CN204261396U - Solid-liquid two-phase Gravity Separation tower in processing of stone sewage disposal and Treated sewage reusing - Google Patents
Solid-liquid two-phase Gravity Separation tower in processing of stone sewage disposal and Treated sewage reusing Download PDFInfo
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- CN204261396U CN204261396U CN201520039310.4U CN201520039310U CN204261396U CN 204261396 U CN204261396 U CN 204261396U CN 201520039310 U CN201520039310 U CN 201520039310U CN 204261396 U CN204261396 U CN 204261396U
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- liquid
- sewage
- tank body
- cone cylinder
- solid
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- 239000010865 sewage Substances 0.000 title claims abstract description 66
- 239000007788 liquid Substances 0.000 title claims abstract description 43
- 230000005484 gravity Effects 0.000 title claims abstract description 20
- 239000004575 stone Substances 0.000 title claims abstract description 20
- 238000000926 separation method Methods 0.000 title claims abstract description 18
- 230000003139 buffering Effects 0.000 claims abstract description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 33
- 230000002787 reinforcement Effects 0.000 claims description 5
- 238000007789 sealing Methods 0.000 claims description 5
- 241000196435 Prunus domestica subsp. insititia Species 0.000 claims description 4
- 239000003814 drug Substances 0.000 claims description 4
- 229940079593 drugs Drugs 0.000 claims description 4
- 238000001556 precipitation Methods 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 8
- 230000001112 coagulant Effects 0.000 abstract description 5
- 239000002244 precipitate Substances 0.000 abstract description 5
- 239000010802 sludge Substances 0.000 abstract description 5
- 238000002156 mixing Methods 0.000 abstract description 3
- 238000004062 sedimentation Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 239000000428 dust Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 238000007605 air drying Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 206010006451 Bronchitis Diseases 0.000 description 1
- 206010006458 Bronchitis chronic Diseases 0.000 description 1
- 208000007451 Chronic Bronchitis Diseases 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 230000002262 irrigation Effects 0.000 description 1
- 238000003973 irrigation Methods 0.000 description 1
- 238000007517 polishing process Methods 0.000 description 1
- 230000000630 rising Effects 0.000 description 1
- 201000010001 silicosis Diseases 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000005429 turbidity Methods 0.000 description 1
Abstract
Solid-liquid two-phase Gravity Separation tower in the sewage disposal of this processing of stone and Treated sewage reusing, comprising: tank body, slower conical tube body, vortex mixer, oral siphon, buffering cone cylinder I and buffering cone cylinder II.Sewage after mixing enters buffering cone cylinder I through oral siphon under gravity, sewage is sprayed to radially buffering cone cylinder II outer surface, sewage can only from buffering cone cylinder II outer surface to periphery scattering, reduce the disturbance of liquid, and the contact area with sewage can be increased through the inner conical surface of buffering cone cylinder I and the male cone (strobilus masculinus) of buffering cone cylinder II, make sewage produce precipitation herein, accelerate deposition efficiency.Sewage flows into the slower conical tube body of tank base afterwards, precipitates further, solid-liquid is fully separated when the conical surface of slower conical tube body, and sludge coagulating is deposited in bottom, and the water liquid after precipitation rises gradually in tank body, discharges eventually through Graceful water pipe.Treatment effeciency is high, and treatment effect is excellent, and floor space is little, can not affect the environment of periphery.
Description
Technical field
The utility model relates to technical field of environment protection equipment, is specifically related to a kind of solid-liquid two-phase Gravity Separation tower.
Background technology
The fast development of stone material industry brings the problem of a series of environmental pollution, the wasting of resources.Stone material, in cutting with polishing process, produces a large amount of high-turbidity sewage.Current most producer disposes of sewage only by simple sedimentation basin, and by natural air drying process stone flour mud, what have does not even directly discharge through any process, works the mischief to earth's surface drinking water, field irrigation, scenic reserve, rivers and lakes etc.And sludge air drying can produce a lot of dust smog, these dust and smog suspend in atmosphere, can be inhaled in human body, with concentration and the stone material character of dust smog, cause the different occupation such as chronic bronchitis, silicosis to be critically ill evil to site personnel.In these pollute, be also mingled with equipment and vehicle travels the pollution of being kicked up by the dust being deposited on ground, enterprise, urban environment all caused and damages in various degree.
Summary of the invention
The utility model in order to overcome the deficiency of above technology, provide a kind for the treatment of effeciency high, can continuous seepage, without the need to the solid-liquid two-phase Gravity Separation tower in the processing of stone sewage disposal of sedimentation basin and Treated sewage reusing.
