CN208038243U - A kind of sewage integrated treatment equipment - Google Patents
A kind of sewage integrated treatment equipment Download PDFInfo
- Publication number
- CN208038243U CN208038243U CN201721911081.6U CN201721911081U CN208038243U CN 208038243 U CN208038243 U CN 208038243U CN 201721911081 U CN201721911081 U CN 201721911081U CN 208038243 U CN208038243 U CN 208038243U
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- Prior art keywords
- room
- grid
- conduit
- chamber
- mud chamber
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000010865 sewage Substances 0.000 title claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 61
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 53
- 230000003647 oxidation Effects 0.000 claims abstract description 51
- 230000003197 catalytic effect Effects 0.000 claims abstract description 26
- 230000007062 hydrolysis Effects 0.000 claims abstract description 22
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 22
- 230000020477 pH reduction Effects 0.000 claims abstract description 22
- 239000000945 filler Substances 0.000 claims description 12
- 239000010802 sludge Substances 0.000 claims description 9
- 238000005276 aerator Methods 0.000 claims description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 230000001590 oxidative effect Effects 0.000 claims description 2
- 238000000034 method Methods 0.000 description 8
- 238000001914 filtration Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 238000005273 aeration Methods 0.000 description 2
- 241001148470 aerobic bacillus Species 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 102000010637 Aquaporins Human genes 0.000 description 1
- 108010063290 Aquaporins Proteins 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model proposes a kind of sewage integrated treatment equipments, including:Apparatus casing, grid room is sequentially installed in apparatus casing from left to right, hydrolysis acidification room, level-one catalytic oxidation room, two-stage biological contact oxidation room, mud chamber, clean water chamber, wherein, the inside left of grid room is equipped with intake tunnel, water inlet pipe connects intake tunnel, it is installed with grid on the right side of intake tunnel, it is connected by the first conduit between grid room and hydrolysis acidification room, it is connected by the second conduit between hydrolysis acidification room and level-one catalytic oxidation room, it is connected by third conduit between level-one catalytic oxidation room and two-stage biological contact oxidation room, it is connected by the 4th conduit between two-stage biological contact oxidation room and mud chamber, inclined tube is installed inside mud chamber, it is connected by the 5th conduit between mud chamber and clean water chamber, outlet pipe is connected at the top of clean water chamber.The utility model is simple in structure, at low cost, and water treatment efficiency is good.
Description
Technical field
The utility model is related to technical field of sewage, more particularly to a kind of sewage integrated treatment equipment.
Background technology
There are many sewage treatment process used both at home and abroad, wherein it is broadly divided into two kinds of activated sludge process and biofilm, I
Common common aeration, oxidation ditch process, A/B methods, A/O it is owned by France in the former, biological rotating disk, contact oxidation method belong to the latter.
Integrated sewage treating apparatus is the equipment that a heavy pond, I, II grades of contact-oxidation pools, secondary settling tank, sludge-tank are concentrated one, and
Blast aeration is carried out in I, II grades of contact-oxidation pools, so that contact oxidation method and activated sludge process is effectively combined, simultaneously
The shortcomings that having the advantages of the two, and overcoming the two, makes sewage disposal level further increase.
Utility model content
In view of the above-mentioned problems, the purpose of this utility model is that propose a kind of sewage integrated treatment equipment, it is simple in structure,
It is at low cost, and water treatment efficiency is good.
Technical solution is used by the utility model solves above-mentioned technical problem:A kind of sewage integrated treatment equipment,
Including:Apparatus casing is sequentially installed with grid room, hydrolysis acidification room, level-one catalytic oxidation in the apparatus casing from left to right
Room, two-stage biological contact oxidation room, mud chamber, clean water chamber, between each room independently of each other, and each room is closing chamber body, wherein described
The inside left of grid room is equipped with intake tunnel, and the water inlet pipe connects the intake tunnel, fixed on the right side of the intake tunnel
Grid is installed, the lower end of the grid room is connected with the first blow-off pipe, leads between the grid room and the hydrolysis acidification room
The connection of the first conduit is crossed, one end of first conduit connects the top of the grid room, and the other end connects the hydrolysis acidification
The bottom of room is connected between the hydrolysis acidification room and level-one catalytic oxidation room by the second conduit, second conduit
One end connect the top of the hydrolysis acidification room, the other end connects the bottom of level-one catalytic oxidation room, and the level-one connects
It touches and is connected by third conduit between oxidizing chamber and the two-stage biological contact oxidation room, one end connection described one of the third conduit
The top of grade catalytic oxidation room, the other end connect the bottom of the two-stage biological contact oxidation room, the two-stage biological contact oxidation room and institute
It states and is connected by the 4th conduit between mud chamber, one end of the 4th conduit connects the top of the two-stage biological contact oxidation room,
The other end connects the side of the mud chamber, and the bottom of the mud chamber is connected with the second blow-off pipe, pacifies inside the mud chamber
It equipped with inclined tube, is connected by the 5th conduit between the mud chamber and the clean water chamber, one end of the 5th conduit connects institute
The top of mud chamber is stated, the other end connects the bottom of the clean water chamber, is connected with outlet pipe at the top of the clean water chamber, and described one
It is separately installed with aerator, level-one catalytic oxidation room and two at the top of grade catalytic oxidation room and the two-stage biological contact oxidation room
The inside of grade catalytic oxidation room is separately installed with filler.
Further, the lower end of the grid is flushed with the lower end of the intake tunnel, the lower end of the grid and the lattice
First settling zone is formed on the bottom of grid room, and the first clear water zone is formed between the upper end and the top of grid room of the grid.
Further, the second settling zone, institute are formed between the bottom of the inclined tube of the mud chamber and the bottom of the mud chamber
It is taper to state the second settling zone, and the second clear water zone is formed between the top of the inclined tube and the top of the mud chamber.
Further, the water inlet pipe, which is located in grid room, is equipped with the first strainer in the port of one end, the 4th conduit
Second strainer is installed in the port of one end in mud chamber.
Further, it is separately installed with sludge pump in first settling zone and second settling zone.
Further, the filler uses novel elastic 3-D filler.
The utility model has the advantage of:The top and bottom of grid indoor grille section and grid room formed the first clear water zone and
First settling zone, water enter the indoor bottom of grid from water inlet pipe by intake tunnel, and water is overflow from bottom to top, is carried out by grid
Preliminary filtering, filters out bigger floating material, and floating material is discharged from the first blow-off pipe, and the clear water after filtering out enters the first clear water
Area enters hydrolysis acidification pool by the first conduit, and grid room uses this structure, can increase the filter area of water, filter out more
Add clean;It is connected from top to bottom by conduit between each room, water is gone out at the top of each room, is entered from bottom, has been not only able to
Effect prevents water from flowing back, and cost is greatly saved, and is all to introduce the water into it using power-equipments such as suction pumps in the prior art
His chamber body, the utility model utilize the overflow of water, other chamber bodies are flowed to by the gravity of water itself;Indoor location inclined tube is precipitated,
Using tube settling principle, filter area is considerably increased, enhances filter effect, and mud chamber inclined tube bottom and mud chamber bottom
Portion forms the second settling zone, can store a certain amount of sludge, eliminate the work that a sludge-tank is separately provided in the prior art
Cost is greatly saved in sequence;One end port of water inlet pipe and the 4th conduit is separately installed with the first strainer and the second strainer, can
It effectively prevent sludge to enter water inlet pipe and the 4th conduit.
Description of the drawings
It, below will be right in order to illustrate more clearly of specific embodiment of the present invention or technical solution in the prior art
Specific implementation mode or attached drawing needed to be used in the description of the prior art are briefly described, it should be apparent that, it is described below
In attached drawing be that some embodiments of the utility model are not paying creativeness for those of ordinary skill in the art
Under the premise of labour, other drawings may also be obtained based on these drawings.
Fig. 1 is a kind of structural schematic diagram of sewage integrated treatment equipment of the utility model.
Wherein:1, apparatus casing;2, grid room;3, hydrolysis acidification room;4, level-one catalytic oxidation room;5, Secondary contact oxygen
Change room;6, mud chamber;7, clean water chamber;8, water inlet pipe;9, the first conduit;10, the second conduit;11, third conduit;12, it the 4th leads
Pipe;13, inclined tube;14, the 5th conduit;15, outlet pipe;16, intake tunnel;17, grid;18, the first blow-off pipe;19, the first filter
Net;20, the second strainer;21, the second blow-off pipe;22, aerator;23, filler.
Specific implementation mode
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing, it is clear that described
Embodiment is the utility model a part of the embodiment, instead of all the embodiments.Based on the embodiments of the present invention, originally
The every other embodiment that field those of ordinary skill is obtained without making creative work, belongs to this practicality
Novel protected range.
It is in the description of the present invention, it should be noted that term "center", "upper", "lower", "left", "right", " perpendicular
Directly ", the orientation or positional relationship of the instructions such as "horizontal", "inner", "outside" is to be based on the orientation or positional relationship shown in the drawings, and is only
The utility model and simplifying describes for ease of description, do not indicate or imply the indicated device or element must have it is specific
Orientation, with specific azimuth configuration and operation, therefore should not be understood as limiting the present invention.In addition, term " the
One ", " second ", " third " are used for description purposes only, and are not understood to indicate or imply relative importance.
As shown in Figure 1, a kind of sewage integrated treatment equipment, including:Apparatus casing 1, the interior left side certainly of the apparatus casing 1 is extremely
The right side is sequentially installed with 17 Room 2 of grid, hydrolysis acidification room 3, level-one catalytic oxidation room 4, two-stage biological contact oxidation room 5, mud chamber 6, clear
Hydroecium 7, between each room independently of each other, and each room is closing chamber body, wherein the inside left of 17 Room 2 of the grid be equipped with into
Aquaporin 16, the water inlet pipe 8 connect the intake tunnel 16, and 16 right side of the intake tunnel is installed with grid 17, institute
The lower end for stating 17 Room 2 of grid is connected with the first blow-off pipe 18, passes through between 17 Room 2 of the grid and the hydrolysis acidification room 3
One conduit 9 connects, and one end of first conduit 9 connects the top of 17 Room 2 of the grid, and the other end connects the hydrolysis acidification
The bottom of room 3, hydrolysis acidification room 3 are exactly that the waste water in water is carried out certain anaerobism and is sent out to being pre-processed before sewage disposal
Ferment improves the biodegradability of sewage, this is can to directly affect the sewage in later stage to step important before sewage disposal
The efficiency of processing and processing time can improve the efficiency of sewage disposal and reduce consumption to the greatest extent.
It is connected by the second conduit 10 between the hydrolysis acidification room 3 and level-one catalytic oxidation room 4, described second leads
One end of pipe 10 connects the top of the hydrolysis acidification room 3, and the other end connects the bottom of level-one catalytic oxidation room 4, described
It is connected by third conduit 11 between level-one catalytic oxidation room 4 and the two-stage biological contact oxidation room 5, the one of the third conduit 11
End connects the top of level-one catalytic oxidation room 4, and the other end connects the bottom of the two-stage biological contact oxidation room 5, using two-stage
Catalytic oxidation room, the mean residence time of catalytic oxidation was at 6 hours or more, and most of organic matter obtains degradation and net herein in water
Change, aerobic bacteria is carrier with filler 23, is foodstuff using the organic matter in sewage, the organic matter in sewage is resolved into inorganic salts
Class, to reach purification purpose.It is connected by the 4th conduit 12 between the two-stage biological contact oxidation room 5 and the mud chamber 6, institute
The one end for stating the 4th conduit 12 connects the top of the two-stage biological contact oxidation room 5, and the other end connects the side of the mud chamber 6,
The bottom of the mud chamber 6 is connected with the second blow-off pipe 21, is equipped with inclined tube 13 inside the mud chamber 6, the mud chamber 6 with
It being connected by the 5th conduit 14 between the clean water chamber 7, one end of the 5th conduit 14 connects the top of the mud chamber 6,
The other end connects the bottom of the clean water chamber 7, and the top of the clean water chamber 7 is connected with outlet pipe 15, the level-one catalytic oxidation
The top of room 4 and the two-stage biological contact oxidation room 5 is separately installed with aerator 22, and sufficient oxygen is provided for aerobic bacteria.It is described
The inside of level-one catalytic oxidation room 4 and two-stage biological contact oxidation room 5 is separately installed with filler 23.
Further, the lower end of the grid 17 is flushed with the lower end of the intake tunnel 16, the lower end of the grid 17 with
First settling zone is formed on the bottom of 17 Room 2 of the grid, and the is formed between the top of 17 Room 2 of upper end and grid of the grid 17
One clear water zone.
Further, the second precipitation is formed between the bottom and the bottom of the mud chamber 6 of the inclined tube 13 of the mud chamber 6
Area, second settling zone are taper, and the second clear water is formed between the top of the inclined tube 13 and the top of the mud chamber 6
Area.
Further, the water inlet pipe 8, which is located in 17 Room 2 of grid, is equipped with the first strainer 19 in the port of one end, and described
Four conduits 12, which are located in mud chamber 6, is equipped with the second strainer 20 in the port of one end.
Further, it is separately installed with sludge pump in first settling zone and second settling zone.
Further, the filler 23 is using novel elastic 3-D filler 23.23 surface area ratio of filler is big, service life
It is length, easy to be filmed, corrosion-resistant.
A kind of sewage integrated treatment equipment of the utility model, the top and bottom shape of grid indoor grille section and grid room
At the first clear water zone and the first settling zone, water enters the indoor bottom of grid from water inlet pipe by intake tunnel, and water is from bottom to top
It is unrestrained, it is tentatively filtered by grid, filters out bigger floating material, floating material is discharged from the first blow-off pipe, clear after filtering out
Water enters the first clear water zone, enters hydrolysis acidification pool by the first conduit, grid room uses this structure, can increase the mistake of water
Filtering surface accumulates, and filters out more clean;Connected from top to bottom by conduit between each room, water is gone out at the top of each room, from bottom into
It enters, be not only able to that water is effectively prevent to flow back, and cost is greatly saved, is set using power such as suction pumps in the prior art
Standby to introduce the water into other chamber bodies, the utility model utilizes the overflow of water, other chamber bodies is flowed to by the gravity of water itself;Mud chamber
Interior installation inclined tube considerably increases filter area using tube settling principle, enhances filter effect, and mud chamber inclined tube bottom
Portion forms the second settling zone with mud chamber bottom, can store a certain amount of sludge, eliminate and one is separately provided in the prior art
The process of a sludge-tank, is greatly saved cost;One end port of water inlet pipe and the 4th conduit be separately installed with the first strainer and
Second strainer can effectively prevent sludge to enter water inlet pipe and the 4th conduit.
Finally it should be noted that:The above various embodiments is only to illustrate the technical solution of the utility model, rather than limits it
System;Although the utility model has been described in detail with reference to the foregoing embodiments, those skilled in the art should
Understand:It still can be with technical scheme described in the above embodiments is modified, either to which part or whole
Technical characteristic carries out equivalent replacement;And these modifications or replacements, this practicality that it does not separate the essence of the corresponding technical solution are new
The range of each embodiment technical solution of type.
Claims (6)
1. a kind of sewage integrated treatment equipment, which is characterized in that including:Apparatus casing, in the apparatus casing from left to right
It is sequentially installed with grid room, hydrolysis acidification room, level-one catalytic oxidation room, two-stage biological contact oxidation room, mud chamber, clean water chamber, each room
Between independently of each other, and each room is closing chamber body, wherein the inside left of the grid room is equipped with intake tunnel, water inlet pipe
The intake tunnel is connected, is installed with grid on the right side of the intake tunnel, the lower end of the grid room is connected with first row
Dirt pipe, is connected between the grid room and the hydrolysis acidification room by the first conduit, and one end of first conduit connects institute
The top of grid room is stated, the other end connects the bottom of the hydrolysis acidification room, and the hydrolysis acidification room contacts oxygen with the level-one
Change is connected between room by the second conduit, and one end of second conduit connects the top of the hydrolysis acidification room, and the other end connects
The bottom of level-one catalytic oxidation room is connect, passes through third between level-one catalytic oxidation room and the two-stage biological contact oxidation room
Conduit connects, and one end of the third conduit connects the top of level-one catalytic oxidation room, and the other end connects the two level and connects
The bottom for touching oxidizing chamber is connected between the two-stage biological contact oxidation room and the mud chamber by the 4th conduit, and the described 4th leads
One end of pipe connects the top of the two-stage biological contact oxidation room, and the other end connects the side of the mud chamber, the mud chamber
Bottom is connected with the second blow-off pipe, and inclined tube is equipped with inside the mud chamber, is passed through between the mud chamber and the clean water chamber
5th conduit connects, and one end of the 5th conduit connects the top of the mud chamber, and the other end connects the bottom of the clean water chamber
Portion is connected with outlet pipe, the top of level-one catalytic oxidation room and the two-stage biological contact oxidation room at the top of the clean water chamber
It is separately installed with aerator, the inside of level-one catalytic oxidation room and two-stage biological contact oxidation room is separately installed with filler.
2. a kind of sewage integrated treatment equipment according to claim 1, which is characterized in that the lower end of the grid and institute
The lower end for stating intake tunnel flushes, and the first settling zone, the grid are formed on the lower end of the grid and the bottom of the grid room
Upper end and the top of grid room between form the first clear water zone.
3. a kind of sewage integrated treatment equipment according to claim 2, which is characterized in that the inclined tube of the mud chamber
The second settling zone is formed between bottom and the bottom of the mud chamber, second settling zone is taper, the top of the inclined tube
The second clear water zone is formed between the top of the mud chamber.
4. a kind of sewage integrated treatment equipment according to claim 1, which is characterized in that the water inlet pipe is located at grid
First strainer is installed, the 4th conduit is located in mud chamber is equipped with second in the port of one end in the port of indoor one end
Strainer.
5. a kind of sewage integrated treatment equipment according to claim 3, which is characterized in that first settling zone and institute
It states in the second settling zone and is separately installed with sludge pump.
6. a kind of sewage integrated treatment equipment according to claim 1, which is characterized in that the filler uses novel bullet
Property 3-D filler.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721911081.6U CN208038243U (en) | 2017-12-30 | 2017-12-30 | A kind of sewage integrated treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721911081.6U CN208038243U (en) | 2017-12-30 | 2017-12-30 | A kind of sewage integrated treatment equipment |
Publications (1)
Publication Number | Publication Date |
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CN208038243U true CN208038243U (en) | 2018-11-02 |
Family
ID=63956522
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201721911081.6U Expired - Fee Related CN208038243U (en) | 2017-12-30 | 2017-12-30 | A kind of sewage integrated treatment equipment |
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CN (1) | CN208038243U (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109626735A (en) * | 2018-12-29 | 2019-04-16 | 江苏金梓环境科技股份有限公司 | Precipitation Separation Technique for distributing small apartment sewage treatment unit |
CN109621543A (en) * | 2018-12-29 | 2019-04-16 | 江苏金梓环境科技股份有限公司 | Precipitation separation device and its integrated multielement sewage disposal system |
CN109621499A (en) * | 2018-12-29 | 2019-04-16 | 江苏金梓环境科技股份有限公司 | Disengagement zone uses the integrated multielement sewage disposal system of inclined plate separation |
-
2017
- 2017-12-30 CN CN201721911081.6U patent/CN208038243U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109626735A (en) * | 2018-12-29 | 2019-04-16 | 江苏金梓环境科技股份有限公司 | Precipitation Separation Technique for distributing small apartment sewage treatment unit |
CN109621543A (en) * | 2018-12-29 | 2019-04-16 | 江苏金梓环境科技股份有限公司 | Precipitation separation device and its integrated multielement sewage disposal system |
CN109621499A (en) * | 2018-12-29 | 2019-04-16 | 江苏金梓环境科技股份有限公司 | Disengagement zone uses the integrated multielement sewage disposal system of inclined plate separation |
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Legal Events
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181102 |
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CF01 | Termination of patent right due to non-payment of annual fee |