CN206127439U - Full -automatic hypochlorite generator system based on improved generation - Google Patents
Full -automatic hypochlorite generator system based on improved generation Download PDFInfo
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- CN206127439U CN206127439U CN201620992039.0U CN201620992039U CN206127439U CN 206127439 U CN206127439 U CN 206127439U CN 201620992039 U CN201620992039 U CN 201620992039U CN 206127439 U CN206127439 U CN 206127439U
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- salt
- electrolysis
- kettle
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- automatic
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- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 title claims abstract description 86
- 150000003839 salts Chemical class 0.000 claims abstract description 89
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 61
- 239000007788 liquid Substances 0.000 claims abstract description 48
- 238000012544 monitoring process Methods 0.000 claims abstract description 20
- 230000006855 networking Effects 0.000 claims abstract description 18
- 238000004891 communication Methods 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 34
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 33
- 239000011780 sodium chloride Substances 0.000 claims description 33
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 18
- 238000009434 installation Methods 0.000 claims description 14
- 239000012267 brine Substances 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 13
- 238000007789 sealing Methods 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 10
- 239000012530 fluid Substances 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 9
- 229920006395 saturated elastomer Polymers 0.000 claims description 6
- 239000003792 electrolyte Substances 0.000 claims description 5
- 238000001914 filtration Methods 0.000 claims description 5
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 2
- 229910021536 Zeolite Inorganic materials 0.000 claims description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 2
- 239000003456 ion exchange resin Substances 0.000 claims description 2
- 229920003303 ion-exchange polymer Polymers 0.000 claims description 2
- 239000010457 zeolite Substances 0.000 claims description 2
- 238000005507 spraying Methods 0.000 claims 1
- 230000002452 interceptive effect Effects 0.000 abstract 1
- 239000005708 Sodium hypochlorite Substances 0.000 description 9
- 238000010586 diagram Methods 0.000 description 9
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 9
- 238000007726 management method Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- 238000002360 preparation method Methods 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 238000013024 troubleshooting Methods 0.000 description 3
- BZSXEZOLBIJVQK-UHFFFAOYSA-N 2-methylsulfonylbenzoic acid Chemical compound CS(=O)(=O)C1=CC=CC=C1C(O)=O BZSXEZOLBIJVQK-UHFFFAOYSA-N 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 230000005520 electrodynamics Effects 0.000 description 2
- 229920006351 engineering plastic Polymers 0.000 description 2
- 230000005764 inhibitory process Effects 0.000 description 2
- 238000005381 potential energy Methods 0.000 description 2
- 239000011833 salt mixture Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- 229910000881 Cu alloy Inorganic materials 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 208000031481 Pathologic Constriction Diseases 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 102000005393 Sodium-Potassium-Exchanging ATPase Human genes 0.000 description 1
- 108010006431 Sodium-Potassium-Exchanging ATPase Proteins 0.000 description 1
- 229910000639 Spring steel Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000008233 hard water Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- KQPBSBAEBKRAAU-UHFFFAOYSA-N hypochlorous acid;sodium Chemical compound [Na].ClO KQPBSBAEBKRAAU-UHFFFAOYSA-N 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000032696 parturition Effects 0.000 description 1
- 210000000664 rectum Anatomy 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 229920002379 silicone rubber Polymers 0.000 description 1
- 239000004945 silicone rubber Substances 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000008234 soft water Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 238000002604 ultrasonography Methods 0.000 description 1
- 210000001215 vagina Anatomy 0.000 description 1
- 238000010200 validation analysis Methods 0.000 description 1
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model relates to a full -automatic hypochlorite generator system based on improved generation, this system include soluble salt device, automatic proportioning device, electrolytic device and throw the feeder apparatus, and each functional device is the series connection in proper order, all is equipped with the control unit among each functional device and respectively through data line and PLC control cabinet signal connection, its characterized in that still includes on -line customer's station terminal, data line and PLC control cabinet signal connection are passed through to on -line customer's station terminal, still carry out interactive wireless data communication with outer net monitored control system, the soluble salt device includes that cascaded soluble salt equipment, automatic proportioning device include that liquid constant current control ware, electrolytic device include that the integrated form prevents the electrolysis equipment of scale deposit. The utility model discloses both optimize the unit device of intranet operation greatly, satisfied the needs with the management of outer net networking operation monitoring and controlling again to it lands to show improves the operating efficiency of full -automatic hypochlorite generator system.
Description
Technical field
This utility model belongs to domestic water processing equipment technical field, it is more particularly to a kind of based on it is follow-on it is complete from
Dynamic hypochlorite generator's system.
