CN106435640B - One kind is based on follow-on full-automatic hypochlorite generator's system and implementation method - Google Patents
One kind is based on follow-on full-automatic hypochlorite generator's system and implementation method Download PDFInfo
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- CN106435640B CN106435640B CN201610777295.2A CN201610777295A CN106435640B CN 106435640 B CN106435640 B CN 106435640B CN 201610777295 A CN201610777295 A CN 201610777295A CN 106435640 B CN106435640 B CN 106435640B
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/24—Halogens or compounds thereof
- C25B1/26—Chlorine; Compounds thereof
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/02—Process control or regulation
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
Abstract
Follow-on full-automatic hypochlorite generator's system and implementation method are based on the present invention relates to one kind, the system includes dissolved salt device, automatic matching device, electrolysis unit and throwing device, each functional device is sequentially connected in series, control unit is equipped with each functional device and is connected respectively by data wire with PLC console signals, it is characterized in that, also include on-line customer's station terminal, on-line customer's station terminal is connected by data wire with PLC console signals, also interacts formula RFDC with outer net monitoring system；The dissolved salt device includes staged dissolved salt equipment, automatic matching device includes the electrolysis installation of integrated form good antiscale property including liquid constant-flow controller, electrolysis unit.The present invention had both greatly optimized the unit of interior network operation operation, meet with outer net networking operation monitoring management again the need for, so as to significantly increase the operational efficiency of full-automatic hypochlorite generator's system.
Description
Technical field
It is more particularly to a kind of based on follow-on full-automatic time the invention belongs to domestic water processing equipment technical field
Sodium chlorate generator system and implementation method.
Background technology
At present, known full-automatic hypochlorite generator's system is application surface in domestic water processing equipment technical field
Extensively measure big domestic water processing equipment.Although full automatic hypochlorite generator's system has many excellent compared with similar products
Point, but not enough closed because each unit devices such as dissolved salt device, automatic matching device, electrolysis unit and PLC consoles also have design
The problems such as reason, configuration not enough optimize and operational efficiency is not high, the interior network operation operating system particularly built by PLC consoles,
Networking monitoring operation can not be carried out with outer net to run so that the practicality and cost performance of the system receive high-end market hair in the industry
The challenge of exhibition demand.
, it is necessary to which the salt solution that 3% or so is prepared using saturated brine is used as electrolytic cell in sodium hypochlorite preparation process
Electrolytic solution, Chinese patent application 201420290748.5 employs the method that gas mixing solution produces saturated brine solution,
Because bubble cause salt and solution to seethe from below to up, a large amount of salt not dissolved are had in the solution of outflow and are existed,
The preparation of follow-up weak brine is influenceed, and structure is complex.
In sodium hypochlorite preparation process, salt solution automatic matching device is mostly pressurized using water pump and supplied to water supply line
Water, as starting or stoping for water pump can cause the water pressure of pipeline to produce change, causes the apopore of identical latus rectum to be flowed through
Flow have larger difference.Chinese patent application CN201020141294.7 discloses a kind of for pipeline hydraulic pressure flow cavitation result
Automatic constant-pressure constant-flow valve, it is to reach that water-carrying capacity is not stressed by the change in the gap of spring to change and realize constant control
Purpose, but spring steel long period of soaking inevitably causes corrosion in water, causes the coefficient of elasticity of spring to change,
Therefore the gap of spring can also change, and cause instability of flow etc., it is difficult to really realize constant control water-carrying capacity.
In sodium hypochlorite preparation process, electrolysis unit causes sodium hypochlorite hair because being limited by hard water condition
Give birth to the electrode surface fouling of the electrolytic cell of device device and hang with attachment etc., its electrolytic efficiency is decreased obviously.Conventional electrolysis at present
The preceding prefabricated softened water good antiscale property of normal temperature, the electrode scale removal of falling pole is set, the good antiscale property that cools to electrolytic cell and ultrasonic wave foaming is utilized
The solutions such as fouling are hindered, but are all not met by effectively preventing the problem of electrode surface fouling etc..Chinese patent application
201511033467.7 disclose " a kind of electrification sterilization hydrotreater ", can realize that electrolytic cell is sent out after reaction certain time
Raw positive and negative electrode switching, electrode instantaneously increases electric current to remove the effect of the dirt fouling on negative electrode, but electrode damage is larger, leads
The life-span for sending a telegraph pole greatly shortens, and needs real-time shutdown processing, influences the continuous operation of electrolytic cell, reduces the operation of electrolytic cell
Efficiency.
Chinese patent application 201120289631.1 discloses a kind of " integrated full-automatic drinking water sterilization device ", mainly
It is made up of rectification switch board, demineralizer, dissolved salt case, strong brine pump, electrolysis generator, sodium hypochlorite tank and dosing pump, with reality
Existing full automatic continuous working, economy and practical purpose.Chinese patent application 201520262103.5 discloses one kind
" full-automatic static formula hypochlorite generator ", including rectifier, dissolved salt case, water softener, electrolyte tank, storage tank, running water inlet pipe,
Hydrogen comb, salt solution add pump, sodium hypochlorite add pump, soft water water inlet motor-driven valve and sodium hypochlorite go out liquid motor-driven valve composition, with
Realize and improve the purpose such as automaticity and electrolytic efficiency.But also there is following obvious deficiency in these schemes：One be it is so-called it is complete from
Dynamic also only the PLC of each unit device is controlled in single set water treatment facilities, without outer net network savvy, it is impossible to outer net
Master control platform carries out networking operation monitoring management；Two be because the master control platform with outer net is without networking operation function, Yong Hudan
The failure being likely to occur in set water treatment facilities operation can not be excluded automatically in real time, directly affect reliability of operation；Three be not
The operational efficiency of single set water treatment facilities with outer net network savvy is not high, not only impacted to real-time troubleshooting, and to fortune
Row, stoppage in transit and maintenance etc. are also impacted, i.e., without the self-service function of being networked with outer net.
In summary, how to overcome the shortcomings of that having turned into current domestic water processing equipment technology present in prior art leads
One of emphasis problem urgently to be resolved hurrily in domain.
The content of the invention
The purpose of the present invention is a kind of based on follow-on full-automatic to overcome the shortcomings of to provide present in prior art
Hypochlorite generator's system and implementation method, the present invention are filled by using on-line customer's station terminal and improved dissolved salt
Put, automatic matching device and electrolysis unit, both greatly optimized the unit of interior network operation operation, and met again and outer net joins
The need for network operation monitoring management, so as to significantly increase the operational efficiency of full-automatic hypochlorite generator's system.
According to proposed by the present invention a kind of based on follow-on full-automatic hypochlorite generator's system, including dissolved salt dress
Put, automatic matching device, electrolysis unit and throwing device, each functional device is sequentially connected in series, is equipped with each functional device
Control unit is simultaneously connected by data wire with PLC console signals respectively, it is characterised in that also whole including on-line customer's station
End, on-line customer's station terminal is connected with PLC console signals by data wire, also interacted with outer net monitoring system
Formula RFDC；The dissolved salt device include staged dissolved salt equipment, automatic matching device include liquid constant-flow controller,
Electrolysis unit includes the electrolysis installation of integrated form good antiscale property, wherein：
On-line customer's station terminal include data processor respectively with signal conversion module, RFDC mould
Block, the state data acquisition module of hypochlorite generator's device, the self-help operation routine data of hypochlorite generator's device
Module, failture evacuation operation sequence data module and the connection of video and audio prompting device signal, and it is whole for on-line customer's station
Hold the power management module of power supply；The signal conversion module includes being used to change on-line customer's station terminal input and defeated
Go out the analog-to-digital conversion module and D/A converter module of signal.
The staged dissolved salt equipment, including water inlet, liquid outlet, bung, ladle body, bucket bottom, sparge pipe and staged salt
Slot structure, the sparge pipe is connected with water inlet, is fixed on the top of ladle body, and sparge pipe has equally distributed water spray
Hole；The staged salt slot structure includes being provided with first floor salt bath and bottom salt bath, and first floor salt bath is ring channel structures, ladle body and head
Layer salt bath is structure as a whole；Bottom salt bath is circular configuration, and bucket bottom is structure as a whole with bottom salt bath；In bottom salt bath and ladle body
Between be saturated salt tank, saturated salt tank is connected with liquid outlet；
The liquid constant-flow controller, including upper valve body, lower valve body, cushion and valve element, the upper valve body are provided with interior spiral shell
Line, the lower valve body is provided with the external screw thread with upper valve mates, and upper valve body and lower valve body are connected and formed by internal and external threads
In valve cavity after upper valve body and lower valve body combination, the valve cavity, the axial direction along upper valve body to lower valve body is sequentially provided with
Cushion and mobilizable valve element with holes, mobilizable valve element includes semicircle sealing and cylindric guide part, half
The outer surface in circular seal portion is provided with projection, and the circumferential wall of the cylindrical shape guide part, which is provided with, is available for the valve element of liquid communication to lead to
Hole, the cushion with holes is provided with the sealing surface fitted with the semicircle sealing；
The electrolysis installation of the integrated form good antiscale property, including the liquid flow increasing pump that clean salt solution kettle passes through carrying liqs pipe conveying fluid
It is connected with separating formula electrolysis group；The clean salt solution kettle includes the salt solution heating kettle with heater and the hot salt brine with filter material
The brine temp that filtering kettle adjoins in connection, the clean salt solution heating kettle is 50-100 DEG C；The power of the liquid flow increasing pump is 10-
100w, lift are 25-35m；It is described to separate formula electrolysis group including 2 to N number of electrolysis kettle, wherein each passing through liquid between electrolysis kettle
Flow increasing pipe is connected；Be equipped with the single pair of electrode including plate and cathode plate in each electrolysis kettle, the single pair of electrode with
It is electrolysed the dc source connection outside kettle；The flow stream velocity for separating the electrolyte in formula electrolysis group is not less than clean salt solution kettle
In salt solution water velocity.
The present invention realization principle be：It is proposed by the present invention a kind of based on follow-on full-automatic hypochlorite generator system
System and implementation method are the integrated technology improvement to existing traditional full-automatic hypochlorite generator's system, are specifically：Match somebody with somebody
The dissolved salt device of saturated brine processed is staged dissolved salt equipment, mixed from eminence repeat impact using the kinetic energy and potential energy of water itself
The salt in salt storehouse is closed, salt is sufficiently mixed with water；Liquid constant-flow controller is employed in automatic matching device, flow channel for liquids can be made
Section with fluid pressure change present inverse proportion change, ensure that fluid flow is invariable；Electrolysis unit is
The electrolysis installation of integrated form good antiscale property, formula electricity is separated using prefabricated clean high temperature salt solution, increase flow stream velocity and many kettles before electrolysis
New departure of solution, it integrates the measure of scale removal, antiscale and scale inhibition, and has played the effect of collaboration good antiscale property well；Connection
Network users station terminal cooperates with structure both to have realized that carrying out interior network operation with each functional unit of the system operated with PLC consoles,
With outer net networking operation monitoring management, can not only greatly optimize the unit of interior network operation operation again, meet again with outside
The need for net networking operation monitoring management.
Its remarkable advantage is the present invention compared with prior art：
First, filled the present invention be directed to existing known dissolved salt device, automatic matching device, electrolysis unit and PLC control
The cell arrangement such as put also in the presence of the one kind for designing not reasonable, configuration not enough optimization and the not high problem of operational efficiency and proposing to change
Enter full-automatic hypochlorite generator's system of type, and each unit device has played good synergy, therefore the present invention
Practicality and cost performance are significantly improved, and disclosure satisfy that the demand of this area high-end market development.
Second, the hypochlorite generator's device for the integrated form good antiscale property that the present invention is built, by taking pre- before electrolysis
The clean salt solution of system, increase flow stream velocity and many kettles separate the measures such as formula electrolysis, have played scale removal, the antiscale of good integrated form
With the synergy of scale inhibition, achieve than the more significant effect of prior art good antiscale property measure.
3rd, the dissolved salt device for the preparation saturated brine that the present invention is built is staged salt slot device, using water itself
Kinetic energy and potential energy from the salt in eminence repeat impact salt-mixture storehouse, it is ensured that salt is sufficiently mixed with water, improve saturated brine prepare
Efficiency.
4th, the fluid flow constant control device for automatic matching device that the present invention is built can make flow channel for liquids
Section with fluid pressure change present inverse proportion change, ensure that fluid flow is invariable, meet precisely
The need for metering.
5th, on-line customer's station terminal that the present invention is built both can be by PLC consoles and each functional unit of the system
Device carries out interior network operation operation, can be greatly increased follow-on full-automatic time with outer net networking operation monitoring management again
The operational reliability and efficiency of sodium chlorate generator system.
Brief description of the drawings
Fig. 1 is a kind of internal web structure side based on follow-on full-automatic hypochlorite generator's system proposed by the present invention
Frame schematic diagram.
Fig. 2 is a kind of Intranet and outer net based on follow-on full-automatic hypochlorite generator's system proposed by the present invention
The structure block diagram of networking.
Fig. 3 is the cross-sectional view of staged dissolved salt equipment proposed by the present invention.
Fig. 4 is the structure block diagram of on-line customer's station terminal proposed by the present invention.
Fig. 5 is the structural representation of liquid constant-flow controller proposed by the present invention；Fig. 5 include Fig. 5-1, Fig. 5-2, Fig. 5-3,
Fig. 5-4, Fig. 5-5, Fig. 5-6, Fig. 5-7；Wherein：Fig. 5-1 is dimensional structure diagram；Fig. 5-2 is overall cross-sectional view；
Fig. 5-3 is valve cavity cross-sectional view；Fig. 5-4 is the dimensional structure diagram of cushion；Fig. 5-5 cuts open for cushion
Face structural representation；Fig. 5-6 is the dimensional structure diagram of mobilizable valve element；Fig. 5-7 is the section knot of mobilizable valve element
Structure schematic diagram.
Fig. 6 is the vertical structure schematic diagram of the electrolysis unit of integrated form good antiscale property proposed by the present invention.
Fig. 7 is the horizontal type structure schematic diagram of the electrolysis unit of integrated form good antiscale property proposed by the present invention.
Fig. 8 is a kind of implementation method based on follow-on full-automatic hypochlorite generator's system proposed by the present invention
Process blocks schematic diagram.
Embodiment
The embodiment to the present invention is described in further detail with reference to the accompanying drawings and examples.
Embodiment 1.It is proposed by the present invention a kind of based on follow-on full-automatic hypochlorite generator's system with reference to Fig. 1,
Including dissolved salt device (1), automatic matching device (2), electrolysis unit (3) and throwing device (4), each functional device passes through connecting tube
(5) it is sequentially connected in series, control unit is equipped with each functional device and is believed respectively by data wire (6) and PLC consoles (7)
Number connection, it is characterised in that also including on-line customer's station terminal (8), on-line customer's station terminal (8) passes through data wire
(6) it is connected with PLC consoles (7) signal, also interacts formula RFDC with outer net monitoring system (9)；The dissolved salt
Device (1), which includes staged dissolved salt equipment, automatic matching device (2), includes liquid constant-flow controller, electrolysis unit (3) including collecting
The electrolysis installation of accepted way of doing sth good antiscale property.It is proposed by the present invention a kind of based on follow-on full-automatic hypochlorite generator with reference to Fig. 2
The preferred scheme of system is that the outer net monitoring system (9) includes backstage cloud server, wireless data communication network and intelligence
Can remote group Self-Service device, the wireless data communication network respectively with backstage cloud server and intelligent remote team control from
Server is helped to enter row data communication connection；The backstage cloud server by wireless data communication network support it is intelligent cluster controlled from
Server is helped to interact formula data communication with on-line customer's station terminal.Therefore, the present invention can both pass through on-line customer's station
Terminal (8) carries out interior network operation with each functional unit of the system and operated, and the present invention can also pass through on-line customer's station terminal
(8) with outer net networking operation monitoring management, the reliable of follow-on full-automatic hypochlorite generator's system is improved really
Property and efficiency.
Embodiment 2.With reference to Fig. 3, on-line customer's station terminal (8) of the present invention include data processor respectively with signal
Modular converter, wireless data communication module, the state data acquisition module of hypochlorite generator's device, hypochlorite generator
Self-help operation routine data module, failture evacuation operation sequence data module and the connection of video and audio prompting device signal of device, with
And the power management module powered for on-line customer's station terminal；The signal conversion module includes described for changing
The analog-to-digital conversion module and D/A converter module of network users station terminal input and output signal.
Embodiment 3.With reference to Fig. 4, staged dissolved salt equipment of the present invention, including water inlet (1-1), liquid outlet (1-2),
Bung (1-3), ladle body (1-4), bucket bottom (1-5), sparge pipe (1-6) and staged salt slot structure, the sparge pipe (1-6) is with entering
(1-1) is connected at the mouth of a river, is fixed on ladle body (1-4) top, and sparge pipe (1-6) has equally distributed hole for water spraying；It is described
Staged salt slot structure includes being provided with first floor salt bath (1-7.1) and bottom salt bath (1-7.2), and first floor salt bath (1-7.1) is annular
Slot structure, ladle body (1-4) is structure as a whole with first floor salt bath (1-7.1)；Bottom salt bath (1-7.2) is circular configuration, bucket bottom (1-
5) it is structure as a whole with bottom salt bath (1-7.2)；It is saturated salt tank between bottom salt bath (1-7.2) and ladle body (1-4), satisfies
It is connected with saline slot with liquid outlet (1-2).Its preferred scheme is additionally included in the first floor salt bath (1-7.1) and bottom salt bath
The intermediate layer salt bath (1-7.3) of loop configuration is set between (1-7.2), the width of rebate of the intermediate layer salt bath (1-7.3) from
First floor salt bath (1-7.1) starts to each intermediate layer salt bath (1-7.3) progressively to widen, and forms ladder-type structure, intermediate layer salt bath (1-
7.3) one or more layers is set to, ladle body (4) is structure as a whole with intermediate layer salt bath (1-7.3).
Embodiment 4.With reference to Fig. 5, liquid constant-flow controller of the present invention, including upper valve body (2-1), lower valve body (2-2),
Cushion (2-3) and mobilizable valve element (2-4), the upper valve body (2-1) are provided with internal thread (2-1.1), the lower valve body (2-
2) external screw thread (2-2.1) being engaged with upper valve body (2-1) is provided with, upper valve body (2-1) and lower valve body (2-2) pass through internal and external threads
Connect and form upper valve body (2-1) and lower valve body (2-2) combination after valve cavity (2-5), in the valve cavity (2-5),
Cushion (2-3) and mobilizable valve element (2-4) with holes is sequentially provided with along upper valve body (2-1) to the axial direction of lower valve body (2-2),
Mobilizable valve element (2-4) includes the guide part (2-4.2) of semicircular sealing (2-4.1) and cylindrical shape, semicircle
The outer surface of sealing (2-4.1) be provided with raised (2-4.4), the circumferential wall of the columnar guide part (2-4.2) and set
There is the valve core through hole (2-4.3) for being available for liquid communication, the cushion (2-3) with holes is provided with and the semicircular sealing
The sealing surface (2-3.1) of (2-4.1) laminating；The cushion (2-3) with holes is cylindric, and it, which is axially arranged with, is available for liquid flow
The cushion through hole (2-3.2) crossed, a diameter of 0.1-5mm of cushion through hole (2-3.2).Its preferred scheme also includes the circle
Provided with the gap (2-6) circulated for liquid between the guide part (2-4.2) and lower valve body (2-2) of tubular, the gap (2-6)
Width is 0.2-5mm；Raised (2-4.4's) is shaped as hemispherical, and the height of the projection (2-4.4) is 0.2-5mm；Institute
The material for stating upper valve body (2-1) and lower valve body (2-2) is stainless steel, copper alloy, aluminium alloy or engineering plastics；It is described with holes
The material of cushion (2-3) is rubber, silica gel or silicon rubber；The material of the movable valve core (2-4) is ceramics or engineering plastic
Material.
Embodiment 5.With reference to Fig. 6 and Fig. 7, the electrolysis installation of integrated form good antiscale property of the present invention, including clean salt solution kettle
It is connected by the liquid flow increasing pump (3-5) of carrying liqs pipe conveying fluid (3-6) with separating formula electrolysis group (3-9)；The clean salt solution kettle
Adjoin connection, institute including the salt solution heating kettle (3-1) with heater (3-3) and the hot salt brine filtering kettle (3-2) with filter material (3-4)
It is 50-100 DEG C to state the brine temp in clean salt solution heating kettle (3-1)；The power of the liquid flow increasing pump (3-5) is 10-
100w, lift are 25-35m；It is described to separate formula electrolysis group (3-9) including 2 to N number of electrolysis kettle, wherein each leading between electrolysis kettle
Cross liquid flow increasing pipe (3-8) connection；Single pair of electrode (the 3- including plate and cathode plate is equipped with each electrolysis kettle
7), the single pair of electrode (3-7) is connected with the dc source outside electrolysis kettle；The electrolysis separated in formula electrolysis group (3-9)
The flow stream velocity of liquid is not less than the water velocity of the salt solution in clean salt solution kettle.Its preferred scheme also includes：The salt solution heating
The heater (3-3) of kettle (3-1) is arranged on the inside of salt solution heating kettle (3-1) or the outside of salt solution heating kettle (3-1)；The salt
Brine temp in water heating kettle (3-1) is 70 DEG C；The filter material (3-4) of the hot salt brine filtering kettle (3-2) is natural boiling
Stone or ion exchange resin；The electrical power of liquid flow increasing pump (3-5) in the electrolysis installation of the integrated form good antiscale property be 40w,
Lift is 30 meters；The water velocity of hot salt brine in clean salt solution kettle and the liquid stream for separating the electrolyte in formula electrolysis group (3-9)
Speed is not less than 1 meter per second；The nozzle diameter of the liquid flow increasing pipe (3-8) is the nozzle diameter of liquid pipe conveying fluid (3-6)
1/2 to 3/4.
Embodiment 6.It is proposed by the present invention a kind of based on follow-on full-automatic hypochlorite generator's system with reference to Fig. 8
Implementation method, comprise the following specific steps that：
Step 1, start networking control：The operation Job readiness of full-automatic hypochlorite generator's equipment of user terminal is just
Thread, user opens the user equipment logon account of on-line customer's station terminal (8), and the startup information of input correspondence user terminal refers to
Make each control unit of PLC consoles and dissolved salt device (1), automatic matching device (2), electrolysis unit (3) and throwing device (4)
The Intranet operation control system of structure enters starting state；Start of the on-line customer's station terminal (8) correspondence user terminal simultaneously
Reception of the information reporting to outer net monitoring system (9) and completion to feedback command, until the full-automatic sodium hypochlorite of user terminal is sent out
Raw device device power-up is networked successfully and enters running status；
Step 2, networking operation is controlled：Full-automatic hypochlorite generator's device power-up networking of user terminal described in step 1
Succeed and enter after running status, dissolved salt device (1), automatic matching device (2), electrolysis unit (3) and throwing device (4) it is each
Control unit receives the instruction that PLC consoles (7) issue and implements the control of each functional unit respectively, while on-line customer's station
The operation and control information of the integrated Intranet operation control system of PLC consoles (7) is reported outer net monitoring system by terminal (8)
(9) back up；
Step 3, networking troubleshooting control：In networking operation control described in step 2, if there is full-automatic time of correspondence user terminal
Sodium chlorate generator apparatus runs not normal situation, then outer net monitoring system can be whole according to the on-line customer's station for corresponding to user terminal
The operation and control information that end (8) is reported provides the information alert that instruction on-line customer's station terminal (8) carries out failture evacuation operation,
Until full-automatic hypochlorite generator's equipment of correspondence user terminal switchs to normal operation by operation is not normal, while on-line customer's work
Position terminal (8) backs up troubleshooting information reporting to outer net monitoring system (9)；
Step 4, shutdown networking control：When full-automatic hypochlorite generator's equipment needs of correspondence user terminal are out of service
And when shutting down, on-line customer's station terminal (8) stops transport the shutdown of full-automatic hypochlorite generator's equipment of correspondence user terminal
Information reporting outer net monitoring system (9), the outer net monitoring system (9) is then provided to application according to the shutdown stop information reported
On-line customer's station terminal (8) at family end is shut down and follow-up to full-automatic hypochlorite generator's equipment progress cleaning operation program
Information alert, until full-automatic hypochlorite generator's equipment of correspondence user terminal completes cleaning operation program and reports cleaning
Operation information gives outer net monitoring system (9), is stopped with backing up full-automatic hypochlorite generator's equipment of correspondence user terminal and having been enter into
The state only run.
All explanations not related to belong to techniques known in the embodiment of the present invention, refer to known skill
Art is carried out.
The present invention achieves satisfied trial effect through validation trial.
Above embodiment and embodiment are to proposed by the present invention a kind of based on follow-on full-automatic hypochlorous acid
The specific support of sodium generator system and implementation method technological thought, it is impossible to which protection scope of the present invention is limited with this, it is every to press
According to technological thought proposed by the present invention, any equivalent variations done on the basis of the technical program or equivalent change, still
Belong to the scope of technical solution of the present invention protection.
Claims (10)
1. one kind is based on follow-on full-automatic hypochlorite generator's system, including dissolved salt device (1), automatic matching device
(2), electrolysis unit (3) and throwing device (4), each functional device is sequentially connected in series by connecting tube (5), in each functional device
It is equipped with control unit and is connected respectively by data wire (6) with PLC consoles (7) signal, it is characterised in that also including networking
User's station terminal (8), on-line customer's station terminal (8) is connected by data wire (6) with PLC consoles (7) signal, also
Formula RFDC is interacted with outer net monitoring system (9)；The dissolved salt device (1) includes staged dissolved salt equipment, from
Dynamic matching device (2) includes liquid constant-flow controller, and electrolysis unit (3) includes the electrolysis installation of integrated form good antiscale property, wherein：
On-line customer's station terminal (8) includes data processor, signal conversion module, wireless data communication module, secondary chlorine
The state data acquisition module of sour sodium generating apparatus, the self-help operation routine data module of hypochlorite generator's device, event
Barrier excludes operation sequence data module, data memory module, video and audio prompting device and power management module；Wherein：The data
Processor respectively with signal conversion module, wireless data communication module, hypochlorite generator's device state data acquisition mould
Block, the self-help operation routine data module of hypochlorite generator's device, failture evacuation operation sequence data module, data storage
Module and video and audio prompting device carry out signal connection, and the power management module is powered for on-line customer's station terminal (8)；
The signal conversion module includes the analog-to-digital conversion mould for being used to change on-line customer's station terminal (8) input and output signal
Block and D/A converter module.
The staged dissolved salt equipment, including water inlet (1-1), liquid outlet (1-2), bung (1-3), ladle body (1-4), bucket bottom
(1-5), sparge pipe (1-6) and staged salt slot structure, the sparge pipe (1-6) are connected with water inlet (1-1), are fixed on bucket
The top of body (1-4), sparge pipe (1-6) has equally distributed hole for water spraying；The staged salt slot structure includes first floor salt
Groove (1-7.1) and bottom salt bath (1-7.2), first floor salt bath (1-7.1) are ring channel structures, ladle body (1-4) and first floor salt bath (1-
7.1) it is structure as a whole；Bottom salt bath (1-7.2) is circular configuration, and bucket bottom (1-5) is integrated knot with bottom salt bath (1-7.2)
Structure；It is saturated salt tank between bottom salt bath (1-7.2) and ladle body (1-4), saturated salt tank is connected with liquid outlet (1-2)
It is logical；
The liquid constant-flow controller, including upper valve body (2-1), lower valve body (2-2), cushion (2-3) and mobilizable valve element
(2-4), the upper valve body (2-1) is provided with internal thread (2-1.1), and the lower valve body (2-2) is provided with and upper valve body (2-1) is engaged
External screw thread (2-2.1), upper valve body (2-1) and lower valve body (2-2) by internal and external threads connect and form upper valve body (2-1) and under
Valve cavity (2-5) after valve body (2-2) combination, in the valve cavity (2-5), along upper valve body (2-1) to lower valve body (2-2)
Axial direction be sequentially provided with cushion (2-3) and mobilizable valve element (2-4) with holes, mobilizable valve element (2-4) includes
Semicircular sealing (2-4.1) and the guide part (2-4.2) of cylindrical shape, the outer surface of semicircular sealing (2-4.1) is set
Have raised (2-4.4), the circumferential wall of the columnar guide part (2-4.2) is provided with the valve core through hole for being available for liquid communication
(2-4.3), the cushion (2-3) with holes is provided with the sealing surface (2- fitted with the semicircular sealing (2-4.1)
3.1)；The cushion (2-3) with holes is cylindric, and it is axially arranged with the cushion through hole (2-3.2) for being available for liquid to flow through,
A diameter of 0.1-5mm of cushion through hole (2-3.2)；
The electrolysis installation of the integrated form good antiscale property, including the salt solution heating kettle (3-1) with heater (3-3), band filter material
The hot salt brine filtering kettle (3-2) of (3-4), the liquid flow increasing pump (3-5) of carrying liqs pipe conveying fluid (3-6) and separate formula electrolysis group (3-
9)；The salt solution heating kettle (3-1) constitutes the clean salt solution kettle for adjoining connection, the clean salt solution kettle with hot salt brine filtering kettle (3-2)
It is connected by liquid flow increasing pump (3-5) with separating formula electrolysis group (3-9)；Salt water temperature in the clean salt solution heating kettle (3-1)
Spend for 50-100 DEG C；The power of the liquid flow increasing pump (3-5) is that 10-100w, lift are 25-35m；It is described to separate formula electrolysis group
(3-9) includes 2 to N number of electrolysis kettle, wherein each being connected between electrolysis kettle by liquid flow increasing pipe (3-8)；In each electrolysis kettle
The single pair of electrode (3-7) including plate and cathode plate is equipped with, the single pair of electrode (3-7) is straight outside kettle with being electrolysed
Flow power supply connection；The flow stream velocity for separating the electrolyte in formula electrolysis group (3-9) is not less than the salt solution in clean salt solution kettle
Water velocity.
2. it is according to claim 1 a kind of based on follow-on full-automatic hypochlorite generator's system, it is characterised in that
The outer net monitoring system (9) includes backstage cloud server, wireless data communication network and intelligent remote team control Self-Service
Device, the wireless data communication network carries out data with backstage cloud server and intelligent remote team control Self-Service device respectively and led to
Letter connection；The backstage cloud server supports intelligent cluster controlled Self-Service device and on-line customer by wireless data communication network
Station terminal interacts formula data communication.
3. it is according to claim 2 a kind of based on follow-on full-automatic hypochlorite generator's system, it is characterised in that
The staged dissolved salt equipment, which is additionally included between first floor salt bath (1-7.1) and bottom salt bath (1-7.2), sets loop configuration
Intermediate layer salt bath (1-7.3), the width of rebate of the intermediate layer salt bath (1-7.3) is since the first floor salt bath (1-7.1) in each
Interbed salt bath (1-7.3) is progressively widened, and forms ladder-type structure, and intermediate layer salt bath (1-7.3) is set to one or more layers, ladle body
(4) it is structure as a whole with intermediate layer salt bath (1-7.3).
4. it is according to claim 3 a kind of based on follow-on full-automatic hypochlorite generator's system, it is characterised in that
Provided with the gap (2-6) circulated for liquid, the gap between the columnar guide part (2-4.2) and lower valve body (2-2)
The width of (2-6) is 0.2-5mm；Raised (2-4.4's) is shaped as hemispherical, and the height of the projection (2-4.4) is
0.2-5mm。
5. it is according to claim 4 a kind of based on follow-on full-automatic hypochlorite generator's system, it is characterised in that
The heater (3-3) of the salt solution heating kettle (3-1) is arranged on inside or the salt solution heating kettle (3-1) of salt solution heating kettle (3-1)
Outside；Brine temp in the salt solution heating kettle (3-1) is 70 DEG C.
6. it is according to claim 5 a kind of based on follow-on full-automatic hypochlorite generator's system, it is characterised in that
The filter material (3-4) of the hot salt brine filtering kettle (3-2) is natural zeolite or ion exchange resin.
7. it is according to claim 6 a kind of based on follow-on full-automatic hypochlorite generator's system, it is characterised in that
The electrical power of liquid flow increasing pump (3-5) in the electrolysis installation of the integrated form good antiscale property is that 40w, lift are 30 meters.
8. it is according to claim 7 a kind of based on follow-on full-automatic hypochlorite generator's system, it is characterised in that
The water velocity of the hot salt brine in clean salt solution kettle in the electrolysis installation of the integrated form good antiscale property is with separating formula electrolysis group (3-
9) flow stream velocity of the electrolyte in is not less than 1 meter per second.
9. it is according to claim 8 a kind of based on follow-on full-automatic hypochlorite generator's system, it is characterised in that
The nozzle diameter of liquid flow increasing pipe (3-8) in the electrolysis installation of the integrated form good antiscale property is the pipe of liquid pipe conveying fluid (3-6)
The 1/2 to 3/4 of mouth diameter.
10. a kind of according to claim any one of 1-9 is based on follow-on full-automatic hypochlorite generator's system
Implementation method, it is characterised in that comprise the following specific steps that：
Step 1, start networking control：The operation Job readiness of full-automatic hypochlorite generator's equipment of user terminal is ready, uses
The user equipment logon account of on-line customer's station terminal (8) is opened at family, and the startup information of input correspondence user terminal instructs PLC
Each control unit of console and dissolved salt device (1), automatic matching device (2), electrolysis unit (3) and throwing device (4) is built
Intranet operation control system enter starting state；While boot-strap information of the on-line customer's station terminal (8) correspondence user terminal
The reception of outer net monitoring system (9) and completion to feedback command is reported, until the full-automatic hypochlorite generator of user terminal
Device power-up is networked successfully and enters running status；
Step 2, networking operation is controlled：Full-automatic hypochlorite generator's device power-up of user terminal described in step 1 is networked successfully
And enter after running status, dissolved salt device (1), automatic matching device (2), each control of electrolysis unit (3) and throwing device (4)
Unit receives the instruction that PLC consoles (7) issue and implements the control of each functional unit respectively, while on-line customer's station terminal
(8) that the operation and control information of the integrated Intranet operation control system of PLC consoles (7) is reported outer net monitoring system (9) is standby
Part；
Step 3, networking troubleshooting control：In networking operation control described in step 2, if there is the full-automatic hypochlorous acid of correspondence user terminal
Sodium generator apparatus runs not normal situation, then outer net monitoring system can be according to the on-line customer's station terminal for corresponding to user terminal
