CN207685084U - sanitary wastewater processing system - Google Patents

sanitary wastewater processing system Download PDF

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Publication number
CN207685084U
CN207685084U CN201721624791.0U CN201721624791U CN207685084U CN 207685084 U CN207685084 U CN 207685084U CN 201721624791 U CN201721624791 U CN 201721624791U CN 207685084 U CN207685084 U CN 207685084U
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CN
China
Prior art keywords
biogas
sanitary wastewater
processing system
wastewater processing
reaction warehouse
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Expired - Fee Related
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CN201721624791.0U
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Chinese (zh)
Inventor
王立坤
杨坤
王晶
王莹
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Individual
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Individual
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Anticipated expiration legal-status Critical

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  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

The utility model provides a kind of sanitary wastewater processing system, including reaction warehouse, Water warfare storehouse, water storehouse, biogas collector, biogas generator, voltage conversion device and battery;Reaction warehouse, Water warfare storehouse and water storehouse are sequentially communicated from top to bottom;Reaction warehouse is equipped with sanitary wastewater entrance;And the top of reaction warehouse is connected to by exhaust pipe with biogas memory;Biogas memory is connected to the air intake of biogas generator;First output end of biogas generator is electrically connected with voltage conversion device;The DC voltage output end of voltage conversion device is connect with battery.The utility model can make the energy of the organic substance in sanitary wastewater be fully used.

Description

Sanitary wastewater processing system
Technical field
The utility model belongs to technical field of waste water processing more particularly to a kind of sanitary wastewater processing system.
Background technology
With the development of society, the use of water resource is more and more, and the pollution of water resource is also increasingly heavier, in daily life In work, we not only need to save water resource, more adequately to be utilized to used waste water, in the production of rural households In life, a large amount of debirs are will produce, these debirs can be directly discharged into river with dampening, not only waste in this way Water resource and organic substance, and environment is polluted, for this purpose, it is proposed that a kind of sanitary wastewater processing system for rural area.
Utility model content
In view of this, the utility model embodiment provides sanitary wastewater processing system.
The utility model embodiment provides a kind of sanitary wastewater processing system, including reaction warehouse, Water warfare storehouse, water storehouse, Biogas collector, biogas generator, voltage conversion device and battery;The reaction warehouse, the Water warfare storehouse and the water storehouse It is sequentially communicated from top to bottom;The reaction warehouse is equipped with sanitary wastewater entrance;And the top of the reaction warehouse passes through exhaust pipe and institute State the connection of biogas memory;The biogas memory is connected to the air intake of the biogas generator;The biogas generator First output end is electrically connected with the voltage conversion device;The DC voltage output end of the voltage conversion device and the battery Connection;
Wherein, the voltage conversion device includes AC-DC power conversion modules and DC-DC power source conversion module;The natural pond First output end of gas generator is connect with the input terminal of the AC-DC power conversion modules;The AC-DC power conversion modules Output end connect with the DC voltage output end of the DC-DC power source conversion module;
Wherein, the Water warfare storehouse includes the coarse filtration area being sequentially communicated, precipitation hydrolysis area, catalytic oxidation area and disinfection Area;The outlet of the sterile zones is connect with the water storehouse;The bottom in the coarse filtration area is equipped with filter screen, the coarse filtration area Top entry be connected to the reaction warehouse.
Wherein, the top of the top in the coarse filtration area and the precipitation hydrolysis area passes through exhaust pipe and the biogas respectively Memory is connected to.
Wherein, the side wall of the sterile zones is equipped with sterilizing unit, and the sterilizing unit is ultraviolet lamp group or ozone sterilization Device;The bottom of the sterile zones is equipped with thin filter layer;
One piece of baffle plate is at least installed, the baffle plate was equipped with the mouth of a river in the precipitation hydrolysis area;
The sanitary wastewater processing system further includes wind turbine;The catalytic oxidation area is equipped with filler, in the bottom end of filler position Aeration tube is installed, the aeration tube is connect with the wind turbine.
Wherein, the thin filter layer is made of filter cotton and activated carbon superposition.
Wherein, the sanitary wastewater processing system further includes soda acid detector, acid storage tank and alkaline storage tank;It is described The bottom of sterile zones is equipped with soda acid detector;It is respectively equipped with acid feeding port on the upside of the side wall of the reaction warehouse and alkalinity feeds intake Mouthful;And the interior intracavitary of the acid feeding port is equipped with the first solenoid valve;It is equipped with second in the inner cavity of the alkalinity feeding port Solenoid valve.
Wherein, it is connected to by pipeline between the reaction warehouse and the coarse filtration area;Third electromagnetism is equipped in the pipeline Valve.
Wherein, the sanitary wastewater processing system further includes controller;The controller respectively with the battery, the acid Alkali detector, the biogas generator, the wind turbine, first solenoid valve, the second solenoid valve and the third electromagnetism Valve is electrically connected.
Wherein, the biogas collector is equipped with biogas amount detecting device;The biogas amount detecting device and the controller Electrical connection.
Existing advantageous effect is the utility model embodiment compared with prior art:Using reaction warehouse and biogas collector Structure so that the organic substance in waste water is fully used, that is, utilize marsh gas power generation, and be powered for battery, and will storage The battery for having self generating electric energy is that the control system of its own is powered, and is not needed outside so as to which electric power is self-sufficient Portion's energy.
Description of the drawings
It is required in being described below to embodiment in order to illustrate more clearly of the technical scheme in the embodiment of the utility model Attached drawing to be used is briefly described, it should be apparent that, the accompanying drawings in the following description is only some realities of the utility model Example is applied, it for those of ordinary skill in the art, without having to pay creative labor, can also be attached according to these Figure obtains other attached drawings.
Fig. 1 is the structural schematic diagram for the sanitary wastewater processing system that the utility model embodiment provides.
Specific implementation mode
In being described below, for illustration and not for limitation, it is proposed that such as tool of particular system structure, technology etc Body details, to understand thoroughly the utility model embodiment.However, it will be clear to one skilled in the art that there is no these The utility model can also be realized in the other embodiments of detail.In other situations, omit to well-known system, The detailed description of apparatus, circuit and method, in case unnecessary details interferes the description of the utility model.
The utility model embodiment provides a kind of sanitary wastewater processing system comprising reaction warehouse 1, Water warfare storehouse, water storage Storehouse 3, biogas collector 4, biogas generator 5, voltage conversion device 6 and battery 7;The reaction warehouse, the Water warfare storehouse and institute Water storehouse 3 is stated to be sequentially communicated from top to bottom;The reaction warehouse 1 is equipped with sanitary wastewater entrance;And pass through at the top of the reaction warehouse Exhaust pipe is connected to the biogas collector;The biogas collector is connected to the air intake of biogas generator 5;The biogas hair First output end of motor 5 is electrically connected with the voltage conversion device;The DC voltage output end of the voltage conversion device with The battery 7 connects.
