CN205275374U - Smelly oxidation treatment of catalysis printing and dyeing sewage equipment - Google Patents
Smelly oxidation treatment of catalysis printing and dyeing sewage equipment Download PDFInfo
- Publication number
- CN205275374U CN205275374U CN201520806683.XU CN201520806683U CN205275374U CN 205275374 U CN205275374 U CN 205275374U CN 201520806683 U CN201520806683 U CN 201520806683U CN 205275374 U CN205275374 U CN 205275374U
- Authority
- CN
- China
- Prior art keywords
- tank
- fixed
- catalytic oxidation
- jar
- connecting tube
- 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 Oxidation Or Reduction (AREA)
Abstract
The utility model discloses a smelly oxidation treatment of catalysis printing and dyeing sewage equipment, including waste water import and grid well, the inner chamber of grid well is fixed with slope grid board, the right side of grid well is connected with the one end of water pump, the other end and the left side of flocculation jar of water pump are connected, the inner wall left and right sides of flocculation jar is fixed with positive electrode and negative electrode respectively, and still is fixed with the air membrane between negative electrode and the positive electrode, the right side of flocculation jar and the left side that pH adjusted the jar are connected, the inner chamber that pH adjusted the jar is provided with the pH tester, the top of pH regulation jar is passed through the solenoid valve and is connected with the doser, the right -hand member of pH regulation jar passes through the connecting pipe and is connected with the left side of catalytic oxidation jar, the catalytic oxidation jar passes through the connecting pipe to be connected with the upper left side of sedimentation tank, and the right downside of sedimentation tank still is fixed with the treated water outlet. This effluent treatment plant simple structure can effectual improvement waste water treatment efficiency and quality.
Description
Technical field
This utility model relates to technical field of sewage, is specially a kind of catalytic ozonation and processes dyeing and printing sewage equipment.
Background technology
Dyeing waste water is mainly derived from dye and dye intermediate production industry, by the material run off in various products and the mother solution of intermediate crystallization, production process and wash away the sewage etc. on ground and form. Discharging desized wastewater, boiled-off waste water, bleaching effluent and mercerizing waste water at pretreatment stage, dyeing process discharges dyeing waste-water, and revenue stamp process discharges printing waste water and soap lye waste water, and arranging process then discharges arrangement waste water. The composite waste of all kinds of waste water above, or the comprehensive wastewater except bleaching effluent is usually said dyeing and printing sewage. Because of each printing and dyeing mill produce material, produce kind, production technology, management level different, dyeing waste water water quality is separated with difference.
Along with developing rapidly of dye industry, New-type adjuvant, dyestuff, finishing agent etc. are widely used in dyeing so that it is difficult degradation, toxic component content also get more and more. Some or even Organic substance carcinogenic, mutagenic, to the threat of environment especially water environment with endanger increasing. And traditional dyeing and printing sewage processes equipment and cannot meet the modern times and purify water standard so that conventional waste water processes the sewage quality after equipment processes or very poor.
Utility model content
The purpose of this utility model is in that to provide a kind of catalytic ozonation to process dyeing and printing sewage equipment, with the problem solving to propose in above-mentioned background technology.
For achieving the above object, this utility model provides following technical scheme: a kind of catalytic ozonation processes dyeing and printing sewage equipment, including waste water inlet and grille well, described waste water inlet is positioned at the upper left side of grille well, the inner chamber of described grille well is fixed with inclination flase floor, the right side of described grille well is connected with one end of water pump by connecting tube, the other end of described water pump is connected by the left side of connecting tube with flocculation tank, the inwall left and right sides of described flocculation tank is respectively fixed with anelectrode and negative electrode, and between negative electrode and anelectrode, it is further fixed on air film, the right side of described flocculation tank is connected with the left side of pH regulator tank by connecting tube, described PH regulates the inner chamber of tank and is provided with pH tester, the top of described pH regulator tank is connected with electromagnetic valve cooperation and drug feeding device by connecting tube, and electromagnetic valve and pH tester are electrically connected, the right-hand member of described pH regulator tank is connected with the left side of catalytic oxidation tank by connecting tube, the lower left side of described catalytic oxidation tank and lower right side are respectively arranged with ozone inlet and go out water ring, described ozone inlet is connected with control valve cooperation and ozonator by connecting tube, the intracavity bottom of described catalytic oxidation tank is separated with air chamber by air inlet porous plate, the inner chamber top of described catalytic oxidation tank is further fixed on into water porous plate, it is fixed with activated carbon packed layer between described water inlet porous plate and air inlet porous plate, the upper left side of described catalytic oxidation tank and upper right side are also respectively provided with water inlet and offgas outlet, described catalytic oxidation tank is connected with the upper left side of sedimentation tank by connecting tube, and the lower right side of sedimentation tank is further fixed on treated water outlet.
Preferably, described inclination flase floor is fixed be connected by the mode of clamping or pin connection and the inwall of grille well, and the angle of inclination tilting flase floor is 30 to 45 degree.
Preferably, described catalytic oxidation tank is cylindrical, and air inlet porous plate is socketed in out on water ring.
Preferably, described air film is diametrically the cavernous structure of 0.05 to 0.1 millimeter, and air film is fixed on the inwall of flocculation tank by clamping or the mode that is spirally connected.
Compared with prior art, the beneficial effects of the utility model are: it is simple that this catalytic ozonation processes dyeing and printing sewage device structure, by with activated carbon packed layer for carrier, adopt the method for wastewater treatment of catalytic ozonation, make wastewater treatment efficiency better, the pollutant of macromole high stability of can degrading, and adopt socket joint type go out water ring and air inlet porous plate, make catalytic ozonation reaction more thorough, improve purification rate, and, by cooperating of drug feeding device and pH tester, can effectively regulate the acid-base value in waste water, ensure the carrying out normally and efficiently of follow-up catalytic oxidation.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation;
Fig. 2 is this utility model catalytic oxidation jar structure schematic diagram;
Fig. 3 is this utility model catalytic oxidation tank top view.
In figure: 1 waste water inlet, 2 grille wells, 21 tilt flase floors, 3 water pumps, 4 flocculation tanks, 41 negative electrodes, 42 anelectrodes, 43 air films, 5pH regulate tank, 51pH tester, 6 drug feeding devices, 61 electromagnetic valves, 7 catalytic oxidation tanks, 71 ozone inlet, 72 go out water ring, 73 air inlet porous plates, 74 air chambers, 75 water inlet porous plates, 76 activated carbon packed layers, 77 water inlets, 78 offgas outlet, 8 ozonators, 81 control valve, 9 sedimentation tanks, 10 treated water outlets.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is clearly and completely described, it is clear that described embodiment is only a part of embodiment of this utility model, rather than whole embodiments. Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art obtain under not making creative work premise, broadly fall into the scope of this utility model protection.
Refer to Fig. 1-3, this utility model provides a kind of technical scheme: a kind of catalytic ozonation processes dyeing and printing sewage equipment, including waste water inlet 1 and grille well 2, waste water effectively can be carried out pretreatment by grille well 2, filter the large particulate matter in waste water or other impurity, waste water inlet 1 is positioned at the upper left side of grille well 2, the inner chamber of grille well 2 is fixed with inclination flase floor 21, tilt flase floor 21 to fix be connected by the mode of clamping or pin connection and the inwall of grille well 2, and the angle of inclination tilting flase floor 21 is 30 to 45 degree, tilt clapboard 21 can make filter effect more preferably, and raising filters speed, the right side of grille well 2 is connected with one end of water pump 3 by connecting tube, the other end of water pump 3 is connected by the left side of connecting tube with flocculation tank 4, the inwall left and right sides of flocculation tank 4 is respectively fixed with anelectrode 42 and negative electrode 41, and between negative electrode 41 and anelectrode 42, it is further fixed on air film 43, air film 43 is diametrically the cavernous structure of 0.05 to 0.1 millimeter, and air film 43 is fixed on the inwall of flocculation tank 4 by clamping or the mode that is spirally connected, by adopting electricity flocculence, anelectrode 42 is utilized to coordinate with negative electrode 41, it is carried out electricity flocculation treatment, can effectively decompose the partial contamination thing filtered in waste water, make water treatment effect better, the right side of flocculation tank 4 is connected with the left side of pH regulator tank 5 by connecting tube, the inner chamber of pH regulator tank 5 is provided with PH tester 51, the top of pH regulator tank 5 is connected with electromagnetic valve 61 cooperation and drug feeding device 6 by connecting tube, and electromagnetic valve 61 is electrically connected with pH tester 51, by cooperating of electromagnetic valve on drug feeding device 6 61 and pH tester 51, can effectively control the acid-base value of waste water, a good environment is provided for follow-up oxidation catalysis reaction, ensure subsequent reactions carrying out normally and efficiently, the right-hand member of pH regulator tank 5 is connected with the left side of catalytic