CN106904773A - A kind of dyeing waste water TRT - Google Patents
A kind of dyeing waste water TRT Download PDFInfo
- Publication number
- CN106904773A CN106904773A CN201710280853.9A CN201710280853A CN106904773A CN 106904773 A CN106904773 A CN 106904773A CN 201710280853 A CN201710280853 A CN 201710280853A CN 106904773 A CN106904773 A CN 106904773A
- Authority
- CN
- China
- Prior art keywords
- waste water
- chamber
- dyeing waste
- quartz sand
- saline slot
- 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.)
- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/16—Biochemical fuel cells, i.e. cells in which microorganisms function as catalysts
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Abstract
The present invention relates to a kind of dyeing waste water TRT, including quartz sand filtration chamber, waste water for generating electricity groove, flocculation chamber and activated carbon chamber.It is configured by waste water for generating electricity groove so that carry out the re-using that chemical energy is converted into electric energy according to the characteristics of dyeing waste water.In combination with to flocculate chamber transformation, and activated carbon chamber transformation so that on the basis for the treatment of of dyeing wastewater rate is improved significantly, moreover it is possible to produce a part of electric energy, reached maximally utilizing for waste.
Description
Technical field
The invention belongs to generation of electricity by new energy and field of waste water treatment, and in particular to a kind of dyeing waste water TRT.
Background technology
Current TRT is all that the energy of other forms is converted into electric energy, has heat energy, kinetic energy, potential energy, and incite somebody to action
The application that chemical energy is converted into electric energy is fewer.And galvanic principles are well-known principles, charging electricity is currently used primarily in
, also there are Many researchers in pond field being generated electricity using salt solution completely, but the preparation of salt solution also has certain cost,
And the generating efficiency of this generation mode is relatively low.
The treatment of dyeing waste water is all the time the difficult point in sewage disposal, and wherein salinity is very high, and COD is extremely difficult
Removal, bad decolouring, processing cost is very high, and how to find a kind of method of high-activity treatment of textile dye waste is field of waste water treatment
Attain problem to be solved.
The content of the invention
The present invention is by proposing a kind of dyeing waste water TRT.
Realized especially by following technological means:
A kind of dyeing waste water TRT, including quartz sand filtration chamber, waste water for generating electricity groove, flocculation chamber and activated carbon chamber.
Wherein quartz sand filtration chamber includes dyeing waste water entrance, quartz sand filtration cavity main body and distributive pipe road, the printing and dyeing
Waterwater entrance is incorporated into the quartz sand filtration cavity main body after dyeing waste water is pressurizeed, inside the quartz sand filtration cavity main body
Granular quartz sand is provided with, for removing water insoluble impurity in dyeing waste water, the distributive pipe road is used as quartz sand
The outlet of filter chamber, connection quartz sand main body one end is an entrance, and the one end for connecting waste water for generating electricity groove is that horizontal two go out
Mouthful.
The waste water for generating electricity groove includes the first saline slot, the second saline slot, salt bridge, first electrode, second electrode, electric energy storage
Can box, convex lens and convex lens mirror support.
First saline slot and the second saline slot horizontal Tile are set, will stream by two outlets in the distributive pipe road
First saline slot and second saline slot are injected separately into through the dyeing waste water in quartz sand filtration chamber, the salt bridge is
One saline slot is connected the two with the second saline slot top, and the first electrode is placed in first saline slot, institute
State second electrode to be placed in second saline slot, the first electrode and second electrode pass through wire and the electric energy energy storage
The electrical power input part connection of box, the electrical power storage that the electrical power input part is used to be produced between two electrodes is stored up in electric energy
In energy box;The convex lens are provided with two, are set up in first saline slot and second by two convex lens mirror supports respectively
Saline slot top.
The flocculation chamber includes flocculation chamber inlet duct, flocculation chamber enclosure, Flocculent plate and flocculation chamber outlet conduit, the wadding
Solidifying chamber inlet duct will flow through the first saline slot respectively and the dyeing waste water of the second saline slot is imported into flocculation chamber enclosure, described
Flocculent plate includes two pieces of copper coins and one piece of zine plate, and the zine plate is arranged at the centre of flocculation chamber enclosure, and two pieces of copper coins are arranged at two
End, and the chamber inlet duct that will flocculate is respectively arranged at the centre position of copper coin and zine plate, flocculation chamber outlet conduit with it is described
The entrance in activated carbon chamber is connected.
The activated carbon chamber is internally provided with the continuous activated carbon filter of multilayer, and the dyeing waste water after treatment is through making a living
Property charcoal chamber outlet outflow.
Preferably, flocculation chamber outlet conduit is contraction-like setting, it is wide opening near flocculation chamber side, near activity
Charcoal chamber side is slot.
Preferably, the copper coin and the equal longitudinal measure in zine plate both sides have non-crystaline amorphous metal bar, the non-crystaline amorphous metal bar
Material(Atomic ratio)It is Sr21Ca25Mg15Zn21La8Cu8B1。
Preferably, the salt bridge is internally provided with fixed many hole sizers, KCl solution is provided with many hole sizers.
Preferably, the convex lens are provided with two, first salt is set up in by two convex lens mirror supports respectively
Tank and the second saline slot top, and two convex lens are different from horizontal plane angle, and two convex lens are same with horizontal plane
Angular separation sum is 180 °.
Preferably, two convex lens are respectively 51 ° and 129 ° with horizontal plane same direction angle.
Preferably, the continuous activated carbon filter of multilayer that the activated carbon chamber inside is set is double-layer porous metal
Intralamellar part is provided with activated carbon granule.
Preferably, the granular quartz sand particle mean size that the quartz sand filtration cavity main body inside is set is 2 ~ 5mm,
The granular quartz sand surface is provided with loose structure.
Preferably, the copper coin and the equal longitudinal measure in zine plate both sides have non-crystaline amorphous metal bar, the non-crystaline amorphous metal bar
3 ~ 5 are provided with each copper coin, 5 ~ 8 are respectively arranged with zine plate both sides(It is more highly preferred to 6 ~ 8).
Effect of the invention is that:
1, salinity is higher in dyeing waste water, and the species of wherein salinity is very more, and the present invention is set to two grooves, makes
Galvanic cell, the purpose of generating is reached using wherein different salinities respectively as negative pole and positive pole(Although in two saline slots
Liquid component be substantially identical, but due to wherein containing many different salinities, therefore there is situation in Different electrodes
Under, wherein different salt in the first saline slot and in the second saline slot take part in reaction), although the electricity of generating is not very
It is many, but after being processed by galvanic cell, dyeing waste water is more prone to the removal decolourized with COD by ionization, sends
Electric energy exists as byproduct, while the byproduct is produced, improves treatment of dyeing wastewater efficiency, has reached the effect of doulbe-sides' victory
Really(If ionized to dyeing waste water using additional power source, need to increase considerably cost, and also safety problem
Consider, thus at present few people consider it ionize increase its ionization property, and the present invention as setting side
Formula solves above-mentioned two problems well).
2, there is provided flocculation chamber so that saline slot out after dyeing waste water again flocculate chamber in flocculated, by
Dyeing waste water in saline slot out be by ionization, therefore be very easy to flocculation.And by copper coin and zine plate table
A plurality of non-crystaline amorphous metal bar is provided with face, it is maximized useless to printing and dyeing in the space that non-crystaline amorphous metal bar and copper coin and zine plate are formed
Water carries out flocculation operation, has reached the effect of waste-water treatment efficient rate low cost.
3, the invention on saline slot top is provided with convex lens, and is set to differentiation to convex lens
(Angle is set each other so that worked when substantially different)So that sunshine(Or other light)From the irradiation of same direction
When on to convex lens, certain part in a saline slot can form local high temperature wherein, so as to cause salt solution
Temperature is uneven in groove, and local eddy currents are formed in saline slot, so as to heated in real-time both can be carried out to liquid in saline slot, may be used also
Strengthen liquid and flow to cause local eddy currents, strengthen power generation process.
Brief description of the drawings
Fig. 1 is the structural representation of waste water for generating electricity groove of the present invention.
Fig. 2 is the structural representation that dyeing waste water TRT of the present invention is overlooked.
Wherein:11- dyeing waste water entrances, 1- quartz sand filtrations chamber, 2- distributive pipes road, the saline slots of 31- first, 32- second
Saline slot, 33- salt bridges, 34- convex lens mirror supports, 35- convex lens, 36- electric energy energy storage boxes, 37- first electrodes, 38- second electrodes,
4- flocculations chamber, 41- flocculation chamber inlet ducts, 42- copper coins, 43- zine plates, 51- flocculation chamber outlet conduits, 5- activated carbons chamber, 52- lives
Property charcoal chamber outlet.
Specific embodiment
Embodiment 1
As depicted in figs. 1 and 2.
A kind of dyeing waste water TRT, including quartz sand filtration chamber, waste water for generating electricity groove, flocculation chamber and activated carbon chamber.
Wherein quartz sand filtration chamber includes dyeing waste water entrance, quartz sand filtration cavity main body and distributive pipe road, the printing and dyeing
Waterwater entrance is incorporated into the quartz sand filtration cavity main body after dyeing waste water is pressurizeed, inside the quartz sand filtration cavity main body
Granular quartz sand is provided with, for removing water insoluble impurity in dyeing waste water, the distributive pipe road is used as quartz sand
The outlet of filter chamber, connection quartz sand main body one end is an entrance, and the one end for connecting waste water for generating electricity groove is that horizontal two go out
Mouthful.
The waste water for generating electricity groove includes the first saline slot, the second saline slot, salt bridge, first electrode, second electrode, electric energy storage
Can box, convex lens and convex lens mirror support.
First saline slot and the second saline slot horizontal Tile are set, will stream by two outlets in the distributive pipe road
First saline slot and second saline slot are injected separately into through the dyeing waste water in quartz sand filtration chamber, the salt bridge is
One saline slot is connected the two with the second saline slot top, and the first electrode is placed in first saline slot, institute
State second electrode to be placed in second saline slot, the first electrode and second electrode pass through wire and the electric energy energy storage
The electrical power input part connection of box, the electrical power storage that the electrical power input part is used to be produced between two electrodes is stored up in electric energy
In energy box;The convex lens are provided with two, are set up in first saline slot and second by two convex lens mirror supports respectively
Saline slot top.
The flocculation chamber includes flocculation chamber inlet duct, flocculation chamber enclosure, Flocculent plate and flocculation chamber outlet conduit, the wadding
Solidifying chamber inlet duct will flow through the first saline slot respectively and the dyeing waste water of the second saline slot is imported into flocculation chamber enclosure, described
Flocculent plate includes two pieces of copper coins and one piece of zine plate, and the zine plate is arranged at the centre of flocculation chamber enclosure, and two pieces of copper coins are arranged at two
End, and the chamber inlet duct that will flocculate is respectively arranged at the centre position of copper coin and zine plate, flocculation chamber outlet conduit with it is described
The entrance in activated carbon chamber is connected.
Flocculation chamber outlet conduit is contraction-like setting, is wide opening near flocculation chamber side, near activated carbon chamber side
It is slot.
The activated carbon chamber is internally provided with the continuous activated carbon filter of multilayer, and the dyeing waste water after treatment is through making a living
Property charcoal chamber outlet outflow.
The copper coin and the equal longitudinal measure in zine plate both sides have non-crystaline amorphous metal bar, the material of the non-crystaline amorphous metal bar(It is former
Sub- ratio)It is Sr21Ca25Mg15Zn21La8Cu8B1。
The salt bridge is internally provided with fixed many hole sizers, and KCl solution is provided with many hole sizers.
The convex lens are provided with two, are set up in first saline slot and second by two convex lens mirror supports respectively
Saline slot top, and two convex lens are different from horizontal plane angle, two convex lens and the same angular separation of horizontal plane it
Be 180 °.
Two convex lens are respectively 51 ° and 129 ° with horizontal plane same direction angle.
The continuous activated carbon filter of multilayer that the activated carbon chamber inside is set is inside double-layer porous metallic plate and sets
It is equipped with activated carbon granule.
The granular quartz sand particle mean size that the quartz sand filtration cavity main body inside is set is 3mm, the graininess
Quartz sand surface be provided with loose structure.
The copper coin and the equal longitudinal measure in zine plate both sides have non-crystaline amorphous metal bar, and the non-crystaline amorphous metal bar is in each copper coin
On be provided with 3, be respectively arranged with 6 in zine plate both sides.
By detection, percent of decolourization of dyeing waste water is 98.2%, and averagely COD clearances are 91% first.
Comparative example 1
Other set-up modes of this comparative example were same as Example 1, and difference is to be not provided with convex lens, by 24 hours
After treatment, it is the 91% of embodiment 1 to measure probability of meeting water quality standard.
Embodiment 2
A kind of dyeing waste water TRT, including quartz sand filtration chamber, waste water for generating electricity groove, flocculation chamber and activated carbon chamber.
Wherein quartz sand filtration chamber includes dyeing waste water entrance, quartz sand filtration cavity main body and distributive pipe road, the printing and dyeing
Waterwater entrance is incorporated into the quartz sand filtration cavity main body after dyeing waste water is pressurizeed, inside the quartz sand filtration cavity main body
Granular quartz sand is provided with, for removing water insoluble impurity in dyeing waste water, the distributive pipe road is used as quartz sand
The outlet of filter chamber, connection quartz sand main body one end is an entrance, and the one end for connecting waste water for generating electricity groove is that horizontal two go out
Mouthful.
The waste water for generating electricity groove includes the first saline slot, the second saline slot, salt bridge, first electrode, second electrode, electric energy storage
Can box, convex lens and convex lens mirror support.
First saline slot and the second saline slot horizontal Tile are set, will stream by two outlets in the distributive pipe road
First saline slot and second saline slot are injected separately into through the dyeing waste water in quartz sand filtration chamber, the salt bridge is
One saline slot is connected the two with the second saline slot top, and the first electrode is placed in first saline slot, institute
State second electrode to be placed in second saline slot, the first electrode and second electrode pass through wire and the electric energy energy storage
The electrical power input part connection of box, the electrical power storage that the electrical power input part is used to be produced between two electrodes is stored up in electric energy
In energy box;The convex lens are provided with two, are set up in first saline slot and second by two convex lens mirror supports respectively
Saline slot top.
The flocculation chamber includes flocculation chamber inlet duct, flocculation chamber enclosure, Flocculent plate and flocculation chamber outlet conduit, the wadding
Solidifying chamber inlet duct will flow through the first saline slot respectively and the dyeing waste water of the second saline slot is imported into flocculation chamber enclosure, described
Flocculent plate includes two pieces of copper coins and one piece of zine plate, and the zine plate is arranged at the centre of flocculation chamber enclosure, and two pieces of copper coins are arranged at two
End, and the chamber inlet duct that will flocculate is respectively arranged at the centre position of copper coin and zine plate, flocculation chamber outlet conduit with it is described
The entrance in activated carbon chamber is connected.
The activated carbon chamber is internally provided with the continuous activated carbon filter of multilayer, and the dyeing waste water after treatment is through making a living
Property charcoal chamber outlet outflow.
Flocculation chamber outlet conduit is contraction-like setting, is wide opening near flocculation chamber side, near activated carbon chamber side
It is slot.
The copper coin and the equal longitudinal measure in zine plate both sides have non-crystaline amorphous metal bar, the material of the non-crystaline amorphous metal bar(It is former
Sub- ratio)It is Sr21Ca25Mg15Zn21La8Cu8B1。
The salt bridge is internally provided with fixed many hole sizers, and KCl solution is provided with many hole sizers.
The convex lens are provided with two, are set up in first saline slot and second by two convex lens mirror supports respectively
Saline slot top, and two convex lens are different from horizontal plane angle, two convex lens and the same angular separation of horizontal plane it
Be 180 °.And two convex lens are respectively 50 ° and 130 ° with horizontal plane same direction angle.
The continuous activated carbon filter of multilayer that the activated carbon chamber inside is set is inside double-layer porous metallic plate and sets
It is equipped with activated carbon granule.
The granular quartz sand particle mean size that the quartz sand filtration cavity main body inside is set is 2.5mm, the particle
The quartz sand surface of shape is provided with loose structure.
The copper coin and the equal longitudinal measure in zine plate both sides have non-crystaline amorphous metal bar, and the non-crystaline amorphous metal bar is in each copper coin
On be provided with 5, be respectively arranged with 6 in zine plate both sides.
Comparative example 2
This comparative example is various to set same as Example 2, and difference is, by the non-crystaline amorphous metal removal in wherein flocculation chamber, to survey
It is the 88.2% of embodiment 2 to obtain the amount of water up to standard.
Embodiment 3
A kind of dyeing waste water TRT, including quartz sand filtration chamber, waste water for generating electricity groove, flocculation chamber and activated carbon chamber.
Wherein quartz sand filtration chamber includes dyeing waste water entrance, quartz sand filtration cavity main body and distributive pipe road, the printing and dyeing
Waterwater entrance is incorporated into the quartz sand filtration cavity main body after dyeing waste water is pressurizeed, inside the quartz sand filtration cavity main body
Granular quartz sand is provided with, for removing water insoluble impurity in dyeing waste water, the distributive pipe road is used as quartz sand
The outlet of filter chamber, connection quartz sand main body one end is an entrance, and the one end for connecting waste water for generating electricity groove is that horizontal two go out
Mouthful.
The waste water for generating electricity groove includes the first saline slot, the second saline slot, salt bridge, first electrode, second electrode, electric energy storage
Can box, convex lens and convex lens mirror support.
First saline slot and the second saline slot horizontal Tile are set, will stream by two outlets in the distributive pipe road
First saline slot and second saline slot are injected separately into through the dyeing waste water in quartz sand filtration chamber, the salt bridge is
One saline slot is connected the two with the second saline slot top, and the first electrode is placed in first saline slot, institute
State second electrode to be placed in second saline slot, the first electrode and second electrode pass through wire and the electric energy energy storage
The electrical power input part connection of box, the electrical power storage that the electrical power input part is used to be produced between two electrodes is stored up in electric energy
In energy box;The convex lens are provided with two, are set up in first saline slot and second by two convex lens mirror supports respectively
Saline slot top.
The flocculation chamber includes flocculation chamber inlet duct, flocculation chamber enclosure, Flocculent plate and flocculation chamber outlet conduit, the wadding
Solidifying chamber inlet duct will flow through the first saline slot respectively and the dyeing waste water of the second saline slot is imported into flocculation chamber enclosure, described
Flocculent plate includes two pieces of copper coins and one piece of zine plate, and the zine plate is arranged at the centre of flocculation chamber enclosure, and two pieces of copper coins are arranged at two
End, and the chamber inlet duct that will flocculate is respectively arranged at the centre position of copper coin and zine plate, flocculation chamber outlet conduit with it is described
The entrance in activated carbon chamber is connected.
The activated carbon chamber is internally provided with the continuous activated carbon filter of multilayer, and the dyeing waste water after treatment is through making a living
Property charcoal chamber outlet outflow.
Flocculation chamber outlet conduit is contraction-like setting, is wide opening near flocculation chamber side, near activated carbon chamber side
It is slot.
The copper coin and the equal longitudinal measure in zine plate both sides have non-crystaline amorphous metal bar, the material of the non-crystaline amorphous metal bar(It is former
Sub- ratio)It is Sr21Ca25Mg15Zn21La8Cu8B1。
The salt bridge is internally provided with fixed many hole sizers, and KCl solution is provided with many hole sizers.
The convex lens are provided with two, are set up in first saline slot and second by two convex lens mirror supports respectively
Saline slot top, and two convex lens are different from horizontal plane angle, two convex lens and the same angular separation of horizontal plane it
Be 180 °.And two convex lens are respectively 55 ° and 125 ° with horizontal plane same direction angle.
The continuous activated carbon filter of multilayer that the activated carbon chamber inside is set is inside double-layer porous metallic plate and sets
It is equipped with activated carbon granule.
The granular quartz sand particle mean size that the quartz sand filtration cavity main body inside is set is 3.9mm, the particle
The quartz sand surface of shape is provided with loose structure.
The copper coin and the equal longitudinal measure in zine plate both sides have non-crystaline amorphous metal bar, and the non-crystaline amorphous metal bar is in each copper coin
On be provided with 3, be respectively arranged with 8 in zine plate both sides.
Claims (9)
1. a kind of dyeing waste water TRT, it is characterised in that:Including quartz sand filtration chamber, waste water for generating electricity groove, flocculation chamber and
Activated carbon chamber;
Wherein quartz sand filtration chamber includes dyeing waste water entrance, quartz sand filtration cavity main body and distributive pipe road, the dyeing waste water
Entrance is incorporated into the quartz sand filtration cavity main body after dyeing waste water is pressurizeed, and the quartz sand filtration cavity main body inside is set
There is granular quartz sand, for removing water insoluble impurity in dyeing waste water, the distributive pipe road is used as quartz sand filtration
The outlet in chamber, connection quartz sand main body one end is an entrance, and the one end for connecting waste water for generating electricity groove is two horizontal outlets;
The waste water for generating electricity groove includes the first saline slot, the second saline slot, salt bridge, first electrode, second electrode, electric energy energy storage
Box, convex lens and convex lens mirror support;
First saline slot and the second saline slot horizontal Tile are set, and stone will be flowed through by two outlets in the distributive pipe road
The dyeing waste water of sand filter chamber is injected separately into first saline slot and second saline slot, and the salt bridge is in the first salt
Tank and the second saline slot top are connected the two, and the first electrode is placed in first saline slot, and described
Two electrodes are placed in second saline slot, and the first electrode and second electrode pass through wire and the electric energy energy storage box
Electrical power input part is connected, and the electrical power input part is used for the electrical power storage that will be produced between two electrodes in electric energy energy storage box
In;The convex lens are provided with two, are set up in first saline slot and the second salt solution by two convex lens mirror supports respectively
Groove top;
The flocculation chamber includes flocculation chamber inlet duct, flocculation chamber enclosure, Flocculent plate and flocculation chamber outlet conduit, the flocculation chamber
Inlet duct will flow through the first saline slot respectively and the dyeing waste water of the second saline slot is imported into flocculation chamber enclosure, the flocculation
Plate includes two pieces of copper coins and one piece of zine plate, and the zine plate is arranged at the centre of flocculation chamber enclosure, and two pieces of copper coins are arranged at two ends, and
The chamber inlet duct that flocculates is respectively arranged at the centre position of copper coin and zine plate, flocculation chamber outlet conduit and the activated carbon
The entrance in chamber is connected;
The activated carbon chamber is internally provided with the continuous activated carbon filter of multilayer, and the dyeing waste water after treatment is by activated carbon
Chamber outlet outflow.
2. dyeing waste water TRT according to claim 1, it is characterised in that flocculation chamber outlet conduit is to shrink
Shape is set, and is wide opening near flocculation chamber side, is slot near activated carbon chamber side.
3. dyeing waste water TRT according to claim 1, it is characterised in that the copper coin and the zine plate both sides are equal
Longitudinal measure has non-crystaline amorphous metal bar, the material of the non-crystaline amorphous metal bar(Atomic ratio)It is Sr21Ca25Mg15Zn21La8Cu8B1。
4. dyeing waste water TRT according to claim 1, it is characterised in that the salt bridge is internally provided with fixed
Many hole sizers, are provided with KCl solution in many hole sizers.
5. dyeing waste water TRT according to claim 1, it is characterised in that the convex lens are provided with two, point
First saline slot and the second saline slot top, and two convex lens and level are not set up in by two convex lens mirror supports
Face angle is different, and two convex lens are 180 ° with the same angular separation sum of horizontal plane.
6. dyeing waste water TRT according to claim 5, it is characterised in that two convex lens and the same side of horizontal plane
51 ° and 129 ° are respectively to angle.
7. dyeing waste water TRT according to claim 1, it is characterised in that it is many that the activated carbon chamber inside is set
The continuous activated carbon filter of layer is double-layer porous metallic plate and is internally provided with activated carbon granule.
8. dyeing waste water TRT according to claim 1, it is characterised in that inside the quartz sand filtration cavity main body
The granular quartz sand particle mean size for setting is 2 ~ 5mm, and the granular quartz sand surface is provided with loose structure.
9. dyeing waste water TRT according to claim 1, it is characterised in that the copper coin and the zine plate both sides are equal
Longitudinal measure has non-crystaline amorphous metal bar, and the non-crystaline amorphous metal bar is provided with 3 ~ 5 on each copper coin, is respectively provided with zine plate both sides
There are 5 ~ 8(It is preferred that 6 ~ 8).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710280853.9A CN106904773A (en) | 2017-04-26 | 2017-04-26 | A kind of dyeing waste water TRT |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710280853.9A CN106904773A (en) | 2017-04-26 | 2017-04-26 | A kind of dyeing waste water TRT |
Publications (1)
Publication Number | Publication Date |
---|---|
CN106904773A true CN106904773A (en) | 2017-06-30 |
Family
ID=59210866
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710280853.9A Withdrawn CN106904773A (en) | 2017-04-26 | 2017-04-26 | A kind of dyeing waste water TRT |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106904773A (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101875522A (en) * | 2010-06-09 | 2010-11-03 | 南京大学 | Grading recycle device for electric flocculation and electric floatation purification bathing and washing wastewater |
KR20110012918A (en) * | 2009-07-31 | 2011-02-09 | 한국염색기술연구소 | Device for producing fuel of dyeing wastewater sludge in coal-fired power utility boiler plant and method thereof |
CN104326615A (en) * | 2014-11-28 | 2015-02-04 | 马涛 | Energy-saving high-salt wastewater treatment system and treatment method |
CN205277729U (en) * | 2015-11-17 | 2016-06-01 | 绍兴文理学院 | Printing and dyeing heat energy driving system is produced to slot type solar thermal energy electricity federation |
-
2017
- 2017-04-26 CN CN201710280853.9A patent/CN106904773A/en not_active Withdrawn
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20110012918A (en) * | 2009-07-31 | 2011-02-09 | 한국염색기술연구소 | Device for producing fuel of dyeing wastewater sludge in coal-fired power utility boiler plant and method thereof |
CN101875522A (en) * | 2010-06-09 | 2010-11-03 | 南京大学 | Grading recycle device for electric flocculation and electric floatation purification bathing and washing wastewater |
CN104326615A (en) * | 2014-11-28 | 2015-02-04 | 马涛 | Energy-saving high-salt wastewater treatment system and treatment method |
CN205277729U (en) * | 2015-11-17 | 2016-06-01 | 绍兴文理学院 | Printing and dyeing heat energy driving system is produced to slot type solar thermal energy electricity federation |
Non-Patent Citations (1)
Title |
---|
陈金宝等: "《医用化学》", 31 January 2017 * |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2005068373B1 (en) | Electrochemicla water purifier | |
CN104926004A (en) | Capacitive sea water desalting equipment and method based on direct-current electric field effect | |
CN104944647A (en) | Capacitance type sewage and waste water treatment device and method based on action of direct current electric field | |
CN104556315B (en) | A kind of membrane stack and electro-desalting assembly | |
CN204848534U (en) | Based on capacitanc sewage and waste water treatment equipment under direct current field effect | |
CN106348397A (en) | Electric desalinating device | |
Safwat | Coupling microbial fuel cells with electrocoagulation cells to form an integrated system for wastewater treatment | |
Rahman et al. | Experimental study of batch electrocoagulation treatment of peat water in Sarawak with aluminium electrodes | |
CN102092821A (en) | Application method of high-property activated carbon fibers in treatment of industrial waster water by electrocoagulation | |
EA026258B1 (en) | Device and process for improved recovery of deionised water | |
CN106904773A (en) | A kind of dyeing waste water TRT | |
CN104609614A (en) | Purification component and water purifier | |
CN103663808B (en) | Heavy metal wastewater thereby film integrated treating device | |
CN216273532U (en) | Electromagnetic coupling sea water desalination device | |
CN204039110U (en) | A kind of electroplating wastewater processing low voltage pulsed electric flocculation technology device | |
JP6877004B2 (en) | Particle coagulation separation device and particle coagulation separation method | |
CN210764485U (en) | Electric flocculation device | |
CN210145851U (en) | Efficient water-saving system for circulating water pollution discharge | |
CN203683290U (en) | Membrane integrated treatment device for heavy metal wastewater | |
CN207567084U (en) | A kind of bipolarity device for electrolysis, pressure filtration and dehydration | |
CN204474471U (en) | Purification assembly and water-purifying machine | |
CN207699269U (en) | A kind of water process electrochemical descaling device of Modular assembled | |
CN206720930U (en) | A kind of new electric flocculation Waste Water Treatment containing coal | |
CN210286852U (en) | Electrolytic phosphorus removal device | |
CN201379996Y (en) | Electromagnetic flocculation precipitation accelerator |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WW01 | Invention patent application withdrawn after publication |
Application publication date: 20170630 |
|
WW01 | Invention patent application withdrawn after publication |