Wherein, the voltage conversion device includes AC-DC power conversion modules and DC-DC power source conversion module;The natural pond First output end of gas generator is connect with the input terminal of the AC-DC power conversion modules;The AC-DC power conversion modules Output end connect with the DC voltage output end of the DC-DC power source conversion module.Specifically, DC-DC power source converts Module can be booster type or voltage-dropping type, this depends on the required supply voltage of battery.DC-DC power source conversion module is for being Battery is powered.
Wherein, the Water warfare storehouse includes the coarse filtration area 21 being sequentially communicated, precipitation hydrolysis area 22,23 and of catalytic oxidation area Sterile zones 24;The outlet of the sterile zones is connect with the water storehouse;The bottom in the coarse filtration area is equipped with filter screen 211, institute The top entry for stating coarse filtration storehouse is connected to the reaction warehouse.
Wherein, the top of the top in the coarse filtration area and the precipitation hydrolysis area passes through exhaust pipe and the biogas respectively Collector is connected to.Coarse filtration area also will produce a small amount of biogas with precipitation hydrolysis area, therefore, more in order to acquire as far as possible Biogas, need its connecting with biogas collector.
Wherein, the side wall of the sterile zones is equipped with sterilizing unit 241, and the sterilizing unit 241 is ultraviolet lamp group or smelly Oxygen sterilizing unit;The bottom of the sterile zones 24 is equipped with thin filter layer 242;One piece of folding is at least installed in the precipitation hydrolysis area Plate washer is flowed, the baffle plate was equipped with the mouth of a river;
The sanitary wastewater processing system further includes wind turbine, and the catalytic oxidation area is equipped with filler, in the bottom end of filler position Aeration tube is installed, the aeration tube is connect with the wind turbine.
Precipitating the effect of hydrolysis area is:Make waste water that acidification reaction and precipitation be hydrolyzed.It generally suspends in sanitary sewage solid Body content is larger, can increase subsequent biochemical processing load if not removing and being directly entered biochemical section, sewage enters precipitation hydrolysis area Most of suspended solid, which is deposited, to be removed.Acidification reaction is hydrolyzed under the action of a large amount of hydrolytic bacteria, acidification bacterium, it will be difficult The larger molecular organics of degradation are decomposed into degradable small organic molecule, are easy to the processing of subsequent biochemical section.In precipitation hydrolysis area One piece of hydraulic barrier is inside further at least installed, hydraulic barrier was equipped with the mouth of a river, more when the quantity of hydraulic barrier is polylith Block hydraulic barrier is arranged in parallel, and the mouth of a river of crossing on polylith hydraulic barrier is arranged in the way of interlocking up and down, and sewage is made to precipitate It is flowed according to multi-way mode up and down reciprocatingly in hydrolysis area.The setting of hydraulic barrier increases sewage waterpower flow, reinforce precipitation and Hydrolysis effect.
The sewage handled through catalytic oxidation area is flowed into sterile zones by water passage.Above-mentioned filler is preferably filled out using compound Material.The effect in catalytic oxidation area is:To in waste water organic matter carry out oxygenolysis, compared to it is existing frequently with aerobic place Reason, with purification efficiency height, processing time is short, to intake organic loading variation adaptability relatively by force, need not carry out sludge reflux, There is no the advantages that sludge bulking problem, operational management facilitate simultaneously.
Wherein, the thin filter layer is made of filter cotton and activated carbon superposition.
Wherein, the sanitary wastewater processing system further includes soda acid detector 243, acid storage tank 244 and alkaline storing Tank 245;The bottom of the sterile zones is equipped with soda acid detector;Be respectively equipped on the upside of the side wall of the reaction warehouse acid feeding port and Alkaline feeding port;And the interior intracavitary of the acid feeding port is equipped with the first solenoid valve A;Pacify in the inner cavity of the alkalinity feeding port Equipped with second solenoid valve B.
Wherein, it is connected to by pipeline between the reaction warehouse and the coarse filtration area;Third electromagnetism is equipped in the pipeline Valve C.
Wherein, the sanitary wastewater processing system further includes controller;The controller respectively with the battery, the acid Alkali detector, the biogas generator, the wind turbine, first solenoid valve, the second solenoid valve and the third electromagnetism Valve is electrically connected.Wherein, the outer wall in reaction warehouse 1, Water warfare storehouse 2 and water storehouse 3 can be arranged in battery 7.
Wherein, the biogas collector is equipped with biogas amount detecting device;The biogas amount detecting device and the controller Electrical connection.
So that the organic substance in waste water is fully used using the structure of reaction warehouse and biogas collector, that is, utilizes biogas Power generation, and be powered for battery, and the battery for storing self generating electric energy is supplied for the control system of its own Electricity does not need extra power so as to which electric power is self-sufficient.It, can be in addition, by the setting in each area in Water warfare storehouse Good catharsis is played to waste water and acid-base value is adjusted, to make purified sanitary wastewater reach the standard of drinking water.
Embodiment described above is only to illustrate the technical solution of the utility model, rather than its limitations;Although with reference to before Embodiment is stated the utility model is described in detail, it will be understood by those of ordinary skill in the art that:It still can be with Technical scheme described in the above embodiments is modified or equivalent replacement of some of the technical features;And These modifications or replacements, the spirit for various embodiments of the utility model technical solution that it does not separate the essence of the corresponding technical solution And range, it should be included within the scope of protection of this utility model.

