CN105858819B - The tea maker of degradable remains of pesticide - Google Patents
The tea maker of degradable remains of pesticide Download PDFInfo
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- CN105858819B CN105858819B CN201610215333.5A CN201610215333A CN105858819B CN 105858819 B CN105858819 B CN 105858819B CN 201610215333 A CN201610215333 A CN 201610215333A CN 105858819 B CN105858819 B CN 105858819B
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- 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
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
-
- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47G—HOUSEHOLD OR TABLE EQUIPMENT
- A47G19/00—Table service
- A47G19/12—Vessels or pots for table use
- A47G19/14—Coffee or tea pots
-
- 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
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
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- 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
- C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
- C02F1/4698—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electro-osmosis
-
- 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
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- 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
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/46—Apparatus for electrochemical processes
- C02F2201/461—Electrolysis apparatus
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- 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
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2307/00—Location of water treatment or water treatment device
- C02F2307/04—Location of water treatment or water treatment device as part of a pitcher or jug
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Electrochemistry (AREA)
- Health & Medical Sciences (AREA)
- Analytical Chemistry (AREA)
- Molecular Biology (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The present invention relates to a kind of tea makers of degradable remains of pesticide, belong to the water quality advanced processing technology field of Drinking Water.The tea maker includes a pair of of anodic-cathodic, for the electrolysis power and Insulating frame of anodic-cathodic power supply, water penetration diaphragm is equipped between anodic-cathodic, negative electrode and positive electrode are the tubular electrodes being fixed on Insulating frame, negative electrode is formed with mesh, partition and the lower chambers by partition by tubular negative electrode inside division at upper chamber and placement tealeaves are equipped in negative electrode, positive electrode is set in upper chamber, water penetration diaphragm, which is expired tilt and set, to be coated on positive electrode outer surface, when in use, negative electrode immerses in tea water, positive electrode is only contacted with the infiltration water that tea water is permeated by water penetration diaphragm.The advantages of tea maker can safely and efficiently remove chemical residual degradation in tea.
Description
Technical field
The present invention relates to a kind of tea makers of degradable remains of pesticide, belong to the water quality advanced processing technique of Drinking Water
Field.
Background technique
Water pollution is mainly caused by the pollutant that mankind's activity generates, it includes industrial pollution source, agricultural pollution source with
Domestic pollution source three parts.Increasingly the water pollution aggravated constitutes significant threat to the living safety of the mankind, and it is strong to become the mankind
Health, the major obstacles of economy and society sustainable development.It investigates according to authoritative institution of the world, is at least made because drinking unhygienic water every year
Dead at global 20,000,000 people, therefore, water pollution is referred to as " world's number one killer ".Currently, water environment is exacerbated, sternly
Weight threat to life continue, especially when happen suddenly natural and man-made calamities when more so.More poor and backward area, drink is to completely
Trust that water is even almost luxurious for general public.If can make the common people that can all drink with simple, cheap, efficient means
To completely trusting water, when for how immeasurable beneficence!
Domestic and international most of waterworks are so far still using precipitating, filtering, the outmoded process of chlorination, by rivers
Water or underground water are simply processed into drinkable water.However, spreading unchecked and pouring in face of trade effluent, rural sewage and sanitary sewage wildness
Life water source, waterworks can't bear the heavy load helpless.Along with tap water from water factory through water transfer pipe network and high-rise water storage
Case reaches and adds pollution brought by drinking water terminal, and it is health that municipal tap water dare not have been said.Especially, tap water adds
Although chlorine can be killed effectively except germ, can also generate more halogenated hydrocarbon compound simultaneously, the contents of these chlorinated organics at
Increase again, is the significant source for causing the mankind to suffer from various diseases.Even boiling tap water, above-mentioned residue still drive no
It goes, the carcinogenic substances such as nitrite and chloroform can also increased.Also that is, even if the safety coefficient of drinking water is also not high
's.
Since direct drinking public water supply is difficult to ensure safety, water purifier comes into being, and becomes common people's hard requirement.However, existing
Using city for tap water as the purification of water quality product or drinking water related product of source water, essentially medium absorption or use various bore filters
Water pollutant is intercepted the physical treatment technology filtered out by film.Since active carbon class adsorbent material is easy to saturation failure,
And various filter membranes are easy to be contaminated by bacterial or organic matter obstruction or damaged, therefore actual conditions be can not be as theory is set
Meter is desired to be accomplished to the sufficiently cleaned up of water pollutant like that.It is existing to be adsorbed with medium in face of the source water pollution got worse
Or water pollutant is intercepted to the physics mode water treatment technology filtered out using various bore filter films and far can not
Guarantee water quality reaching standard.In addition, traditional RO membrane reverse osmosis filter method is very serious to the waste of water resource, 1 liter is often purified
Pure water just needs to be discharged 3 liters of concentration waste water.But physics mode water treatment technology also has its points of course: not generating poison usually
By-product.
In comparison, though Water Treatment technique has many advantages, such as being inexpensively simple and efficient, and it is unsuitable for civilian
Terminal Drinking Water field.To find out its cause, first is that the Water Treatment process requirement enough reaction time, and in daily life
With water occasion, water purifier is from booting water inlet to water outlet only several seconds or even shorter, and the residence time is too in water purifier for pollutant
It is short, have little time to complete related chemistry reaction treatment at all;The second is Water Treatment technique is usually made with certain poison is secondary
With.For example, although chemical oxidation reaction can potent inactivation of bacterial, depth degradation organic matter, go water removal in various harmful substances,
But the chemical oxidization method all kinds of Strong oxdiative factors generated are substantially non-selectivity, uncontrollable, if dealing with improperly most probably raw
The novel substance not having in Cheng Yuanshui even strong carcinogen, jeopardizes safe drinking water instead.And reduction reaction controls improper also bring along
Similar problems, such as nitrate may be converted into strong carcinogen nitrite;Just because of this, it is had no so far in Drinking Water
Purified treatment field especially family's drinking-water terminal promotes and applies.
Fortunately, in daily life, drinking water needs often have the characteristics that at times, interval.For example, family three times
Meal water and bathing peak are concentrated mainly on the time in the morning, afternoon and evening;Wash water then presses week/time calculating.Drinking water is deposited in daily life
Storage device leads to the drinking water terminal for referring to and having water tank (tank, container), such as: 1) pipeline water purification system terminal wall-hanger, desk-top
Or vertical drinking;2) RO water purification machine water outlet pressure store bucket (case) and water glass, pot;3) public supply mains high level is built
Build top layer installation high water tank in addition rural resident's groundwater abstraction to roof water tank.At present existing for such system
Common problem is that bacterial micro-organism is exceeded in water in water tank, and it is smelly to seriously affect water quality even peculiar smell.The solution that there is no so far
Certainly method.
Meanwhile drinking tea is part indispensable in people's life.However being excessively used due to pesticide, the agriculture in tealeaves
Medicine residual (predominantly trace pesticide substance and its toxic metabolite degradation product) increasingly increases, and to drinking tea, safety constitutes a threat to.It grinds
Study carefully and show that the accumulation delay for a long time in human body of fruits and vegetables and pesticide residue from tea can cause slow poisoning, induces many chronic diseases
Disease, such as cardiovascular and cerebrovascular diseases, diabetes, hepatopathy, cancer, it is more more fearful than acute poisoning.People is more allowed to be difficult to expect and take precautions against
Be: pesticide is in the intracorporal accumulation of people, it is also possible to be transmitted to the next generation by pregnancy and lactation, bring disaster to the health of descendants.
Development has many Pesticide Residues in Tea degradation techniques so far, for example, microbial degradation agriculture is residual, ozone degradation agriculture is residual,
Photochemical degradating agriculture is residual, hydrogen peroxide degradation agriculture is residual etc., but concentrates on the plantation, processing and storage stage of tealeaves.In tea ceremony
In wash tea process.However experimental verification, pesticide residue on tealeaves can not effectively be washed off by washing tea.
In short, how to hold make tea this entrance of drinking tea before last line of defense, in being made tea using home terminal tap water, both
So that the home terminal tap water made tea carried out depth purified treatment, but the removal that Pesticide Residues in Tea can be degraded can
The tea maker of deteriorating pesticide residue.
Summary of the invention
First technical problem that the present invention solves be, in view of the shortcomings of the prior art, proposing that one kind can safely will be in tea
The tea maker of the degradable remains of pesticide of chemical residual degradation removal.
Second technical problem that the present invention solves is, on the basis of solving above-mentioned first technical problem, for existing
Technical deficiency proposes a kind of tea maker that toxic byproduct is less generated when carrying out degradation Organic substance in water to tea water.
Applicant explores by repetition test and for many years, it was found that electrochemistry as a kind of advanced oxidation water treatment technology,
Attached poison seondary effect is small far beyond conventional chemical water treatment technology, and electro-chemical water treatment process can pass through electrical parameter
Adjustment carrys out intensive treatment intensity and reduces the reaction time.Overcome physics water treatment technology soft in this way, electrochemical water treatment technology has
Rib, the certain potentiality that can be used for Drinking Water purified treatment.
Electrochemical water treatment technology is to make polluter that Direct Electrochemistry reaction occur on the electrode or utilize electrode table
Face generates strong oxidizing property active material and oxidation reaction occurs and is converted electrochemical techniques and its is aided with other high-level oxidation technologies
Group technology, referred to as electrochemical system, including electrode electro-catalysis, electricity-Fenton, electricity-O3, sound-electric, optical-electronic etc..
Electro-chemical water processing be unable to do without electrode effect, is specifically divided into electrode and directly reacts and electrode indirect reaction.Electrode is straight
It is reversed to refer to that pollutant is directly oxidated or reduced on the electrode and removes from water.Direct Electrolysis can be divided into anodic process and
Cathodic process.Anodic process is exactly that pollutant aoxidizes in anode surface and is converted to the lesser substance of toxicity or easily biological-degradable
Substance, or even generation organic matter are inorganization, to achieve the purpose that reduction, removal pollutant.Cathodic process is exactly that pollutant exists
Cathode surface is restored and is removed.
Electrode indirect reaction is then to make to pollute using the redox materials of electrochemistry generation as reactant or catalyst
Object is converted to the smaller substance of toxicity.Anode indirect reaction, generated redox materials, generally include following several in water
Class: (1) with chlorate, the hypochlorite etc. of strong oxidizing property;Elecrtonegativity can be removed by anode;(2) H2O2、O3(standard electric
Electrode potential 2.07, half-life period 30-60min) etc. the Strong oxdiatives factor;(3) strong oxidizing property and service life that electrochemical reaction generates are extremely short
Intermediate, including e (solvated electron), OH, HO2·、·O2Equal free radicals can be with degradation of organic substances based on OH.
But still belong to chemical treatment technology in electrochemical nature, even toxic side effect is small again, still there are the Biological indicators for making water
The risk of reduction.Water environment it is unprecedented it is serious pollution, in conventional physical water purifier today unable to do what one wishes, examine closely again
Study Water Treatment --- especially electrochemical water treatment technology is a possibility that Drinking Water purified treatment is applied, innovation
Water pollutant, again the electrochemical treatments technique of non-toxic by-products or even electro-chemical water processing can efficiently be removed by developing one kind
Technique cooperateed with physisorptive filter technique associated with completely new method for purifying water and device, there is highly important reality meaning
Justice.
In order to solve above-mentioned first technical problem, the present inventor proposes following skill on the basis of above-mentioned cognition
Art scheme: a kind of tea maker of degradable remains of pesticide, including a pair of of anodic-cathodic, the electrolysis powered for the anodic-cathodic
Power supply and Insulating frame are equipped with water penetration diaphragm between anodic-cathodic, and the negative electrode and positive electrode are to be fixed on insulation frame
Tubular electrode on frame, the negative electrode are formed with mesh, partition are equipped in the negative electrode and will be in tubular negative electrode by partition
Part is cut into upper chamber and places the lower chambers of tealeaves, and the positive electrode is set in the upper chamber, and the water penetration diaphragm is full
Tilt, which is set, to be coated on the positive electrode outer surface, and when in use, the negative electrode immerses in tea water, the positive electrode only with
The tea water is contacted by the infiltration water that the water penetration diaphragm permeates.
The beneficial effect of the tea maker technical solution of the degradable remains of pesticide of aforementioned present invention is: apparatus of the present invention
Positive electrode is only contacted with the infiltration water that tea water is permeated by water penetration diaphragm, normal in the cell reaction for guaranteeing apparatus of the present invention
On the basis of progress, anode direct oxidation reaction is transferred to container (container for containing tea) and is carried out outside, reaction product of anode
Drain outside container, will not return again to and pollute water quality in container.Meanwhile the negative pollutant such as chlorine residue etc. in water, by anode
Voltage effect can also move to container outer anode region from water penetration diaphragm is penetrated in container in water.
Of particular note is that: anode direct oxidation reaction does not need, but anode reaction product (such as it is smelly
Oxygen) there may be toxic side effects, including negative pollutant may still be had certain toxicity by anode direct oxidation reaction product,
Anode is arranged to external container the present invention, and above-mentioned toxic byproduct is directly with regard to outlet;And source water electrolysis is given in positive electrode
On the great discharge space such as reaction product such as oxygen, ozone, chlorine, can be fallen by outside direct emission, will not be penetrated
Diaphragm returns again to the water quality in container in pollution container, will not remain in container in water, to significantly reduce above-mentioned strong oxygen
The toxic side effect of compound.
In addition, positive electrode is set in upper chamber, the infiltration that positive electrode is only permeated with the tea water by water penetration diaphragm
Water contact, remains chlorine residue in tea and various harmful anions face south electrode transfer, be pierced by water penetration diaphragm enter positive electrode with
It water body and is discharged between film.Meanwhile tealeaves being put into the lower chambers of tubular negative electrode, the present apparatus is put into water container (tea
Pot, teacup, teacup class) it makes tea, by the cathode reaction of tubular negative electrode, the ultra micro gas largely based on hydrogen is generated in water
Bubble, the oxidation-reduction potential of water quickly reduce, and alkalinity increases, and water tends in small molecule cluster, surface tension, emulsibility of water etc.
Characteristic substantially improves, since organophosphorus pesticide includes that orthene contains P=S and C=O double bond mostly, in above-mentioned water characteristic item
Under part, nucleopilic reagent is easily broken its double bond, and SN2 nucleophilic substitution occurs, makes remains of pesticide accelerated degradation.Therefore,
Remains of pesticide in tea is acted on by negative electrode degradation and positive electricity pole tension, is moved to tea outer anode region, is contained in tea
Amount is few, and comprehensive treatment effect is splendid.
The present invention is to solve above-mentioned second technical problem, and improvement to above-mentioned technical proposal is: the water penetration diaphragm
It is water penetration diaphragm made of non-conductive material, the water penetration diaphragm has the permeable micropore of uniform pore size.
It should be noted that apparatus of the present invention processing to seeming home terminal drinking-water, usually city for tap water, as
Described in background technique, present water pollution is got worse, and it is (or perhaps special that home terminal drinking-water has become a kind of micro-polluted water
Different contaminant water), pollution sources include the pollution and pipeline secondary pollution of environmental pollution (such as pesticide residue), chlorination generation
Deng.
The working mechanism and beneficial effect of the tea maker technical solution of degradable remains of pesticide disclosed in aforementioned present invention
It is presented below.
The present invention, which passes through, will have the water penetration diaphragm of the micropore of uniform pore size to be arranged between cathode and anode, in conventional electricity
It is brought other than solution reaction process and forms the reaction of water body low pressure cold plasma discharge in micropore in water penetration diaphragm, analysis is such as
Under:
Apparatus of the present invention structure feature is, referring to Fig. 1, to be boundary with water penetration diaphragm, set up separately inside and outside water penetration diaphragm
The anodic-cathodic pair of two sides: tubular negative electrode inside division at upper chamber and is placed into tea equipped with partition in negative electrode and by partition
The lower chambers of leaf, positive electrode are set in the upper chamber, and water penetration diaphragm, which is expired tilt and set, to be coated on positive electrode outer surface.
After the decomposition voltage of electrolysis power is applied to external electrode (positive electrode) and interior electrode (negative electrode), formed following
Voltage landing relationship:
The outer positive electrode (+) of film → voltage drop U1 → water penetration diaphragm direct impedance of moisture film generates between positive electrode and film
The pressure of the anti-generation of water resistance between negative electrode in pressure drop U2 → water penetration diaphragm and container (tea maker make tea container used)
U3 drops.
In the present invention, the effect of water penetration diaphragm is not only and will be isolated inside and outside container, due to the structure of itself: permeable
Property diaphragm is water penetration diaphragm made of non-conductive material, it is microcosmic on show as the water passage regions of countless uniform micros
(micropore with uniform pore size) can also form water body low pressure under decomposition voltage effect in water penetration diaphragm in micropore
Cold plasma discharge reaction.Low temperature plasma is rich in electronics, ion, free radical and excited state molecule, and electronics and ion have very
High reactivity can be such that the chemical reaction for being difficult to carry out or speed is difficult under usual conditions becomes very rapidly.
Traditional water body plasma discharge technology is imported often through outside into water to generate water body plasma discharge
Gas, and impose and increase strength pulse voltage or hot conditions.Plasma discharge is then directed to water penetration diaphragm by the present invention
Countless small water storage spaces carry out, and by the gas that positive electrode generates water electrolysis liberation of hydrogen, oxygen evolution reaction, partially enter in film and lure
Flooding, (the infiltration water due to penetrating through water penetration diaphragm in positive electrode and container contacts, in this way, positive electrode pastes for body itself gasification
Nearly water penetration diaphragm, the oxygen etc. of anode reaction is easily accessible membrane micropore and generates bubble in millipore water, narrow in membrane micropore
In environment, bubble breaking generates localized hyperthermia's high pressure), and then efficient water body plasma discharge is inspired with minimum voltage,
Hydroxyl free base class transient state oxidation factor is generated in water, the extremely strong oxidisability of the hydroxyl radical free radical transient state oxidation factor (is more than smelly
Oxygen) simultaneously in water there are the time again it is extremely short, therefore can after generation rapidly to Organic substance in water (such as bacterium) pollute
Object is reduced directly to water after forming extremely strong degradation and itself rapid oxidation, does not stay any toxic side effect.
Since conventional chemical water treatment technology is in purified treatment common people's daily life drinking water, all kinds of Strong oxdiatives of generation
The factor is substantially non-selectivity, uncontrollable, jeopardizes safe drinking water, the strong carcinogen nitrite etc. that reduction reaction generates, no
It is suitably applied in common people's daily life drink water purifying processing occasion.Therefore, current conditions and conventional thinking limit chemical water
Application of the treatment process in terms of common people's daily life drinking water.All kinds of Strong oxdiatives that the present invention generates Conventional electrochemical water because
The uncontrollable of son becomes controllable, and the present invention is exactly to utilize these characteristics of hydroxy radical, this special for tap water for city
On the one hand anode direct oxidation reaction is drawn out to water in container by ingehious design in structure by micro-polluted water water quality characteristics
Outside occurs, and excludes oxidation reaction toxic byproduct.On the other hand by anode indirect oxidation effect perform to it is ultimate attainment, realize to source water
The extremely purification of depth and safety!
The beneficial effect for summarizing the tea maker technical solution of the degradable remains of pesticide of aforementioned present invention is: 1) sufficiently sharp
With electrochemical water treatment technology, be unable to reach with reaching existing physics water treatment technology, to the depth degradation of source water pollutant,
Anode direct oxidation reaction is drawn out to outside device and carries out, ozone is inhibited to generate by the effect efficiently removed, to reduce in container
The risk of toxic byproduct is generated in interior water;2) it relies primarily on hydroxy kind strong oxidizing property and the service life is extremely short and between having no toxic side effect
Electrochemistry intermediate is connect, to realize desired electro-chemical water treatment effect;3) microorganism in tea, by water penetration diaphragm with
The electric field action of U3 between negative electrode in container and inactivate.
The further improvement of the present invention on that basis of the above technical scheme is: the water penetration diaphragm is hydrophilic permeable
Property diaphragm.
Water penetration diaphragm of the invention is hydrophilic water penetration diaphragm, and it is orderly that hydrophilic film surface can form hydrogen bond with water
Structure can improve fenestra water-filling wet face state, and the plasma discharge process in film that is conducive to persistently carries out.
The further improvement of the present invention on that basis of the above technical scheme is: when using electric discharge, the permeable micropore
Middle formation plasma discharge.
The further improvement of the present invention on that basis of the above technical scheme is: when using electric discharge, each permeable micropore
In be respectively formed plasma discharge.
The shape and pore size and uniformity of membrane micropore influence plasma discharge in film very big.For can be ultralow
Plasma group is efficiently produced under discharge voltage, as shown in figure 3, water penetration diaphragm employed in the present invention, when using electric discharge,
Direction of an electric field penetrates each permeable micropore, and Faradaic current circulates through micropore each in film between two electrodes, is equivalent to a big face
Product electrode has been divided into the small electrode of numerous a tip-likes, so that the electric discharge curvature of electrode reduces, discharging efficiency is improved, together
When, the present invention carries out the countless small water storage spaces that plasma discharge is directed to water penetration diaphragm, by water electrolysis liberation of hydrogen,
The gas that oxygen evolution reaction generates partially enters in film and induces water body itself gasification, and then inspires efficient water with minimum voltage
Body plasma discharge, can excite water-outlet body plasma discharge, generate the transient state oxidation factor of great sterilizing ability in water, greatly
The big degradation efficiency for improving pollutant in water body.
The present invention on that basis of the above technical scheme improve first is that: the Insulating frame is insulating panel, the positive electricity
Pole top surface is tightly attached on the insulating panel, and the water penetration diaphragm, which completely hides, is wrapped in positive electrode others in addition to top surface
The inside of the positive electrode is closed as a closed chamber, the space with positive electrode is provided on the insulating panel by outer surface
The exhaust outlet of connection.
The present invention on that basis of the above technical scheme improve second is that: physical absorption filtering layer is equipped in the closed chamber.
By being equipped with physical absorption filtering layer in closed chamber, strong adsorption is played to anode reaction by-product, degradation is made
With, it is ensured that the water quality safety of tea.
The present invention on that basis of the above technical scheme improve third is that: the physical absorption filtering layer be seed activity layer of charcoal,
Sintering activity layer of charcoal, activated carbon fiber layers, micro-filtration material layer or the micro-filtration material layer made of porous ceramics made of PP cotton.
The present invention on that basis of the above technical scheme improve fourth is that: the permeable aperture of the water penetration diaphragm be respectively less than etc.
In 2 millimeters and it is more than or equal to the permeable aperture sizes of all micropores in 1 nanometer and water penetration diaphragm phase each other between each other
Difference is less than 20%.
In apparatus of the present invention, if the permeable aperture of water penetration diaphragm excessive (i.e. microporous space is excessive) is equivalent to covert increasing
Big electrode diameter (electrode curvature radius) causes discharge in water starting excitation voltage to increase, and makes to generate bubble volume and become larger
Reduce the catalytic specific surface area of gas-liquid two-phase.And the permeable aperture of water penetration diaphragm is too small (i.e. microporous space is too small),
Electrolysis can be made, which to produce gas, can not occur or gas producing efficiency is extremely low, it is small will lead to a certain extent it is countless in each micropore in diaphragm
The point discharge of a small curvature radius electrode can not be normally carried out.Therefore, by the repetition test of inventor, permeable aperture is determined
Range is 2 millimeters -1 nanometer.
The present invention on that basis of the above technical scheme improve fifth is that: the water penetration diaphragm is by according to the following steps
Manufactured diaphragm:
1) by nanometer titanium dioxide titanium solution ultraviolet case internal irradiation 10-30 minutes that temperature is 40 DEG C -60 DEG C;
2) film liquid is formed by the raw material of following mass ratio:
PVDF:20%-30%
Pore-foaming agent: 2-5%
Nano-titanium dioxide after step 1) irradiation: 2%-4%
Surfactant: 3%-5%
Solvent: 70%-80%;
3) configured film liquid is passed through supersonic oscillations 20-40 minutes;
4) spread to liquid film with knifing machine, liquid film stood to 10-30 seconds in air, be then immersed in solidification liquid be frozen into every
Film;
5) diaphragm is to impregnate 10-40 minutes in 10% alcohol water blend in concentration, is then placed in deionized water and floats
It washes;
6) diaphragm is placed in the pure water tank for being applied with 10kv DC pulse high voltage and is handled 1 hour.
Specific practical function is: to make electric discharge in film be easy to carry out, it is required that water penetration diaphragm has uniform pore size
Micropore, this can be by being modified acquisition to existing water penetration diaphragm, and water penetration diaphragm uses titania modified technology,
Increase nano-titanium dioxide hydrophilic monomer in ultrafiltration membrane surface by using irradiation technique, improves ultrafiltration membrane hydrophily, enhance film
Stain resistance, prolonging service lifetime of film.It mutually promotes simultaneously with plasma discharge cold in water, Organic substance in water can be effectively improved
Degradation rate also effectively prevents the deterioration that biological index is easily led to because current density is excessive.
Detailed description of the invention
The tea maker of degradable remains of pesticide of the invention is described further with reference to the accompanying drawing.
Fig. 1 is the inside partial structural diagram of the tea maker of the degradable remains of pesticide of the embodiment of the present invention one.
Fig. 2 is the inside partial structural diagram of the tea maker of the degradable remains of pesticide of the embodiment of the present invention four.
Fig. 3 is the permeable microcellular structure schematic diagram in the water penetration diaphragm of Fig. 1.
Specific embodiment
Embodiment one
The tea maker of the degradable remains of pesticide of the present embodiment, referring to Fig. 1, including a pair of of negative electrode 22 and positive electrode
It 23, is the electrolysis power and Insulating frame 25 of anodic-cathodic power supply.Water penetration diaphragm 21 is equipped between anodic-cathodic.
Negative electrode 22 and positive electrode 23 are the tubular electrodes being fixed on Insulating frame 25, and negative electrode 22 is formed with mesh,
Partition and the lower chambers 14 by partition by tubular negative electrode inside division at upper chamber 13 and placement tealeaves are equipped in negative electrode 22.
Positive electrode 23 is set in upper chamber 13.Water penetration diaphragm 21, which is expired tilt and set, to be coated on 23 outer surface of positive electrode.When in use, negative
Electrode 22 immerses in tea water, and positive electrode 23 is only contacted with tea water by the infiltration water that water penetration diaphragm 21 permeates.
The water penetration diaphragm 21 of the present embodiment is water penetration diaphragm made of non-conductive material, and water penetration diaphragm 21 has
The permeable micropore of uniform pore size.The permeable micropore of uniform pore size is that the shape in pore size and hole is generally uniform, for example, a film
In be all the hole of the same shape, for example be all the hole of ellipse, the hole of triangle, etc..Pore size in one film is all
The hole, etc. of same size.
The infiltration water of apparatus of the present invention is successively to generate.The positive electrode 23 of apparatus of the present invention and water penetration diaphragm 21 it
Between be only clamped with water membrane, can be in cell reaction in this way, be not no water on remaining side of the positive electrode of apparatus of the present invention
Outside being normally carried out, reaction of the source water electrolysis on positive electrode is also especially reduced.Meanwhile positive electrode is close to water penetration diaphragm, it is positive
The oxygen etc. of pole reaction is easily accessible membrane micropore and generates bubble in millipore water, in the narrow environment of membrane micropore, bubble breaking
Localized hyperthermia's high pressure is generated, partially enters in film and induces water body itself gasification, and then efficient water body is inspired with minimum voltage
Plasma discharge generates hydroxyl free base class transient state oxidation factor in water.
The water penetration diaphragm 21 of the present embodiment is the non-conductive material filter membranes such as single layer micro-filtration-nanofiltration.When using electric discharge,
Plasma discharge is formed in permeable micropore.For more preferable more generation hydroxyl radical free radical plasma groups, when using electric discharge, often
Plasma discharge is respectively formed in a permeable micropore.
It, can be with so that plasma preferably discharges in film in order to which water penetration diaphragm 21 obtains the micropore of uniform pore size
Produce acquisition by being modified to water penetration diaphragm 21, water penetration diaphragm 21 have uniform pore size micropore be by according to
Diaphragm made of lower step:
1) by nanometer titanium dioxide titanium solution ultraviolet case internal irradiation 10-30 minutes that temperature is 40 DEG C -60 DEG C;
2) film liquid is formed by the raw material of following mass ratio:
PVDF:20%-30%
Pore-foaming agent: 2-5%
Nano-titanium dioxide after step 1) irradiation: 2%-4%
Surfactant: 3%-5%
Solvent: 70%-80%;
3) configured film liquid is passed through supersonic oscillations 20-40 minutes;
4) spread to liquid film with knifing machine, liquid film stood to 10-30 seconds in air, be then immersed in solidification liquid be frozen into every
Film;
5) diaphragm is to impregnate 10-40 minutes in 10% alcohol water blend in concentration, is then placed in deionized water and rinses;
6) diaphragm is placed in the pure water tank for being applied with 10kv DC pulse high voltage and is handled 1 hour.
The water penetration diaphragm 21 of the present embodiment selects hydrophilic water penetration diaphragm.The water penetration diaphragm 21 of the present embodiment
Permeable aperture is respectively less than the permeable aperture size for being equal to 2 millimeters and being more than or equal to all micropores in 1 nanometer and water penetration diaphragm 21
It is differed each other less than 20% between each other.It is preferred that ultrafiltration membrane.
One, 1 is tested
The present invention is located in kettle, fills tap water manually in kettle body, with the city in DaLian, China area for tap water
For, electrolysis power uses average voltage as the DC power supply of the high level narrow spaces of 40V, provides constant current 800mA, permeable
Property diaphragm 21 use ultrafiltration membrane, full tilt is located on 23 outer surface of positive electrode.
Chlorine residue and various harmful anions are remained in the water of source to migrate to anode, are pierced by diaphragm and are entered water body between anode and film
And it is discharged.By testing inspection, total plate count < 2CFU/ml in water;0.001 mg/L of phenol compounds <;Anion synthesis
Detergent < 0.001mg/L;0.001 mg/L of carbon tetrachloride <;Chloroform < 0.013mg/L, opposite city is for tap water, very
Good improves water quality.
In order to prevent anions and canons precipitate 21 surface of electrode and water penetration diaphragm deposition fouling, in electrolytic process
In suitably switch the electrolysis power polarity for being applied to pairs of electrode.
Embodiment two
The tea maker of the degradable remains of pesticide of the present embodiment is improvement on the basis of embodiment one, with embodiment one
The difference is that:
The present embodiment fills tap water manually in kettle body, still by taking the city in DaLian, China area is for tap water as an example, electrolysis
Power supply is greater than the component pulse-changing power of backward voltage level, average voltage 15V, water penetration diaphragm 21 using forward voltage level
The spacing δ between positive electrode 23 using microfiltration membranes, microfiltration membranes and on the outside of film is 15 millimeters.
Embodiment three
The tea maker of the degradable remains of pesticide of the present embodiment is improvement on the basis of embodiment one, with embodiment one
The difference is that: it is located on the positive electrode 23 in 21 outside of water penetration diaphragm in the present embodiment and is provided with several through-holes, water penetration
Diaphragm 21 uses nanofiltration membrane.
The present embodiment still by taking the city in DaLian, China area is for tap water as an example, water penetration diaphragm 21 be located at diaphragm on the outside of
Spacing δ between positive electrode 23 is respectively 0 millimeter, 10 millimeters and is tested.
Example IV
The tea maker of the degradable remains of pesticide of the present embodiment is improvement on that basi of the above embodiments, with above-mentioned reality
Apply example the difference is that: as shown in Fig. 2, the Insulating frame 25 of the present embodiment is insulating panel, 23 top surface of positive electrode is close to
On insulating panel, water penetration diaphragm 21, which completely hides, is wrapped in the other outer surfaces in addition to top surface of positive electrode 23, by positive electrode 23
Inside be closed as a closed chamber, the exhaust outlet 15 being connected to the space of positive electrode 23 is provided on insulating panel.
Physical absorption filtering layer 24 is equipped in the closed chamber of the present embodiment.Physical absorption filtering layer 24 be seed activity layer of charcoal,
Sintering activity layer of charcoal, activated carbon fiber layers, micro-filtration material layer or the micro-filtration material layer made of porous ceramics made of PP cotton.
The tea maker of degradable remains of pesticide of the invention is not limited to the above embodiment the specific technical solution,
Such as: 1) electrolysis power be high level narrow spaces direct current pulse power source or forward voltage level be greater than backward voltage level friendship
Become the pulse power;2) positive electrode 23 is to be combined by active carbon or active carbon with titanium coating platinum group oxide;3) of the invention
The technical solution of above-mentioned each embodiment new technical solution, etc. can be formed with combined crosswise each other.All use equally is replaced
Change the technical solution to be formed be the present invention claims protection scope.
Claims (9)
1. a kind of tea maker of degradable remains of pesticide, including a pair of of anodic-cathodic, the electrolysis powered for the anodic-cathodic
Power supply and Insulating frame are equipped with water penetration diaphragm between anodic-cathodic, it is characterised in that: the negative electrode and positive electrode are solid
The tubular electrode being scheduled on Insulating frame, the negative electrode are formed with mesh, partition are equipped in the negative electrode and by partition by cylinder
At the lower chambers of upper chamber and placement tealeaves, the positive electrode is set in the upper chamber shape negative electrode inside division, described
Aqueous diaphragm, which is expired tilt and set, to be coated on the positive electrode outer surface, and the Insulating frame is insulating panel, the positive electrode top
Face is tightly attached on the insulating panel, and the water penetration diaphragm, which completely hides, is wrapped in the positive electrode other appearances in addition to top surface
The inside of the positive electrode is closed as a closed chamber, is provided on the insulating panel and is connected to the space of positive electrode by face
Exhaust outlet, the permeable aperture of the water penetration diaphragm, which is respectively less than, to be equal to 2 millimeters and is more than or equal to 1 nanometer, when in use, described
Negative electrode immerses in tea water, and the positive electrode is only connect with the tea water by the infiltration water that the water penetration diaphragm permeates
Touching.
2. the tea maker of degradable remains of pesticide according to claim 1, it is characterised in that: the water penetration diaphragm right and wrong
Water penetration diaphragm made of conductive material, the water penetration diaphragm have the permeable micropore of uniform pore size.
3. the tea maker of degradable remains of pesticide according to claim 2, it is characterised in that: the water penetration diaphragm is parent
Aqueous water penetration diaphragm.
4. the tea maker of degradable remains of pesticide according to claim 3, it is characterised in that: formed in the permeable micropore
Plasma discharge.
5. the tea maker of degradable remains of pesticide according to claim 4, it is characterised in that: when using electric discharge, each
Plasma discharge is respectively formed in permeable micropore.
6. the tea maker of degradable remains of pesticide according to claim 5, it is characterised in that: be equipped in the closed chamber
Physical absorption filtering layer.
7. the tea maker of degradable remains of pesticide according to claim 6, it is characterised in that: the physical absorption filtering layer is
Seed activity layer of charcoal, sintering activity layer of charcoal, activated carbon fiber layers, the micro-filtration material layer made of PP cotton are made of porous ceramics
Micro-filtration material layer.
8. according to claim 1 to 5 any degradable remains of pesticide tea maker, it is characterised in that: it is described permeable
The permeable aperture size of all micropores is differed each other less than 20% between each other in property diaphragm.
9. according to claim 1 to 5 any degradable remains of pesticide tea maker, it is characterised in that: it is described permeable
Property diaphragm is the diaphragm made of according to the following steps:
1) by nanometer titanium dioxide titanium solution ultraviolet case internal irradiation 10-30 minutes that temperature is 40 DEG C -60 DEG C;
2) film liquid is formed by the raw material of following mass ratio:
PVDF:20%-30%
Pore-foaming agent: 2-5%
Nano-titanium dioxide after step 1) irradiation: 2%-4%
Surfactant: 3%-5%
Solvent: 70%-80%;
3) configured film liquid is passed through supersonic oscillations 20-40 minutes;
4) liquid film is spread to knifing machine, liquid film is stood to 10-30 seconds in air, is then immersed in solidification liquid and is frozen into diaphragm;
5) diaphragm is to impregnate 10-40 minutes in 10% alcohol water blend in concentration, is then placed in deionized water and rinses;
6) diaphragm is placed in the pure water tank for being applied with 10kv DC pulse high voltage and is handled 1 hour.
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CN105858819B (en) * | 2015-09-20 | 2019-01-11 | 大连双迪创新科技研究院有限公司 | The tea maker of degradable remains of pesticide |
CN109044105A (en) * | 2018-08-31 | 2018-12-21 | 大连双迪创新科技研究院有限公司 | The tea maker of tea stain can be washed and its wash after tea stain method of making tea |
CN109090993A (en) * | 2018-08-31 | 2018-12-28 | 大连双迪创新科技研究院有限公司 | The tea maker of tea can be washed and its wash the method for making tea and wash tea stain method |
CN109008627A (en) * | 2018-08-31 | 2018-12-18 | 大连双迪创新科技研究院有限公司 | A kind of tea device and its method of making tea wash the method for making tea and wash tea stain method |
CN109497790A (en) * | 2018-08-31 | 2019-03-22 | 大连双迪创新科技研究院有限公司 | Tea device and its method of making tea wash the method for making tea and wash tea stain method |
CN111557358A (en) * | 2020-04-13 | 2020-08-21 | 复旦大学 | Device and method for industrially and rapidly preparing cold-making tea |
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CN103936109A (en) * | 2014-04-12 | 2014-07-23 | 大连双迪创新科技研究院有限公司 | Drinking water electrolysis preparation device |
CN103951020A (en) * | 2014-04-12 | 2014-07-30 | 大连双迪科技股份有限公司 | Health water dispenser |
CN205603274U (en) * | 2015-09-20 | 2016-09-28 | 大连双迪创新科技研究院有限公司 | Device of making tea of degradable remains of pesticide |
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JP4665880B2 (en) * | 2006-09-26 | 2011-04-06 | パナソニック電工株式会社 | Electrolyzed water generator |
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CN103936109A (en) * | 2014-04-12 | 2014-07-23 | 大连双迪创新科技研究院有限公司 | Drinking water electrolysis preparation device |
CN103951020A (en) * | 2014-04-12 | 2014-07-30 | 大连双迪科技股份有限公司 | Health water dispenser |
CN205603274U (en) * | 2015-09-20 | 2016-09-28 | 大连双迪创新科技研究院有限公司 | Device of making tea of degradable remains of pesticide |
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