Background technology
At present, known full-automatic hypochlorite generator's system is application surface in domestic water processing equipment technical field
Big domestic water processing equipment is measured extensively.Although full automatic hypochlorite generator's system has many excellent compared with similar products
Point, but not enough close because each unit devices such as dissolved salt device, automatic matching device, electrolysis unit and PLC control stations also have design
The problems such as reason, configuration not enough optimize and operational efficiency is not high, the interior network operation operating system for particularly being built by PLC control stations,
Networking monitoring operation operation cannot be carried out with outer net so that the practicality and cost performance of the system receives high-end market in the industry and send out
The challenge of exhibition demand.
In sodium hypochlorite preparation process, the saline for needing using saturated brine to prepare 3% or so is used as electrolysis bath
Electrolytic solution, Chinese patent application 201420290748.5 employ the method that gas mixing solution produces saturated brine solution,
As bubble causes Sal and solution to seethe from below to up, the Sal not dissolved in a large number is had in the solution for flowing out and is existed,
The preparation of follow-up weak brine is affected, and structure is complex.
In sodium hypochlorite preparation process, saline automatic matching device is mostly pressurized using water pump and is 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 flow 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 be the gap by spring change come reach discharge be not stressed 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 real realizes constant control discharge.
In sodium hypochlorite preparation process, electrolysis unit is because being limited by hard water condition, and sodium hypochlorite is sent out
Give birth to the electrode surface fouling of the electrolysis bath of device equipment and hang with attachment etc., its electrolytic efficiency is decreased obviously.Conventional electrolysis at present
The prefabricated softened water good antiscale property of front room temperature, the electrode scale removal of falling pole is set, good antiscale property of lowering the temperature to electrolysis bath and using ultrasound wave foaming
The solutions such as resistance fouling, but be all not met by effectively preventing a difficult problem for electrode surface fouling etc..Chinese patent application
201511033467.7 disclose " a kind of electrification sterilization hydrotreater ", can realize electrolysis bath after reaction certain hour
Generation positive and negative electrode switches, and electrode instantaneously increases electric current to remove the effect of the dirt fouling on negative electrode, but electrode damage is larger,
Cause the life-span of electrode to greatly shorten, and need real-time shutdown to process, affect the continuous operation of electrolysis bath, reduce the fortune of electrolysis bath
Line 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 commutator, dissolved salt case, water softener, electrolyte tank, storage tank, tap water inlet pipe,
Hydrogen comb, saline add pump, sodium hypochlorite add pump, soft water water inlet electrodynamic valve and sodium hypochlorite go out liquid electrodynamic valve composition, with
Realize improving 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
The PLC controls of the dynamic each unit device also only in single set water treatment facilities, not with outer net network savvy, it is impossible to outer net
Master control platform carries out networking operation monitoring management, and its operational efficiency is not high；Two be because with the master control platform of outer net without networking
Operation function, the failure that user is likely to occur in singly covering water treatment facilities operation cannot be excluded in real time automatically, directly affect operation
Reliability；Three is that the single set water treatment facilities with the self-service function of being networked with outer net are not only received to operation, real-time troubleshooting
Affect, and it is also impacted to stoppage in transit and maintenance etc..
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 to overcome the shortcomings of to provide a kind of based on follow-on complete existing for prior art
Automatically hypochlorite generator's system, this utility model by using on-line customer's station terminal and improved dissolved salt device,
Automatic matching device and electrolysis unit, had both been greatly optimized the unit of interior network operation operation, and had met again and networked with outer net
The needs of operation monitoring management, so as to significantly increase the operational efficiency of full-automatic hypochlorite generator's system.
