CN208684463U - A kind of anti-blocking separation of solid and liquid dissolving - Google Patents
A kind of anti-blocking separation of solid and liquid dissolving Download PDFInfo
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- CN208684463U CN208684463U CN201821039229.6U CN201821039229U CN208684463U CN 208684463 U CN208684463 U CN 208684463U CN 201821039229 U CN201821039229 U CN 201821039229U CN 208684463 U CN208684463 U CN 208684463U
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- bulge
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Abstract
The utility model is that a kind of anti-blocking is separated by solid-liquid separation dissolving, including tank body and ejector, the tank body two sides are respectively equipped with water inlet and access hole, the top of the tank is respectively equipped with air inlet, pressure gauge connection and relief valve connection, the tank base is equipped with water outlet, the tank body top is equipped with liquidometer, it is characterized by: the ejector includes sequentially connected nozzle, suction chamber, diffuser pipe, straight tube and bend pipe, the bend pipe is down-set, the nozzle is connect with the water inlet, the suction chamber connects gas-guide tube, the straight tube bottom is equipped with support base, the support base is connect with the tank base;The top of the tank is equipped with bulge-structure, and the bulge-structure is equipped with backwash interface, and the backwash interface is arranged above the gas-guide tube.
Description
Technical field
The utility model relates to a kind of dissolved air flotation devices, especially disclose a kind of anti-blocking separation of solid and liquid dissolving, answer
For sewage treatment field.
Background technique
Dissolved air flotation process is using the characteristic of water different solubility at various pressures, under pressurization or condition of negative pressure
Make to generate microbubble in water, instead of the air-float technology of traditional bleed equipment Xiang Shuizhong bleed.The work of dissolved air flotation process is former
Manage as follows: effluent part circulation after processing flows into dissolving, under forced air state, air supersaturation dissolution, then
It is mixed in flotation tank with the waste water that flocculant is added, since pressure reduces, oversaturated air is released, and is formed a large amount of micro-
Minute bubbles come into full contact with the suspended matter in waste water, and are adsorbed in the suspended matter that wadding has collected in slow uphill process, make it
Big flocculation group of the density decline to not float floating to the water surface is then deposited to flotation tank bottom of pond and is periodically cleared up.
Existing dissolving mainly has vertical dissolving and two kinds of horizontal dissolving, and vertical dissolving: tank interior is equipped with
Filler and liquidometer control aerating by liquidometer, the purpose of molten gas are realized by filler effect, in order to guarantee molten gas effect,
Hydraulic detention time is generally 4~10 minutes, and the molten gas of vertical dissolving is relatively inefficient, and bubble is big, after mixing wastewater with air
Water outlet is easy to scatter, and causes molten gas ineffective, will cause in the case where influent turbidity is big or suspended matter long-term accumulation
Tank interior blocking, molten gas efficiency reduce.
Horizontal dissolving: ejector and liquidometer is arranged in tank interior, controls aerating by liquidometer, is inhaled by ejector
The purpose of molten gas is realized in gas effect, and hydraulic detention time is 2~4 minutes, and molten gas efficiency is relatively high, but general ejector
The molten gas mode of level-one is all used, the air of sucking cannot reach maximum molten gas ratio, and the air not dissolved in can be released, be made
It is easy to scatter in water outlet at the waste of energy consumption, and after mixing wastewater with air, it is ineffective to will cause molten gas.One is run in system
Section the time after, the gas-guide tube of ejector can generate obstruction, once blocking, need to disassemble entire dissolving, then into
The internal great purge of row, but in the sewage disposal system of continuous operation, this maintenance be it is very fatal, can seriously affect entire
The operation of system.
Summary of the invention
Utility model aims to solve the defects of the prior art, provide a kind of anti-blocking separation of solid and liquid dissolving,
Its structure is simple, manufacturing cost is low, molten gas effect is good, can prevent air guide pipe choking, by ejector exit add to
Mixing wastewater with air liquid after the molten gas of level-one is introduced into the water surface hereinafter, forming the molten gas of second level, greatly increased by the bend pipe of lower setting
Gas-water ratio, improves mixing wastewater with air degree, to increase molten gas effect;The utility model will be arranged at the top of gas-guide tube on tank body top
In the bulge-structure in portion, the probability that gas-guide tube blocks is greatly reduced, once block, it can be by being arranged in air guide
Backwash interface above pipe is rinsed gas-guide tube, removes obstruction, has ensured the continuous and steady operation of system, reduced maintenance
The cost of overhaul.
The utility model is realized in this way: a kind of anti-blocking separation of solid and liquid dissolving, including tank body and ejector, it is described
Tank body two sides are respectively equipped with water inlet and access hole, and the top of the tank is respectively equipped with air inlet, pressure gauge connection and safety valve
Interface, the tank base are equipped with water outlet, and the tank body top is equipped with liquidometer, it is characterised in that: the ejector includes
Sequentially connected nozzle, suction chamber, diffuser pipe, straight tube and bend pipe, the bend pipe is down-set, the nozzle and the water inlet
Connection, the suction chamber connect gas-guide tube, and the straight tube bottom is equipped with support base, and the support base and the tank base connect
It connects;The top of the tank is equipped with bulge-structure, and the bulge-structure is equipped with backwash interface, and the backwash interface is arranged described
Above gas-guide tube.
The top of the gas-guide tube is arranged in the bulge-structure.The bend pipe is U-tube.
The beneficial effects of the utility model are: the utility model structure is simple, manufacturing cost is low, molten gas effect is good, can be with
Air guide pipe choking is prevented, by adding down-set bend pipe in ejector exit, the air water after the molten gas of level-one is mixed
It closes liquid and introduces the water surface hereinafter, forming the molten gas of second level, considerably increase gas-water ratio, improve mixing wastewater with air degree, to increase molten
Gas effect.The utility model will be arranged in the bulge-structure of top of the tank at the top of gas-guide tube, greatly reduce gas-guide tube
The probability of obstruction can be rinsed gas-guide tube by the way that the backwash interface above gas-guide tube is arranged in once blocking, only
It needs one minute or so that obstruction can be removed, has ensured the continuous and steady operation of system, reduced Maintenance and Repair cost, very
It is suitably applied in large-scale sewage disposal system.The support base of the utility model prevents in dissolving for consolidating ejector
Portion's turbulent flow impacts ejector, guarantees molten gas effect.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
In figure: 1, tank body;2, ejector;3, water inlet;4, access hole;5, air inlet;6, pressure gauge connection; 7,
Relief valve connection;8, water outlet;9, liquidometer;10, nozzle;11, suction chamber;12, diffuser pipe;13, straight tube;14, curved
Pipe;15, gas-guide tube;16, support base;17, bulge-structure;18, backwash interface.
Specific embodiment
The utility model is described in further detail with reference to the accompanying drawing.
With reference to the accompanying drawings 1, the utility model is that a kind of anti-blocking is separated by solid-liquid separation dissolving, including tank body 1 and ejector 2, institute
It states 1 two sides of tank body and is respectively equipped with water inlet 3 and access hole 4, air inlet 5, pressure gauge connection 6 are respectively equipped at the top of the tank body 1
With relief valve connection 7,1 bottom of tank body is equipped with water outlet 8, and 1 top of tank body is equipped with liquidometer 9;The ejector 2 wraps
Sequentially connected nozzle 10, suction chamber 11, diffuser pipe 12, straight tube 13 and bend pipe 14 are included, the bend pipe 14 is down-set, the spray
Mouth 10 is connect with the water inlet 3, and the suction chamber 11 connects gas-guide tube 15, and 13 bottom of straight tube is equipped with support base 16, institute
Support base 16 is stated to connect with 1 bottom of tank body;It is equipped with bulge-structure 17 at the top of the tank body 1, is set on the bulge-structure 17
There is backwash interface 18, the backwash interface 18 is arranged above the gas-guide tube 15.
The top of the gas-guide tube 15 is arranged in the bulge-structure 17.The bend pipe 14 is U-tube.
The course of work of the utility model is as follows: liquid by high-pressure pump from water inlet 3 enter ejector 2 in, liquid with
High speed is sprayed from nozzle 10, can form vacuum in suction chamber 11 when swiftly flowing liquid passes through suction chamber 11, suction chamber 11 is logical
The air that gas-guide tube 15 sucks 1 top of tank body is crossed, mixing wastewater with air liquid is introduced by liquid level or less by bend pipe 14 after mixing wastewater with air
Secondary mixing is carried out, the molten gas of second level is formed, considerably increases gas-water ratio, improve mixing wastewater with air degree, increase molten gas effect, so
Flotation tank is flowed by water outlet 8 by the mixing wastewater with air liquid after the molten gas of second level.
The top of the gas-guide tube 15 is arranged in the bulge-structure 17 at 1 top of tank body, greatly reduces the hair of gas-guide tube 15
The probability of raw obstruction can open backwash interface 18 and be rinsed to gas-guide tube 15 once blocking, it is only necessary to one minute left side
The right side can remove obstruction, ensure the continuous and steady operation of system, reduce Maintenance and Repair cost, be highly suitable to be applied for big
In the sewage disposal system of type.The support base 16 prevents dissolving internal turbulence from making to ejector 2 for consolidating ejector 2
At influence, guarantee molten gas effect.
As the air in tank body 1 is constantly soluble in water and is discharged, the air in tank body 1 is reduced, and liquid level rises, and works as tank
When liquid level in body 1 is higher than the liquid level that liquidometer 9 is set, liquidometer 9 issues signal, carries out tonifying Qi, and compressed air passes through air inlet
Mouth 5 enters tank body 1, makes pressure increase in tank body 1, causes to reduce into water, water outlet increases, reduces liquid level, be down to and set when liquid level
When determining liquid level, liquidometer 9 issues signal, stops tonifying Qi.
The utility model is equipped with safety valve and pressure gauge by relief valve connection 7 and pressure gauge connection 6, when in tank body 1
Pressure be more than pressure gauge setting rated pressure when, safety valve, which automatically opens, to be released stress, and the utility model can be with time control
The size of pressure in tank body 1 processed, it is ensured that the safety of equipment operation and the safety of staff.
Above-described embodiment is merely to illustrate the utility model rather than limitation the scope of the utility model, it should be appreciated that
After the content for having read the utility model elaboration, those skilled in the art can make different form but effect to the utility model
Identical various changes or modification, these equivalent forms modify the range for equally falling within the limited protection of the claim of this application book
Within.
Claims (3)
1. a kind of anti-blocking is separated by solid-liquid separation dissolving, including tank body and ejector, the tank body two sides be respectively equipped with water inlet and
Access hole, the top of the tank are respectively equipped with air inlet, pressure gauge connection and relief valve connection, and the tank base is equipped with water outlet
Mouthful, the tank body top is equipped with liquidometer, it is characterised in that: the ejector includes sequentially connected nozzle, suction chamber, diffusion
Pipe, straight tube and bend pipe, the bend pipe is down-set, and the nozzle is connect with the water inlet, and the suction chamber connects gas-guide tube,
The straight tube bottom is equipped with support base, and the support base is connect with the tank base;The top of the tank is equipped with bulge-structure,
The bulge-structure is equipped with backwash interface, and the backwash interface is arranged above the gas-guide tube.
2. a kind of anti-blocking is separated by solid-liquid separation dissolving according to claim 1, it is characterised in that: the top of the gas-guide tube
Portion is arranged in the bulge-structure.
3. a kind of anti-blocking is separated by solid-liquid separation dissolving according to claim 1, it is characterised in that: the bend pipe is U-shaped
Pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201821039229.6U CN208684463U (en) | 2018-06-29 | 2018-06-29 | A kind of anti-blocking separation of solid and liquid dissolving |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201821039229.6U CN208684463U (en) | 2018-06-29 | 2018-06-29 | A kind of anti-blocking separation of solid and liquid dissolving |
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CN208684463U true CN208684463U (en) | 2019-04-02 |
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CN201821039229.6U Active CN208684463U (en) | 2018-06-29 | 2018-06-29 | A kind of anti-blocking separation of solid and liquid dissolving |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114737931A (en) * | 2022-03-23 | 2022-07-12 | 四川宏华石油设备有限公司 | Natural gas desanding system and desanding method by utilizing pressure and flow velocity regulation |
-
2018
- 2018-06-29 CN CN201821039229.6U patent/CN208684463U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114737931A (en) * | 2022-03-23 | 2022-07-12 | 四川宏华石油设备有限公司 | Natural gas desanding system and desanding method by utilizing pressure and flow velocity regulation |
CN114737931B (en) * | 2022-03-23 | 2023-12-15 | 四川宏华石油设备有限公司 | Natural gas sand removal system and method using pressure and flow rate to adjust |
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