Claims (8)

1. a kind of sanitary wastewater processing system, which is characterized in that including reaction warehouse, Water warfare storehouse, water storehouse, biogas collector, Biogas generator, voltage conversion device and battery;The reaction warehouse, the Water warfare storehouse and the water storehouse are from top to bottom successively Connection;The reaction warehouse is equipped with sanitary wastewater entrance;And the top of the reaction warehouse is connected to by exhaust pipe with biogas memory; The biogas memory is connected to the air intake of the biogas generator;First output end of the biogas generator and the electricity Press conversion equipment electrical connection;The DC voltage output end of the voltage conversion device is connect with the battery;
Wherein, the voltage conversion device includes AC-DC power conversion modules and DC-DC power source conversion module;The biogas hair First output end of motor is connect with the input terminal of the AC-DC power conversion modules;The AC-DC power conversion modules it is defeated Outlet is connect with the DC voltage output end of the DC-DC power source conversion module;
Wherein, the Water warfare storehouse includes the coarse filtration area being sequentially communicated, precipitation hydrolysis area, catalytic oxidation area and sterile zones;Institute The outlet for stating sterile zones is connect with the water storehouse;The bottom in the coarse filtration area is equipped with filter screen, the top in the coarse filtration area Portion's entrance is connected to the reaction warehouse.
2. sanitary wastewater processing system as described in claim 1, which is characterized in that the top in the coarse filtration area and described heavy The top of shallow lake hydrolysis area is connected to by exhaust pipe with the biogas memory respectively.
3. sanitary wastewater processing system as claimed in claim 2, which is characterized in that the side wall of the sterile zones is equipped with sterilization and fills It sets, the sterilizing unit is ultraviolet lamp group or ozone-sterilizing device;The bottom of the sterile zones is equipped with thin filter layer;
One piece of baffle plate is at least installed, the baffle plate was equipped with the mouth of a river in the precipitation hydrolysis area;
The sanitary wastewater processing system further includes wind turbine;The catalytic oxidation area is equipped with filler, is set in the bottom position of filler There are aeration tube, the aeration tube to be connect with the wind turbine.
4. sanitary wastewater processing system as claimed in claim 3, which is characterized in that the thin filter layer is by filter cotton and activity Charcoal superposition is constituted.
5. sanitary wastewater processing system as claimed in claim 4, which is characterized in that the sanitary wastewater processing system further includes Soda acid detector, acid storage tank and alkaline storage tank;The bottom of the sterile zones is equipped with soda acid detector;The reaction warehouse Acid feeding port and alkaline feeding port are respectively equipped on the upside of side wall;And the interior intracavitary of the acid feeding port is equipped with the first electromagnetism Valve;Second solenoid valve is installed in the inner cavity of the alkalinity feeding port.
6. sanitary wastewater processing system as claimed in claim 5, which is characterized in that the reaction warehouse and the coarse filtration area it Between be connected to by pipeline;Third solenoid valve is equipped in the pipeline.
7. sanitary wastewater processing system as claimed in claim 6, which is characterized in that the sanitary wastewater processing system further includes Controller;The controller respectively with the battery, the soda acid detector, the biogas generator, the wind turbine, described One solenoid valve, the second solenoid valve and third solenoid valve electrical connection.
8. sanitary wastewater processing system as claimed in claim 7, which is characterized in that the biogas memory is examined equipped with methane quantity Survey device;The biogas amount detecting device is electrically connected with the controller.
CN201721624791.0U 2017-11-29 2017-11-29 sanitary wastewater processing system Expired - Fee Related CN207685084U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721624791.0U CN207685084U (en) 2017-11-29 2017-11-29 sanitary wastewater processing system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721624791.0U CN207685084U (en) 2017-11-29 2017-11-29 sanitary wastewater processing system

Publications (1)

Publication Number Publication Date
CN207685084U true CN207685084U (en) 2018-08-03

Family

ID=62999620

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721624791.0U Expired - Fee Related CN207685084U (en) 2017-11-29 2017-11-29 sanitary wastewater processing system

Country Status (1)

Country Link
CN (1) CN207685084U (en)

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Granted publication date: 20180803

Termination date: 20201129