CN206328262U - A kind of hydrocone type waste water treatment reactor - Google Patents
A kind of hydrocone type waste water treatment reactor Download PDFInfo
- Publication number
- CN206328262U CN206328262U CN201621469404.6U CN201621469404U CN206328262U CN 206328262 U CN206328262 U CN 206328262U CN 201621469404 U CN201621469404 U CN 201621469404U CN 206328262 U CN206328262 U CN 206328262U
- Authority
- CN
- China
- Prior art keywords
- reactor body
- waste water
- reactor
- liquid level
- wall
- 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.)
- Active
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model belongs to field of waste water treatment, and in particular to a kind of hydrocone type waste water treatment reactor.The reactor includes reactor body, the open topped of reactor body, partition wall and filter membrane are provided with reactor body, partition wall and filter membrane will be divided into two parts of reaction chamber and filtrate chamber inside reactor body, open topped of the upper end wall of partition wall close to reactor body, the lower end wall of partition wall is spaced apart with the bottom wall of reactor body, the both sides end wall of partition wall and the side wall of reactor body are tightly connected, filter membrane is located at the bottom of filtrate chamber, tank is provided near reactor body, tank is with filtrate chamber by being connected in the siphon pipe of reverse U shape, the water of filtrate chamber can be automatically drawn into tank by siphon pipe.The beneficial effects of the utility model are to be transformed on the basis of Conventional waste water treatment reactor, easily transformation, and the liquid after transformation in filtrate chamber is automatically transferred in tank by siphon pipe, reduces power-equipment, are conducive to saving the energy, reduce operating cost.
Description
Technical field
The utility model belongs to field of waste water treatment, and in particular to a kind of hydrocone type waste water treatment reactor.
Background technology
With more and more higher of the country to environmental requirement, wastewater treatment demand is also increasing, various Wastewater Treatment Technologies
Art is also constantly being improved, but the design of reactor all has that pipeline valve is more, investment is big, equipment operating cost mostly
The characteristics of height, complex management, it is difficult to promote in the underdeveloped area of technology.
Siphon is the effect force phenomenon using liquid level difference, after liquid is full of in an inverted U-shaped tubular structure, will
The high one end of opening is placed in the container for filling liquid, and the liquid in container can continue through siphon pipe from being opened on lower position
Outflow is put, this process does not need any power-equipment, when the liquid level of eminence drops to the water inlet end of siphon pipe, siphonic process is certainly
It is dynamic to terminate.The transfer of liquid is carried out using siphon principle, is conducive to saving the energy.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of hydrocone type waste water treatment reactor, and it utilizes siphon
Principle carries out liquid transfer, can effectively save the energy and operating cost.
The technical scheme that the utility model solves above-mentioned technical problem is as follows:A kind of hydrocone type waste water treatment reactor, its
Including reactor body, the open topped of the reactor body is provided with partition wall and filter membrane in the reactor body, described
Partition wall and filter membrane will be divided into two parts of reaction chamber and filtrate chamber inside the reactor body, the upper end wall of the partition wall is close
The open topped of the reactor body, the lower end wall of the partition wall is spaced apart with the bottom wall of the reactor body, it is described every
The both sides end wall of wall is tightly connected with the side wall of the reactor body, and the filter membrane is located at the bottom of the filtrate chamber and described
The periphery of filter membrane is fixedly connected with the lower end wall of the partition wall and the side wall of the reactor body, near the reactor body
Tank is provided with, the tank is connected with the filtrate chamber by siphon pipe, the siphon pipe can be by the water of the filtrate chamber certainly
In the dynamic suction tank, the siphon pipe is stretched into the filtrate chamber by the through hole on the wall of the reactor body side.For
Cleaning sludge is convenient, and door body of removing contamination able to turn on or off can be set in the bottom of the reaction chamber.
On the basis of above-mentioned technical proposal, the utility model can also do following improvement.
Further, the liquid level gauge for monitoring its interior liquid level height, the reactor are provided with the reactor body
Elevator pump is provided near main body, the elevator pump and coupled pipeline can send into waste water in the reactor body,
The elevator pump and liquid level gauge are connected with controller signals, the liquid level gauge can by the liquid level information transmission monitored to
The controller, the controller controls the keying of the elevator pump according to the liquid level signal received.Reactor body
Reaction chamber in be preset with the first liquid level and the second liquid level, the first liquid level is higher than the peak of siphon pipe, the second liquid level and filtrate
The entrance point liquid level of siphon pipe is equal in chamber, the elevation information of the first liquid level and the second liquid level as the controller default letter
Breath.
