ammonia storage tank 11, a transmission pump 12 and a sludge pump 13, wherein the adjusting tank 2 is arranged at the right side of the wastewater disposal basin 1 and is connected with the wastewater disposal basin 1 through a pipeline, and the transmission pump 12 is arranged on the pipeline; the flocculating agent box 3 is positioned above the regulating tank 2 and is connected with the regulating tank 2 through a pipeline, and a transmission pump 12 is arranged on the pipeline; the coagulating sedimentation tank 4 is positioned at the right side of the regulating tank 2, is connected with the regulating tank 2 through a pipeline, and is provided with a transmission pump 12; the vertical flow sedimentation tank 5 is positioned at the right side of the coagulating sedimentation tank 4, is connected with the coagulating sedimentation tank 4 through a pipeline, and is provided with a transmission pump 12; the adsorption tank 6 is positioned at the right side of the vertical flow sedimentation tank 5 and is connected with the vertical flow sedimentation tank 5 through a pipeline, and a transfer pump 12 is arranged on the pipeline; the sludge concentration tank 7 is positioned below the coagulating sedimentation tank 4, is connected with the coagulating sedimentation tank 4 through a pipeline, and is provided with a sludge pump 13; the dehydrator 8 is positioned below the sludge concentration tank 7 and is connected with the sludge concentration tank 7 through a pipeline, and a sludge pump 13 is arranged on the pipeline; the high-temperature deamination box 10 is positioned at the lower side of the adsorption tank 6, is connected with the adsorption tank 6 through a pipeline, and is provided with a transmission pump 12; the liquid ammonia storage tank 11 is positioned below the high-temperature deamination tank 10 and is connected with the high-temperature deamination tank 10 through a pipeline; 8 transfer pumps 12 are adopted; 3 sludge pumps 13 are adopted.
A stirrer is arranged in the adjusting tank 2; the vertical flow sedimentation tank 5 is connected with a sludge concentration tank 7 through a pipeline, and a sludge pump 13 is arranged on the pipeline; the dehydrator 8 is connected with the regulating tank 2 through a pipeline, and a transmission pump 12 is arranged on the pipeline.
A discharge pipeline is arranged above the coagulating sedimentation tank 4; 20 activated carbon layers are arranged in the adsorption tank 6, and are connected with the regulating tank 2 through pipelines, and a discharge pipeline is arranged above the adsorption tank; the connection part of the flocculating agent box 3 and the adjusting tank 2 is connected through a screw conveyor.
The transmission pump 12 is of an MPH-423 type and is connected with a power supply through a lead; the sludge pump 13 is G135-2 type and is connected with a power supply through a lead; and the discharge pipes of the coagulation sedimentation tank 4 and the adsorption tank 6 are provided with purification detectors.
The dehydrator 8 comprises a base 81, an electric control cabinet 82, a motor 83, a feeding funnel 84, a filtrate storage box 85, an auger roller 86, a roller 87 and a back pressure plate 88, wherein the electric control cabinet 82 is fixed on the left side above the base 81 through bolts; the motor 83 is fixed at the middle position above the base 81 through a bolt and is connected with the electric control cabinet 82 through a wire, and an output shaft penetrates into the feeding hopper 84; the feeding hopper 84 is welded on the left side above the base 81; the filtrate storage tank 85 is fixed on the right side of the base 81 through bolts and is connected with a pipeline; the auger roller 86 is fixed on the left side of the feeding funnel 84 through a bearing, penetrates into the feeding funnel 84 and is connected with an output shaft of the motor 83 through a coupler; the roller 87 is sleeved outside the auger roller 86, the right side of the roller is fixed on the left side of the feeding hopper 84 through bolts, and a plurality of through holes are formed in the roller; the back pressure plate 88 is fixed to the left end of the roller 87 by bolts and penetrates into the roller 87.
Principle of operation
In the utility model, the flocculating agent in the flocculating agent box 3 is conveyed into the regulating reservoir 2 through the conveying motor, the flocculating agent is fused with the waste water, the flocculating agent is fully reacted through stirring, tiny colloid particles and suspended solid particles in the waste water are combined together under the action of colloid substances, large particles in the waste water are adsorbed, the waste water is pretreated, the waste water is conveyed to the coagulating sedimentation tank 4 through the transmission pump 12 and is precipitated for 5 to 6 hours, the adsorbed harmful substances are precipitated at the bottom, the precipitated waste water is detected by the purification detector, the water quality reaches the standard and is discharged through the discharge pipe, the precipitated sludge is conveyed to the sludge concentration tank 7 through the sludge pump 13, the sludge is filtered to separate a part of water from the sludge, the water is conveyed to the regulating reservoir 2 through the pipeline, the residual sludge is conveyed to the dehydrator 8 through the pipeline through the sludge pump 13, the sludge is thoroughly separated from the water through the extrusion mode, the extruded water is conveyed to an adjusting tank 2, sludge is conveyed away by a mud cake external conveying vehicle 9, if unqualified wastewater is detected by a purification detector, the wastewater is conveyed to a vertical flow sedimentation tank 5 for secondary sedimentation, the precipitated sludge is conveyed to a sludge concentration tank 7, the wastewater is conveyed to an adsorption tank 6, the wastewater is adsorbed by an activated carbon layer, the detection of the detector is qualified, the wastewater is discharged through a discharge pipeline, if the wastewater does not reach the standard, the wastewater is conveyed to the adjusting tank 2 for purification again, the activated carbon layer which is fully adsorbed is conveyed to a high-temperature deamination tank 10, ammonia gas in the activated carbon layer is separated, the activated carbon layer can be recycled, the utilization rate of the activated carbon layer is improved, and the running cost of a water regeneration system is reduced.