oxidation tank 7 by connecting tube, the lower left side of catalytic oxidation tank 7 and lower right side are respectively arranged with ozone inlet 71 and go out water ring 72, ozone inlet 71 is connected with control valve 81 cooperation and ozonator 8 by connecting tube, the intracavity bottom of catalytic oxidation tank 7 is separated with air chamber 74 by air inlet porous plate 73, the inner chamber top of catalytic oxidation tank 7 is further fixed on into water porous plate 75, it is fixed with activated carbon packed layer 76 between water inlet porous plate 75 and air inlet porous plate 73, catalytic oxidation tank 7 is cylindrical, and air inlet porous plate 73 is socketed in out on water ring 72, the upper left side of catalytic oxidation tank 7 and upper right side are also respectively provided with water inlet 77 and offgas outlet 78, by with activated carbon packed layer 76 for carrier, adopt the method for wastewater treatment of catalytic ozonation, make wastewater treatment efficiency better, the pollutant of macromole high stability of can degrading, and adopt socket joint type go out water ring 72 and air inlet porous plate 73, make catalytic ozonation reaction more thorough, improve purification rate, catalytic oxidation tank 7 is connected with the upper left side of sedimentation tank 9 by connecting tube, and the lower right side of sedimentation tank 9 is further fixed on treated water outlet 10.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art, being appreciated that when without departing from principle of the present utility model and spirit and these embodiments can be carried out multiple change, amendment, replacement and modification, scope of the present utility model is defined by the appended claims and the equivalents thereof.
Claims (4)
1. a catalytic ozonation processes dyeing and printing sewage equipment, including waste water inlet (1) and grille well (2), it is characterized in that: described waste water inlet (1) is positioned at the upper left side of grille well (2), the inner chamber of described grille well (2) is fixed with inclination flase floor (21), the right side of described grille well (2) is connected with one end of water pump (3) by connecting tube, the other end of described water pump (3) is connected by the left side of connecting tube with flocculation tank (4), the inwall left and right sides of described flocculation tank (4) is respectively fixed with anelectrode (42) and negative electrode (41), and between negative electrode (41) and anelectrode (42), it is further fixed on air film (43), the right side of described flocculation tank (4) is connected with the left side of pH regulator tank (5) by connecting tube, the inner chamber of described pH regulator tank (5) is provided with pH tester (51), the top of described pH regulator tank (5) is connected with electromagnetic valve (61) cooperation and drug feeding device (6) by connecting tube, and electromagnetic valve (61) is electrically connected with pH tester (51), the right-hand member of described pH regulator tank (5) is connected with the left side of catalytic oxidation tank (7) by connecting tube, the lower left side of described catalytic oxidation tank (7) and lower right side are respectively arranged with ozone inlet (71) and go out water ring (72), described ozone inlet (71) is connected with control valve (81) cooperation and ozonator (8) by connecting tube, the intracavity bottom of described catalytic oxidation tank (7) is separated with air chamber (74) by air inlet porous plate (73), the inner chamber top of described catalytic oxidation tank (7) is further fixed on into water porous plate (75), it is fixed with activated carbon packed layer (76) between described water inlet porous plate (75) and air inlet porous plate (73), the upper left side of described catalytic oxidation tank (7) and upper right side are also respectively provided with water inlet (77) and offgas outlet (78), described catalytic oxidation tank (7) is connected by the upper left side of connecting tube with sedimentation tank (9), and the lower right side of sedimentation tank (9) is further fixed on treated water outlet (10).
2. a kind of catalytic ozonation according to claim 1 processes dyeing and printing sewage equipment, it is characterized in that: described inclination flase floor (21) is fixed be connected by the mode of clamping or pin connection and the inwall of grille well (2), and the angle of inclination tilting flase floor (21) is 30 to 45 degree.
3. a kind of catalytic ozonation according to claim 1 processes dyeing and printing sewage equipment, it is characterised in that: described catalytic oxidation tank (7) is cylindrical, and air inlet porous plate (73) is socketed in out on water ring (72).