According to the utility model proposes one kind be based on follow-on full-automatic hypochlorite generator's system, including dissolved salt
Device, automatic matching device, electrolysis unit and throwing device, each functional device are sequentially connected in series, and are all provided with each functional device
There is control unit and be connected with PLC control station signals by data wire respectively, it is characterised in that also including on-line customer's station end
End, on-line customer's station terminal is connected with PLC control station signals by data wire, on-line customer's station terminal also with outer net
Monitoring system interacts formula RFDC；The dissolved salt device includes staged dissolved salt equipment, automatic matching device bag
Including 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 equipment, the self-help operation routine data of hypochlorite generator's equipment
The connection of module, failture evacuation operation sequence data module and video and audio prompting apparatuss signal, and be on-line customer's station end
The power management module of end power supply；The signal conversion module includes being input into and defeated for changing on-line customer's station terminal
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, drum head, sparge pipe and staged salt
Slot structure, the sparge pipe are connected with water inlet, are 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 drum head 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
Stricture of vagina, the lower valve body are provided with the external screw thread with upper valve mates, and upper valve body and lower valve body are connected by internal and external threads and formed
Valve cavity after upper valve body and lower valve body combination, in the valve cavity, the axial direction along upper valve body to lower valve body is sequentially provided with
Cushion with holes and mobilizable valve element, mobilizable valve element include semicircle sealing and cylindric guide part, partly
The outer surface in circular seal portion is provided with projection, and the circumferential wall of the cylindrical shape guide part is provided with and is available for the valve element of liquid communication to lead to
Hole, the cushion with holes are provided with the sealing surface fitted with the semicircle sealing；
The electrolysis installation of the integrated form good antiscale property, including liquid flow increasing pump of the clean saline kettle by carrying liqs pipe conveying fluid
It is connected with formula electrolysis group is separated；The clean saline kettle includes the saline heating kettle with heater and the hot salt brine with filter material
Filtering kettle adjoins connection, and the brine temp in the clean saline 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 and include 2 to N number of electrolysis kettle, wherein pass through liquid between each electrolysis kettle
Flow increasing pipe connects；Be equipped with the single pair of electrode including plate and cathode plate in each electrolysis kettle, the single pair of electrode with
DC source connection outside electrolysis kettle；The flow stream velocity for separating the electrolyte in formula electrolysis group is not less than clean saline kettle
In saline water velocity.
It is of the present utility model to realize that principle is：The utility model proposes one kind be based on follow-on full-automatic hypochlorous acid
Sodium generator system and implementation method are that the integrated technology to existing traditional full-automatic hypochlorite generator's system is improved,
Specifically：The dissolved salt device for preparing saturated brine is staged dissolved salt equipment, using the kinetic energy and potential energy of water itself from eminence
Salt in repeat impact salt-mixture storehouse, salt is sufficiently mixed with water；Liquid constant-flow controller is employed in automatic matching device, can
Make the section of flow channel for liquids as the change of fluid pressure is presented inverse proportion change, ensure that fluid flow is invariable；
Electrolysis installation of the electrolysis unit for integrated form good antiscale property, using prefabricated clean high temperature saline before electrolysis, increases flow stream velocity and many
Kettle separates new departure of formula electrolysis, and it integrates the measure of scale removal, antiscale and scale inhibition, and has played collaboration good antiscale property well
Effect；On-line customer's station terminal to be built both be capable of achieving with the collaboration of PLC control stations and carry out Intranet with each functional unit of the system
Operation operation, with outer net networking operation monitoring management, can not only greatly optimize the unit of interior network operation operation again, again full
Needs of the foot with outer net networking operation monitoring management.
Its remarkable advantage is this utility model compared with prior art：
First, this utility model is controlled for existing known dissolved salt device, automatic matching device, electrolysis unit and PLC
The cell arrangements such as device processed also there is not reasonable design, configuration not enough optimization and the not high difficult problem of operational efficiency and propose one
Follow-on full-automatic hypochlorite generator's system is planted, and each unit device has played good synergism, therefore this reality
Significantly improved with new practicality and cost performance, disclosure satisfy that the demand of this area high-end market development.
Second, electrolysis installation of the electrolysis unit that this utility model builds for integrated form good antiscale property, by adopting before electrolysis
Take prefabricated clean high temperature saline, increase flow stream velocity and many kettles and separate the measures such as formula electrolysis, play good integrated form
The synergism of scale removal, antiscale and scale inhibition, achieves the effect more more significantly than prior art good antiscale property measure.
3rd, the dissolved salt device of the preparation saturated brine that this utility model builds is staged dissolved salt equipment, using water
Salt of the kinetic energy and potential energy of itself from eminence repeat impact salt-mixture storehouse, it is ensured that salt is sufficiently mixed with water, improves saturated brine
The efficiency of preparation.
4th, the automatic matching device that this utility model builds is liquid constant-flow controller, can make the section of flow channel for liquids
As the change of fluid pressure is presented inverse proportion change, ensure that fluid flow is invariable, meet accurate metering
Need.
5th, on-line customer's station terminal that this utility model builds both can be each with this utility model by PLC control stations
Functional unit equipment carries out interior network operation operation, can greatly increase follow-on with outer net networking operation monitoring management again
The operational reliability and efficiency of full-automatic hypochlorite generator's system.
Description of the drawings
Fig. 1 be the utility model proposes a kind of Intranet based on follow-on full-automatic hypochlorite generator's system tie
Structure block diagram.
Fig. 2 be the utility model proposes a kind of Intranet based on follow-on full-automatic hypochlorite generator's system with
The structure block diagram of outer net networking.
Fig. 3 be the utility model proposes staged dissolved salt equipment cross-sectional view.
Fig. 4 be the utility model proposes on-line customer's station terminal structure block diagram.
Fig. 5 be the utility model proposes liquid constant-flow controller dimensional structure diagram.
Fig. 6 be the utility model proposes liquid constant-flow controller overall cross-sectional view.
Fig. 7 be the utility model proposes liquid constant-flow controller valve cavity cross-sectional view.
Fig. 8 be the utility model proposes liquid constant-flow controller cushion dimensional structure diagram.
Fig. 9 be the utility model proposes liquid constant-flow controller cushion cross-sectional view.
Figure 10 be the utility model proposes liquid constant-flow controller mobilizable valve element dimensional structure diagram.
Figure 11 be the utility model proposes liquid constant-flow controller mobilizable valve element cross-sectional view.
Figure 12 be the utility model proposes integrated form good antiscale property electrolysis installation vertical structure schematic diagram.
Figure 13 be the utility model proposes integrated form good antiscale property electrolysis installation horizontal type structure schematic diagram.
Figure 14 be the utility model proposes a kind of realization based on follow-on full-automatic hypochlorite generator's system
The process blocks schematic diagram of method.
Specific embodiment
With reference to the accompanying drawings and examples specific embodiment of the present utility model is described in further detail.
Embodiment 1.With reference to Fig. 1, the utility model proposes one kind be based on follow-on full-automatic hypochlorite generator
System, including dissolved salt device (1), automatic matching device (2), electrolysis unit (3) and throwing device (4), each functional device pass through
Connecting tube (5) is sequentially connected in series, and is equipped with control unit and is controlled with PLC by data wire (6) in each functional device respectively
Platform (7) signal connects, and also including on-line customer's station terminal (8), on-line customer's station terminal (8) is by data wire (6)
It is connected with PLC control stations (7) signal, it is wireless that on-line customer's station terminal (8) also interacts formula with outer net monitoring system (9)
Data communication；The dissolved salt device (1) including staged dissolved salt equipment, automatic matching device (2) including liquid constant-flow controller,
Electrolysis installation of the electrolysis unit (3) including integrated form good antiscale property.
With reference to Fig. 2, the utility model proposes it is a kind of based on the excellent of follow-on full-automatic hypochlorite generator's system
Scheme is selected to be the outer net monitoring system (9) including backstage cloud server, wireless data communication network and intelligent remote group
Control Self-Service device, the wireless data communication network respectively with backstage cloud server and intelligent remote team control Self-Service device
Enter row data communication connection；The backstage cloud server supports intelligent cluster controlled Self-Service device by wireless data communication network
Formula RFDC is interacted with on-line customer's station terminal.
Therefore, this utility model both can carry out Intranet with each functional unit of the system by on-line customer's station terminal (8)
Operation operation, and this utility model can also pass through on-line customer's station terminal (8) and outer net networking operation monitoring management, really
Improve the operational reliability and efficiency of follow-on full-automatic hypochlorite generator's system.
Embodiment 2.With reference to Fig. 4, on-line customer's station terminal (8) described in the utility model including data processor respectively with
Signal conversion module, wireless data communication module, the state data acquisition module of hypochlorite generator's equipment, sodium hypochlorite are sent out
Self-help operation routine data module, failture evacuation operation sequence data module and the video and audio prompting apparatuss signal for giving birth to device equipment connects
Connect, and the power management module powered for on-line customer's station terminal；The signal conversion module is included for changing
The analog-to-digital conversion module and D/A converter module of on-line customer's station terminal input and output signal.