Utilize technical scheme, or technical personnel in the field are in the utility model discloses under technical scheme's the inspiration, design similar technical scheme, and reach above-mentioned technological effect, all fall into the utility model discloses a protection scope.
Claims (5)
1. A novel water regeneration treatment system is characterized in that: the device comprises a wastewater tank (1), an adjusting tank (2), a flocculating agent box (3), a coagulating sedimentation tank (4), a vertical flow sedimentation tank (5), an adsorption tank (6), a sludge concentration tank (7), a dehydrator (8), a mud cake external transport vehicle (9), a high-temperature deamination tank (10), a liquid ammonia storage tank (11), a transmission pump (12) and a sludge pump (13), wherein the adjusting tank (2) is arranged on the right side of the wastewater tank (1) and is connected with the wastewater tank (1) through a pipeline, and the transmission pump (12) is arranged on the pipeline; the flocculant box (3) is positioned above the adjusting tank (2) and is connected with the adjusting tank (2) through a pipeline, and a transmission pump (12) is arranged on the pipeline; the coagulating sedimentation tank (4) is positioned at the right side of the regulating tank (2), is connected with the regulating tank (2) through a pipeline, and is provided with a transmission pump (12); the vertical flow sedimentation tank (5) is positioned on the right side of the coagulating sedimentation tank (4), is connected with the coagulating sedimentation tank (4) through a pipeline, and is provided with a transmission pump (12); the adsorption tank (6) is positioned at the right side of the vertical flow sedimentation tank (5), is connected with the vertical flow sedimentation tank (5) through a pipeline, and is provided with a transfer pump (12); the sludge concentration tank (7) is positioned below the coagulating sedimentation tank (4), is respectively connected with the coagulating sedimentation tank (4) and the regulating tank (2) through pipelines, and is provided with a sludge pump (13) and a transmission pump (12); the dehydrator (8) is positioned below the sludge concentration tank (7), is connected with the sludge concentration tank (7) through a pipeline, and is provided with a sludge pump (13); the high-temperature deamination tank (10) is positioned at the lower side of the adsorption tank (6), is connected with the adsorption tank (6) through a pipeline, and is provided with a transmission pump (12); the liquid ammonia storage tank (11) is positioned below the high-temperature deamination tank (10) and is connected with the high-temperature deamination tank (10) through a pipeline; 8 conveying pumps (12) are adopted; the number of the sludge pumps (13) is 3.
2. The novel water reclamation treatment system as recited in claim 1, wherein: a stirrer is arranged in the adjusting tank (2); the vertical flow sedimentation tank (5) is connected with the sludge concentration tank (7) through a pipeline, and a sludge pump (13) is arranged on the pipeline; the dehydrator (8) is connected with the adjusting tank (2) through a pipeline, and a transmission pump (12) is arranged on the pipeline.
3. The novel water reclamation treatment system as recited in claim 1, wherein: a discharge pipeline is arranged above the coagulating sedimentation tank (4); 20 activated carbon layers are arranged in the adsorption tank (6), and are connected with the regulating tank (2) through pipelines, and a discharge pipeline is arranged above the adsorption tank; the connection part of the flocculating agent box (3) and the adjusting tank (2) is connected through a screw conveyor.
4. The novel water reclamation treatment system as recited in claim 1, wherein: the transmission pump (12) is of an MPH-423 type and is connected with a power supply through a lead; the sludge pump (13) is G135-2 type and is connected with a power supply through a lead; and the coagulating sedimentation tank (4) and the discharge pipe of the adsorption tank (6) are both provided with a purification detector.
5. The novel water reclamation treatment system as recited in claim 1, wherein: the dehydrator (8) comprises a base (81), an electric control cabinet (82), a motor (83), a feeding hopper (84), a filtrate storage box (85), a packing auger roller (86), a roller (87) and a back pressing plate (88), wherein the electric control cabinet (82) is fixed on the left side above the base (81) through bolts; the motor (83) is fixed in the middle position above the base (81) through bolts and is connected with the electric control cabinet (82) through a lead, and an output shaft penetrates into the feeding hopper (84); the feeding hopper (84) is welded on the left side above the base (81); the filtrate storage tank (85) is fixed on the right side of the base (81) through bolts and is connected with a pipeline; the auger roller (86) is fixed on the left side of the feeding hopper (84) through a bearing, penetrates into the feeding hopper (84), and is connected with an output shaft of the motor (83) through a coupler; the roller (87) is sleeved outside the auger roller (86), the right side of the roller is fixed on the left side of the feeding hopper (84) through bolts, and a plurality of through holes are formed; the back pressure plate (88) is fixed at the left end of the roller (87) through a bolt and penetrates into the roller (87).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920726169.3U CN210150858U (en) | 2019-05-21 | 2019-05-21 | Novel water regeneration treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920726169.3U CN210150858U (en) | 2019-05-21 | 2019-05-21 | Novel water regeneration treatment system |
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| Publication Number | Publication Date |
|---|---|
| CN210150858U true CN210150858U (en) | 2020-03-17 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920726169.3U Active CN210150858U (en) | 2019-05-21 | 2019-05-21 | Novel water regeneration treatment system |
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| Country | Link |
|---|---|
| CN (1) | CN210150858U (en) |
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- 2019-05-21 CN CN201920726169.3U patent/CN210150858U/en active Active
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