CN104098159A - Spiral liquid multistage layer eco-friendly intelligent printing and dyeing water treatment device - Google Patents
Spiral liquid multistage layer eco-friendly intelligent printing and dyeing water treatment device Download PDFInfo
- Publication number
- CN104098159A CN104098159A CN201310114725.9A CN201310114725A CN104098159A CN 104098159 A CN104098159 A CN 104098159A CN 201310114725 A CN201310114725 A CN 201310114725A CN 104098159 A CN104098159 A CN 104098159A
- Authority
- CN
- China
- Prior art keywords
- spiral liquid
- electrolytic
- water treatment
- treatment device
- intelligent printing
- 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.)
- Granted
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 49
- 239000007788 liquid Substances 0.000 title claims abstract description 43
- 238000004043 dyeing Methods 0.000 title claims abstract description 26
- 238000007639 printing Methods 0.000 title claims abstract description 26
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 27
- 230000003647 oxidation Effects 0.000 claims abstract description 24
- 239000010865 sewage Substances 0.000 claims abstract description 17
- 238000004140 cleaning Methods 0.000 claims description 63
- 230000008676 import Effects 0.000 claims description 13
- 150000001875 compounds Chemical class 0.000 claims description 11
- 238000012856 packing Methods 0.000 claims description 5
- 230000009471 action Effects 0.000 claims description 4
- 230000005540 biological transmission Effects 0.000 claims description 3
- 239000002689 soil Substances 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 12
- 238000000746 purification Methods 0.000 abstract description 11
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 230000001954 sterilising effect Effects 0.000 abstract description 5
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 5
- 238000005516 engineering process Methods 0.000 abstract description 4
- 238000001035 drying Methods 0.000 abstract description 2
- 125000004122 cyclic group Chemical group 0.000 abstract 1
- 238000000034 method Methods 0.000 description 11
- 239000007789 gas Substances 0.000 description 10
- 230000008569 process Effects 0.000 description 9
- 239000000126 substance Substances 0.000 description 6
- 238000010521 absorption reaction Methods 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 238000001816 cooling Methods 0.000 description 4
- 238000005868 electrolysis reaction Methods 0.000 description 4
- 238000006722 reduction reaction Methods 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 230000015556 catabolic process Effects 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 230000002000 scavenging effect Effects 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000005202 decontamination Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 231100001240 inorganic pollutant Toxicity 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- VXAUWWUXCIMFIM-UHFFFAOYSA-M aluminum;oxygen(2-);hydroxide Chemical compound [OH-].[O-2].[Al+3] VXAUWWUXCIMFIM-UHFFFAOYSA-M 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- JYYOBHFYCIDXHH-UHFFFAOYSA-N carbonic acid;hydrate Chemical compound O.OC(O)=O JYYOBHFYCIDXHH-UHFFFAOYSA-N 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000007770 graphite material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- -1 hydrogen ions Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000005405 multipole Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- AHKZTVQIVOEVFO-UHFFFAOYSA-N oxide(2-) Chemical compound [O-2] AHKZTVQIVOEVFO-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses a spiral liquid multistage layer eco-friendly intelligent printing and dyeing water treatment device. The spiral liquid multistage layer eco-friendly intelligent printing and dyeing water treatment device comprises an electrolytic purification tower or an electrolytic purification tower system comprising more than two electrolytic purification towers connected in series. An inlet of the bottom of an electrolytic oxidation tower or the electrolytic purification tower system is connected to an electrolytic cell by a pipe, the pipe is provided with a valve and a flowmeter, the inlet of the electrolytic oxidation tower or the electrolytic purification tower system is connected to an oxide generation device by a pipe, the top of the electrolytic purification tower or the electrolytic purification tower system is connected to a spiral liquid separator, the bottom of the spiral liquid separator is connected to a dirt pipe and a dirt drying tank, and the top of the spiral liquid separator is communicated with a filter. The spiral liquid multistage layer eco-friendly intelligent printing and dyeing water treatment device prevents secondary pollution in the whole reaction process, has thorough sterilization effects, is not limited by environment conditions, can realize effective electrolytic purification treatment on various sewage, can be used conveniently and flexibly, can be used individually to realize sewage discharge satisfying the standard and can be combined with other water treatment unit technologies to realize sewage cyclic utilization and zero discharge.
Description
Technical field
The present invention relates to a kind of water treatment field, especially utilize electrochemical treatment printing and dyeing water treatment device.
Background technology
, there is technological line length, complex structure, equipment is many, functional efficiency is low, floor space is large, invest large shortcoming in traditional printing and dyeing water treatment device.And complex structure, is difficult for installation and maintenance, work-ing life is short, and in whole reaction process, the poisonous machine thing of hard degradation or inorganic pollutant are oxidized to innoxious substance, and thoroughly sterilization is subject to the envrionment conditions restriction impact that adjusting changes as harsh climate.
Summary of the invention
In view of this, the technical problem to be solved in the present invention is to provide the multistage layer of a kind of spiral liquid environment-protecting intelligent printing and dyeing water treatment device, and electrolytic cleaning is disposed of sewage, and realizes the qualified discharge of sewage.
For solving the problems of the technologies described above, technical scheme of the present invention is achieved in that the multistage layer of spiral liquid environment-protecting intelligent printing and dyeing water treatment device, comprise an electrolytic cleaning tower or two above electrolytic cleaning tower electrolytic cleaning tower groups in series, the bottom inlet of electrolytic oxidation tower or electrolytic cleaning tower group is connected with electrolyzer by pipeline, and on this pipeline, be provided with valve and under meter, should or the import of electrolytic cleaning tower group also by pipeline, be connected with oxide compound generating unit, the top of electrolytic cleaning tower or electrolytic cleaning tower group is connected with spiral liquid flow separator, the bottom of this spiral liquid flow separator is connected with dirt loft drier with soil pipe, the top of this spiral liquid flow separator is communicated with strainer.
Further, described electrolytic cleaning tower inner bottom part is provided with spiral propeller, and under powered, sewage from bottom to top arrives the top of tower through multistage layer electrode, flow guiding disc, packing layer.
Further, electrolytic oxidation thing generating unit can arrange one or more, and its inside is fixed with respectively mini air pump, micro pump or minipump, and is electrically connected to the action button in being located at machine shell panel.
Further, between a plurality of electrolytic oxidation thing generating units, by water pipe, be connected, respectively by volume pump under sensor and electronically controlled timely and appropriate discovery in most electrolytic cleaning towers.
Further, in described electrolytic oxidation thing generating unit, be fixed with electrode slice, electrode slice is consisted of netted, the tabular or membranaceous anode of multi-disc and negative electrode serial or parallel connection.
Further, in described cast electrolyzer, be fixed with the negative electrode and positive electrode that multi-disc is netted, plate electrode plate serial or parallel connection forms.
Further, the multistage layer of described spiral liquid environment-protecting intelligent printing and dyeing water treatment device also comprises electronic system and the coupled panel computer for real-time Transmission information, operation.
The technique effect that the present invention reaches is as follows: the process that electric energy of the present invention and chemical energy transform mutually.Two electrodes have chemical reaction to occur directly in conducting process, produce the intermediate product that has strong oxidation under the effect of indirect oxidation reduction reaction anodic reaction, for toxic organic compound or the inorganic pollutant of hard degradation, are oxidized to innoxious substance.In whole reaction process, non-secondary pollution and sterilization are thorough, particularly be not subject to the impact of envrionment conditions restriction as the variation of harsh climate condition etc., electrolytic cleaning is processed various sewage very effectively, easy to use and flexible, can be used alone and realize the qualified discharge of sewage, also can with other unit for treating water technical combinations, realize recycle and the zero release thereof of sewage.Be not subject to the restriction of temperature environment condition, can in normal temperature and pressure environment, carry out.Anodic oxidation, cathodic reduction reaction generation oxide water solution can supply water to process and use.Under the configuration of sensor and electronically controlled and 3G panel computer, realize accurate safe and intelligentization operation.The advantages such as equipment is simple, rational in infrastructure, operational path is short, floor space is little, less investment is fast.