Solid-liquid two-phase Gravity Separation tower in the sewage disposal of this processing of stone and Treated sewage reusing, comprising:
Tank body, it is vertically arranged, and its top end opening place is airtight;
Slower conical tube body, it is rounding taper type, and the airtight bottom being connected to tank body, its top;
Vortex mixer, it is vertically arranged at the top of tank body, and its porch is connected to drug liquid tube and sewage pipe;
Oral siphon, its upper end is connected to the port of export of vortex mixer;
Buffering cone cylinder I in truncated cone, its top is connected to the lower end of oral siphon;
Buffering cone cylinder II in truncated cone, its top is inserted in the inner chamber of buffering cone cylinder I, and its top end opening place closes, and described tank body upper end is provided with Graceful water pipe.
In order to improve sedimentation effect, also comprise the clear water being horizontally placed on tank interior top and overflow weir notch and the settling vessel in annular, the external diameter of described clear water spilling weir notch is less than the internal diameter of tank body, its inside is provided with groove, described settling vessel is plugged in groove, and described settling vessel upper end edge circumferencial direction is provided with some double wedges raised up, and forms teeth groove between described every two adjacent double wedges, described clear water overflows on weir notch and is provided with delivery port, and described delivery port is connected with Graceful water pipe.
In order to improve sedimentation effect further, also comprise the inner conical-tube in rounding taper type, the lower end of described inner conical-tube is fixed with the cone circle of annular, and the top of described inner conical-tube is along the circumferential direction connected with the inner wall sealing of tank body, and described cone circle is positioned at directly over buffering cone cylinder I.
In order to accelerate the coagulative precipitation of mud, also comprise helical blade, described helical blade spiral is fixedly installed on the inwall of tank body.
Put mud to realize time switch, above-mentioned slower conical tube body outlet at bottom end is provided with internally piloted valve.
In order to realize Full water alarm, also comprise the liquid level sensor being arranged at inner tank wall top.
In order to improve intensity, above-mentioned tank body outer surface is welded with the reinforcement of some annulars from top to bottom.
The beneficial effects of the utility model are: the sewage after mixing enters buffering cone cylinder I through oral siphon under gravity, because buffering cone cylinder I is in truncated cone, therefore its lower ending opening is large, thus sewage is sprayed to radially buffering cone cylinder II outer surface, due to buffering cone cylinder 2nd liquid level truncated cone, and its upper end closed, therefore sewage can only from buffering cone cylinder II outer surface to periphery scattering, reduce the disturbance of liquid, and the contact area with sewage can be increased through the inner conical surface of buffering cone cylinder I and the male cone (strobilus masculinus) of buffering cone cylinder II, sewage is made to produce precipitation herein, accelerate deposition efficiency.Sewage flows into the slower conical tube body of tank base afterwards, precipitates further, solid-liquid is fully separated when the conical surface of slower conical tube body, and sludge coagulating is deposited in bottom, and the water liquid after precipitation rises gradually in tank body, discharges eventually through Graceful water pipe.Solid-liquid two-phase Gravity Separation tower in the sewage disposal of this processing of stone and Treated sewage reusing, because whole processing procedure is carried out continuously, therefore its treatment effeciency is high, and treatment effect is excellent, and does not need to use sedimentation basin, and floor space reduces greatly.Whole processing procedure is all carried out under the environment of sealing simultaneously, can not affect the environment of periphery.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is settling vessel structural representation of the present utility model;
In figure, 1. tank body 2. vortex mixer 3. slower conical tube body 4. helical blade 5. oral siphon 6. clear water spilling weir notch 7. settling vessel 8. Graceful water pipe 9. inner conical-tube 10. is bored circle 11. and is cushioned cone cylinder I 12. buffering cone cylinder II 13. internally piloted valve 14. liquid level sensor 15. reinforcement 16. double wedge.
Detailed description of the invention
Be described further below in conjunction with accompanying drawing 1, accompanying drawing 2 pairs of the utility model.
Solid-liquid two-phase Gravity Separation tower in the sewage disposal of this processing of stone and Treated sewage reusing, comprising: tank body 1, it is vertically arranged, and its top end opening place is airtight; Slower conical tube body 3, it is rounding taper type, and the airtight bottom being connected to tank body 1, its top; Vortex mixer 2, it is vertically arranged at the top of tank body 1, and its porch is connected to drug liquid tube and sewage pipe; Oral siphon 5, its upper end is connected to the port of export of vortex mixer 2; Buffering cone cylinder I 11 in truncated cone, its top is connected to the lower end of oral siphon 5; Buffering cone cylinder II 12 in truncated cone, its top is inserted in the inner chamber of buffering cone cylinder I 11, and its top end opening place closes, and tank body 1 upper end is provided with Graceful water pipe 8.Liquid and sewage enter in vortex mixer 2 respectively by elevator pump through drug liquid tube and sewage pipe, and two liquid streams because the pyramidal structure of vortex mixer inwall, thus form eddy current, and sewage and liquid are mixed naturally.Sewage after mixing enters buffering cone cylinder I 11 through oral siphon 5 under gravity, because buffering cone cylinder I 11 is in truncated cone, therefore its lower ending opening is large, thus sewage is sprayed to radially buffering cone cylinder II 12 outer surface, due to buffering cone cylinder II 12 liquid level truncated cone, and its upper end closed, therefore sewage can only from buffering cone cylinder II 12 outer surface to periphery scattering, reduce the disturbance of liquid, and the contact area with sewage can be increased through the inner conical surface of buffering cone cylinder I 11 and the male cone (strobilus masculinus) of buffering cone cylinder II 12, sewage is made to produce precipitation herein, accelerate deposition efficiency.Sewage flows into the slower conical tube body 3 bottom tank body 1 afterwards, precipitate further when the conical surface of slower conical tube body 3, solid-liquid is fully separated, sludge coagulating is deposited in bottom, and the water liquid after precipitation rises gradually in tank body 1, discharge eventually through Graceful water pipe 8.Solid-liquid two-phase Gravity Separation tower in the sewage disposal of this processing of stone and Treated sewage reusing, because whole processing procedure is carried out continuously, therefore its treatment effeciency is high, and treatment effect is excellent, and does not need to use sedimentation basin, and floor space reduces greatly.Whole processing procedure is all carried out under the environment of sealing simultaneously, can not affect the environment of periphery.
The clear water being horizontally placed on tank body 1 inner tip can also be comprised and overflow weir notch 6 and the settling vessel 7 in annular, the external diameter of clear water spilling weir notch 6 is less than the internal diameter of tank body 1, its inside is provided with groove, settling vessel 7 is plugged in groove, described settling vessel 7 upper end edge circumferencial direction is provided with some double wedges 16 raised up, form teeth groove between every two adjacent double wedges 16, clear water overflows on weir notch 6 and is provided with delivery port, and delivery port is connected with Graceful water pipe 8.After sewage precipitates in slower conical tube body 3, water liquid is above-mentioned in tank body 1 gradually, when rising to settling vessel 7 place, because settling vessel 7 is annular, and its circumferencial direction is provided with some double wedges 16, therefore double wedge 16 can slow down water velocity, during the teeth groove of effluent stream between two adjacent double wedges 16, carry out generation Separation of Solid and Liquid, thus further increase the effect of sewage disposal.The delivery port that clear water after precipitation overflows weir notch 6 from clear water is discharged through Graceful water pipe 8.
Can also comprise the inner conical-tube 9 in rounding taper type, the lower end of inner conical-tube 9 is fixed with the cone circle 10 of annular, and the top of inner conical-tube 9 is along the circumferential direction connected with the inner wall sealing of tank body 1, and cone circle 10 is positioned at directly over buffering cone cylinder I 11.Sewage from oral siphon 5 after buffering cone cylinder I 11 and buffering cone cylinder II 12 flow into and precipitate slower conical tube body 3 in, water liquid water level after precipitation rises gradually from cone circle 10 and enters into inner conical-tube 9, because the inclined-plane in inner conical-tube 9 can increase the contact area with current, thus can make oettIed sewage in inner conical-tube 9, again increase settling velocity or the solids of sedimentation amount in the unit interval further, thus realize the object of further lifting sewage treatment effeciency.
Can also comprise helical blade 4, described helical blade 4 spiral is fixedly installed on the inwall of tank body 1.When sewage rises in tank body 1, it, along the flowing of helical blade 4 surface, can accelerate the coagulative precipitation of mud further, and can not produce large stirring to clear water after precipitation in tower when sewage enters in tower, further increases settling velocity.
Slower conical tube body 3 outlet at bottom end is provided with internally piloted valve 13.Mud can be discharged by time switch by internally piloted valve 13, thus ensures that in tank body 1, sludge reaction is even, also ensures that mud can not overflow.The liquid level sensor 14 being arranged at tank body 1 inwall top can also be comprised.Prescribe a time limit when the water in tank body 1 arrives on tank body 1, liquid level sensor 14 measures level value, and it controls to report to the police, and prevents sewage excessive from the solid-liquid two-phase Gravity Separation tower the sewage disposal of this processing of stone and Treated sewage reusing, further increases the reliability of use.
The outer surface of tank body 1 can be welded with the reinforcement 15 of some annulars from top to bottom.Reinforcement 15 can play the effect improving tank body 1 intensity, extends the reliability of its service life and its work of raising.
