CN206127009U - Hydraulic loom's waste water recovery system - Google Patents
Hydraulic loom's waste water recovery system Download PDFInfo
- Publication number
- CN206127009U CN206127009U CN201620988402.1U CN201620988402U CN206127009U CN 206127009 U CN206127009 U CN 206127009U CN 201620988402 U CN201620988402 U CN 201620988402U CN 206127009 U CN206127009 U CN 206127009U
- Authority
- CN
- China
- Prior art keywords
- water
- waste water
- jet loom
- exchanger
- flocculation
- 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
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model discloses a hydraulic loom's waste water recovery system belongs to hydraulic loom's waste water treatment field, a hydraulic loom's waste water recovery system, including useless water discharging tube, flocculation and precipitation pond, air supporting pond, activated carbon filter, ion exchanger and the reuse water conveyer pipe that communicates in proper order, still include the waste residue collecting pit of all being connected with flocculation and precipitation pond and air supporting pond, be equipped with filter screen A and oil interceptor between useless water discharging tube and the flocculation and precipitation pond, the waste residue collecting pit is connected with the pressure filter. The utility model discloses a perfect physics and chemical processing method and more fully eliminate the harmful substance in hydraulic loom's the waste water, and to waste water recycle, it is energy -concerving and environment -protective.
Description
Technical field
The utility model is related to the field of waste water treatment of water-jet loom, particularly relates to a kind of Sewage treatment of water-jet loom
System.
Background technology
Water-jet loom can produce in the course of the work substantial amounts of waste water, wherein containing substantial amounts of organic matter, in prior art
The method process of the machineries such as simple precipitation and filtration is typically all simply passed through, is finally discharge, not only cause water resource
Waste, and treated waste water is also just discharged without up to standard, and slurry, dyestuff, greasy dirt, impurity in waste water etc. all can be to rings
Border works the mischief, therefore finds a kind of sewage recovering system of the harmful substance in waste water for more fully removing water-jet loom very
It is necessary.
Utility model content
The utility model purpose be more thoroughly remove in water-jet loom waste water harmful substance and by recycling at
A kind of sewage recovering system of the water-jet loom of the waste water after reason.
The utility model is achieved through the following technical solutions：A kind of sewage recovering system of water-jet loom, including connecting successively
Logical wastewater discharge pipe, flocculation sedimentation tank, flotation tank, ion-exchanger and recycle-water delivery pipe；Also include and flocculation sedimentation tank
The waste residue collecting pit being all connected with flotation tank；Screen pack A and oil interceptor are provided between wastewater discharge pipe and flocculation sedimentation tank；Waste residue
Collecting pit is connected with filter press.
Further, it is preferably to realize the utility model, is specifically arranged to following structures：The flocculation sedimentation tank is gentle
Screen pack B is provided between floating pond.
Further, it is preferably to realize the utility model, is specifically arranged to following structures：Flotation tank and activated carbon are filtered
Mechanical filter is provided between device, mechanical filter is connected with waste residue collecting pit.
Further, it is preferably to realize the utility model, is specifically arranged to following structures：The ion-exchanger includes
Anion exchanger and cation exchanger；And anion exchanger is connected with the delivery port of active carbon filter.
Further, it is preferably to realize the utility model, is specifically arranged to following structures：The cationic ion-exchange resin
It is to be formed by Jing sulfuric acid sulfonations after styrene and divinylbenzene polymerization；；Anion exchange resin is containing quaternary ammonium group-N (CH3)
The resin of 3OH groups.
Further, it is preferably to realize the utility model, is specifically arranged to following structures：The cationic ion-exchange resin
It is with anion exchange resin spherical.
The utility model compared with prior art, with advantages below and beneficial effect：
First, the utility model is by arranging flocculation sedimentation tank, flotation tank, active carbon filter, ion-exchanger to from useless
Water discharge pipe discharge containing a large amount of harmful materials, by the method for physics and chemistry sewage is processed simultaneously, to dirt
The process of water is more abundant by simple physical filtering compared to existing technology；
2nd, the utility model is entered again by the sewage processed through physics and chemical process by recycle-water delivery pipe
Enter water-jet loom re-using, cycling use of water energy-conserving and environment-protective；
3rd, the utility model arranges screen pack A, oil interceptor and flocculation sedimentation tank, screen pack A, oil removal at the initial stage for processing
It is heavy that pond can be belonging to chemistry by the harmful substance in basic physics mode preliminary treatment waste water, particularly flocculation sedimentation tank
The reaction tank in shallow lake, can further comparatively large number of impurity processed in waste water, mitigate the processing pressure of follow-up equipment；
Description of the drawings
Fig. 1 is the annexation block diagram between part of the present utility model.