4. a kind of catalytic ozonation according to claim 1 processes dyeing and printing sewage equipment, it is characterized in that: described air film (43) is diametrically the cavernous structure of 0.05 to 0.1 millimeter, and air film (43) is fixed on the inwall of flocculation tank (4) by clamping or the mode that is spirally connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520806683.XU CN205275374U (en) | 2015-10-19 | 2015-10-19 | Smelly oxidation treatment of catalysis printing and dyeing sewage equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520806683.XU CN205275374U (en) | 2015-10-19 | 2015-10-19 | Smelly oxidation treatment of catalysis printing and dyeing sewage equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205275374U true CN205275374U (en) | 2016-06-01 |
Family
ID=56059967
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520806683.XU Expired - Fee Related CN205275374U (en) | 2015-10-19 | 2015-10-19 | Smelly oxidation treatment of catalysis printing and dyeing sewage equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205275374U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110902877A (en) * | 2019-11-27 | 2020-03-24 | 富彤化学有限公司 | Chemical sewage treatment device with multi-stage treatment function |
| CN116462306A (en) * | 2023-05-30 | 2023-07-21 | 中科鑫水源江苏环境科技有限公司 | Catalytic oxidation treatment device and method for printing and dyeing wastewater |
-
2015
- 2015-10-19 CN CN201520806683.XU patent/CN205275374U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110902877A (en) * | 2019-11-27 | 2020-03-24 | 富彤化学有限公司 | Chemical sewage treatment device with multi-stage treatment function |
| CN116462306A (en) * | 2023-05-30 | 2023-07-21 | 中科鑫水源江苏环境科技有限公司 | Catalytic oxidation treatment device and method for printing and dyeing wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106517608B (en) | A kind of preprocess method of high concentration organism P wastewater | |
| CN203144227U (en) | Integrated device for multi-level oxidation treatment of refractory wastewater | |
| CN105253964B (en) | A kind of iron is aerated photocatalysis organic wastewater degraded device | |
| KR100843656B1 (en) | Advanced drinking water treatment system using two-stage submerged membranes | |
| CN106746078B (en) | A kind of pretreatment unit of high concentration organism P wastewater | |
| CN210287029U (en) | Waste water treatment device for production workshop | |
| CN205275374U (en) | Smelly oxidation treatment of catalysis printing and dyeing sewage equipment | |
| CN107285524A (en) | A kind of efficient deeply treating wastewater method and device of coupling type heterogeneous catalysis ozone | |
| CN106915840A (en) | A kind of integrated refractory wastewater and reclamation set and sewage water treatment method | |
| CN202751857U (en) | Sewage filtering device | |
| CN207330484U (en) | A kind of efficient deeply treating wastewater device of coupling type heterogeneous catalysis ozone | |
| CN206359358U (en) | Dye waste water treatment system | |
| CN214115164U (en) | Waste water treatment equipment for circulating water tank of spray tower | |
| CN208964680U (en) | Advanced treatment apparatus for printing and dyeing wastewater | |
| CN202390271U (en) | Electronic control integrated purifier device for electronic flocculation | |
| CN108793592B (en) | Industrial sewage treatment system | |
| CN207294435U (en) | Advanced oxidation bi-membrane method wastewater reusing device | |
| CN206751617U (en) | A kind of groundwater remediation processing system | |
| CN207748988U (en) | A kind of chemical engineering sewage processing unit | |
| CN205990323U (en) | The micro-nano bubble of novel ozone and multi-medium filtering comprehensive water treatment device | |
| CN212293176U (en) | Water supply device of reverse osmosis water treatment device | |
| CN105540952B (en) | Murexide waste water treatment process | |
| CN220056575U (en) | Tobacco waste water treatment device | |
| CN220149356U (en) | Electroplating comprehensive wastewater COD treatment device | |
| CN211871630U (en) | Coal chemical industry waste water salinity draws equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 310000 Zhejiang Hangzhou Binjiang District Changhe street Jianghan Road 1785 new Shuangcheng Building 1 701 room. Patentee after: ZHEJIANG HENGTIAN FANTENG TECHNOLOGY CO.,LTD. Address before: 310000 Zhejiang Hangzhou Binjiang District Changhe street Jianghan Road 1785 new Shuangcheng Building 1 701 room. Patentee before: HANGZHOU PHANTOM TECHNOLOGY CO.,LTD. Address after: 310000 Zhejiang Hangzhou Binjiang District Changhe street Jianghan Road 1785 new Shuangcheng Building 1 701 room. Patentee after: HANGZHOU PHANTOM TECHNOLOGY CO.,LTD. Address before: 310000 Zhejiang Hangzhou Binjiang District Changhe street Jianghan Road 1785 new Shuangcheng Building 1 701 room. Patentee before: HANGZHOU PHANTOM TECHNOLOGY CO.,LTD. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160601 Termination date: 20191019 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |