CN107098536A - The production method and its process units of a kind of use running water manufacture direct drinking - Google Patents
The production method and its process units of a kind of use running water manufacture direct drinking Download PDFInfo
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- CN107098536A CN107098536A CN201710382612.5A CN201710382612A CN107098536A CN 107098536 A CN107098536 A CN 107098536A CN 201710382612 A CN201710382612 A CN 201710382612A CN 107098536 A CN107098536 A CN 107098536A
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- Prior art keywords
- water
- outer tube
- insulation outer
- direct drinking
- running water
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 155
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 47
- 230000035622 drinking Effects 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims abstract description 22
- 230000008569 process Effects 0.000 title claims abstract description 17
- 238000009413 insulation Methods 0.000 claims abstract description 76
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 30
- 238000002242 deionisation method Methods 0.000 claims abstract description 28
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 22
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 21
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 19
- 239000004917 carbon fiber Substances 0.000 claims description 19
- 239000012528 membrane Substances 0.000 claims description 16
- 238000005341 cation exchange Methods 0.000 claims description 10
- 239000003011 anion exchange membrane Substances 0.000 claims description 9
- 230000005684 electric field Effects 0.000 claims description 6
- 230000005611 electricity Effects 0.000 claims description 6
- 230000004907 flux Effects 0.000 claims description 6
- 230000035699 permeability Effects 0.000 claims description 6
- 229910001220 stainless steel Inorganic materials 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 5
- 238000007789 sealing Methods 0.000 claims description 5
- 239000003245 coal Substances 0.000 claims description 3
- 239000002994 raw material Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 2
- 108091006146 Channels Proteins 0.000 claims 2
- 102000010637 Aquaporins Human genes 0.000 claims 1
- 108010063290 Aquaporins Proteins 0.000 claims 1
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims 1
- 239000003651 drinking water Substances 0.000 abstract description 4
- 235000020188 drinking water Nutrition 0.000 abstract description 3
- 239000008399 tap water Substances 0.000 abstract description 2
- 235000020679 tap water Nutrition 0.000 abstract description 2
- 241000894006 Bacteria Species 0.000 abstract 1
- 231100000989 no adverse effect Toxicity 0.000 abstract 1
- 150000002500 ions Chemical class 0.000 description 11
- 230000001954 sterilising effect Effects 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 7
- 238000004659 sterilization and disinfection Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 230000010354 integration Effects 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 230000000844 anti-bacterial effect Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 239000007772 electrode material Substances 0.000 description 2
- 230000005686 electrostatic field Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000006385 ozonation reaction Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000012271 agricultural production Methods 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 235000012206 bottled water Nutrition 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
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
-
- 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
- C02F1/02—Treatment of water, waste water, or sewage by heating
-
- 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
- C02F1/4691—Capacitive deionisation
-
- 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
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
- C02F1/487—Treatment of water, waste water, or sewage with magnetic or electric fields using high frequency electromagnetic fields, e.g. pulsed electromagnetic fields
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses the production method that a kind of use running water manufactures direct drinking, comprise the following steps：Running water is filtered by active carbon filter core；Subsequently enter the capacitive deionization unit of one or more groups of series connection；Magnetize by Electromagnetic Treatment component, sterilize and heat discharge；Wherein, Electromagnetic Treatment component includes insulation outer tube, the heat conductive rod in insulation outer tube and the magnet coil being wrapped in outside insulation outer tube, insulate and form water stream channel between the inwall of outer tube and the outer wall of the heat conductive rod, the two ends of insulation outer tube are respectively equipped with the water inlet and delivery port connected with water stream channel, its water inlet is connected with the water side of capacitive deionization unit, and delivery port is provided with valve.The invention also discloses the process units that a kind of use running water manufactures direct drinking.The present invention can not only quickly and efficiently purify running water and kill the bacterium in running water, realize the purpose of production direct drinking, and tap water quality is almost had no adverse effect, safe and environment-friendly and cost is low.
Description
Technical field
The present invention relates to tap water purifying field, and in particular to a kind of production method of use running water manufacture direct drinking and
Its process units.
Background technology
Along with the development and the increase of population of industrial and agricultural production, life and production pollutant emission are increasing, water money
Source pollution is increasingly severe.Water is Source of life, and the quality of Drinking Water matter is healthy closely related with people's.People
The Drinking Water water quality pursued with going from bad to worse to healthy living forms sharp contradiction.To meet health of people, it is fast
Prompt life style, various Potable water equipments emerge in an endless stream.