Specific embodiment
The utility model is described in further detail with reference to embodiment, but embodiment of the present utility model is not
It is limited to this.
Embodiment 1：
In the present embodiment, as shown in figure 1, a kind of sewage recovering system of water-jet loom, including the waste water row being sequentially communicated
Outlet pipe, flocculation sedimentation tank, flotation tank, ion-exchanger and recycle-water delivery pipe；Also include equal with flocculation sedimentation tank and flotation tank
The waste residue collecting pit of connection；Screen pack A and oil interceptor are provided between wastewater discharge pipe and flocculation sedimentation tank；Waste residue collecting pit connects
There is filter press.
The course of work of the present utility model is：Waste water in water-jet loom passes through wastewater discharge pipe, successively by screen pack A mistakes
Filter than relatively large and obvious impurity, will dispose with the mutual exclusive oily matter of water subsequently into oil interceptor, then enter
Enter flocculation basin, add the later impurity sedimentation that will can not pass through tentatively to filter out in waste water of corresponding flocculant to the bottom of flocculation basin
Portion, this step belongs to chemical method process, can process the not treatable dissolubility harmful substance of physical filtering, then will be miscellaneous with pump
Matter is extracted out from the bottom of flocculation basin, and from flocculation basin waste water out impurity is further removed in flotation tank, process be
Without the impurity of abundant sedimentation in flocculation basin；Detached impurity enters waste residue collecting pit from flocculation sedimentation tank and flotation tank
In, then the impurity filter press in waste residue collecting pit is processed, and is processed with rear impurity environmental protection treatment, and the water isolated is discharged；Water from
Out later further across the process of ion-exchanger in flotation tank, the process of ion-exchanger belongs to finer process
Mode, further understands the not treatable impurity of physical treatment, allows water quality largely to be lifted, from ion-exchanger
Water out is recycled in recycle-water delivery pipe.Above-mentioned structure and processing mode causes the utility model to sewage
The step of processing physics and chemical method is combined, and process is more, compared to existing technology by simple physical filtering more
Fully；Re-use after wastewater treatment, cycling use of water energy-conserving and environment-protective,
Embodiment 2：
The present embodiment further sets up screen pack B, the flocculation sedimentation tank and flotation tank on the basis of above-described embodiment
Between be provided with screen pack B, the impurity in flocculation sedimentation tank during being pumped out can disturbed liquid internal, it is very big by one
Part can be entered in flotation tank, can so increase the workload of flotation tank, and can affect the working effect of flotation tank, in waste water
Filtered using screen pack B between flotation tank, can allow the more abundant of impurity treatment.The other parts and embodiment of the present embodiment
1 is identical, repeats no more here.
Embodiment 3：
The present embodiment further sets up mechanical filter, flotation tank and active carbon filter on the basis of above-described embodiment
Between be provided with mechanical filter, from flotation tank waste water out also contain many impurity, by the further of mechanical filter
Filter, and mechanical filter is connected with waste residue collecting pit, the impurity produced after filtration enters waste residue collecting pit.The present embodiment its
He is partly identical with above-described embodiment, repeats no more here.
Embodiment 4：
The present embodiment further limits ion exchange on the basis of above-described embodiment, the ion-exchanger include it is cloudy from
Sub- exchanger and cation exchanger；And anion exchanger is connected with the delivery port of active carbon filter, while there is anion
Exchanger and cation exchanger can more fully remove the harmful substance in waste water, the disposal ability of ion exchange resin
Greatly, applied range, capacity is high, can remove a variety of ions, can be used with repeated regeneration, long working life, running cost
With relatively low.The other parts of the present embodiment are identical with above-described embodiment, repeat no more here.
Embodiment 5：
The present embodiment further limits anion exchanger and cation exchanger on the basis of above-described embodiment, described
Cationic ion-exchange resin is formed by Jing sulfuric acid sulfonations after styrene and divinylbenzene polymerization, can adsorb harmful in waste water
Cation；Anion exchange resin is containing belonging to alkaline quaternary ammonium group-N (CH3) 3OH groups resin, in waste water be harmful to
Anion (such as cryanide ion, thiocyanate ion) can be by quaternary ammonium group-N (CH3) 3OH groups resin adsorption removing.This reality
The other parts for applying example are identical with above-described embodiment, repeat no more here.
Embodiment 6：
The present embodiment further limits anion exchanger and cation exchanger on the basis of above-described embodiment, described
Cationic ion-exchange resin and anion exchange resin are spherical, and its size is about 0.5～1.0mm, spherical resin and waste water
Contact area it is big, be more beneficial for the absorption of harmful zwitterion.The other parts of the present embodiment are identical with above-described embodiment,
Here repeat no more.