Accompanying drawing explanation
Fig. 1 is the multistage layer of the spiral liquid environment-protecting intelligent printing and dyeing water treatment device setting that is provided with 3 electrolytic cleaning towers and oxide compound generating unit;
Fig. 2 is the multistage layer of the spiral liquid environment-protecting intelligent printing and dyeing water treatment device setting that is provided with 2 electrolytic cleaning towers and oxide compound generating unit;
Fig. 3 is the multistage layer of the spiral liquid environment-protecting intelligent printing and dyeing water treatment device setting that is provided with 1 electrolytic cleaning tower and oxide compound generating unit;
Fig. 4 is the process flow sheet of the multistage layer of spiral liquid environment-protecting intelligent printing and dyeing water treatment device;
Fig. 5 is the structural representation of cast slot electrode;
Fig. 6 is the structural representation of flow guiding disc;
Fig. 7 is the sectional view at flow guiding disc A-A place in Fig. 5.
Embodiment
As shown in Figure 1, for the multistage layer of spiral liquid of the present invention environment-protecting intelligent printing and dyeing water treatment device, comprise an electrolytic cleaning tower or two above electrolytic cleaning tower electrolytic cleaning tower groups in series, the bottom inlet of electrolytic oxidation tower or electrolytic cleaning tower group is connected with electrolyzer by pipeline, and on this pipeline, be provided with valve and under meter, should or the import of electrolytic cleaning tower group also by pipeline, be connected with oxide compound generating unit, the top of electrolytic cleaning tower or electrolytic cleaning tower group is connected with spiral liquid flow separator, the bottom of this spiral liquid flow separator is connected with dirt loft drier with soil pipe, the top of this spiral liquid flow separator is communicated with strainer.Wherein, electrolytic cleaning tower group can have two-stage or three grades or more multistage, corresponding two-stage or three grades of being provided with of connected oxide compound generating unit simultaneously, and three grades of electrolytic cleaning tower groups and three s' the oxide compound generating unit of take below describes as example.
Dyeing and printing sewage is sent into tube type electrolytic tank 46, by manual valve 48, under meter 18 control flows, is entered successively the first electrolytic cleaning tower 1, the second electrolytic cleaning tower 102, the 3rd electrolytic cleaning tower 103 bottoms by water pump.The first oxide compound generating unit 15, the second oxide compound generating unit 16, trioxide generating unit 17 rear pipeline parallel with one another are connected with volume pump 3,301,302.Through sensor prosecution sewage quality, oxide solution is injected in the first electrolytic cleaning tower 1, the second electrolytic cleaning tower 102, the 3rd electrolytic cleaning tower 103 and is carried out electrolytic oxidation processing by volume pump 3,301,302.Under the effect of electric energy, chemical energy and kinetic energy, in water, dirt is oxidized rapidly, deoxidization, degradation is converted into innoxious substance, and dirt gathers by little increase under charge effect, is deposited in wastecan 25 at the bottom of tower, non-pollution discharge after the solid-state shape of dirt moisture eliminator 28.Sewage enters under the pushing effect of the first electrolytic cleaning tower 1 inner bottom part by spiral propeller 34, from bottom to top through multistage layer electrode 12, flow guiding disc 11, packing layer 54, arrive the top of tower, the gas producing in electrolytic acid cleaning oxydation process rising arrives gas absorption tank 26 through tower top cooling purifier 44 and carries out purifying treatment.The import of spiral liquid flow separator 21 is connected with the first electrolytic cleaning tower 1, the second electrolytic cleaning tower 102, the 3rd electrolytic cleaning tower 103 top outlet pneumavalves 46 respectively.Electrolytic cleaning water enters spiral liquid flow separator 21 precipitation separations by scavenging tower top through pneumavalve discharge, and wastecan 20 outlets are connected with 28 imports of dirt loft drier.Spiral liquid flow separator 21 top exits are connected with the second electrolytic cleaning tower 102 end import, by the second electrolytic cleaning tower 102 inner bottom parts under the pushing effect of spiral propeller 34, from bottom to top through multistage layer electrode 12, flow guiding disc 11, packing layer 54, arrive the top of tower, the gas producing in electrolytic acid cleaning oxydation process rises and arrives gas absorption tank 26 through tower top cooling purifier 44.Electrolytic cleaning water is discharged and is entered spiral liquid flow separator 21 precipitation separations through pneumavalve by scavenging tower top, and the outlet of wastecan 20 is connected with wastecan 20 imports of dirt loft drier 28 bottoms.The first electrolytic cleaning tower 1, the second electrolytic cleaning tower 102, the 3rd electrolytic cleaning tower 103 overhead gas outlets are connected with cooling purifier 44, gas absorption tank 26 imports.Gas absorption tank 26 outlets are connected with wastecan 25 imports, the water outlet of the 3rd electrolytic cleaning tower 103, spiral liquid flow separator 21 is connected with strainer 22,220 imports, strainer (22,220) top exit is connected with hold-up vessel 27 imports of purifying waste water, and strainer (22,220) bottom emissions mouth is connected with 28 imports of dirt loft drier.The second electrolytic cleaning tower 102 is connected with the 3rd electrolytic cleaning tower 103 bottom inlet through spiral liquid flow separator 21 top exits, under the promotion of spiral propeller 34, from bottom to top pass through multistage layer electrode 12, flow guiding disc 11, packing layer 54 arrives the top of tower, the gas producing in electrolytic acid cleaning oxydation process rises and arrives gas absorption tank 26 through tower top cooling purifier 44, electrolytic cleaning water is discharged and is entered spiral liquid flow separator 21 precipitation separations through pneumavalve by scavenging tower top, spiral liquid flow separator 21 bottoms, wastecan 20 is connected with 28 imports of dirt loft drier, the curing non-pollution discharge protection of the environment that reaches of dirt drying.Spiral liquid flow separator 21 top exits are connected with strainer 22,220, at the water purification filtering through multistage layer, enter water purification hold-up vessel and store or discharge or recycling.The present invention is applicable to printing and dyeing, papermaking, electric degree, hospital, industry and sanitary sewage disposal.
The first electrolytic oxidation thing generating unit 15, the second electrolytic oxidation thing generating unit 16, interior mini air pump, micro pump or the minipump of being fixed with respectively of the 3rd electrolytic oxidation thing generating unit 17, and be electrically connected to the action button in being located at machine shell panel, for increasing the oxygen content in device, also be fixed with miniature multipole water pump, in the same apparatus in parallel or the first electrolytic cleaning tower 1, the second electrolytic cleaning tower 102, the 3rd electrolytic cleaning tower 103 water fillings.
The multistage layer of spiral liquid environment-protecting intelligent printing and dyeing water treatment device also comprises electronic system 32 and coupled panel computer 30, panel computer 30 real-time Transmission information, and user can select to control according to sewage quality, automatic or manual operator scheme.
Between the first electrolytic oxidation thing generating unit 15, the second electrolytic oxidation thing generating unit 16, the 3rd electrolytic oxidation thing generating unit 17, by water pipe, be connected, by volume pump timely and appropriate discovery under sensor and electronically controlled, inject the first electrolytic cleaning tower 1, the second electrolytic cleaning tower 102 and the 3rd electrolytic cleaning tower 103 respectively.