Further, the liquid level is calculated as ultrasonic liquid level meter.Ultrasonic liquid level meter is flexibly quick and easily carries out signal company with controller
Connect, so as to the Automated condtrol of waste water treatment reactor.
Further, the siphon pipe is in reverse U shape.Its entrance point be located at filtrate chamber in, the port of export be located at tank in or on
Side, entrance point present position is higher than port of export position.
Further, it is provided with mixer above the reactor body, the agitating shaft of the mixer and stirring thereon
Leaf is mixed to stretch into the reaction chamber.Setting mixer can make liquid in reaction chamber and chemical treatment medicine device that some are added into fast
Speed mixing, lifts treatment effeciency.
Further, the side that the filter membrane is obliquely installed and its is of a relatively high is connected with the lower end wall of the partition wall.Tilt
The filter membrane of setting is conducive to increasing the area of filter membrane, reaction intracavity liquid is filtered the speed quickening into the filtrate chamber, improves useless
Water treatment efficiency.
Further, the siphon pipe is stretched into the filtrate chamber by the through hole on the wall of the reactor body side, described
Through hole is 15-80cm with the vertical distance at the reactor body open topped.The peak of siphon pipe is set to be less than reactor
Height at the open topped of main body, is easy to the fixation of the automatic initiation and siphon pipe of siphon pipe water suction in itself.
The beneficial effects of the utility model are:To being transformed on the basis of Conventional waste water treatment reactor, set up put every
Wall and its filter membrane of lower end, the side wall of partition wall, filter membrane and reactor body, which is defined, removes filtrate chamber in filtrate chamber, reactor body
Part in addition is reaction chamber, and the liquid in filtrate chamber is automatically drawn into the water near reactor body by inverted U-shaped siphon pipe
In groove, the power-equipment of conveying liquid is reduced, is conducive to saving the energy and reduces operating cost, on the basis of pre-existing reactors
Upper transformation, improvement cost is low;It is also wastewater treatment process in reaction chamber and filtrate chamber to lift pump water inlet process, and water inlet is close to be terminated
When, trigger automatically the filtrate in siphon, filtrate chamber through siphon pipe automatic ink-suction effect suction tank in, direct qualified discharge or
Carry out the wastewater treatment of next step;The reactor of the utility model offer is sustainable automatically to be handled waste water and reduces liquid
The power-equipment of body conveying, high degree of automation, the saving energy.
Brief description of the drawings
A kind of schematic diagram for hydrocone type waste water treatment reactor that Fig. 1 provides for the utility model.
In accompanying drawing, the list of parts representated by each label is as follows:
1st, reactor body;2. partition wall;3. filter membrane;4. siphon pipe;5. tank;6. ultrasonic liquid level meter;7. elevator pump;8. stir
Mix axle.
Embodiment
Principle of the present utility model and feature are described below in conjunction with accompanying drawing, example is served only for explaining this practicality
It is new, it is not intended to limit scope of the present utility model.
As shown in figure 1, a kind of hydrocone type waste water treatment reactor, it includes reactor body 1, the reactor body 1
Open topped, be provided with partition wall 2 and filter membrane 3 in the reactor body 1, the partition wall 2 and filter membrane 3 are by the reactor master
It is divided into two parts of reaction chamber and filtrate chamber inside body 1, the upper end wall of the partition wall 2 is close to the top of the reactor body 1
Opening, the lower end wall of the partition wall 2 is spaced apart with the bottom wall of the reactor body 1, the both sides end wall of the partition wall 2 with it is described
The side wall of reactor body 1 is tightly connected, and the filter membrane 3 is located at the bottom of the filtrate chamber and periphery and the institute of the filter membrane 3
The side wall of the lower end wall and the reactor body 1 of stating partition wall 2 is fixedly connected, and the reactor body 1 is nearby provided with tank
5, the tank 5 in the siphon pipe 4 of reverse U shape with the filtrate chamber by connecting, and the siphon pipe 4 can be by the filtrate chamber
Water is automatically drawn into the tank 5, and the siphon pipe 4 stretches into the filtrate by the through hole on the side wall of reactor body 1
In chamber.In order to clear up, sludge is convenient, and the bottom of the reaction chamber sets door body of removing contamination able to turn on or off.Door body of removing contamination may be provided at institute
State on the side wall or bottom wall of reaction chamber bottom, when the sludge deposited in reaction chamber is more, door body of removing contamination can be opened, sludge is clear
Reason is gone out.
Further, the liquid level gauge for monitoring its interior liquid level height, the reactor are provided with the reactor body 1
Main body 1 is nearby provided with elevator pump 7, and the elevator pump 7 and coupled pipeline can send into waste water the reactor body 1
Interior, the elevator pump 7 and liquid level gauge are connected with controller signals, and the liquid level gauge can pass the liquid level information monitored
The controller is passed, the controller controls the keying of the elevator pump 7 according to the liquid level signal received.Reactor
Be preset with the first liquid level and the second liquid level in the reaction chamber of main body, the first liquid level is higher than the peak of siphon pipe, the second liquid level with
The entrance point liquid level of siphon pipe is equal in filtrate chamber, and the elevation information of the first liquid level and the second liquid level is used as the pre- of the controller
If information, when liquid level is higher than the first liquid level, controller control elevator pump is closed, and is stopped the feed flow into the reaction chamber, is worked as liquid
When position is less than the second liquid level, controller control elevator pump is opened, and starts the feed flow into the reaction chamber.
Further, the liquid level is calculated as ultrasonic liquid level meter 6.
Further, the top of the reactor body 1 is provided with mixer, and the agitating shaft 8 of the mixer stretches into described
In reaction chamber.
Further, the side that the filter membrane 3 is obliquely installed and its is of a relatively high is connected with the lower end wall of the partition wall 2.
Further, the siphon pipe 4 is stretched into the filtrate chamber by the through hole on the side wall of reactor body 1, institute
It is 15-50cm that through hole, which is stated, with the vertical distance at the open topped of reactor body 1.
Operation principle of the present utility model is:Waste water enters the reaction chamber of waste water treatment reactor, reaction by elevator pump 7
Waste water fast reaction in reaction chamber is handled in device, while effluent part, which begins through filter membrane 3, enters filtrate chamber, reaction chamber and filter
The liquid level of sap cavity rises, when the liquid level of filtrate chamber rises to the peak of submergence siphon pipe 4, because liquid level difference triggers siphon
Pipe, then siphon pipe can the spontaneous liquid by filtrate chamber suck in pond 5, the water inlet of elevator pump 7 is very fast, then the liquid level of reaction chamber
Continue to rise, (upper dotted line in Fig. 1, higher than the peak of the siphon pipe), controller control when it is higher than the first liquid level
Elevator pump 7 processed is stopped, water inlet end (flooding time is also key reaction time of the waste water in reaction chamber), now filtrate
The liquid level of chamber and reaction chamber is because the automatic ink-suction of siphon pipe is acted on and declines simultaneously, when liquid level drops to the second liquid level (in Fig. 1
Lower dotted line, it is equal with syphon mouth), siphonic process terminates, and controller control elevator pump is started working, pending useless
Water is again introduced into waste water treatment reactor under lifting pumping action, and so circulation is handled.
Preferred embodiment of the present utility model is the foregoing is only, it is all in this practicality not to limit the utility model
Within new spirit and principle, any modifications, equivalent substitutions and improvements made etc. should be included in guarantor of the present utility model
Within the scope of shield.
Claims (7)
1. a kind of hydrocone type waste water treatment reactor, it is characterised in that including reactor body (1), the reactor body (1)
Open topped, be provided with partition wall (2) and filter membrane (3) in the reactor body (1), the partition wall (2) and filter membrane (3) are by institute
State and be divided into two parts of reaction chamber and filtrate chamber inside reactor body (1), the upper end wall of the partition wall (2) is close to the reaction
The open topped of device main body (1), the lower end wall of the partition wall (2) is spaced apart with the bottom wall of the reactor body (1), it is described every
The side wall of the both sides end wall of wall (2) and the reactor body (1) is tightly connected, and the filter membrane (3) is located at the filtrate chamber
Bottom and the periphery of the filter membrane (3) and the side wall fixation of the lower end wall and the reactor body (1) of the partition wall (2) connect
Connect, the reactor body (1) is nearby provided with tank (5), the tank (5) is connected with the filtrate chamber by siphon pipe (4)
Logical, the water of the filtrate chamber can be automatically drawn into the tank (5) by the siphon pipe (4), and the siphon pipe (4) is by described
Through hole on the wall of reactor body (1) side is stretched into the filtrate chamber.