The above, is only preferred embodiment of the present utility model, and any pro forma limit is not done to the utility model
System, every any simple modification, equivalent variations made to above example according to technical spirit of the present utility model each fall within
Protection domain of the present utility model.
Claims (6)
1. a kind of sewage recovering system of water-jet loom, it is characterised in that including the wastewater discharge pipe, flocculation sediment that are sequentially communicated
Pond, flotation tank, ion-exchanger and recycle-water delivery pipe；Also include being collected with the waste residue that flocculation sedimentation tank and flotation tank are all connected with
Pond；Screen pack A and oil interceptor are provided between wastewater discharge pipe and flocculation sedimentation tank；Waste residue collecting pit is connected with filter press.
2. the sewage recovering system of a kind of water-jet loom according to claim 1, it is characterised in that：The flocculation sedimentation tank
Screen pack B is provided with and flotation tank between.
3. the sewage recovering system of a kind of water-jet loom according to claim 1, it is characterised in that：Flotation tank and activated carbon
Mechanical filter is provided between filter, mechanical filter is connected with waste residue collecting pit.
4. the sewage recovering system of a kind of water-jet loom according to claim 1-3 any one, it is characterised in that：It is described
Ion-exchanger includes anion exchanger and cation exchanger；And the delivery port of anion exchanger and active carbon filter
Connection.
5. the sewage recovering system of a kind of water-jet loom according to claim 4, it is characterised in that：The cation exchange
Resin is formed by Jing sulfuric acid sulfonations after styrene and divinylbenzene polymerization；Anion exchange resin is containing quaternary ammonium group-N (CH)
The resin of 3OH groups.
6. the sewage recovering system of a kind of water-jet loom according to claim 5, it is characterised in that：The cation exchange
Resin and anion exchange resin are spherical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620988402.1U CN206127009U (en) | 2016-08-30 | 2016-08-30 | Hydraulic loom's waste water recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620988402.1U CN206127009U (en) | 2016-08-30 | 2016-08-30 | Hydraulic loom's waste water recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206127009U true CN206127009U (en) | 2017-04-26 |
Family
ID=58566860
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620988402.1U Expired - Fee Related CN206127009U (en) | 2016-08-30 | 2016-08-30 | Hydraulic loom's waste water recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206127009U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108147492A (en) * | 2017-11-24 | 2018-06-12 | 南京悠谷新材料科技有限公司 | Domestic sewage treatment device |
-
2016
- 2016-08-30 CN CN201620988402.1U patent/CN206127009U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108147492A (en) * | 2017-11-24 | 2018-06-12 | 南京悠谷新材料科技有限公司 | Domestic sewage treatment device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104609605B (en) | Device and method for realizing printing and dyeing dyed wastewater reuse and dye recovery | |
| CN104129831B (en) | Method for simultaneous removal and recovery of heavy metal ions and organic acid by using chelating resin | |
| CN103086545A (en) | Method and device for removing and recovering heavy metal in waste water through regenerated active carbon | |
| CN106732825A (en) | A kind of waste denitration catalyst renovation process and its regeneration liquid waste utilization process | |
| CN204550270U (en) | Wastewater from car washer cyclically utilizing treatment facility | |
| CN102092877B (en) | System for comprehensively recycling waste water | |
| CN206127009U (en) | Hydraulic loom's waste water recovery system | |
| CN100400427C (en) | Process of treating and utilizing acid waste water containing heavy metal | |
| CN207581613U (en) | Water recovery device in a kind of dyeing waste water | |
| CN206915894U (en) | High zero release equipment who contains salt waste water treatment | |
| CN204981379U (en) | Sewage treatment filter equipment based on metal film | |
| CN212076637U (en) | Water softening equipment regeneration waste water classification recovery system | |
| CN204897590U (en) | Desulfurization waste water zero release processing system | |
| CN110372125B (en) | Difficult metal ion integrated processing device that gets rid of in waste water | |
| CN203754528U (en) | Device for treating waste water during production of glass | |
| CN207838467U (en) | A kind of cleaning equipment for realizing solid-liquid concentration, separation | |
| CN206666268U (en) | Water circulation processing system for plate making | |
| CN206447683U (en) | A kind of coal chemical industry sewage processing unit | |
| CN220684775U (en) | Underground water source area organic pollution remove device based on ion exchange | |
| CN219752085U (en) | Intermittent type formula ink machine washs waste water recovery processing system | |
| CN206814550U (en) | A kind of efficient waste water reclaiming device | |
| CN105668849B (en) | A kind of ink jet printing waste liquid preprocess method and device | |
| CN114988520B (en) | Process for efficiently recycling acid and salt by utilizing modified special resin | |
| CN210287000U (en) | Nickel-containing wastewater treatment equipment | |
| CN218665664U (en) | Acidic cleaning water recycling system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20170426 Termination date: 20180830 |