CN201400610Y - Textile wastewater treatment and recycling system - Google Patents
Textile wastewater treatment and recycling system Download PDFInfo
- Publication number
- CN201400610Y CN201400610Y CN200920302526XU CN200920302526U CN201400610Y CN 201400610 Y CN201400610 Y CN 201400610Y CN 200920302526X U CN200920302526X U CN 200920302526XU CN 200920302526 U CN200920302526 U CN 200920302526U CN 201400610 Y CN201400610 Y CN 201400610Y
- Authority
- CN
- China
- Prior art keywords
- pipe
- textile
- tank
- sludge
- waste
- 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.)
- Expired - Fee Related
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Filtration Of Liquid (AREA)
Abstract
The utility model relates to a wastewater treatment system, in particular to a textile wastewater treatment and recycling system which mainly aims at solving the technical problems existing in the prior art that the wastewater treatment method is excessively tedious and complicated, and can not be used for wastewater treatment in most textile industries, moreover, as no oil separation device is available, a small quantity of oil matter contained in wastewater can enter a wastewater treatment plant, and is relatively difficult to separate, and the like. The textile wastewater treatment and recycling system comprises a grille oil separator in which textile wastewater can be introduced, wherein the grille oil separator is connected with a water collecting and adjusting tank which is providedwith a sewage lifting pump; the sewage lifting pump is connected with a floatation tank through a sewage pipe; an outlet of the floatation tank is connected with a reaction sedimentation tank throughthe sewage pipe; the upper part of the reaction sedimentation tank is connected with a medicament tank through a medicament pipe, and the lower part thereof is provided with a sedimentation area; thereaction sedimentation tank is connected with a filter tank through the sewage pipe; the filter tank is connected with a clear water storage tank through the sewage pipe; and the floatation tank and the sedimentation area are both communicated with a sludge tank through a sludge pipe.
Description
Technical field
The utility model relates to a kind of Waste Water Treatment, especially relates to a kind of to textile waste processing and the isostructural improvement of reclaiming system.
Background technology
Composition, character and the colourity of general textile industry waste water are different with textile properties, and also the variation with employed dyestuff kind, quantity and other chemical agent changes.Be generally that oil content is more, wastewater biodegradability difference etc., generally based on inorganic pollution, wherein the finish in the waste water strengthens for the pollution of environment, does not directly enter the severe contamination that farmland or water body all can cause environment if do not handle.Chinese patent discloses a kind of method of wastewater treatment, and (publication number: CN 101085695A), it comprises the steps: classification: with the classification of waste of discharging is high-concentration waste water and low concentration wastewater two class sets dress; High-concentration waste water pre-process: air supporting materialization: the high-concentration waste water that will collect dress forms low concentration wastewater and dense suspension through the air supporting materialization; The clarification layering: dense suspension forms low concentration wastewater and solid suspension liquid through the clarification layering, and clarification layering polymerizing agent is an aluminium chlorohydroxide: press filtration: solid suspension liquid is through being separated into low concentration wastewater and discharging mud from press filtration; PH regulates and biochemical treatment: low concentration wastewater enters PH adjusting water reservoir to carry out carrying out the routine biochemistry processing again after conventional PH regulates, be separated into elementary discharge water and active sludge, active sludge is through being separated into discharging mud and press filtration waste water from press filtration, press filtration waste water returns into PH adjusting water reservoir and handles; Chemical treatment: elementary discharge water forms level discharge water eventually through dosing still, reactor, water purification still, and the chemical treatment medicament that the dosing still adds is clorox or aluminium chlorohydroxide; Dosing still in the chemical treatment is equipped with heating unit, and heat form can be sun power, steam or electrically heated.Reactor in the chemical treatment can be 4 compositions, increases between reactor and the water purification still to filter still, and filtering still can be 2, and filter packing is cobble, quartz sand and gac; From pressing press filtration is that active sludge is poured in the woven bag, by active sludge deadweight press filtration the waste water filter is extruded woven bag and forms discharging mud outward.But this method of wastewater treatment is too miscellaneous, can't be used in the wastewater treatment of most of textile industry, and owing to there is not the oil removal device, contains a spot of oily substance in the waste water and can enter wastewater treatment equipment, difficult the separation.
The utility model content
The utility model technical issues that need to address provide a kind of textile waste and handle and reclaiming system, it mainly is that solution existing in prior technology method of wastewater treatment is too miscellaneous, can't be used in the wastewater treatment of most of textile industry, and owing to there is not the oil removal device, contain a spot of oily substance in the waste water and can enter wastewater treatment equipment, difficult technical problem of separating etc.
Above-mentioned technical problem of the present utility model is mainly solved by following technical proposals:
Textile waste of the present utility model is handled and reclaiming system, comprise the grid oil trap that can feed textile waste, it is characterized in that described grid oil trap is connected with the equalizing tank that catchments, the equalizing tank that catchments is provided with sewage pump, sewage pump is connected with air flotation pool by waste pipe, the air flotation pool outlet is connected with reaction settling basin by waste pipe, and there is pharmacy slot on reaction settling basin top by the medicament pipe coupling, and the reaction settling basin bottom is provided with the settling region; Reaction settling basin is connected with filtering basin by waste pipe, and filtering basin connect the clear water storage pool by waste pipe; Air flotation pool all is communicated with sludge sump by sludge pipe with the settling region.The grid oil trap can be removed the oily substance in the waste water earlier.Waste water enters the adjusting homogenizing that the equalizing tank that catchments can carry out water quality and quantity, makes water quantity and quality relatively keep stable.Can feed medicament in the air flotation pool, thereby react, make that oils and particulate matter are removed in the waste water, can reduce COD concentration in the waste water with waste water.Can feed medicament by pharmacy slot in the reaction settling basin,, after the inclined tube mud-water separation, enter into filtering basin again with waste water generation flocculation reaction.
As preferably, described sludge sump is connected with pneumatic diaphragm pump by sludge pipe, and the sludge pump outlet is connected with the sludge press filtration machine.Pneumatic diaphragm pump can be transported to mud in the sludge press filtration machine, and the sludge press filtration machine becomes filter cake with sludge press filtration, transports outward landfill then.
As preferably, described sludge sump is communicated with the equalizing tank that catchments by waste pipe.The supernatant liquor that sludge sump top produces can be recycled to the equalizing tank place that catchments again and handle once more.
As preferably, described sludge press filtration machine is communicated with the equalizing tank that catchments by waste pipe.The sludge press filtration machine with sludge press filtration after, the filtrate that leaches can be recycled to the equalizing tank place that catchments through waste pipe and handle once more.
As preferably, described filtering basin are the valveless water filter pond, are provided with filtering layer in the pond, and the filtering layer top is provided with the outer comb of siphon and is communicated with outer comb.The sewage that is in the below in the pond can be discharged through outer comb, and the clear water above being in the pond can be sent in the clear water storage pool.
As preferably, described sewage pump is connected with reaction container by waste pipe, and the reaction container bottom is communicated with bottom air flotation pool.Sewage can react with medicament earlier in reaction container, and then sends into air flotation pool.
As preferably, be provided with packing layer in the described reaction settling basin, the settling region of reaction settling basin bottom is 2.After system runs to for some time, in the contact-oxidation pool a large amount of active sludge will be arranged, most of mud with biomembranous form apposition growth on packing layer, thereby the higher sewage of concentration of treatment.
As preferably, described clear water storage pool is connected with the water pump that Chi Shui can be delivered to each workshop reuse by water pipe.
Therefore, the utlity model has the wastewater treatment that can be used in most of textile industry, and system front end is provided with the grid oil trap again, containing a spot of oily substance in the waste water can be removed, can not enter the subsequent wastewater treatment system, characteristics such as simple and reasonable for structure.
Description of drawings
Accompanying drawing 1 is a kind of structural representation of the present utility model.
Component, position and numbering among the figure: grid oil trap 1, the equalizing tank 2 that catchments, sewage pump 3, waste pipe 4, air flotation pool 5, reaction settling basin 6, medicament pipe 7, pharmacy slot 8, settling region 9, filtering basin 10, clear water storage pool 11, sludge pipe 12, sludge sump 13, pneumatic diaphragm pump 14, sludge press filtration machine 15, filtering layer 16, the outer comb 17 of siphon, reaction container 18, water pump 19.
Embodiment
Below by embodiment, and in conjunction with the accompanying drawings, the technical solution of the utility model is described in further detail.