Current direct drinking production technology on the market, main active carbon adsorption, membrane separation technique, ozonation technology
Deng, or various treatment technologies group technology.Wherein active carbon adsorption or ozonation technology handle water outlet, it is difficult to reach
To higher direct drinking quality.Membrane separation technique can retain ion and organic matter, with that separative efficiency is high, effluent quality is good etc. is excellent
Point；But fouling membrane easily occurs for the technology, and membrane material price and operating cost are high.
The content of the invention
It is an object of the invention to provide a kind of safe and stable, efficient and lower-cost use running water manufacture direct drinking
Production method and its process units.
To achieve the above object, a kind of use running water provided by the present invention manufactures the production method of direct drinking, and it is special
Levy and be, running water is filtered by active carbon filter core；Subsequently enter the capacitive deionization unit of one or more groups of series connection；By electricity
Magnetic treatment component magnetizes, sterilizes and heat discharge；
Wherein, the Electromagnetic Treatment component includes insulation outer tube, the heat conductive rod in the insulation outer tube and winding
Magnet coil outside the insulation outer tube, the insulation outer tube is in the hollow circuit cylinder bodily form, the insulation outer tube and the heat conduction
Rod is coaxially disposed, and is formed between the inwall of the insulation outer tube and the outer wall of the heat conductive rod outside water stream channel, the insulation
The two ends of pipe are respectively equipped with the water inlet and delivery port connected with the water stream channel, the water inlet of the insulation outer tube with it is described
The water side connection of capacitive deionization unit, the delivery port of the insulation outer tube is provided with valve.
It is used as the preferred technical scheme of the production method of above-mentioned use running water manufacture direct drinking, the Electromagnetic Treatment component
Also include CPU and control module and for the electromagnetic variable-frequency mould for the high frequency magnetic energy that 50Hz electric energy is converted into 25-60KHz
Group, the magnet coil is electrically connected with the electromagnetic variable-frequency module, and the electromagnetic variable-frequency module is electrically connected with CPU control modules
Connect.
It is used as the preferred technical scheme of the production method of above-mentioned use running water manufacture direct drinking, the outer wall of the heat conductive rod
Guiding gutter is provided with, the guiding gutter is set around the heat conductive rod spiral.
As the preferred technical scheme of the production method of above-mentioned use running water manufacture direct drinking, the active carbon filter core
Raw material is shell activated carbon or coal mass active carbon；Specific surface area is more than 800m2/g。
It is used as the preferred technical scheme of the production method of above-mentioned use running water manufacture direct drinking, the capacitive deionization list
Member is made up of positive pole, negative pole and insulation net, and the positive pole is by positive pole stainless steel plate, the active carbon fiber electrode and anion of positive pole
Exchange membrane is constituted, and the thickness of the active carbon fiber electrode of the positive pole is 3-10mm, specific surface area 1300-2000m2/g；It is described
The thickness of anion-exchange membrane is 115-135 μm, and differential permeability is more than 90%, water flux 4 × 10-5ml/(Pa·m2·h)-
8×10-5ml/(Pa·m2H), pH scopes are 2-10；The negative pole is by negative pole stainless steel plate, the active carbon fiber electrode of negative pole
And cation-exchange membrane composition, the thickness of the active carbon fiber electrode of the negative pole is 3-10mm, specific surface area 1300-
2000m2/g；The thickness of the cation-exchange membrane is 125-145 μm, and differential permeability is more than 93%, water flux 8 × 10-5ml/
(Pa·m2·h)-12×10-5ml/(Pa·m2H), pH scopes are 4-12；The seepage discharge of the insulation net water is more than
500ml/min, thickness is 1-4mm.
Further, the active carbon fiber electrode of the positive pole is identical with anion-exchange membrane size, and area is 0.01-
0.03m2, length-width ratio is 1-2；The active carbon fiber electrode of the negative pole is identical with cation-exchange membrane size, and area is 0.01-
0.03m2, length-width ratio is 1-2.
Further, the active carbon fiber electrode of the positive pole, the active carbon fiber electrode of negative pole, anion-exchange membrane, sun
Amberplex and insulation net week side are sealed using sealing ring；The one end open of the sealing ring connects the work by water inlet pipe
Property carbon filtration core water side, another end opening by outlet pipe connect it is described insulation outer tube water inlet.
Further, the electric field applied voltage of the capacitive deionization unit is 1-2V.
In order to solve identical technical problem, present invention also offers a kind of production dress of use running water manufacture direct drinking
Put, it includes active carbon filter core, the capacitive deionization list of one or more groups of series connection set gradually along the water (flow) direction of running water
Member and Electromagnetic Treatment component；Wherein, the Electromagnetic Treatment component includes insulation outer tube, the heat conduction in the insulation outer tube
Rod and the magnet coil being wrapped in outside the insulation outer tube, the insulation outer tube is in the hollow circuit cylinder bodily form, the insulation outer tube
It is coaxially disposed with the heat conductive rod, and water stream channel is formed between the inwall of the insulation outer tube and the outer wall of the heat conductive rod,
The two ends of the insulation outer tube are respectively equipped with the water inlet and delivery port connected with the water stream channel, and the insulation outer tube enters
The mouth of a river is connected with the water side of the capacitive deionization unit, and the delivery port of the insulation outer tube is provided with valve；The heat conductive rod
Outer wall be provided with guiding gutter, the guiding gutter sets around the heat conductive rod spiral；The Electromagnetic Treatment component also includes CPU and controlled
Molding group and for the electromagnetic variable-frequency module for the high frequency magnetic energy that 50Hz electric energy is converted into 25-60KHz, the electromagnetism
Coil is electrically connected with the electromagnetic variable-frequency module, and the electromagnetic variable-frequency module is electrically connected with CPU control modules.
As the preferred technical scheme of the process units of above-mentioned use running water manufacture direct drinking, in addition to preheating assembly,
The preheating assembly includes thermal conductive water pipe, heat conduction clamshell and lagging casing, and the water inlet end of the thermal conductive water pipe is gone with the electric capacity
The water side connection of ion unit, the water side of the thermal conductive water pipe is connected with the water inlet of the insulation outer tube；The heat conduction
Clamshell is located at the electromagnetic variable-frequency module with CPU control modules, multiple rows of tube seat is provided with the outer surface of the heat conduction clamshell,
The thermal conductive water pipe is arranged on the heat conduction clamshell along the tube seat is roundabout, and the lagging casing is located at the heat conduction clamshell
With the outside of the thermal conductive water pipe.
Implement the production method and its process units of a kind of use running water manufacture direct drinking of the present invention, with prior art
Compare, have the advantages that：
It is of the invention main using active carbon filter core filtering, capacitive deionization unit removal harmful ion and Electromagnetic Treatment component
The process integration purification running water for magnetizing, sterilizing and heat produces pure direct drinking.Wherein, active carbon filter core filtering is to remove
The technique of a small amount of suspension and organic matter in running water；Capacitive deionization be by applying electrostatic field, force ion to
The electrode transfer of opposite charges, makes its electric double layer absorption produced by electrode surface and is removed from solution, so as to reach removal
The purpose of harmful ion in running water；Electromagnetic Treatment component is to produce high frequency strong magnetic in insulation outer tube by high-frequency impulse
With intensive magnetic field lines, the water by water stream channel is carried out every sky sensing sterilization, due to magnetic field under non high temperature environment
Concentrate, whole sterilization process has that energy consumption is low, sterilizing time is short, and bactericidal effect good spy strong to microorganism killing ability
Point, meanwhile, the high frequency magnetic field that current will be produced during by water stream channel by magnet coil is quickly heated, this to add
Hot mode can thoroughly realize electricity separation, ensure the safety of user；And the water meeting after being handled through this Electromagnetic Treatment component
Become magnetized water, activity is strong, is difficult in water stream channel to generate incrustation scale.Thus, in the presence of process integration, by controlling work
Skill condition is entirely capable of realizing the purpose of production direct drinking, and uses this method, and material cost and operating cost are low, to running water
Good purification.In addition, capacitive deionization unit makes electric field disappear or be filled with counter current by short circuit, make the former ion adsorbed
Depart from the electric double layer of electrode so that electrode material regenerates, during the not chemicals such as consumption acids, alkali, salt, be a kind of green
Production process.
Brief description of the drawings
Fig. 1 is the principle schematic of the process units of the use running water manufacture direct drinking of the present invention；
Fig. 2 is the front view of capacitive deionization unit；
Fig. 3 is the A-A sectional views in structure shown in Fig. 2；
Fig. 4 is the B-B sectional views in structure shown in Fig. 3；
Structural representation when Fig. 5 is Electromagnetic Treatment component and preheating assembly connection；
Fig. 6 is the sectional view of Electromagnetic Treatment component.
Embodiment
With reference to the accompanying drawings and examples, the embodiment to the present invention is described in further detail.Implement below
Example is used to illustrate the present invention, but is not limited to the scope of the present invention.
As shown in Figures 1 to 6, a kind of use running water provided by the present invention manufactures the production method of direct drinking, specifically
It is as follows：Running water is filtered by active carbon filter core 1 first, removes a small amount of suspension and organic matter therein；Subsequently enter one group
Or the capacitive deionization unit 2 of multigroup series connection, the harmful ion in removing running water in the presence of electric field；By Electromagnetic Treatment
Component 3 is discharged after magnetizing, sterilize and heating, and discharge water is pure direct drinking.Wherein, the heating temperature of Electromagnetic Treatment component 3
Degree is controllable, you can normal temperature or high-temperature water outlet.
In the present embodiment, the raw material of the active carbon filter core 1 is shell activated carbon or coal mass active carbon；Specific surface area is more than
800m2/g。
In the present embodiment, the capacitive deionization unit 2 is made up of positive pole, negative pole and insulation net 25, positive pole, insulation net
25 and negative pole tightened together by bolt, nut.Wherein, the positive pole is fine by the activated carbon of positive pole stainless steel plate 21, positive pole
Dimension electrode 22 and anion-exchange membrane 23 are constituted, active carbon fiber electrode 22 and the size phase of anion-exchange membrane 23 of the positive pole
Together, its area is 0.01-0.03m2, length-width ratio is 1-2, and thickness is 3-10mm, specific surface area 1300-2000m2/g；It is described it is cloudy from
The thickness of proton exchange 23 is 115-135 μm, and differential permeability is more than 90%, water flux 4 × 10-5ml/(Pa·m2·h)-8
×10-5ml/(Pa·m2H), pH scopes are 2-10.The negative pole is by negative pole stainless steel plate 29, the activated carbon fiber electricity of negative pole
Pole 28 and cation-exchange membrane 26 are constituted, and the active carbon fiber electrode 28 of the negative pole is identical with the size of cation-exchange membrane 26,
Its area is 0.01-0.03m2, length-width ratio is 1-2, and thickness is 3-10mm, specific surface area 1300-2000m2/g；The cation
The thickness of exchange membrane 26 is 125-145 μm, and differential permeability is more than 93%, water flux 8 × 10-5ml/(Pa·m2·h)-12×
10-5ml/(Pa·m2H), pH scopes are 4-12.The seepage discharge of the insulation water of net 25 is more than 500ml/min, and thickness is 1-
4mm.Further, active carbon fiber electrode 28, the anion-exchange membrane of the active carbon fiber electrode 22 of the positive pole, negative pole
23rd, cation-exchange membrane 26 and the insulation periphery of net 25 are sealed using sealing ring；The one end open of the sealing ring passes through water inlet pipe
The water side of the 241 connection active carbon filter cores 1, another end opening connects the Electromagnetic Treatment component 3 by outlet pipe 242
Water inlet.The electric field applied voltage of the capacitive deionization unit 2 is 1-2V.In addition, the group number of the capacitive deionization unit 2
Require to determine by influent quality and water outlet conductivity, the electrical conductivity that need to be removed is more, and required group of number is more.
