CN205616670U - Hydrologic cycle sewage treatment system - Google Patents
Hydrologic cycle sewage treatment system Download PDFInfo
- Publication number
- CN205616670U CN205616670U CN201620054435.9U CN201620054435U CN205616670U CN 205616670 U CN205616670 U CN 205616670U CN 201620054435 U CN201620054435 U CN 201620054435U CN 205616670 U CN205616670 U CN 205616670U
- Authority
- CN
- China
- Prior art keywords
- water tank
- pipeline
- water
- filter vat
- sewage
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Links
- 239000010865 sewage Substances 0.000 title claims abstract description 38
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 94
- 239000002351 wastewater Substances 0.000 claims description 8
- 238000004140 cleaning Methods 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 4
- 238000000746 purification Methods 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 239000008394 flocculating agent Substances 0.000 abstract 3
- 239000012528 membrane Substances 0.000 description 11
- 238000000108 ultra-filtration Methods 0.000 description 8
- 238000005276 aerator Methods 0.000 description 3
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 238000009991 scouring Methods 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 239000011236 particulate material Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
A hydrologic cycle sewage treatment system, belong to the sewage purification field, the system comprises a sewage pool, the sewage intake pump, water intake pipe, the flocculating agent pipeline, the flocculating agent pump, the flocculating agent holding vessel, the cabin intakes, the filter vat, the outlet pipe way, clean water pipeline and clean water storage jar, adopt the funnel filter vat and leak hopper -shaped milipore filter technique, it erodees the milipore filter surface to make sewage constantly circulate in the filter vat, thereby produce stronger pressure, sewage treatment's efficiency has been accelerated, and be in flow state owing to leak the sewage on hopper -shaped milipore filter surface, so also arrived cleaning effect to surperficial its of milipore filter, make the extension of clean cycle of milipore filter.
Description
Technical field
The utility model belongs to sewage purification field.
Background technology
For the process making sewage reach a certain water body of draining or it is purified by the water quality requirement reusing, current sewage disposal
System multifunctional membrane technology is used as the Main Means of sewage disposal, and all uses film in the sewage disposal system using currently on the market
Assembly carries out dirty water purification, due to membrane module many employings club shaped structure, is placed in cylindrical vessel, the speed of its infiltration
Very slow, inefficiency, and steep for a long time in sewage due to membrane module, surface is easy to be adhered to by grease and the foul of sewage,
Affect permeability of the membrane.
Content of the invention
The purpose of this utility model is to provide a kind of water circulating sewage processing system, uses funnel filter vat and funnel-form milipore filter skill
Art, makes sewage constantly circulation scouring ultrafiltration membrane surface in filter vat, thus produces stronger pressure, accelerate sewage disposal
Efficiency, and owing to the sewage of funnel-form ultrafiltration membrane surface is at flow regime all the time, thus also to ultrafiltration membrane surface its
Arrive cleaning action, made the cleaning cycle of milipore filter extend.
For achieving the above object, this use is novel by the following technical solutions: a kind of water circulating sewage processing system, including sewage
Pond, wastewater influent pump, inlet pipeline, flocculant pipeline, flocculant pump, flocculant holding vessel, enter water tank, filter vat, go out
Water lines, clean water pipeline and clean water storage tank, filter vat is funnel-form, enters water tank, water inlet described in the setting of filter vat top
Cabin is circular, enters water tank and is provided with water tank water inlet and several water tank delivery port, and water tank delivery port is circumferentially spaced apart successively,
Being located at gate on described water tank delivery port, water tank delivery port is correspondingly positioned at the top of milipore filter, and the lower end of described filter vat is provided with out
The mouth of a river, is provided with milipore filter inside described filter vat, described milipore filter is funnel-form, the inwall of described milipore filter and described filter vat
Interval, face is arranged, and forms clean water collection cabin between the internal face of described milipore filter and described filter vat, under described milipore filter
End arranges lower port and this lower port is connected with delivery port, and the side wall lower ends of described filter vat is provided with clean water outlet, clean water
Outlet is connected with clean water storage tank by clean water pipeline, and described delivery port is connected with cesspool by outlet pipeline, cesspool
Being connected with described water tank water inlet by inlet pipeline, inlet pipeline is provided with described wastewater influent pump, and flocculant holding vessel passes through
Flocculant pipeline connects described inlet pipeline, and described flocculant pipeline is provided with described flocculant pump.
The position that arranges of described filter vat is higher than described cesspool.
The position that arranges of described filter vat is higher than described clean water storage tank.
Described cesspool sets aerator in (1).
A kind of water circulating sewage processing system described in the utility model, uses funnel filter vat and funnel-form ultrafiltration membrane technique, makes
Sewage constantly circulation scouring ultrafiltration membrane surface in filter vat, thus produce stronger pressure, accelerate the efficiency of sewage disposal,
And owing to the sewage of funnel-form ultrafiltration membrane surface is at flow regime all the time, so also to ultrafiltration membrane surface, it has arrived cleaning
Effect, makes the cleaning cycle of milipore filter and the life of milipore filter, just uses a main intake pump just permissible due to water inlet system
Complete whole water cycle process, save energy resource consumption, more environmentally-friendly economy.
Brief description
Fig. 1 is structure chart of the present utility model.
Detailed description of the invention
A kind of water circulating sewage processing system as shown in Figure 1, including the 4th, cesspool the 1st, wastewater influent pump the 2nd, inlet pipeline flocculates
The 17th, agent pipeline the 5th, flocculant pump the 3rd, flocculant holding vessel enters water tank the 8th, filter vat the 11st, outlet pipeline the 15th, clean water pipeline 12
With clean water storage tank 13, filter vat 11 in funnel-form, filter vat 11 top arrange described in enter water tank 8, enter water tank 8 in circular,
Entering the annular solid that water tank 8 is hollow, entering water tank 8 and be provided with water tank water inlet 16 and several water tank delivery port 7, water tank delivery port 7 is along circle
Zhou Yici is distributed in inside water tank 8, and described water tank delivery port 7 is provided with gate 6, and water tank delivery port 7 is correspondingly positioned at ultrafiltration
The top of film 10, the downwardly directed milipore filter of water tank delivery port 7 10, make the sewage stream that water tank delivery port 7 is gone out on milipore filter 10,
The lower end of described filter vat 11 is provided with delivery port 14, the internal milipore filter 10 that is provided with of described filter vat 11, and described milipore filter 10 is in funnel
Shape, is arranged for interval between described milipore filter 10 and the internal face of described filter vat 11, and described milipore filter 10 and described filtration
Forming clean water between the internal face of bucket 11 and gathering cabin 9, described milipore filter 10 lower end arranges lower port and this lower port and delivery port
14 connect, and the side wall lower ends of described filter vat 11 is provided with clean water outlet, and clean water exports by clean water pipeline 12 and clean water
Storage tank 13 connects, and described delivery port 14 is connected with cesspool 1 by outlet pipeline 15, cesspool 1 by inlet pipeline 4 with described
Water tank water inlet 16 connects, and described inlet pipeline 4 is provided with described wastewater influent pump 2, and flocculant holding vessel 17 passes through flocculant pipe
Road 5 connects described inlet pipeline 4, and the end of flocculant pipeline 5 is connected to the water inlet between wastewater influent pump 2 and water tank water inlet 16
On pipeline 4, described flocculant pipeline 5 is provided with described flocculant pump 3.
The position that arranges of described filter vat 11 is higher than described cesspool 1.
The position that arranges of described filter vat 11 is higher than described clean water storage tank 13.
Aerator 18 is set in described cesspool 1.Aerator 18 produces microbubble and upwards carries the flocculate in cesspool 1 to table
Layer, then removed by slag-treating machine.
In use, the sewage in cesspool 1 is sent in water tank 8 together with flocculant by wastewater influent pump 2 and flocculant pump 3,
Flocculant enters to react in water tank 8 generation flocculation sediment with sewage, enters water tank 8 and is looped around into the water tank water outlet inside water tank 8 by several
Sewage is guided the surface of milipore filter 10 by mouthfuls 7, makes sewage be downwardly towards delivery port 14 along the surface of milipore filter 10, owing to sewage washes away
Produced pressure, makes milipore filter 10 can gather clean water penetration to clean water in cabin 9, thus reaches the purpose that sewage is evolved,
Owing to water system of the present utility model makes constantly to circulate, so producing described in large-scale particulate material in sewage and flocculant
Raw flocculation sediment all will not be at the remained on surface of milipore filter 10, so without being carried out milipore filter 10 frequently, saving
Substantial amounts of manpower, adds the life-span of milipore filter 10.
Claims (3)
1. a water circulating sewage processing system, it is characterised in that: include cesspool (1), wastewater influent pump (2), inlet pipeline
(4), flocculant pipeline (5), flocculant pump (3), flocculant holding vessel (17), enter water tank (8), filter vat (11), outlet pipe
Road (15), clean water pipeline (12) and clean water storage tank (13), filter vat (11) in funnel-form, filter vat (11)
Water tank (8) is entered described in arranging in top, enters water tank (8) in circular, enters water tank (8) and be provided with water tank water inlet (16) and several water tank
Delivery port (7), water tank delivery port (7) is circumferentially distributed in successively into water tank (8) inner side, described water tank delivery port (7)
Being provided with gate (6), water tank delivery port (7) is correspondingly positioned at the top of milipore filter (10), the lower end of described filter vat (11)
Being provided with delivery port (14), described filter vat (11) is internal is provided with milipore filter (10), described milipore filter (10) in funnel-form,
Described milipore filter (10) is arranged with the internal face interval of described filter vat (11), and described milipore filter (10) and described mistake
Forming clean water between the internal face of lauter tub (11) and gathering cabin (9), described milipore filter (10) lower end arranges lower port and is somebody's turn to do
Lower port is connected with delivery port (14), and the side wall lower ends of described filter vat (11) is provided with clean water outlet, and clean water outlet is logical
Cross clean water pipeline (12) to be connected with clean water storage tank (13), described delivery port (14) by outlet pipeline (15) with
Cesspool (1) connects, and cesspool (1) is connected with described water tank water inlet (16) by inlet pipeline (4), inlet pipeline (4)
Being provided with described wastewater influent pump (2), flocculant holding vessel (17) connects described inlet pipeline (4), institute by flocculant pipeline (5)
State flocculant pipeline (5) and be provided with described flocculant pump (3).
2. a kind of water circulating sewage processing system as claimed in claim 1, it is characterised in that: setting of described filter vat (11)
Seated position is higher than described cesspool (1).
3. a kind of water circulating sewage processing system as claimed in claim 1, it is characterised in that: setting of described filter vat (11)
Seated position is higher than described clean water storage tank (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620054435.9U CN205616670U (en) | 2016-01-13 | 2016-01-13 | Hydrologic cycle sewage treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620054435.9U CN205616670U (en) | 2016-01-13 | 2016-01-13 | Hydrologic cycle sewage treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205616670U true CN205616670U (en) | 2016-10-05 |
Family
ID=57033439
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620054435.9U Active CN205616670U (en) | 2016-01-13 | 2016-01-13 | Hydrologic cycle sewage treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205616670U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109809625A (en) * | 2017-11-20 | 2019-05-28 | 陈化 | Sewage disposal reaction tank and sewage treatment-purification system |
-
2016
- 2016-01-13 CN CN201620054435.9U patent/CN205616670U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109809625A (en) * | 2017-11-20 | 2019-05-28 | 陈化 | Sewage disposal reaction tank and sewage treatment-purification system |
| CN109809625B (en) * | 2017-11-20 | 2023-12-26 | 陈化 | Sewage treatment reaction tank and sewage treatment-purification system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 830019 No. 1442 Xingxing Street, Midong District, Urumqi City, Xinjiang Uygur Autonomous Region Patentee after: CHINA PETROLEUM ENGINEERING CONSTRUCTION Co.,Ltd. XINJIANG DESIGN BRANCH Address before: 830019 No. 1442 Petrochemical Zhongxing Street, Midong District, Urumqi City, Xinjiang Uygur Autonomous Region Patentee before: XINJIANG DESIGN BRANCH, CHINA PETROLEUM ENGINEERING & CONSTRUCTION Corp. |
|
| CP03 | Change of name, title or address | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190521 Address after: 838600 No. 27 Huainan Road, Dushanzi District, Karamay City, Xinjiang Uygur Autonomous Region Patentee after: XINJIANG HUANQIU ENGINEERING CO. Address before: 830019 No. 1442 Xingxing Street, Midong District, Urumqi City, Xinjiang Uygur Autonomous Region Patentee before: CHINA PETROLEUM ENGINEERING CONSTRUCTION Co.,Ltd. XINJIANG DESIGN BRANCH |
|
| TR01 | Transfer of patent right |