Embodiment: this routine textile waste is handled and reclaiming system, as Fig. 1, a grid oil trap 1 that feeds textile waste is arranged, grid oil trap 1 is connected with the equalizing tank 2 that catchments, catchment and be connected with sewage pump 3 by waste pipe 4 in the equalizing tank 2, sewage pump is connected with reaction container 18 by waste pipe, and reaction container 18 bottoms are communicated with air flotation pool 5.The sewage outlet of air flotation pool 5 is communicated with reaction settling basin 6 by waste pipe, is communicated with two pharmacy slots 8 depositing medicament by medicament pipe 7 in the reaction settling basin, and reaction settling basin inside is provided with filler, and the bottom is provided with 2 settling regions 9.Settling region 9 all is communicated with sludge sump 13 by sludge pipe 12 with air flotation pool 5, and sludge sump is connected with sludge press filtration machine 15 by pneumatic diaphragm pump 14.Sludge sump 13 all is communicated with the equalizing tank 2 that catchments by water pipe with sludge press filtration machine 15.The sewage outlet place of reaction settling basin 6 is connected with filtering basin 10 by waste pipe, and filtering basin are the valveless water filter pond, is provided with filtering layer 16 in the pond, and the filtering layer top is provided with the outer comb 17 of siphon and is communicated with outer comb.The clear water output place of filtering basin 10 is communicated with clear water storage pool 11, and clear water storage pool 11 is connected with the water pump 19 that Chi Shui can be delivered to each workshop reuse by water pipe.
Waste water enters in the sewage works district after collecting, owing to contain a spot of oily substance in the waste water, earlier waste water is fed grid oil trap 1 and carries out the oil removal processing.Enter the equalizing tank 2 that catchments through pretreated waste water and carry out the adjusting of water quality and quantity, make water quantity and quality relatively keep stable.Waste water after the homogenizing is promoted to air flotation pool 5 by sewage pump 3, by the abundant reaction of medicament and waste water, makes that oils and particulate matter are removed in the waste water, thereby can reduce COD concentration in the waste water in air flotation pool.Handle back water outlet gravity flow through air flotation pool 5 and enter into reaction settling basin 6, flocculation reaction in reaction tank enters into filtering basin 10 again and carries out filtration treatment after the inclined tube mud-water separation, and it is standby that the water outlet gravity flow enters into clear water storage pool 11.The mud of air flotation pool 5 and reaction settling basin 6 can utilize the effect that hydrostatic head is pressed in the pond to send into sludge sump 13.Supernatant liquor in the sludge sump 13 flows back to the equalizing tank 2 that catchments, and mud is then delivered to sludge press filtration machine 15 by pneumatic diaphragm pump 14 and handled.Mud cake should be transported to the useless admittedly processing company of specialty outward and disposes behind the sludge dehydrating and drying.
Claims (8)
1. a textile waste is handled and reclaiming system, comprise the grid oil trap (1) that can feed textile waste, it is characterized in that described grid oil trap (1) is connected with the equalizing tank that catchments (2), the equalizing tank that catchments is provided with sewage pump (3), sewage pump is connected with air flotation pool (5) by waste pipe (4), the air flotation pool outlet is connected with reaction settling basin (6) by waste pipe, reaction settling basin top is connected with pharmacy slot (8) by medicament pipe (7), and the reaction settling basin bottom is provided with settling region (9); Reaction settling basin (6) is connected with filtering basin (10) by waste pipe, and filtering basin connect clear water storage pool (11) by waste pipe; Air flotation pool (5) all passes through sludge pipe (12) with settling region (9) and is communicated with sludge sump (13).
2. textile waste according to claim 1 is handled and reclaiming system, it is characterized in that described sludge sump (13) is connected with pneumatic diaphragm pump (14) by sludge pipe (12), and sludge pump (14) outlet is connected with sludge press filtration machine (15).
3. textile waste according to claim 2 is handled and reclaiming system, it is characterized in that described sludge sump (13) is communicated with the equalizing tank that catchments (2) by waste pipe (4).
4. textile waste according to claim 2 is handled and reclaiming system, it is characterized in that described sludge press filtration machine (15) is communicated with the equalizing tank that catchments (2) by waste pipe (4).
5. handle and reclaiming system according to claim 1 or 2 or 3 or 4 described textile wastes, it is characterized in that described filtering basin (10) for the valveless water filter pond, are provided with filtering layer (16) in the pond, the filtering layer top is provided with the outer comb (17) of siphon and is communicated with outer comb.
6. handle and reclaiming system according to claim 1 or 2 or 3 or 4 described textile wastes, it is characterized in that described sewage pump (3) is connected with reaction container (18) by waste pipe (4), the reaction container bottom is communicated with air flotation pool (5) bottom.
7. handle and reclaiming system according to claim 1 or 2 or 3 or 4 described textile wastes, it is characterized in that being provided with packing layer in the described reaction settling basin (6), the settling region (9) of reaction settling basin bottom is 2.