In the present embodiment, the Electromagnetic Treatment component 3 includes insulation outer tube 31, the heat conduction in the insulation outer tube 31
Rod 32 and the magnet coil 33 being wrapped in outside the insulation outer tube 31, the insulation outer tube 31 is in the hollow circuit cylinder bodily form, described
Insulation outer tube 31 be coaxially disposed with the heat conductive rod 32, and it is described insulation outer tube 31 inwall and the heat conductive rod 32 outer wall it
Between form water stream channel 34, the two ends of the insulation outer tube 31 be respectively equipped with the water inlet 35 that is connected with the water stream channel 34 and
Delivery port 36, the water inlet 35 of the insulation outer tube 31 is connected with the water side of the capacitive deionization unit 2, outside the insulation
The delivery port 36 of pipe 31 is provided with valve.Further, the Electromagnetic Treatment component 3 also includes CPU control modules 37 and for inciting somebody to action
50Hz electric energy is converted into the electromagnetic variable-frequency module 38 of 25-60KHz high frequency magnetic energy, the magnet coil 33 and the electromagnetism
Frequency conversion module 38 is electrically connected, and the electromagnetic variable-frequency module 38 is electrically connected with CPU control modules 37.The heat conductive rod 32
Outer wall is provided with guiding gutter 39, and the setting of guiding gutter 39 can not only be carried out to incrustation scale that may be present in water stream channel 34 automatically
Further cleaning is washed away, and prevents the generation of incrustation scale, and can also guide current quickly through water stream channel 34.Especially, it is described
Guiding gutter 39 is set around the spiral of heat conductive rod 32, so as to form screw type water stream channel, can be realized to the comprehensive sterilization of water,
Improve bactericidal effect.It is of course also possible to set guiding gutter 39 on the inwall of insulation outer tube 31.
In order to solve identical technical problem, present invention also offers a kind of production dress of use running water manufacture direct drinking
Put, it includes active carbon filter core 1, the capacitive deionization list of one or more groups of series connection set gradually along the water (flow) direction of running water
Member 2 and Electromagnetic Treatment component 3；Wherein, the Electromagnetic Treatment component 3 includes insulation outer tube 31, located at the insulation outer tube 31
Interior heat conductive rod 32 and the magnet coil 33 being wrapped in outside the insulation outer tube 31, the insulation outer tube 31 is in hollow circular cylinder
Shape, the insulation outer tube 31 is coaxially disposed with the heat conductive rod 32, and the inwall and the heat conductive rod 32 of the insulation outer tube 31
Outer wall between formed water stream channel 34, it is described insulation outer tube 31 two ends be respectively equipped with and entering that the water stream channel 34 is connected
The mouth of a river 35 and delivery port 36, the water inlet 35 of the insulation outer tube 31 are connected with the water side of the capacitive deionization unit 2, institute
The delivery port 36 for stating insulation outer tube 31 is provided with valve.Further, the Electromagnetic Treatment component 3 also include CPU control module 37 with
And for the electromagnetic variable-frequency module 38 for the high frequency magnetic energy that 50Hz electric energy is converted into 25-60KHz, the magnet coil 33 with
The electromagnetic variable-frequency module 38 is electrically connected, and the electromagnetic variable-frequency module 38 is electrically connected with CPU control modules 37.It is described to lead
The outer wall of hot pin 32 is provided with guiding gutter 39, and the guiding gutter 39 is set around the spiral of heat conductive rod 32.
Based on above-described embodiment, this process units also includes preheating assembly 4, and the preheating assembly 4 includes thermal conductive water pipe
41, thermal conductive water pipe 41 is set round electromagnetic variable-frequency module 38 and CPU control modules 37, the water inlet end of the thermal conductive water pipe 41 and institute
The water side (namely outlet pipe 242) for stating capacitive deionization unit 2 is connected, the water side of the thermal conductive water pipe 41 and the insulation
The water inlet 35 of outer tube 31 is connected.So, current just can directly take away electromagnetic variable-frequency module 38 and CPU controls in thermal conductive water pipe 41
The heat produced by power device on module 37, it is that electromagnetic variable-frequency module 38 and CPU control what module 37 radiated both to have served
Current again can be heated tentatively by effect, it is to avoid thermal loss.
Heat produced by power component is faster and better taken away in order to play, preheating assembly 4 also includes heat conduction clamshell
42 and lagging casing 43, heat conduction clamshell 42 is located on electromagnetic variable-frequency module 38 and CPU control modules 37, heat conduction clamshell 42 it is outer
Multiple rows of tube seat 44 is provided with surface, thermal conductive water pipe 41 is arranged on heat conduction clamshell 42 along tube seat 44 is roundabout, and lagging casing 43 covers
It is located at the outside of heat conduction clamshell 42 and thermal conductive water pipe 41.Here, set heat conduction clamshell 42 to increase heat-conducting area, so lead
The heat produced on power device just quickly can be conducted to thermal conductive water pipe 41 and current by hot clamshell 42, and last current are by heat
Take away；And set tube seat 44 then to increase the contact surface of thermal conductive water pipe 41 and heat conduction clamshell 42, i.e. conducting surface, equally play and add
The effect radiated soon；Lagging casing 43 can then avoid the water in heat conduction clamshell 42, thermal conductive water pipe 41 and thermal conductive water pipe 41 as far as possible
With the medium such as air heat exchange occurs for stream, so that the heat that produces of power device is as far as possible all for heating thermal conductive water pipe
Current in 41.
To sum up, the production method and its process units of a kind of use running water manufacture direct drinking of the present invention are implemented, mainly
Filtered using active carbon filter core 1, capacitive deionization unit 2 removes harmful ion and Electromagnetic Treatment component 3 magnetizes, sterilized and heats
Process integration purification running water produce pure direct drinking.Wherein, active carbon filter core 1 filtering be remove running water in it is a small amount of
The technique of suspension and organic matter；Capacitive deionization is by applying electrostatic field, forcing ion to the electrode with opposite charges
Migration, makes its electric double layer absorption produced by electrode surface and is removed from solution, being harmful in running water is removed so as to reach
The purpose of ion；Electromagnetic Treatment component 3 is to produce high frequency strong magnetic and intensive ring in insulation outer tube 31 by high-frequency impulse
The shape magnetic line of force, is carried out under non high temperature environment to the water by water stream channel 34 every sky sensing sterilization, due to magnetic field concentration, entirely
Sterilization process has that energy consumption is low, sterilizing time is short, and bactericidal effect good strong to microorganism killing ability the characteristics of, meanwhile, water
The high frequency magnetic field that flowing will be produced during by water stream channel 34 by magnet coil 33 is quickly heated, this mode of heating
Electricity separation can be thoroughly realized, the safety of user has been ensured；And the water after being handled through this Electromagnetic Treatment component 3 can become
Magnetized water, activity is strong, is difficult the generation incrustation scale in water stream channel 34.Thus, in the presence of process integration, by controlling technique
Condition is entirely capable of realizing the purpose of production direct drinking, and uses this method, and material cost and operating cost are low, to running water
Good purification.In addition, capacitive deionization unit 2 makes electric field disappear or be filled with counter current by short circuit, make the former ion adsorbed
Depart from the electric double layer of electrode so that electrode material regenerates, during the not chemicals such as consumption acids, alkali, salt, be a kind of green
Production process.
It the above is only the preferred embodiment of the present invention, it is noted that come for those skilled in the art
Say, without departing from the technical principles of the invention, some improvement and replacement can also be made, these, which improve and replaced, also should
It is considered as protection scope of the present invention.
Claims (10)
1. a kind of use running water manufactures the production method of direct drinking, it is characterised in that running water is filtered by active carbon filter core；
Subsequently enter the capacitive deionization unit of one or more groups of series connection；Magnetize by Electromagnetic Treatment component, sterilize and heat discharge；
Wherein, the Electromagnetic Treatment component includes insulation outer tube, the heat conductive rod in the insulation outer tube and is wrapped in institute
The magnet coil outside insulation outer tube is stated, the insulation outer tube is in the hollow circuit cylinder bodily form, and the insulation outer tube and the heat conductive rod are same
Axle is set, and forms water stream channel between the inwall of the insulation outer tube and the outer wall of the heat conductive rod, the insulation outer tube
Two ends are respectively equipped with the water inlet and delivery port connected with the water stream channel, water inlet and the electric capacity of the insulation outer tube
The water side connection of deionization unit, the delivery port of the insulation outer tube is provided with valve.
2. the production method of direct drinking is manufactured using running water as claimed in claim 1, it is characterised in that the Electromagnetic Treatment
Component also includes CPU and controls module and for the electromagnetic variable-frequency for the high frequency magnetic energy that 50Hz electric energy is converted into 25-60KHz
Module, the magnet coil is electrically connected with the electromagnetic variable-frequency module, the electromagnetic variable-frequency module and CPU control module electricity
Connection.
3. the production method of direct drinking is manufactured using running water as claimed in claim 2, it is characterised in that the heat conductive rod
Outer wall is provided with guiding gutter, and the guiding gutter is set around the heat conductive rod spiral.
4. the production method of direct drinking is manufactured using running water as claimed in claim 1, it is characterised in that the active carbon filtration
The raw material of core is shell activated carbon or coal mass active carbon；Specific surface area is more than 800m2/g。
5. as claimed in claim 1 using running water manufacture direct drinking production method, it is characterised in that the electric capacity go from
Subelement is made up of positive pole, negative pole and insulation net, and the positive pole is by positive pole stainless steel plate, the active carbon fiber electrode and the moon of positive pole
Amberplex is constituted, and the thickness of the active carbon fiber electrode of the positive pole is 3-10mm, specific surface area 1300-2000m2/g；
The thickness of the anion-exchange membrane is 115-135 μm, and differential permeability is more than 90%, water flux 4 × 10-5ml/(Pa·m2·
h)-8×10-5ml/(Pa·m2H), pH scopes are 2-10；The negative pole is by negative pole stainless steel plate, the activated carbon fiber of negative pole
Electrode and cation-exchange membrane composition, the thickness of the active carbon fiber electrode of the negative pole is 3-10mm, specific surface area 1300-
2000m2/g；The thickness of the cation-exchange membrane is 125-145 μm, and differential permeability is more than 93%, water flux 8 × 10-5ml/
(Pa·m2·h)-12×10-5ml/(Pa·m2H), pH scopes are 4-12；The seepage discharge of the insulation net water is more than
500ml/min, thickness is 1-4mm.
6. the production method of direct drinking is manufactured using running water as claimed in claim 5, it is characterised in that the work of the positive pole
Property carbon fiber electrode is identical with anion-exchange membrane size, and area is 0.01-0.03m2, length-width ratio is 1-2；The work of the negative pole
Property carbon fiber electrode is identical with cation-exchange membrane size, and area is 0.01-0.03m2, length-width ratio is 1-2.
7. the production method of direct drinking is manufactured using running water as claimed in claim 5, it is characterised in that the work of the positive pole
Property carbon fiber electrode, the active carbon fiber electrode of negative pole, anion-exchange membrane, cation-exchange membrane and insulation net week side using close
Seal is sealed；The one end open of the sealing ring connects the water side of the active carbon filter core, another end opening by water inlet pipe
The water inlet of the insulation outer tube is connected by outlet pipe.
8. as claimed in claim 1 using running water manufacture direct drinking production method, it is characterised in that the electric capacity go from
The electric field applied voltage of subelement is 1-2V.
9. a kind of use running water manufactures the process units of direct drinking, it is characterised in that including what is set gradually along water (flow) direction
Active carbon filter core, the capacitive deionization unit of one or more groups of series connection and Electromagnetic Treatment component；Wherein, the Electromagnetic Treatment group
Part includes insulation outer tube, the heat conductive rod in the insulation outer tube and the magnet coil being wrapped in outside the insulation outer tube,
The insulation outer tube is in the hollow circuit cylinder bodily form, and the insulation outer tube is coaxially disposed with the heat conductive rod, and the insulation outer tube
Water stream channel is formed between the outer wall of inwall and the heat conductive rod, the two ends of the insulation outer tube are respectively equipped with to be led to the current
The water inlet and delivery port of road connection, the water inlet of the insulation outer tube are connected with the water side of the capacitive deionization unit,
The delivery port of the insulation outer tube is provided with valve；The outer wall of the heat conductive rod is provided with guiding gutter, and the guiding gutter is led around described
Hot pin spiral is set；The Electromagnetic Treatment component also includes CPU and controls module and for 50Hz electric energy to be converted into 25-
The electromagnetic variable-frequency module of 60KHz high frequency magnetic energy, the magnet coil is electrically connected with the electromagnetic variable-frequency module, and the electromagnetism becomes
Frequency module is electrically connected with CPU control modules.
10. the production method of direct drinking is manufactured using running water as claimed in claim 1, it is characterised in that also including preheating
Component, the preheating assembly includes thermal conductive water pipe, heat conduction clamshell and lagging casing, the water inlet end of the thermal conductive water pipe and the electricity
Hold the water side connection of deionization unit, the water side of the thermal conductive water pipe is connected with the water inlet of the insulation outer tube；It is described
Heat conduction clamshell is located at the electromagnetic variable-frequency module with CPU control modules, being provided with the outer surface of the heat conduction clamshell multiple rows of
Tube seat, the thermal conductive water pipe is arranged on the heat conduction clamshell along the tube seat is roundabout, and the lagging casing is located at described lead
Hot clamshell and the outside of the thermal conductive water pipe.
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