Claims (7)
1. the solid-liquid two-phase Gravity Separation tower in processing of stone sewage disposal and Treated sewage reusing, is characterized in that: comprising:
Tank body (1), it is vertically arranged, and its top end opening place is airtight;
Slower conical tube body (3), it is rounding taper type, and the airtight bottom being connected to tank body (1), its top;
Vortex mixer (2), it is vertically arranged at the top of tank body (1), and its porch is connected to drug liquid tube and sewage pipe;
Oral siphon (5), its upper end is connected to the port of export of vortex mixer (2);
Buffering cone cylinder I (11) in truncated cone, its top is connected to the lower end of oral siphon (5);
Buffering cone cylinder II (12) in truncated cone, its top is inserted in the inner chamber of buffering cone cylinder I (11), and its top end opening place closes, and described tank body (1) upper end is provided with Graceful water pipe (8).
2. the solid-liquid two-phase Gravity Separation tower in processing of stone sewage disposal according to claim 1 and Treated sewage reusing, it is characterized in that: also comprise the clear water being horizontally placed on tank body (1) inner tip and overflow weir notch (6) and the settling vessel (7) in annular, the external diameter of described clear water spilling weir notch (6) is less than the internal diameter of tank body (1), its inside is provided with groove, described settling vessel (7) is plugged in groove, described settling vessel (7) upper end edge circumferencial direction is provided with some double wedges (16) raised up, teeth groove is formed between described every two adjacent double wedges (16), described clear water overflows on weir notch (6) and is provided with delivery port, described delivery port is connected with Graceful water pipe (8).
3. the solid-liquid two-phase Gravity Separation tower in processing of stone sewage disposal according to claim 1 and Treated sewage reusing, it is characterized in that: also comprise the inner conical-tube (9) in rounding taper type, the lower end of described inner conical-tube (9) is fixed with the cone circle (10) of annular, the top of described inner conical-tube (9) is along the circumferential direction connected with the inner wall sealing of tank body (1), and described cone circle (10) is positioned at directly over buffering cone cylinder I (11).
4. the solid-liquid two-phase Gravity Separation tower in processing of stone sewage disposal according to claim 1 and Treated sewage reusing, it is characterized in that: also comprise helical blade (4), described helical blade (4) spiral is fixedly installed on the inwall of tank body (1).
5. the solid-liquid two-phase Gravity Separation tower in processing of stone sewage disposal as claimed in any of claims 1 to 4 and Treated sewage reusing, is characterized in that: described slower conical tube body (3) outlet at bottom end is provided with internally piloted valve (13).
6. the solid-liquid two-phase Gravity Separation tower in processing of stone sewage disposal according to claim 5 and Treated sewage reusing, is characterized in that: also comprise the liquid level sensor (14) being arranged at tank body (1) inwall top.
7. the solid-liquid two-phase Gravity Separation tower in processing of stone sewage disposal according to claim 5 and Treated sewage reusing, is characterized in that: described tank body (1) outer surface is welded with the reinforcement (15) of some annulars from top to bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520039310.4U CN204261396U (en) | 2015-01-21 | 2015-01-21 | Solid-liquid two-phase Gravity Separation tower in processing of stone sewage disposal and Treated sewage reusing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520039310.4U CN204261396U (en) | 2015-01-21 | 2015-01-21 | Solid-liquid two-phase Gravity Separation tower in processing of stone sewage disposal and Treated sewage reusing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204261396U true CN204261396U (en) | 2015-04-15 |
Family
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520039310.4U Expired - Fee Related CN204261396U (en) | 2015-01-21 | 2015-01-21 | Solid-liquid two-phase Gravity Separation tower in processing of stone sewage disposal and Treated sewage reusing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204261396U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107352592A (en) * | 2017-07-27 | 2017-11-17 | 贵州紫云玉腾石业有限公司 | Marble sewage disposal production line |
| CN109052631A (en) * | 2018-09-18 | 2018-12-21 | 江苏澳洋生态园林股份有限公司 | The long-acting processing unit of flowable state or large-scale black and odorous water |
-
2015
- 2015-01-21 CN CN201520039310.4U patent/CN204261396U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107352592A (en) * | 2017-07-27 | 2017-11-17 | 贵州紫云玉腾石业有限公司 | Marble sewage disposal production line |
| CN109052631A (en) * | 2018-09-18 | 2018-12-21 | 江苏澳洋生态园林股份有限公司 | The long-acting processing unit of flowable state or large-scale black and odorous water |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150415 Termination date: 20170121 |
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| CF01 | Termination of patent right due to non-payment of annual fee |