CN205710206U - A kind of integral type sewage processing means - Google Patents
A kind of integral type sewage processing means Download PDFInfo
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- CN205710206U CN205710206U CN201620587772.4U CN201620587772U CN205710206U CN 205710206 U CN205710206 U CN 205710206U CN 201620587772 U CN201620587772 U CN 201620587772U CN 205710206 U CN205710206 U CN 205710206U
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- zoneofoxidation
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- processing means
- integral type
- type sewage
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- 239000010865 sewage Substances 0.000 title claims abstract description 65
- 239000010802 sludge Substances 0.000 claims abstract description 46
- 238000005189 flocculation Methods 0.000 claims abstract description 28
- 230000016615 flocculation Effects 0.000 claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 238000009833 condensation Methods 0.000 claims abstract description 23
- 230000005494 condensation Effects 0.000 claims abstract description 23
- 238000005276 aerator Methods 0.000 claims abstract description 21
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000002893 slag Substances 0.000 claims abstract description 7
- 238000007790 scraping Methods 0.000 claims abstract description 6
- 238000001556 precipitation Methods 0.000 claims description 11
- 230000018044 dehydration Effects 0.000 claims description 5
- 238000006297 dehydration reaction Methods 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 34
- 238000003911 water pollution Methods 0.000 abstract description 8
- 239000007789 gas Substances 0.000 description 15
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 11
- 238000007254 oxidation reaction Methods 0.000 description 11
- 239000003344 environmental pollutant Substances 0.000 description 8
- 230000003647 oxidation Effects 0.000 description 8
- 231100000719 pollutant Toxicity 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 5
- 239000000377 silicon dioxide Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 238000005273 aeration Methods 0.000 description 3
- 238000005345 coagulation Methods 0.000 description 3
- 230000015271 coagulation Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000005553 drilling Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000006385 ozonation reaction Methods 0.000 description 2
- AHLWZBVXSWOPPL-RGYGYFBISA-N 20-deoxy-20-oxophorbol 12-myristate 13-acetate Chemical compound C([C@]1(O)C(=O)C(C)=C[C@H]1[C@@]1(O)[C@H](C)[C@H]2OC(=O)CCCCCCCCCCCCC)C(C=O)=C[C@H]1[C@H]1[C@]2(OC(C)=O)C1(C)C AHLWZBVXSWOPPL-RGYGYFBISA-N 0.000 description 1
- 241001602688 Pama Species 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 1
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000003403 water pollutant Substances 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Physical Water Treatments (AREA)
Abstract
The utility model embodiment discloses a kind of integral type sewage processing means, including: homogeneous district, condensation region, flocculation zone, settling zone, sludge sump and zoneofoxidation, homogeneous district is connected with condensation region top, bottom, homogeneous district is provided with water inlet, bottom is connected with demulsifier grug feeding jar, condensation region is connected with bottom flocculation zone, it is internally provided with the first paddle, bottom is connected with the first flocculant grug feeding jar, flocculation zone top is connected with settling zone top, flocculation zone is internally provided with the second paddle, bottom is connected with the second flocculant grug feeding jar, settling zone top is connected with zoneofoxidation top, top is provided with Slag Scraping Device, bottom is provided with sludge outlet, sludge sump is positioned at below the gap of settling zone and zoneofoxidation, it is provided with aerator bottom zoneofoxidation, aerator is connected with ozone generator, bottom is provided with delivery port.This integral type sewage processing means floor space is little, is moved easily, is especially suitable for the process of sudden water pollution event.
Description
Technical field
The utility model relates to water treatment field, particularly to a kind of integral type sewage processing means.
Background technology
With economic fast development, China's etesian sudden water pollution event gets more and more, and sudden water is dirty
It is of a great variety that dye event typically has sewage, the complicated feature of pollutant component.
In the existing treatment technology for the pollution of accident water, commonly used combined treatment technology, for example, by electrically
Floating process, Fenton (Fenton) reaction, neutralize flocculation, microfiltration membranes is processed, ultraviolet light reaction, ozone and activated carbon are processed, at absorption
Manage a series of process technique composition, the sewage containing orgnic compound pollution and bio-toxicity pollution can be processed.Also have some to process
Technique uses ozone as the source of the gas of airfloat equipment, by air supporting oxidation pond, Slag Scraping Device, sedimentation basin, settling vessel, clear water reserviors, automatically controlled
System and machine room composition processing equipment.
But, owing to technique is tediously long in above-mentioned process technique, process complex steps, cause processing equipment huge, exist and account for
The shortcoming of the big and mobile inconvenience of ground area, for processing, sudden water pollution event is very inconvenient.
Utility model content
The purpose of the utility model embodiment is to provide a kind of integral type sewage processing means, is used for solving existing process
The problem of the big and mobile inconvenience of the floor space that sudden water pollution event device exists.Technical scheme is as follows:
A kind of integral type sewage processing means, comprising: homogeneous district, condensation region, flocculation zone, settling zone, sludge sump and oxidation
District, wherein,
Described homogeneous district is connected with described condensation region top, and bottom, described homogeneous district is provided with water inlet, described homogeneous
It is connected by pipeline with demulsifier grug feeding jar bottom district；
Described condensation region is connected bottom described flocculation zone, and described condensation region is internally provided with the first paddle, bottom
It is connected by pipeline with the first flocculant grug feeding jar；
Described flocculation zone top is connected by overfall with described settling zone top, and described flocculation zone is internally provided with
Two paddles, bottom is connected by pipeline with the second flocculant grug feeding jar；
Described settling zone top is connected by pipeline with described zoneofoxidation top, and described settling zone top is provided with scrapes slag
Machine, bottom is provided with sludge outlet；
Described sludge sump is positioned at below the gap of described settling zone and described zoneofoxidation, and described sludge outlet is positioned at described
The top of sludge sump；
Being provided with aerator bottom described zoneofoxidation, described aerator is connected with ozone generator by pipeline, described oxygen
Hua Qu top is provided with exhaust outlet, and bottom is provided with delivery port.
In a kind of embodiment of the present utility model, described zoneofoxidation includes: the first sub-zoneofoxidation, the second sub-zoneofoxidation
And the 3rd sub-zoneofoxidation, wherein,
Described first sub-zoneofoxidation is connected with described second sub-zoneofoxidation bottom, described second sub-zoneofoxidation and described the
Three sub-zoneofoxidation tops are connected, and are respectively provided with bottom described first sub-zoneofoxidation, the second sub-zoneofoxidation and the 3rd sub-zoneofoxidation
Having the first aerator, the second aerator and the 3rd aerator, top is provided with exhaust outlet, described first sub-zoneofoxidation top with
Described settling zone top is connected by pipeline, and described 3rd sub-zoneofoxidation bottom is provided with delivery port.
In a kind of embodiment of the present utility model, described settling zone is internally provided with precipitation inclined plate.
In a kind of embodiment of the present utility model, described flocculation zone top is provided with downflow weir, and described downflow weir sets
It is placed in the lower section of described overfall.
In a kind of embodiment of the present utility model, described water inlet is connected with water inlet pipe, and described water inlet pipe is arranged
There is intake pump.
In a kind of embodiment of the present utility model, described integral type sewage processing means also includes: sludge dewatering fills
Putting, described sludge dehydration device is connected by pipeline with described sludge sump, and this pipeline is provided with sludge pump.
In a kind of embodiment of the present utility model, described integral type sewage processing means also includes: vent gas treatment fills
Putting, described exhaust gas processing device is connected by pipeline with described exhaust outlet.
In a kind of embodiment of the present utility model, described integral type sewage processing means is positioned at container.
In a kind of embodiment of the present utility model, described container is placed on truck.
The utility model embodiment provides a kind of integral type sewage processing means, by homogeneous district, condensation region, flocculation zone,
Settling zone and zoneofoxidation composition, form the processing means of integral type, and the water inlet from bottom, homogeneous district for the sewage enters, and sequentially passes through
Homogeneous district, condensation region, flocculation zone, settling zone and zoneofoxidation, the delivery port from zoneofoxidation bottom for the water outlet after process is discharged, it is achieved
Process to sewage.In the technical solution of the utility model, coagulation is combined with ozonation technology, simple to operate, it is processed into
This is low, can be used for the fields such as oil field, gas drilling and advanced treatment of wastewater, this integral type sewage processing means floor space
Little, it is moved easily, be especially suitable for the process of sudden water pollution event.
Brief description
In order to be illustrated more clearly that the utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or the accompanying drawing of required use is briefly described in description of the prior art, it should be apparent that, the accompanying drawing in describing below is only
It is some embodiments of the present utility model, for those of ordinary skill in the art, in the premise not paying creative work
Under, other accompanying drawing can also be obtained according to these accompanying drawings.
The structural representation of a kind of integrated sewage treating apparatus that Fig. 1 is provided by the utility model embodiment；
The structural representation of the another kind of integrated sewage treating apparatus that Fig. 2 is provided by the utility model embodiment.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of making creative work
The every other embodiment being obtained, broadly falls into the scope of the utility model protection.
The utility model provides a kind of integral type sewage processing means, as it is shown in figure 1, this device may include that homogeneous
District the 01st, condensation region the 02nd, flocculation zone the 03rd, settling zone the 04th, sludge sump 05 and zoneofoxidation 06.
Concrete, homogeneous district 01 is connected with condensation region 02 top, and bottom, homogeneous district 01 is provided with water inlet 012, homogeneous
It is connected by pipeline with demulsifier grug feeding jar 011 bottom district 01；Condensation region 02 is connected bottom flocculation zone 03, in condensation region 02
Portion is provided with the first paddle 021, and bottom is connected by pipeline with the first flocculant grug feeding jar 022；Flocculation zone 03 top with heavy
Top, shallow lake district 04 is connected by overfall 033, and flocculation zone 03 is internally provided with the second paddle 031, bottom and the second flocculation
Agent grug feeding jar 032 is connected by pipeline；Settling zone 04 top is connected by pipeline 11 with zoneofoxidation 06 top, settling zone 04 top
Being provided with Slag Scraping Device 041, bottom is provided with sludge outlet 042；Sludge sump 05 is positioned between described settling zone 04 and zoneofoxidation 06
Below gap, and sludge outlet 042 is positioned at the top of sludge sump 05；It is provided with aerator 060, aerator 060 bottom zoneofoxidation 06
Being connected with ozone generator 07 by pipeline, zoneofoxidation 06 top is provided with exhaust outlet, and bottom is provided with delivery port 067.
In actual application, water inlet 012 can be connected with water inlet pipe, and water inlet pipe can arrange intake pump 08.By breaking
The medicament that emulsion grug feeding jar 011 adds in homogeneous district 01 can be: the one in demulsifier, gel breaker, inorganic acids material
Or it is several.Sewage is entered homogeneous district 01 from water inlet 012 by the castering action of intake pump 08, with the medicament in homogeneous district 01
Mixing, eliminates the emulsion in sewage, it is simple to the carrying out of subsequent treatment under pharmacy effect.
After liquid level in homogeneous district 01 reach a certain height, sewage enters in condensation region 02 under gravity.By
The first flocculant that one flocculant grug feeding jar 022 adds in condensation region 02 can be: aluminum sulfate, aluminium polychloride, polymerised sulphur
One or more in acid ferro-aluminum, bodied ferric sulfate.In entrance condensation region 02, sewage is at the stirring action of the first paddle 021
Under, it is sufficiently mixed with the first flocculant, make the less flco that the pollutant in sewage is formed.
Sewage after processing through condensation region 02 enters in flocculation zone 03.By the second flocculant grug feeding jar 032 to flocculation zone
The second flocculant adding in 03 can be: PAMC, PAMA, non-ionic polyacrylamide
And one or more in diatomite.Sewage in entrance flocculation zone 03 is under the stirring action of the second paddle 031, with second
Flocculant is sufficiently mixed, and makes the less flco in sewage form bigger flco, beneficially follow-up precipitation and oxidation processes.
It should be noted that above-mentioned paddle and grug feeding jar can be respectively adopted existing paddle and grug feeding jar, ability
Field technique personnel can select according to factors such as sewage qualities, does not specifically limit at this.
Sewage after flocculation zone 03 is processed is entered by overfall 033 and carries out precipitation process, sewage in settling zone 04
In scum silica frost rise to sewage surface, be removed through the process of Slag Scraping Device.Flco sinks down into formation mud bottom settling zone 04
Discharge from sludge outlet 042.
In actual application, Slag Scraping Device 041 can be through settling zone 04 and zoneofoxidation 06 from the scum silica frost that sewage surface strikes off
Gap falls in sludge sump 05, and the mud discharged from sludge outlet 042 also can enter sludge sump 05.It should be noted that
Sludge outlet 042 can be connected with sludge sump 05 by pipeline, and sludge outlet 042 also can be not attached to sludge sump 05, works as dirt
When mud outlet 042 can be connected with sludge sump 05 by pipeline, mud can be entered in sludge sump 05 by pipeline；Work as mud
When outlet 042 and sludge sump 05 are not attached to, owing to sludge outlet 042 is positioned at the top of sludge sump 05, therefore mud can be direct
Falling in sludge sump 05, this is all rational.
Sewage after precipitation process is entered by pipeline 11 and carries out oxidation processes in zoneofoxidation 06, and ozone generator 07 produces
Raw ozone enters in zoneofoxidation 06 through piping, ozone and the pollutant generation oxidation reaction in sewage, and then by sewage
Pollutant removal.Rising to the tail gas above sewage to pass through outside exhaust outlet discharger, delivery port is passed through in the water outlet after process
067 discharges.
It should be noted that above-mentioned aerator can use existing any aerator, for example, it may be aeration plate etc.,
As long as the purpose of aeration can be reached to carry out in zoneofoxidation, can be by those skilled in the art according to need when actually used
The amount wanting ozone selects, and does not specifically limit at this.Above-mentioned ozone generator also can use existing any ozone
Generator, does not specifically limit at this.
In a kind of preferred embodiment of the present utility model, as in figure 2 it is shown, zoneofoxidation 06 can include three son oxidations
District, is respectively as follows: the first sub-zoneofoxidation the 061st, the second sub-zoneofoxidation 062 and the 3rd sub-zoneofoxidation 063, wherein, the first sub-zoneofoxidation
061 is connected with the second sub-zoneofoxidation 062 bottom, and the second sub-zoneofoxidation 062 is connected with the 3rd sub-zoneofoxidation 063 top, the
It is respectively arranged with the first aerator the 064th, bottom one sub-zoneofoxidation the 061st, the second sub-zoneofoxidation 062 and the 3rd sub-zoneofoxidation 063
Two aerators 065 and the 3rd aerator 066, top is provided with exhaust outlet (not shown), the first sub-zoneofoxidation 061 top
Being connected by pipeline 11 with settling zone 04 top, the 3rd sub-zoneofoxidation 063 bottom is provided with delivery port 067.
The setting of three sub-zoneofoxidations can increase the effective depth of oxidation reaction, and sewage sequentially passes through the first sub-zoneofoxidation
061st, the oxidation processes of the second sub-zoneofoxidation 062 and the 3rd sub-zoneofoxidation 063, makes oxidation reaction more abundant, pollutants removal rate
Higher.
In actual application, the pollutant levels of the sewage in entrance the first sub-zoneofoxidation 061 are the highest, therefore the first son oxidation
It is easier on the first aerator 064 bottom district 061 to assemble pollutant, affect aeration effect.First sub-zoneofoxidation 061 and
The set-up mode that two sub-zoneofoxidation 062 bottoms are connected can well solve this problem, and sewage is from the first sub-zoneofoxidation 061
The pipeline 11 on top enters, and flows into the second sub-zoneofoxidation 062 from bottom, can play souring to the first aerator 064, will
The pollutant assembled on first aerator 064 is taken away, and then carries out further oxidation processes to it.
In a kind of preferred embodiment of the present utility model, precipitation inclined plate 043 can be set in the middle part of settling zone 04 to add
The precipitation of the dirty water pollutant of speed, improves treatment effeciency.This precipitation inclined plate 043 can use existing precipitation inclined plate, for example, and can
To be awave precipitation inclined plate, can reach to accelerate the purpose of precipitation, specifically not limit at this.
In a kind of preferred embodiment of the present utility model, downflow weir 034 can be set on flocculation zone 03 top, specifically
, downflow weir 034 can be arranged at the lower section of overfall 033, and downflow weir 034 can make sewage uniformly overflow from overfall 033,
Can play simultaneously and slow down water velocity, stablize the effect of its flowing, be more conducive to the process of this integral type sewage processing means
The stability of journey.
In a kind of preferred embodiment of the present utility model, above-mentioned integral type sewage processing means can also include: dirty
Mud is dehydrated device 09, and sludge dehydration device 09 can be connected by pipeline with sludge sump 05, and this pipeline can arrange sludge pump
091, by sludge pump 091, the mud in sludge sump 05 and scum silica frost are delivered to, in sludge dehydration device 09, carry out processed,
Make the separation of solid and liquid in mud and scum silica frost, facilitate the follow-up process to mud and scum silica frost.
In order to prevent the ozone in tail gas from polluting air, above-mentioned integral type sewage processing means can also include:
Exhaust gas processing device 10, concrete, exhaust gas processing device 10 can be connected with exhaust outlet by pipeline.First sub-zoneofoxidation is the 061st,
The ozone not reacted in second sub-zoneofoxidation 062 and the 3rd sub-zoneofoxidation 063 can rise to above sewage, passes through exhaust outlet
Entering in exhaust gas processing device 10, after processing through exhaust gas processing device 10, ozone is destroyed, and tail gas is carried out after reaching discharge standard
Discharge, it is to avoid air is polluted.Wherein, above-mentioned exhaust gas processing device 10 can use existing tail gas breaking plant, energy
Enough reach to remove the purpose of ozone in tail gas, be not specifically limited at this.
Processing to sudden water is pollution-free for convenience of mobile above-mentioned integral type sewage processing means, the utility model is real
Execute in example and above-mentioned integral type sewage processing means can also be placed in container, when reality is applied, can be at container
On offer wastewater inlet and outlet of sewer, wastewater inlet for injecting sewage in integral type sewage processing means, outlet of sewer
Discharge from integral type sewage processing means for the water outlet after processing.
In order to increase the mobility of above-mentioned integral type sewage processing means further, above-mentioned container can also be laid
On truck, form vehicular integral type sewage processing means, when sudden water pollution event occurs, truck can be driven
To water contamination accident spot, can be more quick, more easily sudden water pollution event is processed.
Visible, the utility model embodiment provides a kind of integral type sewage processing means, by homogeneous district, condensation region, wadding
Coagulation zone, settling zone and zoneofoxidation composition, form the processing means of integral type, and the water inlet from bottom, homogeneous district for the sewage enters, and depends on
Secondary through homogeneous district, condensation region, flocculation zone, settling zone and zoneofoxidation, the delivery port row from zoneofoxidation bottom for the water outlet after process
Go out, it is achieved the process to sewage.In the technical solution of the utility model, coagulation is combined with ozonation technology, simple to operate,
Processing cost is low, can be used for the fields such as oil field, gas drilling and advanced treatment of wastewater, and this integral type sewage processing means is taken up an area
Area is little, is moved easily, and is especially suitable for the process of sudden water pollution event.
It should be noted that herein, the relational terms of such as first and second or the like is used merely to a reality
Body or operation separate with another entity or operating space, and deposit between not necessarily requiring or imply these entities or operating
Relation or order in any this reality.And, term " includes ", "comprising" or its any other variant are intended to
Comprising of nonexcludability, so that include that the process of a series of key element, method, article or equipment not only include that those are wanted
Element, but also include other key elements being not expressly set out, or also include for this process, method, article or equipment
Intrinsic key element.In the case of there is no more restriction, the key element being limited by statement " including ... ", it is not excluded that
Including the process of described key element, method, article or equipment there is also other identical element.
Each embodiment in this specification all uses related mode to describe, identical similar portion between each embodiment
Dividing and seeing mutually, what each embodiment stressed is the difference with other embodiments.
The foregoing is only preferred embodiment of the present utility model, be not intended to limit protection model of the present utility model
Enclose.All any modification, equivalent substitution and improvement etc. made within spirit of the present utility model and principle, are all contained in this reality
With in novel protection domain.
Claims (9)
1. an integral type sewage processing means, it is characterised in that include: homogeneous district (01), condensation region (02), flocculation zone
(03), settling zone (04), sludge sump (05) and zoneofoxidation (06), wherein,
Described homogeneous district (01) is connected with described condensation region (02) top, and described homogeneous district (01) bottom is provided with water inlet
(012), described homogeneous district (01) bottom is connected by pipeline with demulsifier grug feeding jar (011)；
Described condensation region (02) is connected with described flocculation zone (03) bottom, and described condensation region (02) is internally provided with the first stirring
Oar (021), bottom is connected by pipeline with the first flocculant grug feeding jar (022)；
Described flocculation zone (03) top is connected by overfall (033) with described settling zone (04) top, described flocculation zone
(03) being internally provided with the second paddle (031), bottom is connected by pipeline with the second flocculant grug feeding jar (032)；
Described settling zone (04) top is connected by pipeline (11) with described zoneofoxidation (06) top, described settling zone (04) top
Being provided with Slag Scraping Device (041), bottom is provided with sludge outlet (042)；
Described sludge sump (05) is positioned at below the gap of described settling zone (04) and described zoneofoxidation (06), and described sludge outlet
(042) it is positioned at the top of described sludge sump (05)；
Described zoneofoxidation (06) bottom is provided with aerator (060), and described aerator (060) passes through pipeline and ozone generator
(07) being connected, described zoneofoxidation (06) top is provided with exhaust outlet, and bottom is provided with delivery port (067).
2. integral type sewage processing means as claimed in claim 1, it is characterised in that described zoneofoxidation (06) includes: first
Sub-zoneofoxidation (061), the second sub-zoneofoxidation (062) and the 3rd sub-zoneofoxidation (063), wherein,
Described first sub-zoneofoxidation (061) is connected with described second sub-zoneofoxidation (062) bottom, described second sub-zoneofoxidation
(062) it is connected with described 3rd sub-zoneofoxidation (063) top, described first sub-zoneofoxidation (061), the second sub-zoneofoxidation
(062) it and is respectively arranged with the first aerator (064), the second aerator (065) and the 3rd bottom the 3rd sub-zoneofoxidation (063) to expose
Gas device (066), top is provided with exhaust outlet, and described first sub-zoneofoxidation (061) top leads to described settling zone (04) top
Piping (11) is connected, and described 3rd sub-zoneofoxidation (063) bottom is provided with delivery port (067).
3. integral type sewage processing means as claimed in claim 1, it is characterised in that described settling zone (04) is internal to be arranged
There is precipitation inclined plate (043).
4. integral type sewage processing means as claimed in claim 1, it is characterised in that described flocculation zone (03) top is provided with
Downflow weir (034), described downflow weir (034) is arranged at the lower section of described overfall (033).
5. integral type sewage processing means as claimed in claim 1, it is characterised in that described water inlet (012) be connected with into
Water pipe, described water inlet pipe is provided with intake pump (08).
6. integral type sewage processing means as claimed in claim 1, it is characterised in that also include: sludge dehydration device (09),
Described sludge dehydration device (09) is connected by pipeline with described sludge sump (05), and this pipeline is provided with sludge pump (091).
7. the integral type sewage processing means as described in any one of claim 1-6, it is characterised in that also include: vent gas treatment
Device (10), described exhaust gas processing device (10) is connected by pipeline with described exhaust outlet.
8. integral type sewage processing means as claimed in claim 7, it is characterised in that described integral type sewage processing means position
In container.
9. integral type sewage processing means as claimed in claim 8, it is characterised in that described container is placed on truck.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201620587772.4U CN205710206U (en) | 2016-06-16 | 2016-06-16 | A kind of integral type sewage processing means |
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| CN201620587772.4U CN205710206U (en) | 2016-06-16 | 2016-06-16 | A kind of integral type sewage processing means |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107619101A (en) * | 2017-10-26 | 2018-01-23 | 杨晓艳 | A kind of device and technique that sewage drainage is further handled using tide |
| CN108503095A (en) * | 2018-06-23 | 2018-09-07 | 安徽拓谷物联科技有限公司 | Domestic sewage in rural areas integrated equipment for wastewater treatment |
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| CN117735749A (en) * | 2023-12-05 | 2024-03-22 | 山东省生态环境规划研究院 | A solar powered decentralized sewage treatment system |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107619101A (en) * | 2017-10-26 | 2018-01-23 | 杨晓艳 | A kind of device and technique that sewage drainage is further handled using tide |
| CN108503095A (en) * | 2018-06-23 | 2018-09-07 | 安徽拓谷物联科技有限公司 | Domestic sewage in rural areas integrated equipment for wastewater treatment |
| CN109467213A (en) * | 2018-11-13 | 2019-03-15 | 佛山市雅洁源科技股份有限公司 | A kind of emulsifying liquid waste water processing equipment and its treatment process |
| CN109467213B (en) * | 2018-11-13 | 2021-10-26 | 佛山市雅洁源科技股份有限公司 | Emulsion wastewater treatment equipment and treatment process thereof |
| CN117735749A (en) * | 2023-12-05 | 2024-03-22 | 山东省生态环境规划研究院 | A solar powered decentralized sewage treatment system |
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