In the second electrolytic oxidation thing generating unit 16, be provided with to be fixed with in electrode 161, the first electrolytic oxidation thing generating units 15 and in electrode slice 151, the 3rd electrolytic oxidation thing generating unit 17, be fixed with electrode slice 171 and by netted, the tabular or membranaceous anode of multi-disc and negative electrode serial or parallel connection, formed respectively.
In cast electrolyzer 46, be fixed with the negative electrode and positive electrode that or plate electrode plate serial or parallel connection netted by multi-disc forms respectively, in order to brine electrolysis.In the present embodiment, by three negative electrodes or multi-disc negative electrode and three anodes or multi-disc anode electrolysis plate, be formed in parallel, the material of electrolytic zinc-coated steel sheet is stainless steel plate, in addition, can also manufacture battery lead plate by copper, iron, nickel, titanium, platinum, cadmium, aluminium dioxide, electropaining layer, porous carbon, activated carbon, conductivity ceramics, conductive rubber or graphite material.Because cast electrolyzer 46 communicates with the first electrolytic cleaning tower 1 bottom, sewage is interior by electrolysis at electrolyzer 46, and the macromolecular mass of water is opened into individual molecule, and the inorganic salt compositions such as calcium wherein, magnesium, sodium and other organic impurity are carbonic acid gas and water by electrolysis.After separation, form throw out, electrode device 461,12,13 mechanisms of action are: in electrolytic process, ionogen produces the oxide ion aqueous solution and the abundant oxidizing reaction of sewage, produce and under gas explosion, air supporting campaign, make the rapid emulsification of dirt, expansion, oxidation, reduction, degraded, separated under the power of spiral propeller and the effect of chemical energy microkinetic.In the treatment system of purifying waste water, anode produces a large amount of positively charged ions (oxygen), colloid waste water is condensed, on negative electrode, separate out a large amount of hydrogen ions (hydrogen) microbubble adheres to each other with flocculation particulate matter simultaneously, by strength, promote floating, then by separator, ceaselessly miniature dirt separation is discharged to the heavy particle gathering free setting under the effect of gravity, throw out is processed discharge by the solid-state shape of dirt in time by percolating device, and its water purification can be recycled.Dirt and water thoroughly depart from; By electric appliance and electronic, automatically control, regulate the factors vary such as conductivity, pH value, temperature, water-soluble amount, concentration, bubbles volume, speed, adapt to the requirement purifying water, can high-level efficiency remove colourity, COD, BOD.Oxide compound plays redox, degraded, sterilization effect to organism in water; Under the effect of electric field, whole decontamination process is in non-secondary pollution under environmental friendliness all the time, can realize and really purify thoroughly dirt and sterilization, reaches the object of high-efficiency water-saving energy-saving and emission-reduction consumption reduction.
The present invention brings into play electrochemical techniques effectively, advances and is applied to water treatment field.Three-dimensional, continuously, industrialization and changed traditional old processing technology routine length, complex structure, equipment is many, functional efficiency is low, floor space is large, initial cost is large shortcoming, organically in conjunction with chemical engineering feature by purifying water treatment device three-dimensional, and design multitower and be integrated device, in long-term research and process of the test, accumulated rich experience.Decontamination effect improving significantly, high-efficiency water-saving, environmental protection and energy saving, intellectualized operation be subject to user's favorable comment and authentication deeply.
Rational in infrastructure, sturdy and durable, for ease of maintenaince, use that installation and maintenance are convenient, suitability for industrialized is produced.Selected accessory, material property are stable and be easy to dismounting and assembling, long service life, are convenient to safeguard.
The above, be only preferred embodiment of the present invention, is not intended to limit protection scope of the present invention.