(8) operation and control information reported provides the information alert that instruction on-line customer's station terminal (8) carries out failture evacuation operation, directly
To correspondence user terminal full-automatic hypochlorite generator's equipment by run it is not normal switch to normal operation, while on-line customer's station
Terminal (8) backs up troubleshooting information reporting to outer net monitoring system (9)；
Step 4, shutdown networking control：When full-automatic hypochlorite generator's equipment of correspondence user terminal needs out of service and closes
During machine, shutdown stop information of the on-line customer's station terminal (8) full-automatic hypochlorite generator's equipment of correspondence user terminal
Outer net monitoring system (9) is reported, the outer net monitoring system (9) then provides correspondence user terminal according to the shutdown stop information reported
On-line customer's station terminal (8) shutdown and the follow-up letter that cleaning operation program is carried out to full-automatic hypochlorite generator's equipment
Breath prompting, until full-automatic hypochlorite generator's equipment of correspondence user terminal completes cleaning operation program and reports cleaning operation
Information gives outer net monitoring system (9), and stopping fortune being had been enter into back up full-automatic hypochlorite generator's equipment of correspondence user terminal
Capable state.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610777295.2A CN106435640B (en) | 2016-08-30 | 2016-08-30 | One kind is based on follow-on full-automatic hypochlorite generator's system and implementation method |
| PCT/CN2017/099220 WO2018041059A1 (en) | 2016-08-30 | 2017-08-28 | Improved full-automatic sodium hypochlorite generator system and implementation method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610777295.2A CN106435640B (en) | 2016-08-30 | 2016-08-30 | One kind is based on follow-on full-automatic hypochlorite generator's system and implementation method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106435640A CN106435640A (en) | 2017-02-22 |
| CN106435640B true CN106435640B (en) | 2017-10-13 |
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|---|---|---|---|
| CN201610777295.2A Active CN106435640B (en) | 2016-08-30 | 2016-08-30 | One kind is based on follow-on full-automatic hypochlorite generator's system and implementation method |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN106435640B (en) |
| WO (1) | WO2018041059A1 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106435640B (en) * | 2016-08-30 | 2017-10-13 | 江苏永冠给排水设备有限公司 | One kind is based on follow-on full-automatic hypochlorite generator's system and implementation method |
| CN108588747A (en) * | 2018-06-29 | 2018-09-28 | 山东新日电气设备有限公司 | A kind of constant gradient spaced electrodes electrolysis unit |
| CN109385644B (en) * | 2018-12-21 | 2020-01-24 | 潍坊强源化工有限公司 | But electrolysis trough is used in production of sodium bromate of automatic ratio |
| CN110295374B (en) * | 2019-06-05 | 2021-08-10 | 福建浩达智能科技股份有限公司 | Full-automatic high-concentration sodium hypochlorite generation system |
| CN111304681B (en) * | 2020-03-31 | 2021-05-14 | 山东省科学院能源研究所 | Full-intelligent sodium hypochlorite generator and control method thereof |
| CN113637988B (en) * | 2021-07-29 | 2022-07-22 | 浙江华晨环保有限公司 | High-efficient sodium hypochlorite generator |
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| CN201785505U (en) * | 2010-07-19 | 2011-04-06 | 江苏泽宇环境工程有限公司 | NaCIO generator |
| CN203878224U (en) * | 2014-06-17 | 2014-10-15 | 重庆冰睿原川环保工程有限公司 | Sodium hypochlorite generator |
| CN105401164A (en) * | 2015-12-10 | 2016-03-16 | 中国灌溉排水发展中心 | Portable electrolytic salt sodium hypochlorite generator suitable for various kinds of disinfection in disaster areas |
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| US9719179B2 (en) * | 2012-05-23 | 2017-08-01 | High Sierra Energy, LP | System and method for treatment of produced waters |
| KR101435400B1 (en) * | 2012-10-08 | 2014-08-29 | (주) 테크로스 | Chlorine dioxide generator for ballast water sterillzation |
| CN204752864U (en) * | 2015-04-28 | 2015-11-11 | 上海赛一水处理科技有限公司 | Full -automatic static formula hypochlorite generator |
| CN106435640B (en) * | 2016-08-30 | 2017-10-13 | 江苏永冠给排水设备有限公司 | One kind is based on follow-on full-automatic hypochlorite generator's system and implementation method |
| CN206127439U (en) * | 2016-08-30 | 2017-04-26 | 江苏永冠给排水设备有限公司 | Full -automatic hypochlorite generator system based on improved generation |
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2016
- 2016-08-30 CN CN201610777295.2A patent/CN106435640B/en active Active
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2017
- 2017-08-28 WO PCT/CN2017/099220 patent/WO2018041059A1/en active Application Filing
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201785505U (en) * | 2010-07-19 | 2011-04-06 | 江苏泽宇环境工程有限公司 | NaCIO generator |
| CN203878224U (en) * | 2014-06-17 | 2014-10-15 | 重庆冰睿原川环保工程有限公司 | Sodium hypochlorite generator |
| CN105401164A (en) * | 2015-12-10 | 2016-03-16 | 中国灌溉排水发展中心 | Portable electrolytic salt sodium hypochlorite generator suitable for various kinds of disinfection in disaster areas |
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| CN106435640A (en) | 2017-02-22 |
| WO2018041059A1 (en) | 2018-03-08 |
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