CN206033907U - Hypochlorite generator device of scale deposit is prevented to integrated form - Google Patents
Hypochlorite generator device of scale deposit is prevented to integrated form Download PDFInfo
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- CN206033907U CN206033907U CN201621004875.XU CN201621004875U CN206033907U CN 206033907 U CN206033907 U CN 206033907U CN 201621004875 U CN201621004875 U CN 201621004875U CN 206033907 U CN206033907 U CN 206033907U
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Abstract
The utility model relates to a hypochlorite generator device of scale deposit is prevented to integrated form, the device include that clean salt solution cauldron separates formula electrolysis crowd through the liquid flow increasing pump of taking liquid fluid conveying pipe with the district and is connected, the hot brine that clean salt solution cauldron filtrated the material including the salt hot -water heating cauldron of taking the heater and area filtrates the cauldron and adjoins the antithetical couplet, is salt solution temperature in the salt hot -water heating cauldron 50 100 DEG C, the district separates formula electrolysis crowd and includes 2 to a N electrolysis cauldron, wherein passing through liquids flow increasing union coupling between every electrolysis cauldron, it to the electrode, singly is connected with the outside DC power supply of electrolysis cauldron the electrode all to be equipped with the list in every electrolysis cauldron, the liquid stream speed of the electrolyte of district in formula electrolysis crowd is not less than the water velocity of the salt solution in the clean salt solution cauldron. The utility model discloses collect scale removal, scale control and hinder measure scheme in an organic whole of dirt, and exert fine synergism, consequently the utility model discloses the scale deposit of electrode in the electrolysis trough can be prevented effectively, the operating efficiency of hypochlorite generator device is improved greatly.
Description
Technical field
This utility model belongs to domestic water processing equipment technical field, more particularly to a kind of integrated form good antiscale property time
Sodium chlorate generating apparatus.
Background technology
Existing known hypochlorite generator's device is the big domestic water processing equipment of this area wide application amount.Though
So hypochlorite generator's device has many advantages compared with similar products, but usually because being limited by hard water condition, and
So that the electrode surface fouling of the electrolysis bath of hypochlorite generator's device and attachment etc. is hung with, under its electrolytic efficiency is obvious
Drop.Conventional solution mainly has at present：Room temperature prefabricated softened water good antiscale property before electrolysis, the electrode scale removal of falling pole is set, to electricity
Solve groove cooling good antiscale property and using ultrasound wave foaming resistance fouling etc..However, these schemes are all present necessarily not to some extent
Foot, is not met by effectively preventing the needs of the electrode surface fouling of hypochlorite generator's device etc..
Chinese patent application 201511033467.7 is disclosed " a kind of electrification sterilization hydrotreater ", opaque including sealing
And for containing the water tank of common salt aqueous solution；At least one electrolysis bath, all electrolysis baths are connected with water tank by pump；Each electrolysis
The pole-reversing key being connected with two electrodes is equipped with groove；Open and close for controlling each pole-reversing key, by correspondence electrolysis bath
The time relay that two positive and negative electrodes are switched over, and power supply.Although the electrification sterilization hydrotreater can realize electrolysis
There is positive and negative electrode switching in groove after reaction certain hour, electrode instantaneously increases the dirt that electric current effectively can be removed on negative electrode
The effect of fouling, but also exist following substantially not enough：One is switched using positive and negative electrode, is removed with the instantaneous high current for producing cloudy
Though the dirt fouling extremely gone up is effective, electrode damage is larger, causes the life-span of electrode to greatly shorten；Two is to adopt positive and negative electrode
Switching descaling method, needs real-time shutdown to process, affects the continuous operation of electrolysis bath；Three is to give birth to scale removal again after dirt in a cell
Method is directly affected and reduces the operational efficiency of electrolysis bath.
Chinese patent application 201510648242.6 disclose " it is a kind of electrolysis tap water be used for disinfection electrode can remove
Dirty electrolytic water device ", including the electrolysis bath that electrolytic cell housing (1), anode (2) and negative electrode (3) are constituted, on electrolytic cell housing (1)
Anode (2), negative electrode (3) is provided with, anode (2), negative electrode (3) connect to fall polar circuit (4) by wire respectively, polar circuit (4) point
Control circuit (5) and electrolyzer power source (6) are not connected by wire, electrolytic cell housing (1) is provided with ultrasonic transducer (7),
Ultrasonic transducer (7) connects transducer driving circuit (8) by wire, and transducer driving circuit (8) is controlled by wire connection
Circuit (5) processed.Although the device is with the effect for reducing the generation of electrode surface incrustation scale and has certain scale removal effect, also exist
It is substantially not enough below：One is to switch descaling method using positive and negative electrode, directly affects electrode life, affects continuous operation and drop
The operational efficiency of low electrolysis bath；Though two is have the effect for reducing that electrode surface incrustation scale is generated using ultrasonic transducer foaming,
During centralization type electrolysis bath can not be solved, electrolyte unhurried current is obstructed not smooth and causes a raw dirty serious difficult problem.
In sum, how to overcome the shortcomings of existing for prior art, to have become current domestic water processing equipment technology neck
One of emphasis difficult problem urgently to be resolved hurrily in domain.
The content of the invention
The purpose of this utility model is for overcoming the shortcomings of to provide a kind of integrated form good antiscale property existing for prior art
Hypochlorite generator's device, high-temperature electrolyte of this utility model using prefabricated high temperature saline, increase flow stream velocity before electrolysis
Electrolysis and many kettles separate new departure of formula electrolysis such that it is able to be effectively prevented the electrode fouling of electrolysis bath, greatly improve secondary
Sodium chlorate generating apparatus operational efficiency.
According to the utility model proposes a kind of integrated form good antiscale property hypochlorite generator's device, it is characterised in that：
Group is electrolysed including clean saline kettle by the liquid flow increasing pump of carrying liqs pipe conveying fluid and the formula that separates to be connected；The clean saline kettle bag
Include the saline heating kettle with heater and adjoin connection, the salt water temperature in the saline heating kettle with the hot salt brine filtering kettle with filter material
Spend for 50-100 DEG C；The power of the liquid flow increasing pump is 10-100w, lift is 25-35m；It is described separate formula electrolysis group include 2
To N number of electrolysis kettle, wherein connected by liquid flow increasing pipe between each electrolysis kettle；It is equipped with including anode pole in each electrolysis kettle
The single pair of electrode of plate and cathode plate, the single pair of electrode are connected with the DC source outside electrolysis kettle；It is described to separate formula electrolysis
Water velocity of the flow stream velocity of the electrolyte in group not less than the saline in clean saline kettle.
It is of the present utility model to realize that principle is：This utility model be according to water scale removal, good antiscale property and resistance fouling principle and
Feature and hypochlorite generator's device of a kind of integrated form good antiscale property with new ideas for proposing, with existing known technology institute
Using electrolysis before prefabricated room temperature softened water good antiscale property, the electrode scale removal of falling pole is set, lower the temperature good antiscale property and utilization to electrolysis bath
The schemes such as ultrasound wave foaming resistance fouling are entirely different, and this utility model uses prefabricated clean high temperature saline, increase before electrolysis
The high-temperature electrolyte electrolysis of flow stream velocity and many kettles separate new departure of formula electrolysis.Specific principle effect：One is this practicality
Prefabricated clean high temperature saline scheme before the new electrolysis, can make the fouling impurity such as calcium ions and magnesium ions in saline at 50-100 DEG C
Hot conditionss under switched to profiling and absorption by filter material and then be electrolysed away from follow-up electrolyte by stealth；Two is high
Carry out again increasing the high-temperature electrolyte electrolysis of flow stream velocity after the filtered fouling impurity of warm saline, can be effectively prevented and be electrolysed
In journey, electrolyte forms secondary fouling；Three is the new departure for separating formula electrolysis using many kettles, i.e., by being respectively provided with the 2 of single pair of electrode
It is configured to be electrolysed kettle group to N number of electrolysis kettle, is beneficial to and changes electrolyte institute in the electrolysis kettle that existing multipair electrode centralization type is arranged
The unhurried current state of appearance, is reached with strengthening raising electrolyte flow and is prevented because of electrolyte flow difference and the effect of easy fouling
Really.This utility model integrates the measure scheme of scale removal, antiscale and scale inhibition, and has played good synergism, so as to take
Obtained the remarkable result of hypochlorite generator's device good antiscale property.
Its remarkable advantage is this utility model compared with prior art：
First, a kind of sodium hypochlorite of integrated form good antiscale property that this utility model is proposed on the basis of being built upon new ideas is sent out
Raw device device, it overcomes the prefabricated room temperature softened water good antiscale property adopted by the existing known technology in this area, arranges electrode pole
The deficiency of scale removal, good antiscale property of lowering the temperature to electrolysis kettle or the schemes such as resistance fouling that foamed using ultrasound wave, this utility model are highlighted
Single pair of electrode kettle in electrolysis kettle can effectively prevent the beneficial effect of fouling in electrolytic process.
Second, before electrolysis of the present utility model, prefabricated clean high temperature brine section can make the knot such as calcium ions and magnesium ions in saline
Dirty impurity is switched to profiling by stealth under the high temperature conditions and is further electrolysed away from follow-up electrolyte by the absorption of filter material,
Effect of its actual effect well beyond traditional prefabricated softened water good antiscale property of room temperature.
3rd, the high-temperature electrolyte for increasing flow stream velocity of the present utility model is electrolysed and traditional electrolyte unhurried current electrolysis phase
Than, the condition that the impurity such as fouling land on electrolytic zinc-coated steel sheet has been blocked because electrolyte flow rate increases, and because of high-temperature electrolyte and electricity
The temperature difference less condition that also significantly alleviate fouling of the pole in electrolysis such that it is able to be effectively prevented electrolyte in formation
Secondary fouling.
4th, this utility model separates kettle electrolysis using by single pair of electrode kettle and many kettles, is particularly electrolysed kettle with electrolysis kettle
Between connected by liquid flow increasing pipeline, preferably resolve electrolyte in traditional centralization type electrolysis bath and be obstructed not smooth difficulty
Topic so that the electrolyte in single pair of electrode group kettle is smooth without hindrance, so as to greatly alleviate the condition of fouling.
5th, prefabricated clean high temperature saline, the high-temperature electrolyte of increase flow stream velocity before the electrolysis that this utility model is adopted
It is the measure scheme for integrating scale removal, antiscale and scale inhibition that electrolysis and many kettles separate new departure of formula electrolysis, has been played very well
Synergism, not only achieve the remarkable result of hypochlorite generator's device good antiscale property, and also reduce electrode corrosion
Speed, improves the service life of electrolysis kettle, and this utility model also has the advantages that simple structure and easy to operate.
In sum, this utility model is applied to the not good hypochlorite generator's dress of the existing various scale-preventing performances of replacement
Put.
Description of the drawings
Fig. 1 be the utility model proposes a kind of integrated form good antiscale property hypochlorite generator's device separate formula electrolysis
The block diagram of group's vertical structure.
Fig. 2 be the utility model proposes a kind of integrated form good antiscale property hypochlorite generator's device separate formula electrolysis
The block diagram of group's horizontal type structure.
Fig. 3 be the utility model proposes single electrolysis kettle single pair of electrode arrangement schematic diagram.
Fig. 4 be the utility model proposes a kind of integrated form good antiscale property hypochlorite generator's device using method
Process blocks schematic diagram.
Specific embodiment
With reference to the accompanying drawings and examples specific embodiment of the present utility model is described in further detail.
With reference to Fig. 1, Fig. 2 and Fig. 3, the utility model proposes a kind of integrated form good antiscale property hypochlorite generator dress
Put, group (9) is electrolysed by liquid flow increasing pump (5) of carrying liqs pipe conveying fluid (6) and the formula that separates including clean saline kettle and is connected；It is described
Clean saline kettle includes that the saline heating kettle (1) with heater (3) adjoins connection with hot salt brine filtering kettle (2) with filter material (4),
Brine temp in saline heating kettle (1) is 50-100 DEG C；The power of liquid flow increasing pump (5) is 10-100w, lift
For 25-35m；Formula electrolysis group (9) that separates wherein passes through liquid flow increasing pipe between each electrolysis kettle including 2 to N number of electrolysis kettle
(8) connect；The single pair of electrode (7) including plate with cathode plate, single pair of electrode (7) are equipped with each electrolysis kettle
It is connected with the DC source outside electrolysis kettle；The flow stream velocity for separating the electrolyte in formula electrolysis group (9) is not less than cleaning
The water velocity of the saline in saline kettle.
The utility model proposes a kind of integrated form good antiscale property hypochlorite generator's device further preferred scheme
It is：
The heater (3) of saline heating kettle (1) is arranged on the inside of saline heating kettle (1) or saline heating kettle (1)
Outside；Brine temp in saline heating kettle (1) is 70 DEG C.
The filter material (4) of hot salt brine filtering kettle (2) is natural zeolite or ion exchange resin.
The electrical power of liquid flow increasing pump (5) is 40w, lift is 30 meters.
It is described to be electrolysed kettle vertical or horizontal setting successively by liquid flow increasing pipeline (8) connects 2 to N number of.
The distance between plate and cathode plate of single pair of electrode (7) in described each electrolysis kettle are 2-10mm.
The electrical power of the single pair of electrode (7) in described each electrolysis kettle is equal or unequal.
The water velocity of the saline in the clean saline kettle is electrolysed the flow stream velocity of the electrolyte in group (9) with the formula that separates
It is not less than 1 meter per second.
The nozzle diameter of liquid flow increasing pipe (8) for the nozzle diameter of liquid pipe conveying fluid (6) 1/2 to 3/4.
The utility model proposes a kind of hypochlorite generator's device of integrated form good antiscale property can be effectively prevented electricity
Fouling of the electrode of solution groove in electrolytic process, it is adaptable to substitute the not good hypochlorite generator of existing various scale-preventing performances
Device.
Below with the utility model proposes a kind of integrated form good antiscale property hypochlorite generator's device sodium hypochlorite
Production capacity is 100 Grams Per Hour meters, further discloses the specific embodiment and this utility model of the selection of this utility model partial condition
Using method embodiment.
Embodiment 1.
According to the utility model proposes a kind of integrated form good antiscale property hypochlorite generator's device and preferred version
Determine that implementation condition is as follows：
The heater (3) of saline heating kettle (1) is arranged on the inside of saline heating kettle (1)；In saline heating kettle (1)
It is 70 DEG C that the brine strength weight percentage of customization is 1%, brine temp；The water of the saline in saline heating kettle (1)
Flow velocity degree is 1 meter per second.
Filter material (4) in hot salt brine filtering kettle (2) is natural zeolite；The filling height of filter material (4) is not
Adjoin the overhead stream road junction (10) of connection more than saline heating kettle (1) and (2) two kettle of hot salt brine filtering kettle.
The electrical power of liquid flow increasing pump (5) is 40w, lift is 30 meters.
The electrolysis kettle is 4, and each electrolysis kettle is connected and longitudinally disposed successively by liquid flow increasing pipeline (8) respectively,
Be configured to vertical structure separates formula electrolysis group (9), and the gross electric capacity for separating formula electrolysis group (9) is 500w.
The distance between plate and cathode plate of single pair of electrode (7) in described each electrolysis kettle are 2mm；Each
Electrolysis kettle is provided with liquid-inlet (11) and liquid outlet (12).Referring to Fig. 3.
The electrical power of the single pair of electrode (7) in described each electrolysis kettle is equal；If embodiment 1 is using 4 electrolysis kettles, often
The electrical power of individual electrolysis kettle is 125w.
The flow stream velocity for separating the electrolyte in formula electrolysis group (9) is 1 meter per second.
The nozzle diameter of liquid flow increasing pipe (8) is 10mm；The 20mm of the nozzle diameter of liquid pipe conveying fluid (6).
Embodiment 2.
The heater (3) of saline heating kettle (1) is arranged on the inside of saline heating kettle (1) or saline heating kettle (1)
Outside；In saline heating kettle (1), the brine strength weight percentage of customization is 2%, brine temp for 50 DEG C；Saline
The water velocity of the saline in heating kettle (1) is 1.2 meter per seconds.
The filter material (4) of hot salt brine filtering kettle (2) is ion exchange resin；The filling height of filter material (4)
No more than saline heating kettle (1) and (2) two kettle of hot salt brine filtering kettle adjoin the overhead stream road junction (10) of connection.
The electrical power of liquid flow increasing pump (5) is 10w, lift is 25 meters.
The electrolysis kettle is 4, and each electrolysis kettle is connected and horizontally set successively by liquid flow increasing pipeline (8) respectively；
Be configured to horizontal type structure separates formula electrolysis group (9), and the gross electric capacity for separating formula electrolysis group (9) is 500w.
The distance between plate and cathode plate of single pair of electrode (7) in described each electrolysis kettle are 5mm；Each
Electrolysis kettle is provided with liquid-inlet (11) and liquid outlet (12).Referring to Fig. 3.
The electrical power of the single pair of electrode (7) in described each electrolysis kettle is unequal；If embodiment 2 is using 4 electrolysis kettles
What is built separates formula electrolysis group (9), wherein：The electrical power of the single pair of electrode (7) in the first kettle is 125w；Single pair of in second kettle
The electrical power of electrode (7) is 110w；The electrical power of the single pair of electrode (7) in the 3rd kettle is 130w；Single pair of electrode in 4th kettle
(7) electrical power is 135w.
The flow stream velocity for separating the electrolyte in formula electrolysis group (9) is 1.2 meter per seconds.
The nozzle diameter of liquid flow increasing pipe (8) is 12mm；The 20mm of the nozzle diameter of liquid pipe conveying fluid (6).
Embodiment 3.
The heater (3) of saline heating kettle (1) described in the utility model is arranged on the outside of saline heating kettle (1)；Saline
In heating kettle (1), the brine strength weight percentage of customization is 3%, brine temp for 100 DEG C；Saline heating kettle (1)
In saline water velocity be 1.35 meter per seconds.
The filter material (4) of hot salt brine filtering kettle (2) is natural zeolite；The filling height of filter material (4) is less
Adjoin the overhead stream road junction (10) of connection in saline heating kettle (1) and (2) two kettle of hot salt brine filtering kettle.
The electrical power of liquid flow increasing pump (5) is 100w, lift is 35 meters.
The electrolysis kettle is 4, and each electrolysis kettle is connected and longitudinally disposed successively by liquid flow increasing pipeline (8) respectively,
Be configured to vertical structure separates formula electrolysis group (9), and the gross electric capacity for separating formula electrolysis group (9) is 500w.
The distance between plate and cathode plate of single pair of electrode (7) in described each electrolysis kettle are 10mm；Often
Individual electrolysis kettle is provided with liquid-inlet (11) and liquid outlet (12).Referring to Fig. 3.
The electrical power of the single pair of electrode (7) in described each electrolysis kettle is unequal；If embodiment 3 is using 4 electrolysis kettles
What is built separates formula electrolysis group (9), wherein：The electrical power of the single pair of electrode (7) in the first kettle is 110w；Single pair of in second kettle
The electrical power of electrode (7) is 120w；The electrical power of the single pair of electrode (7) in the 3rd kettle is 130w；Single pair of electrode in 4th kettle
(7) electrical power is 140w.
The flow stream velocity for separating the electrolyte in formula electrolysis group (9) is 1.35 meter per seconds.
The nozzle diameter of liquid flow increasing pipe (8) is 15mm；The 20mm of the nozzle diameter of liquid pipe conveying fluid (6).
Embodiment 4.
With reference to Fig. 4, the utility model proposes a kind of integrated form good antiscale property hypochlorite generator's device user
Method, it includes by saline heating, clean hot salt brine, liquid flow increasing and separates the procedural style continuous processing of formula electrowinning process structure,
Specific implementation step is as follows：
Step 1, saline heating：The saline that upper one procedure customizes concentration is added continuously to into the band heating of clean saline kettle
In the saline heating kettle (1) of device (3), when the saline liquid level reaches the 2/3 of saline heating kettle (1) height, saline heating kettle (1)
The liquid level sensor of middle setting liquid level sends the signal that the saline reaches liquid level to PLC control stations, is controlled by PLC control stations
Heater (3) is heated to saline, obtains the hot salt brine of design temperature；Wherein：In saline heating kettle (1), the saline of customization is dense
Degree weight percentage is 1-3%, saline heating-up temperature is 50-100 DEG C；The current of the saline in saline heating kettle (1)
Speed is not less than 1 meter per second；
Step 2, hot salt brine are clean：The hot salt brine that step 1 is obtained is from saline heating kettle (1) and hot salt brine filtering kettle (2)
Two kettles adjoin the overhead stream road junction (10) of connection and flow in hot salt brine filtering kettle (2), and in hot salt brine filtering kettle (2) overflow filtering material
Material (4), when hot salt brine reaches the liquid level of overhead stream road junction (10), setting liquid level in hot salt brine filtering kettle (2)
Liquid level sensor sends the signal that the hot salt brine reaches liquid level to PLC control stations, sends next process by the control of PLC control stations
Enabling signal；Wherein：The filter material (4) of hot salt brine filtering kettle (2) is natural zeolite or ion exchange resin；
Step 3, liquid flow increasing：Liquid flow increasing pump (5) receive the enabling signal that PLC control stations described in step 2 send and
Operation is opened, hot salt brine is continuously introduced into by liquid fluid conveying pipe (6) in separating formula electrolysis group (9) and is electrolysed；Wherein：Institute
The power for stating liquid flow increasing pump (5) is 10-100w, lift is 25-35 rice；
Step 4, separates formula electrolysis：Separate the liquid angular sensor in formula electrolysis group (9) and receive the transmission of PLC control stations
Enabling signal starts the electrolysis to electrolyte, described to separate formula electrolysis group (9) including 2 to N number of electrolysis kettle, each electrolysis kettle it
Between by liquid flow increasing pipe (8) connect；The single pair of electricity with cathode plate composition including plate is equipped with each electrolysis kettle
The distance between pole (7), plate and cathode plate of single pair of electrode (7) are 2-10mm；Single pair of electrode (7) and electrolysis
DC source connection outside kettle, the electrical power of the single pair of electrode (7) in each electrolysis kettle are equal or unequal；It is described to separate formula
The flow stream velocity of the electrolyte in electrolysis group (9) is not less than 1 meter per second；The nozzle diameter of liquid flow increasing pipe (8) is that liquid is defeated
The 1/2 to 3/4 of the nozzle diameter of flow tube (6)；Electrolyte finished product prepared by Jing electrowinning processes is admitted to next process process.
In specific embodiment of the present utility model, all explanations being not directed to belong to techniques known above, can
It is carried out with reference to known technology.
This utility model Jing validation trials, achieve satisfied trial effect.
Above specific embodiment and embodiment be to the utility model proposes a kind of integrated form good antiscale property hypochlorous acid
The concrete support of sodium generating apparatus technological thought, it is impossible to which protection domain of the present utility model is limited with this, it is every according to this reality
With the technological thought of new proposition, any equivalent variations done on the basis of the technical program or equivalent change, still belong to
In the scope of technical solutions of the utility model protection.
Claims (9)
1. a kind of hypochlorite generator's device of integrated form good antiscale property, it is characterised in that：Including clean saline kettle by band liquid
Liquid flow increasing pump (5) of body pipe conveying fluid (6) is connected with formula electrolysis group (9) is separated；The clean saline kettle includes band heater (3)
Saline heating kettle (1) and hot salt brine filtering kettle (2) with filter material (4) adjoin connection, the saline in saline heating kettle (1)
Temperature is 50-100 DEG C；The power of liquid flow increasing pump (5) is 10-100w, lift is 25-35m；It is described to separate formula electrolysis group
(9) including 2 to N number of electrolysis kettle, wherein connected by liquid flow increasing pipe (8) between each electrolysis kettle；It is all provided with each electrolysis kettle
There is the single pair of electrode (7) with cathode plate including plate, single pair of electrode (7) are connected with the DC source outside electrolysis kettle
Connect；Water velocity of the flow stream velocity for separating the electrolyte in formula electrolysis group (9) not less than the saline in clean saline kettle.
2. hypochlorite generator's device of a kind of integrated form good antiscale property according to claim 1, it is characterised in that described
The heater (3) of saline heating kettle (1) is arranged on the inside of saline heating kettle (1) or the outside of saline heating kettle (1)；The salt
Brine temp in water heating kettle (1) is 70 DEG C.
3. hypochlorite generator's device of a kind of integrated form good antiscale property according to claim 2, it is characterised in that described
The filter material (4) of hot salt brine filtering kettle (2) is natural zeolite or ion exchange resin.
4. hypochlorite generator's device of a kind of integrated form good antiscale property according to claim 3, it is characterised in that described
The electrical power of liquid flow increasing pump (5) is 40w, lift is 30 meters.
5. hypochlorite generator's device of a kind of integrated form good antiscale property according to claim 4, it is characterised in that described
Kettle vertical or horizontal setting successively is electrolysed by liquid flow increasing pipeline (8) connects 2 to N number of.
6. hypochlorite generator's device of a kind of integrated form good antiscale property according to claim 5, it is characterised in that described
The distance between plate and cathode plate of single pair of electrode (7) in each electrolysis kettle are 2-10mm.
7. hypochlorite generator's device of a kind of integrated form good antiscale property according to claim 6, it is characterised in that described
The electrical power of the single pair of electrode (7) in each electrolysis kettle is equal or unequal.
8. hypochlorite generator's device of a kind of integrated form good antiscale property according to claim 7, it is characterised in that described
The mesohalobic water velocity of clean saline kettle is not less than 1 meter per second with the flow stream velocity for separating electrolyte in formula electrolysis group (9).
9. hypochlorite generator's device of a kind of integrated form good antiscale property according to claim 8, it is characterised in that described
The nozzle diameter of liquid flow increasing pipe (8) for the nozzle diameter of liquid pipe conveying fluid (6) 1/2 to 3/4.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621004875.XU CN206033907U (en) | 2016-08-30 | 2016-08-30 | Hypochlorite generator device of scale deposit is prevented to integrated form |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621004875.XU CN206033907U (en) | 2016-08-30 | 2016-08-30 | Hypochlorite generator device of scale deposit is prevented to integrated form |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206033907U true CN206033907U (en) | 2017-03-22 |
Family
ID=58300878
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621004875.XU Withdrawn - After Issue CN206033907U (en) | 2016-08-30 | 2016-08-30 | Hypochlorite generator device of scale deposit is prevented to integrated form |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206033907U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106435641A (en) * | 2016-08-30 | 2017-02-22 | 江苏永冠给排水设备有限公司 | Integrated anti-scaling sodium hypochlorite generator device and realization method |
| CN111286747A (en) * | 2018-12-10 | 2020-06-16 | 彭志军 | Built-in ultrasonic electrolysis system oxyhydrogen device |
-
2016
- 2016-08-30 CN CN201621004875.XU patent/CN206033907U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106435641A (en) * | 2016-08-30 | 2017-02-22 | 江苏永冠给排水设备有限公司 | Integrated anti-scaling sodium hypochlorite generator device and realization method |
| CN111286747A (en) * | 2018-12-10 | 2020-06-16 | 彭志军 | Built-in ultrasonic electrolysis system oxyhydrogen device |
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