Claims (7)
1. the multistage layer of spiral liquid environment-protecting intelligent printing and dyeing water treatment device, it is characterized in that, comprise an electrolytic cleaning tower or two above electrolytic cleaning tower electrolytic cleaning tower groups in series, the bottom inlet of electrolytic oxidation tower or electrolytic cleaning tower group is connected with electrolyzer by pipeline, and on this pipeline, be provided with valve and under meter, should or the import of electrolytic cleaning tower group also by pipeline, be connected with oxide compound generating unit, the top of electrolytic cleaning tower or electrolytic cleaning tower group is connected with spiral liquid flow separator, the bottom of this spiral liquid flow separator is connected with dirt loft drier with soil pipe, the top of this spiral liquid flow separator is communicated with strainer.
2. the multistage layer of spiral liquid as claimed in claim 1 environment-protecting intelligent printing and dyeing water treatment device, it is characterized in that, described electrolytic cleaning tower inner bottom part is provided with spiral propeller, and under powered, sewage from bottom to top arrives the top of tower through multistage layer electrode, flow guiding disc, packing layer.
3. the multistage layer of spiral liquid as claimed in claim 1 environment-protecting intelligent printing and dyeing water treatment device, it is characterized in that, electrolytic oxidation thing generating unit can arrange one or more, its inside is fixed with respectively mini air pump, micro pump or minipump, and is electrically connected to the action button in being located at machine shell panel.
4. the multistage layer of spiral liquid as claimed in claim 3 environment-protecting intelligent printing and dyeing water treatment device, it is characterized in that, between a plurality of electrolytic oxidation thing generating units, by water pipe, be connected, respectively by volume pump under sensor and electronically controlled timely and appropriate discovery in most electrolytic cleaning towers.
5. the multistage layer of spiral liquid as claimed in claim 3 environment-protecting intelligent printing and dyeing water treatment device, it is characterized in that, in described electrolytic oxidation thing generating unit, be fixed with electrode slice, electrode slice is consisted of netted, the tabular or membranaceous anode of multi-disc and negative electrode serial or parallel connection.
6. the multistage layer of spiral liquid as claimed in claim 1 environment-protecting intelligent printing and dyeing water treatment device, is characterized in that, is fixed with the negative electrode and positive electrode that multi-disc is netted, plate electrode plate serial or parallel connection forms in described cast electrolyzer.
7. the multistage layer of spiral liquid as claimed in claim 1 environment-protecting intelligent printing and dyeing water treatment device, it is characterized in that, the multistage layer of described spiral liquid environment-protecting intelligent printing and dyeing water treatment device also comprises electronic system and the coupled panel computer for real-time Transmission information, operation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310114725.9A CN104098159B (en) | 2013-04-03 | 2013-04-03 | Spiral liquid multistage layer environment-protecting intelligent printing and dyeing water treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310114725.9A CN104098159B (en) | 2013-04-03 | 2013-04-03 | Spiral liquid multistage layer environment-protecting intelligent printing and dyeing water treatment device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104098159A true CN104098159A (en) | 2014-10-15 |
| CN104098159B CN104098159B (en) | 2015-09-16 |
Family
ID=51666755
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310114725.9A Active CN104098159B (en) | 2013-04-03 | 2013-04-03 | Spiral liquid multistage layer environment-protecting intelligent printing and dyeing water treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104098159B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105177477A (en) * | 2015-09-03 | 2015-12-23 | 王文姣 | Efficient sewage treatment equipment |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005077831A1 (en) * | 2004-02-12 | 2005-08-25 | Denkai Giken Co. | Electrochemical water treatment method and device |
| CN101746857A (en) * | 2008-12-09 | 2010-06-23 | 欧洲水处理公司 | Method and equipment of electrochemical disinfection for water |
| CN101891324A (en) * | 2010-07-19 | 2010-11-24 | 江苏泽宇环境工程有限公司 | Wastewater electrolytic treatment system |
-
2013
- 2013-04-03 CN CN201310114725.9A patent/CN104098159B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005077831A1 (en) * | 2004-02-12 | 2005-08-25 | Denkai Giken Co. | Electrochemical water treatment method and device |
| CN101746857A (en) * | 2008-12-09 | 2010-06-23 | 欧洲水处理公司 | Method and equipment of electrochemical disinfection for water |
| CN101891324A (en) * | 2010-07-19 | 2010-11-24 | 江苏泽宇环境工程有限公司 | Wastewater electrolytic treatment system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105177477A (en) * | 2015-09-03 | 2015-12-23 | 王文姣 | Efficient sewage treatment equipment |
| CN105177477B (en) * | 2015-09-03 | 2017-12-08 | 盐城市兰丰环境工程科技有限公司 | Efficient sewage treatment installation |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104098159B (en) | 2015-09-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100494101C (en) | A photoelectromagnetic integrated wastewater advanced oxidation method and its device | |
| CN102936072B (en) | Nano-catalysis, electrolysis, flocculation and air-floatation device | |
| CN102774932B (en) | Method for Removing Wastewater COD and Ammonia Nitrogen Using Titanium-Based Lead Dioxide Composite Electrode | |
| CN101908634B (en) | Split type membraneless microbiological fuel cell | |
| CN105355950B (en) | A kind of macro-organism cathode microbial fuel cell stack device | |
| CN212102375U (en) | Electrochemical coupling treatment and reuse device for high-concentration organic wastewater in gas fields | |
| CN204607826U (en) | A kind of sludge ozone cracks reactor | |
| CN201971667U (en) | High-voltage pulsed electric coagulation equipment for treating organic wastewater | |
| CN202519115U (en) | Nano-catalysis, electrolysis, flocculation and air-floatation device | |
| CN104118966B (en) | The three-dimensional electric biological coupling water cleaning systems of a kind of air water anisotropic flow and process for purifying water | |
| CN110357226A (en) | A kind of method of Electrocatalytic Oxidation processing Polyester wastewater | |
| CN207861965U (en) | A kind of multistage out-phase three-dimensional electrochemical reaction unit for waste water treatment | |
| CN207904098U (en) | In conjunction with the organic wastewater treating system of Fenton technology and artificial swamp | |
| CN104098159B (en) | Spiral liquid multistage layer environment-protecting intelligent printing and dyeing water treatment device | |
| CN208648836U (en) | A kind of equipment of locellus processing of industrial waste water by electrolysis | |
| CN203922815U (en) | The micro-electrolyzer of three-dimensional electrocatalysis | |
| CN207498134U (en) | A kind of cylinder type electrode biomembrane reaction unit for handling organic stain disease | |
| CN101244854B (en) | Iron carbon micro electrolyser and method for processing ceramic phenol wastewater | |
| CN116655059A (en) | Wastewater treatment device and method for synchronously removing high-concentration heavy metals and sulfate radicals | |
| CN211111488U (en) | Oily waste water electro-catalytic treatment device | |
| CN203392970U (en) | Air dissolution and electrolysis integrated air floatation equipment | |
| CN101481158A (en) | Low-voltage electrochemical flocculation wastewater treatment device | |
| CN213924348U (en) | Electrochemical treatment device for salt-containing organic wastewater | |
| CN202193651U (en) | Electrolytic catalytic oxidation device | |
| CN217377627U (en) | Efficient landfill leachate preprocessing device and landfill leachate processing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220704 Address after: 222023 room 604, unit 1, building 7, Jianning Road, Haizhou District, Lianyungang City, Jiangsu Province Patentee after: Qian Mingqi Address before: 100101 room 1501, unit 4, building 1, Xuhui aodu, Lishui bridge, Chaoyang District, Beijing Patentee before: Qian Guangwan |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20221104 Address after: 513-34, Floor 5, Building 2, Yard 1, Hangfeng Road, Fengtai District, Beijing 100070 Patentee after: Beijing Yicheng Technology Co.,Ltd. Address before: 222023 room 604, unit 1, building 7, Jianning Road, Haizhou District, Lianyungang City, Jiangsu Province Patentee before: Qian Mingqi |
|
| TR01 | Transfer of patent right |