8. handle and reclaiming system according to claim 1 or 2 or 3 or 4 described textile wastes, it is characterized in that described clear water storage pool (11) is connected with the water pump (19) that Chi Shui can be delivered to each workshop reuse by water pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920302526XU CN201400610Y (en) | 2009-04-24 | 2009-04-24 | Textile wastewater treatment and recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920302526XU CN201400610Y (en) | 2009-04-24 | 2009-04-24 | Textile wastewater treatment and recycling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201400610Y true CN201400610Y (en) | 2010-02-10 |
Family
ID=41660408
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200920302526XU Expired - Fee Related CN201400610Y (en) | 2009-04-24 | 2009-04-24 | Textile wastewater treatment and recycling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201400610Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101928053A (en) * | 2010-09-16 | 2010-12-29 | 江苏新龙鼎环保成套工程有限公司 | Electrocoagulation sedimentation pond |
| CN102531235A (en) * | 2011-12-27 | 2012-07-04 | 福州绿明环保工程有限公司 | Technology for deeply treating stone processing wastewater |
| CN104445737A (en) * | 2014-11-28 | 2015-03-25 | 浙江万龙机械有限公司 | Sewage treatment system |
| CN106517562A (en) * | 2016-12-23 | 2017-03-22 | 钦州市中玻玻璃有限责任公司 | Glass production sewage treatment system |
| WO2022088224A1 (en) * | 2020-10-30 | 2022-05-05 | 单县舜天专用车制造有限公司 | Efficient sludge discharge system for sewage treatment |
-
2009
- 2009-04-24 CN CN200920302526XU patent/CN201400610Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101928053A (en) * | 2010-09-16 | 2010-12-29 | 江苏新龙鼎环保成套工程有限公司 | Electrocoagulation sedimentation pond |
| CN102531235A (en) * | 2011-12-27 | 2012-07-04 | 福州绿明环保工程有限公司 | Technology for deeply treating stone processing wastewater |
| CN104445737A (en) * | 2014-11-28 | 2015-03-25 | 浙江万龙机械有限公司 | Sewage treatment system |
| CN106517562A (en) * | 2016-12-23 | 2017-03-22 | 钦州市中玻玻璃有限责任公司 | Glass production sewage treatment system |
| WO2022088224A1 (en) * | 2020-10-30 | 2022-05-05 | 单县舜天专用车制造有限公司 | Efficient sludge discharge system for sewage treatment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201581023U (en) | River water purifying and recycling system | |
| CN201400610Y (en) | Textile wastewater treatment and recycling system | |
| CN201400628Y (en) | Down wastewater treatment system | |
| CN101798768B (en) | Waste paper regeneration environmental protection device and method | |
| CN201545750U (en) | Printing and dyeing wastewater pretreatment system | |
| CN107585972A (en) | Grease processing waste water handling process and device | |
| CN105384230B (en) | A kind of cellulose sewage pretreatment device and application | |
| CN208717015U (en) | Wiring board abrasive waste water reclaiming system | |
| CN100400427C (en) | Process of treating and utilizing acid waste water containing heavy metal | |
| CN204265597U (en) | Oil field compression fracture returns discharge opeing treatment unit | |
| CN201545754U (en) | System for processing machining-generated wastewater | |
| CN202272806U (en) | Down feather wastewater recycling system | |
| CN206395925U (en) | Deliming anaerobic reactor | |
| CN201400631Y (en) | Plastic cleaning wastewater treatment system | |
| CN108947137A (en) | A kind of kitchen garbage percolation liquid treatment method | |
| CN101428934A (en) | Apparatus for treating waste water apparatus for treating waste water from regeneration slurry boxboard production | |
| CN102849836A (en) | Sludge water concentration and purification treatment method and integrated treatment device | |
| CN206915894U (en) | High zero release equipment who contains salt waste water treatment | |
| CN206244582U (en) | Dyeing and printing sewage processing system | |
| CN102229450A (en) | Integrated membrane purification technology for treating hematite dressing wastewater | |
| CN102092897A (en) | Method for deep purifying domestic waste water of residential area into reclaimed water | |
| CN107857443A (en) | A kind of papermaking wastewater processing system | |
| CN101125722A (en) | Grog paper-making waste water physicochemical circulation biochemical treatment zero discharging technique | |
| CN108929005A (en) | Greasy filth purifying water process technique and its device | |
| CN204569620U (en) | A kind of coking chemical waste water oil removing slag removing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100210 Termination date: 20170424 |