2. a kind of hydrocone type waste water treatment reactor according to claim 1, it is characterised in that the reactor body
(1) liquid level gauge for monitoring its interior liquid level height is provided with, the reactor body (1) is nearby provided with elevator pump (7),
The elevator pump (7) and coupled pipeline can send into waste water in the reactor body (1), the elevator pump (7) and
Liquid level gauge is connected with controller signals, and the liquid level information transmission monitored can be given the controller by the liquid level gauge,
The controller controls the keying of the elevator pump (7) according to the liquid level signal received.
3. a kind of hydrocone type waste water treatment reactor according to claim 2, it is characterised in that the liquid level is calculated as ultrasound
Liquid level gauge (6).
4. a kind of hydrocone type waste water treatment reactor according to claim 1, it is characterised in that the siphon pipe is in U
Font.
5. a kind of hydrocone type waste water treatment reactor according to claim 1, it is characterised in that the reactor body
(1) it is provided with mixer above, the agitating shaft (8) of the mixer and paddle thereon are stretched into the reaction chamber.
6. a kind of hydrocone type waste water treatment reactor according to any one of claim 1 to 5, it is characterised in that the filter
The side that film (3) is obliquely installed and its is of a relatively high is connected with the lower end wall of the partition wall (2).
7. a kind of hydrocone type waste water treatment reactor according to any one of claim 1 to 5, it is characterised in that described logical
Hole is 15-80cm with the vertical distance at the reactor body (1) open topped.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621469404.6U CN206328262U (en) | 2016-12-29 | 2016-12-29 | A kind of hydrocone type waste water treatment reactor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621469404.6U CN206328262U (en) | 2016-12-29 | 2016-12-29 | A kind of hydrocone type waste water treatment reactor |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206328262U true CN206328262U (en) | 2017-07-14 |
Family
ID=59292737
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621469404.6U Active CN206328262U (en) | 2016-12-29 | 2016-12-29 | A kind of hydrocone type waste water treatment reactor |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206328262U (en) |
-
2016
- 2016-12-29 CN CN201621469404.6U patent/CN206328262U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103523918B (en) | Air flow and machinery double-boosting internal circulation-type high suspension solid anaerobic digestion device | |
CN107459213A (en) | A kind of drum type brake integrated sewage treating apparatus | |
CN203976496U (en) | A kind of full-automatic oxygenation ecosystem fast for water treatment | |
CN217129949U (en) | Can carry air lift pump of mud | |
CN203613026U (en) | High suspended solid anaerobic digestion device | |
CN201376917Y (en) | Solid liquid flow mixing device of anaerobic reactor | |
CN206328262U (en) | A kind of hydrocone type waste water treatment reactor | |
CN101508486A (en) | Anaerobic reactor tridimensional flow agitating apparatus | |
CN207525100U (en) | A kind of drum type brake integrated sewage treating apparatus | |
CN203043640U (en) | Water-borne wood paint defoaming equipment capable of controlling automatically | |
CN205892758U (en) | Diamond recovery plant | |
CN109942162A (en) | A kind of device for excess sludge processing | |
CN113786650A (en) | Low-energy-consumption aeration high-efficiency reaction clarification tank | |
CN210085340U (en) | Heparin sodium precipitation liquid drainage device and heparin sodium precipitation device | |
CN203498159U (en) | Energy saving pulse type hydrolytic acidification reactor for sewage treatment | |
CN211141716U (en) | Combined air floatation device | |
CN206645885U (en) | Aerobic particle mud microorganism fungus kind cultivation reactor | |
CN209825080U (en) | Chocolate heat preservation jar of easy cleanness | |
CN113969230A (en) | Sand and scum removing and breaking device for anaerobic fermentation tank and sand and scum removing and breaking method | |
CN112499880A (en) | Biochemical pond sludge collection system of sewage treatment | |
CN215559290U (en) | Low-energy-consumption variable-speed upflow sludge-membrane mixing hydrolysis reactor | |
CN209957760U (en) | Kitchen full-mixing type anaerobic fermentation device | |
CN217627772U (en) | Constant water level self-suction type decanter based on CWSBR (continuous water sequencing batch reactor) process | |
CN206051649U (en) | A kind of novel flocculant chemicals dosing plant | |
CN212954404U (en) | Chlorobutane sewage continuous extraction purifier |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |