CN108793643A - Integrated treating device and processing method are given birth in sewage disposal materialization - Google Patents

Integrated treating device and processing method are given birth in sewage disposal materialization Download PDF

Info

Publication number
CN108793643A
CN108793643A CN201810986053.3A CN201810986053A CN108793643A CN 108793643 A CN108793643 A CN 108793643A CN 201810986053 A CN201810986053 A CN 201810986053A CN 108793643 A CN108793643 A CN 108793643A
Authority
CN
China
Prior art keywords
area
sewage
areas
precipitation
air
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201810986053.3A
Other languages
Chinese (zh)
Inventor
何旭红
周国峰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiangsu State Dna Releaxed Circular Dna Border Science And Technology Development Co Ltd
Original Assignee
Jiangsu State Dna Releaxed Circular Dna Border Science And Technology Development Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Jiangsu State Dna Releaxed Circular Dna Border Science And Technology Development Co Ltd filed Critical Jiangsu State Dna Releaxed Circular Dna Border Science And Technology Development Co Ltd
Priority to CN201810986053.3A priority Critical patent/CN108793643A/en
Publication of CN108793643A publication Critical patent/CN108793643A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/24Treatment of water, waste water, or sewage by flotation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/40Devices for separating or removing fatty or oily substances or similar floating material
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/54Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
    • C02F1/56Macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F2001/007Processes including a sedimentation step
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Physical Water Treatments (AREA)

Abstract

The invention belongs to technical field of sewage, specifically, it is related to a kind of sewage disposal materialization life integrated treating device and processing method, the equipment is in turn divided into demulsification area, oil removal settling zone, the areas PAC, the areas PAM, release area, precipitation-air-flotation area, middle area, hydrolysis acidification area, catalytic oxidation area, sludge settling area and discharge recovery area by partition board along drainage flow direction, and wherein oil removal settling zone and precipitation-air-flotation area shares a floating oil collecting area.The integrated height of integrated treating device is given birth in sewage disposal materialization provided by the invention, it is ingenious in design, oil removal settling zone and precipitation-air-flotation area share a floating oil collecting area and a mud-scraping apparatus, by two scraper plates are installed on mud-scraping apparatus with achieve the purpose that oil removal settling zone and precipitation-air-flotation area synchronize deoil, the advantages of with saving energy consumption, reducing cost;In addition the treatment process of the equipment is comprehensive, and it is splendid to have gathered machinery, chemistry and micro-organism treatment process, treatment effect.

Description

Integrated treating device and processing method are given birth in sewage disposal materialization
Technical field
The invention belongs to technical field of sewage, and integrated processing dress is given birth in particular to a kind of sewage disposal materialization It sets and processing method.
Background technology
With the continuous development of catering industry, the influence of the discharge of sewage from catering business to ambient enviroment is increasingly severe.It is each Relevant rules and regulations are all worked out to determine the qualified discharge of sewage from catering business in place.Since sewage from catering business is mainly by grease group At additionally needing to be respectively completed to oil using different equipment mostly when to sewage disposal including abundance of food residue Separation, the processing of water and residue.So so that sewage disposal device quantity is more, energy consumption is larger, and technique is cumbersome, and handles Effect is sometimes and unsatisfactory.
Invention content
To solve drawbacks described above of the existing technology, the present invention provides a kind of sewage disposal materializations to give birth to integrated processing dress It sets and processing method.
Technical scheme is as follows:
The present invention provides a kind of sewage disposal materializations to give birth to integrated treating device, including dissolving, above-mentioned sewage disposal object Inside metaplasia integrated treating device demulsification area, oil removal settling zone, the areas PAC, PAM are in turn divided into along drainage flow direction by partition board Area, release area, precipitation-air-flotation area, middle area, hydrolysis acidification area, catalytic oxidation area, sludge settling area and discharge recovery area, wherein Oil removal settling zone and precipitation-air-flotation area share a floating oil collecting area.
Demulsification divide into through the first overflow port be connected to first demulsification area and second demulsification area, first demulsification area equipped with into The mouth of a river, the second demulsification area are connected to the second overflow port of oil removal settling zone.
The first outlet pipe is equipped in the middle part of oil removal settling zone, the oil removal settling zone inner wall positioned at the first outlet pipe top is equipped with Above-mentioned floating oil collecting area.
The areas PAC are connected to by the first outlet pipe with oil removal settling zone.
The areas PAM are connected to by third overflow port with the areas PAC.
Release area is connected to by the 4th overflow port with the areas PAM.
Precipitation-air-flotation area is connected to by the 5th overflow port with release area, and the second outlet pipe is equipped in the middle part of precipitation-air-flotation area, Precipitation-air-flotation area inner wall positioned at the second outlet pipe top is equipped with above-mentioned floating oil collecting area.
Middle area is connected to by the second outlet pipe with precipitation-air-flotation area.
Hydrolysis acidification area is connected to by the first overflow pipe with middle area, and is equipped with and is exposed successively from the bottom to top in hydrolysis acidification area Device of air and hydrolysis filling.
Catalytic oxidation area is connected to by the second overflow pipe with hydrolysis acidification area, and is set successively from the bottom to top in catalytic oxidation area There are aerator and catalytic oxidation filler.
Sludge settling area is connected to by central draft tube with catalytic oxidation area, and central draft tube lower end is equipped with lower cone.
Discharge recovery area is connected to by downflow weir with sludge settling area, and is discharged and be additionally provided with refluxing opening on recovery area.
In addition, being additionally provided with mud-scraping apparatus on partition board between oil removal settling zone and precipitation-air-flotation area.
In embodiment provided by the invention, above-mentioned mud-scraping apparatus includes that mud scraper and interval are mounted on mud scraper crawler belt Two scraper plates, two scraper plates are respectively used to scrape the oil slick in oil removal settling zone and precipitation-air-flotation area in sewage level to floating In oil collection area.
In embodiment provided by the invention, above-mentioned aerator is perforated pipe.
In embodiment provided by the invention, band paddle is mounted in above-mentioned first demulsification area, the areas PAC and the areas PAM The blender of piece.
In embodiment provided by the invention, it is above-mentioned first demulsification area, second demulsification area, the areas PAC, the areas PAM, release area and The bottom of discharge recovery area is equipped with drain.
In embodiment provided by the invention, above-mentioned oil removal settling zone, floating oil collecting area, precipitation-air-flotation area, intermediate pool and The bottom in sludge settling area is equipped with mud discharging mouth.
The present invention also provides the processing methods that integrated treating device is given birth in a kind of sewage disposal materialization, include the following steps:
A, the sewage from catering business come out from dissolving is added after demulsifier and flows into the first demulsification area, warp by water inlet thereto So that the grease in sewage from catering business is detached, then by the first overflow port stream after agitating device is sufficiently stirred in first demulsification area Enter progress residue precipitation in the second demulsification area, the sewage from catering business after slagging-off includes mainly grease two parts, then by the second overflow port Oil removal settling zone is flowed into, sewage from catering business upper layer oil slick in oil removal settling zone is scraped to floating oil collecting area, completed to meal by mud-scraping apparatus The first of drink sewage deoils;
B, the less sewage from catering business of oil-containing flows into the areas PAC along the first outlet pipe in the middle part of oil removal settling zone, stirs and fills in the area Under the action of setting, sewage from catering business and flocculant PAC fully react, and the sludge in sewage from catering business starts to flocculate for the first time, and flocculation is blocking Sludge settling to the areas PAC bottom;
C, the sewage from catering business after mud is gone then to flow into the areas PAM by third overflow port for the first time, in the work of area's agitating device Under, sewage from catering business and flocculant PAM fully react, and the sludge in sewage from catering business starts secondary flocculation, caseous sludge of wadding a quilt with cotton It is precipitated to the areas PAM bottom;
D, secondary to go the sewage from catering business after mud to be flowed into release area by the 4th overflow port to carry out first natural sedimentation, go The sludge removed is precipitated to release area bottom again, and the sewage for discharging area top then flows into precipitation-air-flotation by the 5th overflow port Area, mud-scraping apparatus scrape sewage upper layer oil slick in precipitation-air-flotation area to floating oil collecting area, and precipitation-air-flotation area middle part oil-containing is less Sewage from catering business then flows into middle area by the second outlet pipe and carries out secondary natural sedimentation, by sludge settling to middle area bottom Portion;
E, the sewage from catering business in middle area flows into hydrolysis acidification area bottom by the first overflow pipe, and the areas Xian Jinggai perforated pipe exposes Then gas covers the hydrolysis filling in the middle part of the area and flows into catalytic oxidation area bottom from the second overflow pipe again;
F, it after flowing into the same areas the Xian Jinggai perforated pipe aerating regulation of sewage from catering business in catalytic oxidation area, then covers again in the area The catalytic oxidation filler in portion, then flowed into after the downflow weir of side-walls and the central draft tube of area's centre above the area successively Sludge settling area bottom, under the buffering of the lower cone of central draft tube bottom so that the sludge in sewage from catering business precipitates again In the area bottom;
G, the sewage from catering business in sludge settling area flows into discharge recovery area through discharging the downflow weir of side-walls above recovery area, Sewage from catering business in the area is detected, is arranged sewage from catering business by the drain of the area bottom if it meets discharge standard Fall, if it does not meet the water inlet connection on refluxing opening and the first demulsification area in the areas discharge standard Ze Jianggai, repeats above-mentioned step Rapid A to F, until sewage from catering business reaches discharge standard;
H, it after the useless discharge of food and drink, through the first demulsification area, the second demulsification area, the areas PAC, the areas PAM, release area and drains back into Receive area bottom drain, oil removal settling zone, floating oil collecting area, precipitation-air-flotation area, intermediate pool and sludge settling area bottom row Mud mouth respectively cleans each area.
In embodiment provided by the invention, above-mentioned mud-scraping apparatus includes that mud scraper and interval are mounted in above-mentioned steps A Two scraper plates on mud scraper crawler belt, two scraper plates are respectively used to will be in oil removal settling zone and precipitation-air-flotation area in sewage level Oil slick is scraped into floating oil collecting area.
Advantageous effect:The integrated height of integrated treating device, ingenious in design, oil removal are given birth in sewage disposal materialization provided by the invention Settling zone and precipitation-air-flotation area share a floating oil collecting area and a mud-scraping apparatus, are scraped by installing two on mud-scraping apparatus Plate with achieve the purpose that oil removal settling zone and precipitation-air-flotation area synchronize deoil, have and save energy consumption, reduce cost the advantages of; In addition the treatment process of the equipment is comprehensive, and it is splendid to have gathered machinery, chemistry and micro-organism treatment process, treatment effect.
Description of the drawings
It, below will be to required use in embodiment in order to illustrate more clearly of the technical solution of embodiment of the present invention Attached drawing be briefly described, it should be understood that the following drawings illustrates only certain embodiments of the present invention, therefore is not to be seen as It is the restriction to range, it for those of ordinary skill in the art, without creative efforts, can be with root Other relevant attached drawings are obtained according to these attached drawings.
Integrated treating device structure chart is given birth in Fig. 1 sewage disposal materializations provided by the invention;
Integrated treating device stereo unfolding figure is given birth in Fig. 2 sewage disposal materializations provided by the invention.
As shown in the figure:Integrated treating device is given birth in 100- sewage disposal materializations;1- dissolvings;2- demulsifications area;3- oil removals precipitate Area;The areas 4-PAC;The areas 5-PAM;6- discharges area;7- precipitation-air-flotations area;The middle areas 8-;9- hydrolysis acidifications area;10- catalytic oxidations area; 11- sludge settlings area;12- discharges recovery area;13- floating oil collectings area;The first overflow ports of 14-;The demulsifications of 15- first area;16- second Be demulsified area;17- water inlets;The second overflow ports of 18-;The first outlet pipes of 19-;20- third overflow ports;The 4th overflow ports of 21-;22- 5th overflow port;The second outlet pipes of 23-;The first overflow pipes of 24-;25- aerators;26- hydrolysis fillings;27- catalytic oxidations are filled out Material;28- downflow weirs;29- central draft tubes;30- lower cones;31- refluxing openings;32- mud scrapers;33- scraper plates;34- stirring blades; 35- blenders;36- drains;37- mud discharging mouths;The second overflow pipes of 38-.
Specific implementation mode
Present invention will be further explained below with reference to the attached drawings and examples.
To keep the purpose, technical scheme and advantage of embodiment of the present invention clearer, implement below in conjunction with the present invention The technical solution in embodiment of the present invention is clearly and completely described in attached drawing in mode, it is clear that described reality The mode of applying is some embodiments of the invention, rather than whole embodiments.Therefore, the sheet to providing in the accompanying drawings below The detailed description of the embodiment of invention is not intended to limit the range of claimed invention, but is merely representative of the present invention Selected embodiment.Based on the embodiment in the present invention, those of ordinary skill in the art are not making creative work Under the premise of the every other embodiment that is obtained, shall fall within the protection scope of the present invention.
In the description of the present invention, it is to be understood that, the term of indicating position or position relationship is based on shown in attached drawing Orientation or positional relationship, be merely for convenience of description of the present invention and simplification of the description, do not indicate or imply the indicated equipment Or element must have a particular orientation, with specific azimuth configuration and operation, therefore be not considered as limiting the invention.
In the present invention unless specifically defined or limited otherwise, term " installation ", " connected ", " connection ", " fixation " etc. Term shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integral;Can be that machinery connects It connects, can also be electrical connection;It can be directly connected, can also can be indirectly connected through an intermediary in two elements The interaction relationship of the connection in portion or two elements.It for the ordinary skill in the art, can be according to specific feelings Condition understands the concrete meaning of above-mentioned term in the present invention.
Embodiment:
As depicted in figs. 1 and 2, a kind of sewage disposal materialization life integrated treating device 100 is present embodiments provided, including molten Gas tank 1, above-mentioned sewage disposal materialization give birth to and are in turn divided into demulsification along drainage flow direction by partition board inside integrated treating device 100 Area 2, oil removal settling zone 3, the areas PAC 4, the areas PAM 5, release area 6, precipitation-air-flotation area 7, middle area 8, hydrolysis acidification area 9, contact oxygen Change area 10, sludge settling area 11 and discharge recovery area 12, wherein oil removal settling zone 3 and precipitation-air-flotation area 7 shares an oil slick and receive Collect area 13.
Demulsification area 2 divides the first demulsification area 16 of demulsification area 15 and second to be connected to through the first overflow port 14, the first demulsification area 15 are equipped with water inlet 17, and the second demulsification area 16 is connected to oil removal settling zone 3 through the second overflow port 18.In first demulsification area 15 Three-way cock is installed at water inlet 17, demulsifier and sewage from catering business the first demulsification area 15 can be added to simultaneously through three-way cock In.
3 middle part of oil removal settling zone is equipped with the first outlet pipe 19, is located at 3 inner wall of oil removal settling zone on 19 top of the first outlet pipe It is equipped with above-mentioned floating oil collecting area 13.
The areas PAC 4 are connected to by the first outlet pipe 19 with oil removal settling zone 3.
The areas PAM 5 are connected to by third overflow port 20 with the areas PAC 4.
Release area 6 is connected to by the 4th overflow port 21 with the areas PAM 5.
Precipitation-air-flotation area 7 is connected to by the 5th overflow port 22 with release area 6, and 7 middle part of precipitation-air-flotation area goes out equipped with second Water pipe 23,7 inner wall of precipitation-air-flotation area for being located at 23 top of the second outlet pipe are equipped with above-mentioned floating oil collecting area 13.
Middle area 8 is connected to by the second outlet pipe 23 with precipitation-air-flotation area 7.
Hydrolysis acidification area 9 is connected to by the first overflow pipe 24 with middle area 8, and in hydrolysis acidification area 9 from the bottom to top successively Equipped with aerator 25 and hydrolysis filling 26.
Specifically, the type of hydrolysis filling 26 is depending on actual demand.
Catalytic oxidation area 10 is connected to by the second overflow pipe 38 with hydrolysis acidification area 9, and catalytic oxidation area 10 in by down toward On successively be equipped with aerator 25 and catalytic oxidation filler 27.
Specifically, the type of catalytic oxidation filler 27 is depending on actual demand.
Sludge settling area 11 is connected to by central draft tube 29 with catalytic oxidation area 10, and 29 lower end of central draft tube is equipped with Lower cone 30.The downflow weir 28 being connected with central draft tube 29, central draft tube are equipped with above the catalytic oxidation area 10 on side wall 29 settings are mainly worked as a buffer in 11 center of sludge settling area, the lower cone 30 of bottom mounting, prevent the dirt into the area The sludge of the areas Shui Duigai bottom, which generates, directly to be impacted.
Discharge recovery area 12 is connected to by downflow weir 28 with sludge settling area 11, and is discharged and be additionally provided with reflux on recovery area 12 Mouth 31.
In addition, being additionally provided with mud-scraping apparatus on partition board between oil removal settling zone 3 and precipitation-air-flotation area 7.
In the present embodiment, above-mentioned mud-scraping apparatus includes two of mud scraper 32 and interval on 32 crawler belt of mud scraper Scraper plate 33, two scraper plates 33 are respectively used to scrape the oil slick in oil removal settling zone 3 and precipitation-air-flotation area 7 in sewage level to floating In oil collection area 13.
In the present embodiment, above-mentioned aerator 25 is perforated pipe.
In the present embodiment, it is mounted on stirring blade 34 in above-mentioned first demulsification area 15, the areas PAC 4 and the areas PAM 5 Blender 35.
In the present embodiment, demulsification area 16 of above-mentioned first demulsification area 15, second, the areas PAC 4, the areas PAM 5, release area 6 and row The bottom for putting recovery area 12 is equipped with drain 36.
In the present embodiment, above-mentioned oil removal settling zone 3, floating oil collecting area 13, precipitation-air-flotation area 7, intermediate pool 8 and sludge are heavy The bottom in shallow lake area 11 is equipped with mud discharging mouth 37.
This example additionally provides the processing method of sewage disposal materialization life integrated treating device 100, includes the following steps:
A, the sewage from catering business come out from dissolving 1 is added after demulsifier and flows into the first demulsification area by water inlet 17 thereto 15, so that the grease in sewage from catering business is detached, then by first after agitating device in the first demulsification area 15 is sufficiently stirred Overflow port 14 flows into the second demulsification area 16 and carries out residue precipitation, and the sewage from catering business after slagging-off includes mainly grease two parts, then Oil removal settling zone 3 is flowed by the second overflow port 18, mud-scraping apparatus scrapes sewage from catering business upper layer oil slick in oil removal settling zone 3 to oil slick Collecting region 13 is completed to deoil to the first of sewage from catering business;
B, the less sewage from catering business of 3 middle part oil-containing of oil removal settling zone flows into the areas PAC 4 along the first outlet pipe 19, is stirred in the area Under the action of mixing device, sewage from catering business and flocculant PAC fully react, and the sludge in sewage from catering business starts to flocculate for the first time, flocculation Blocking sludge settling is to 4 bottom of the areas PAC;
C, the sewage from catering business after mud is gone then to flow into the areas PAM 5 by third overflow port 20 for the first time, in area's agitating device Under effect, sewage from catering business and flocculant PAM fully react, and the sludge in sewage from catering business starts secondary flocculation, caseous dirt of wadding a quilt with cotton Mud is precipitated to 5 bottom of the areas PAM;
D, secondary to go the sewage from catering business after mud to be flowed into release area 6 by the 4th overflow port 21 to carry out first natural sedimentation, it will The sludge not removed is precipitated to release 6 bottom of area again, and the sewage for discharging 6 top of area is then heavy by the inflow of the 5th overflow port 22 Shallow lake air flotation zone 7, mud-scraping apparatus scrape sewage upper layer oil slick in precipitation-air-flotation area 7 to floating oil collecting area 13,7 middle part of precipitation-air-flotation area The less sewage from catering business of oil-containing then flows into middle area 8 by the second outlet pipe 23 and carries out secondary natural sedimentation, and sludge is sunk It forms sediment to 8 bottom of middle area;
E, the sewage from catering business in middle area 8 flows into 9 bottom of hydrolysis acidification area, the perforation of the areas Xian Jinggai by the first overflow pipe 24 Pipe is aerated, and is then covered the hydrolysis filling 26 in the middle part of the area again and is flowed into 10 bottom of catalytic oxidation area from the second overflow pipe 38;
F, after flowing into the same areas the Xian Jinggai perforated pipe aerating regulation of sewage from catering business in catalytic oxidation area 10, the area is then covered again The catalytic oxidation filler 27 at middle part, then the central draft tube successively through the downflow weir 28 and area's centre of side-walls above the area 11 bottom of sludge settling area is flowed into after 29, under the buffering of the lower cone 30 of 29 bottom of central draft tube so that in sewage from catering business Sludge be deposited in the area bottom again;
G, the sewage from catering business in sludge settling area 11 flows into discharge through discharging the downflow weir 28 of 12 top side-walls of recovery area Recovery area 12 is detected the sewage from catering business in the area, passes through the drain 36 of the area bottom if it meets discharge standard Sewage from catering business is exhausted, if it does not meet the water inlet in the demulsification of the refluxing opening 31 and first in the areas discharge standard Ze Jianggai area 15 17 connections, repeat the above steps A to F, until sewage from catering business reaches discharge standard;
H, after the useless discharge of food and drink, through the first demulsification area 16 of demulsification area 15, second, the areas PAC 4, the areas PAM 5, release area 6 With the drain 36 of discharge 12 bottom of recovery area, oil removal settling zone 3, floating oil collecting area 13, precipitation-air-flotation area 7, intermediate pool 8 and dirt The mud discharging mouth 37 of 11 bottom of mud settling zone respectively cleans each area.
In the present embodiment, above-mentioned mud-scraping apparatus includes that mud scraper 32 and interval are mounted on mud scraper 32 in above-mentioned steps A Two scraper plates 33 on crawler belt, two scraper plates 33 are respectively used to will be in oil removal settling zone 3 and precipitation-air-flotation area 7 in sewage level Oil slick is scraped into floating oil collecting area 13.
Sewage disposal materialization life integrated treating device provided in this embodiment has the beneficial effect that:Sewage provided by the invention The integrated height of processed material metaplasia integrated treating device, ingenious in design, oil removal settling zone and precipitation-air-flotation area share an oil slick and receive Ji Qu and mud-scraping apparatus, by installing two scraper plates on mud-scraping apparatus to reach to oil removal settling zone and precipitation-air-flotation area Synchronize the purpose deoiled, have and save energy consumption, the advantages of reducing cost;In addition the treatment process of the equipment is comprehensive, set Machinery, chemistry and micro-organism treatment process, treatment effect are splendid.
The above is not intended to limit the present invention in any form, although the present invention is disclosed with preferred embodiment As above, however, it is not intended to limit the invention, any person skilled in the art, is not departing from technical solution of the present invention model In enclosing, when the technology contents using the disclosure above make a little change or are modified to the equivalent embodiment of equivalent variations, in every case It is the content without departing from technical solution of the present invention, is simply repaiied to any made by above example according to the technical essence of the invention Change, equivalent variations and modification, in the range of still falling within technical solution of the present invention.

Claims (8)

1. integrated treating device, including dissolving are given birth in a kind of sewage disposal materialization, which is characterized in that the sewage disposal materialization life Inside integrated treating device by partition board along drainage flow direction be in turn divided into demulsification area, oil removal settling zone, the areas PAC, the areas PAM, Discharge area, precipitation-air-flotation area, middle area, hydrolysis acidification area, catalytic oxidation area, sludge settling area and discharge recovery area, interval Oily settling zone and precipitation-air-flotation area share a floating oil collecting area;
The first demulsification area being connected to through the first overflow port and the second demulsification area are divided into demulsification, and the first demulsification area is equipped with water inlet Mouthful, the second demulsification area is connected to the second overflow port of oil removal settling zone;
It is equipped with the first outlet pipe in the middle part of oil removal settling zone, is located at the oil removal settling zone inner wall on the first outlet pipe top equipped with described Floating oil collecting area;
The areas PAC are connected to by the first outlet pipe with oil removal settling zone;
The areas PAM are connected to by third overflow port with the areas PAC;
Release area is connected to by the 4th overflow port with the areas PAM;
Precipitation-air-flotation area is connected to by the 5th overflow port with release area, and the second outlet pipe is equipped in the middle part of precipitation-air-flotation area, is located at The precipitation-air-flotation area inner wall on the second outlet pipe top is equipped with the floating oil collecting area;
Middle area is connected to by the second outlet pipe with precipitation-air-flotation area;
Hydrolysis acidification area is connected to by the first overflow pipe with middle area, and is equipped with aeration dress in hydrolysis acidification area successively from the bottom to top It sets and hydrolysis filling;
Catalytic oxidation area is connected to by the second overflow pipe with hydrolysis acidification area, and is equipped with and is exposed successively from the bottom to top in catalytic oxidation area Device of air and catalytic oxidation filler;
Sludge settling area is connected to by central draft tube with catalytic oxidation area, and central draft tube lower end is equipped with lower cone;
Discharge recovery area is connected to by downflow weir with sludge settling area, and is discharged and be additionally provided with refluxing opening on recovery area;
In addition, being additionally provided with mud-scraping apparatus on partition board between oil removal settling zone and precipitation-air-flotation area.
2. integrated treating device is given birth in sewage disposal materialization according to claim 1, which is characterized in that the mud-scraping apparatus packet Two scraper plates of mud scraper and interval on mud scraper crawler belt are included, two scraper plates are respectively used to oil removal settling zone and precipitation Oil slick in air flotation zone in sewage level is scraped into floating oil collecting area.
3. integrated treating device is given birth in sewage disposal materialization according to claim 1, which is characterized in that the aerator is Perforated pipe.
4. integrated treating device is given birth in sewage disposal materialization according to claim 1, which is characterized in that first demulsification It is mounted on the blender with stirring blade in area, the areas PAC and the areas PAM.
5. integrated treating device is given birth in sewage disposal materialization according to claim 1, which is characterized in that first demulsification Area, the second bottom for being demulsified area, the areas PAC, the areas PAM, release area and discharge recovery area are equipped with drain.
6. integrated treating device is given birth in sewage disposal materialization according to claim 1, which is characterized in that the oil removal precipitation Area, floating oil collecting area, precipitation-air-flotation area, intermediate pool and sludge settling area bottom be equipped with mud discharging mouth.
7. a kind of processing method of sewage disposal materialization life integrated treating device, which is characterized in that include the following steps:
A, the sewage from catering business come out from dissolving is added after demulsifier and flows into the first demulsification area by water inlet, thereto through first So that the grease in sewage from catering business is detached after agitating device is sufficiently stirred in demulsification area, then by the first overflow port inflow the Residue precipitation is carried out in two demulsification areas, the sewage from catering business after slagging-off includes mainly grease two parts, then is flowed by the second overflow port Oil removal settling zone, mud-scraping apparatus scrape sewage from catering business upper layer oil slick in oil removal settling zone to floating oil collecting area, complete to food and drink dirt The first of water deoils;
B, the less sewage from catering business of oil-containing flows into the areas PAC along the first outlet pipe in the middle part of oil removal settling zone, in area's agitating device Under effect, sewage from catering business and flocculant PAC fully react, and the sludge in sewage from catering business starts to flocculate for the first time, caseous dirt of wadding a quilt with cotton Mud is precipitated to the areas PAC bottom;
C, the sewage from catering business after mud is gone then to flow into the areas PAM by third overflow port for the first time, under the action of area's agitating device, Sewage from catering business and flocculant PAM fully react, and the sludge in sewage from catering business starts secondary flocculation, wad a quilt with cotton caseous sludge settling extremely The areas PAM bottom;
D, secondary to go the sewage from catering business after mud to be flowed into release area by the 4th overflow port to carry out first natural sedimentation, by what is do not removed Sludge is precipitated to release area bottom again, and the sewage for discharging area top then flows into precipitation-air-flotation area by the 5th overflow port, scrapes Mud device scrapes sewage upper layer oil slick in precipitation-air-flotation area to floating oil collecting area, and oil-containing less food and drink in precipitation-air-flotation area middle part is dirty Water then flows into middle area by the second outlet pipe and carries out secondary natural sedimentation, by sludge settling to middle area bottom;
E, the sewage from catering business in middle area by the first overflow pipe flow into hydrolysis acidification area bottom, the areas Xian Jinggai perforated pipe aerating regulation, Then the hydrolysis filling in the middle part of the area is covered again flows into catalytic oxidation area bottom from the second overflow pipe;
F, it after flowing into the same areas the Xian Jinggai perforated pipe aerating regulation of sewage from catering business in catalytic oxidation area, then covers again in the middle part of the area Catalytic oxidation filler, then flow into sludge after the downflow weir of side-walls and the central draft tube of area's centre above the area successively Settling zone bottom, under the buffering of the lower cone of central draft tube bottom so that the sludge in sewage from catering business is deposited in this again Area bottom;
G, the sewage from catering business in sludge settling area flows into discharge recovery area through discharging the downflow weir of side-walls above recovery area, to this Sewage from catering business in area is detected, and is exhausted sewage from catering business by the drain of the area bottom if it meets discharge standard, If it does not meet the water inlet connection on refluxing opening and the first demulsification area in the areas discharge standard Ze Jianggai, repeat the above steps A To F, until sewage from catering business reaches discharge standard;
H, after the useless discharge of food and drink, through the first demulsification area, the second demulsification area, the areas PAC, the areas PAM, release area and discharge recovery area The drain of bottom, oil removal settling zone, floating oil collecting area, precipitation-air-flotation area and the mud discharging mouth of sludge settling area bottom are respectively to each Area is cleaned.
8. the processing method of sewage disposal materialization life integrated treating device according to claim 7, which is characterized in that above-mentioned Mud-scraping apparatus described in step A includes two scraper plates of mud scraper and interval on mud scraper crawler belt, two scraper plates difference For scraping the oil slick in oil removal settling zone and precipitation-air-flotation area in sewage level into floating oil collecting area.
CN201810986053.3A 2018-08-28 2018-08-28 Integrated treating device and processing method are given birth in sewage disposal materialization Pending CN108793643A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810986053.3A CN108793643A (en) 2018-08-28 2018-08-28 Integrated treating device and processing method are given birth in sewage disposal materialization

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810986053.3A CN108793643A (en) 2018-08-28 2018-08-28 Integrated treating device and processing method are given birth in sewage disposal materialization

Publications (1)

Publication Number Publication Date
CN108793643A true CN108793643A (en) 2018-11-13

Family

ID=64080916

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810986053.3A Pending CN108793643A (en) 2018-08-28 2018-08-28 Integrated treating device and processing method are given birth in sewage disposal materialization

Country Status (1)

Country Link
CN (1) CN108793643A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112225357A (en) * 2020-10-30 2021-01-15 芜湖海创环保科技有限责任公司 A process water treatment system for oily sludge treatment equipment

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104193097A (en) * 2014-09-02 2014-12-10 山东源宝环保装备有限公司 Air-floatation biochemical integrated equipment
CN206915935U (en) * 2017-03-28 2018-01-23 苏州博瑞水处理有限公司 Emulsifying liquid waste water processing system
CN207193070U (en) * 2017-09-18 2018-04-06 福建省爱善环保科技有限公司 A kind of efficient equipment for processing industrial sewage
CN208917017U (en) * 2018-08-28 2019-05-31 江苏国松环境科技开发有限公司 Integrated treating device is given birth in sewage treatment materialization

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104193097A (en) * 2014-09-02 2014-12-10 山东源宝环保装备有限公司 Air-floatation biochemical integrated equipment
CN206915935U (en) * 2017-03-28 2018-01-23 苏州博瑞水处理有限公司 Emulsifying liquid waste water processing system
CN207193070U (en) * 2017-09-18 2018-04-06 福建省爱善环保科技有限公司 A kind of efficient equipment for processing industrial sewage
CN208917017U (en) * 2018-08-28 2019-05-31 江苏国松环境科技开发有限公司 Integrated treating device is given birth in sewage treatment materialization

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112225357A (en) * 2020-10-30 2021-01-15 芜湖海创环保科技有限责任公司 A process water treatment system for oily sludge treatment equipment

Similar Documents

Publication Publication Date Title
CN106902549A (en) A kind of automatic oily water separating equipment of combined type
CN106927588A (en) A kind of automatic oily water separating equipment of modularization
CN108793643A (en) Integrated treating device and processing method are given birth in sewage disposal materialization
CN208917017U (en) Integrated treating device is given birth in sewage treatment materialization
CN114105350B (en) A wastewater multi-stage separation pretreatment device
CN210885400U (en) Flotation device for sewage treatment
CN221093848U (en) Oil separation and reaction precipitation integrated equipment
CN210103694U (en) Device for treating oily sewage
CN208632149U (en) Total travel scrapes slag air bearing all-in-one machine
CN207645963U (en) A kind of integrating device of improved efficient sedimentation tank and sand filter
CN206858300U (en) Fluid pressure type water separator
CN208265916U (en) A kind of high efficiency composition EPS reactor
CN205258184U (en) Oily wastewater treating device
CN211595087U (en) A air supporting equipment for waste water treatment
CN209367983U (en) A kind of oil separator
SE433489B (en) DEVICE FOR CURRENT WASTE WASTE FLUID IN A SEDIMENTATION POOL Separate from the liquid's surface liquid contaminants
CN211570314U (en) Coagulation reaction sedimentation tank
JP4336059B2 (en) Solid-liquid separator for waste water
CN211226495U (en) Novel integrated inclined tube and inclined plate sedimentation tank
CN210286942U (en) An oil-water separation device
CN219972088U (en) Rainwater treatment equipment
CN206289089U (en) A kind of skewed culvert filter residue air floatation machine
CN219136432U (en) Advection type dissolved air floatation machine
JPH11333210A (en) Sedimentation separation device
CN220223721U (en) Kitchen oil-water separator with two-stage separation

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20181113

RJ01 Rejection of invention patent application after publication