Embodiment 3.With reference to Fig. 3, staged dissolved salt equipment described in the utility model, including water inlet (1-1), liquid outlet
(1-2), bung (1-3), ladle body (1-4), drum head (1-5), sparge pipe (1-6) and staged salt slot structure, the sparge pipe (1-
6) it is connected with water inlet (1-1), is fixed on the top of ladle body (1-4), sparge pipe (1-6) has equally distributed water spray
Hole；The staged salt slot structure includes being provided with first floor salt bath (1-7.1) and bottom salt bath (1-7.2), first floor salt bath (1-7.1)
For ring channel structures, 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,
Drum head (1-5) is structure as a whole with bottom salt bath (1-7.2)；It is saturated salt between bottom salt bath (1-7.2) and ladle body (1-4)
Tank, saturated salt tank are connected with liquid outlet (1-2).Its preferred version is additionally included in the first floor salt bath (1-7.1) and bottom
The intermediate layer salt bath (1-7.3) of loop configuration, the notch of the intermediate layer salt bath (1-7.3) are set between layer salt bath (1-7.2)
Width starts to each intermediate layer salt bath (1-7.3) progressively to widen from first floor salt bath (1-7.1), forms ladder-type structure, intermediate layer
Salt bath (1-7.3) is set to one or more layers, and ladle body (4) is structure as a whole with intermediate layer salt bath (1-7.3).
Embodiment 4.With reference to Fig. 5 to Figure 11, liquid constant-flow controller described in the utility model, including upper valve body (2-1), under
Valve body (2-2), cushion (2-3) and mobilizable valve element (2-4), the upper valve body (2-1) are provided with female thread (2-1.1), institute
State lower valve body (2-2) and be provided with the external screw thread (2-2.1) being engaged with upper valve body (2-1), upper valve body (2-1) and lower valve body (2-2)
Valve cavity (2-5) after internal and external threads connect and formed upper valve body (2-1) and lower valve body (2-2) combination, the valve body
In cavity (2-5), cushion (2-3) with holes and movable is sequentially provided with along upper valve body (2-1) to the axial direction of lower valve body (2-2)
Valve element (2-4), mobilizable valve element (2-4) include semicircular sealing (2-4.1) and cylindrical shape guide part (2-
4.2), the outer surface of semicircular sealing (2-4.1) is provided with raised (2-4.4), the columnar guide part (2-4.2)
Circumferential wall is provided with the valve core through hole (2-4.3) for being available for liquid communication, and the cushion (2-3) with holes is provided with and the semicircle
The sealing surface (2-3.1) that the sealing (2-4.1) of shape is fitted；The cushion (2-3) with holes is cylindric, and which is axially arranged with
It is available for the cushion through hole (2-3.2) that liquid flows through, a diameter of 0.1-5mm of cushion through hole (2-3.2).Its preferred version is also
It is including the gap (2-6) circulated for liquid is provided between the columnar guide part (2-4.2) and lower valve body (2-2), described
The width in gap (2-6) is 0.2-5mm；Raised (2-4.4's) is shaped as hemispherical, the height of the projection (2-4.4)
For 0.2-5mm；The material of the upper valve body (2-1) and lower valve body (2-2) is rustless steel, copper alloy, aluminium alloy or engineering plastic
Material；The material of the cushion (2-3) with holes is rubber, silica gel or silicone rubber；The material of the movable valve core (2-4) is
Ceramics or engineering plastics.
Embodiment 5.With reference to Figure 12 and Figure 13, the electrolysis installation of integrated form good antiscale property described in the utility model, including cleaning
Saline kettle is electrolysed group (3-9) by liquid flow increasing pump (3-5) of carrying liqs pipe conveying fluid (3-6) and the formula that separates and is connected；The cleaning
Saline kettle includes the saline heating kettle (3-1) with heater (3-3) and hot salt brine filtering kettle (3-2) with filter material (3-4)
Adjoin connection, the brine temp in the clean saline heating kettle (3-1) is 50-100 DEG C；The power of the liquid flow increasing pump (3-5)
It is 25-35m for 10-100w, lift；Formula electrolysis group (3-9) that separates including 2 to N number of electrolysis kettle, wherein each electrolysis kettle it
Between by liquid flow increasing pipe (3-8) connect；The single pair of electrode including plate with cathode plate is equipped with each electrolysis kettle
(3-7), the single pair of electrode (3-7) is connected with the DC source outside electrolysis kettle；The electricity separated in formula electrolysis group (3-9)
Water velocity of the flow stream velocity of solution liquid not less than the saline in clean saline kettle.Its preferred version also includes：The saline adds
The heater (3-3) of hot kettle (3-1) is arranged on the inside of saline heating kettle (3-1) or the outside of saline heating kettle (3-1)；Institute
It is 70 DEG C to state the brine temp in saline heating kettle (3-1)；The filter material (3-4) of the hot salt brine filtering kettle (3-2) is day
Right zeolite 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 is
40w, lift are 30 meters；The water velocity of the hot salt brine in clean saline kettle and the electrolyte separated in formula electrolysis group (3-9)
Flow stream velocity is not less than 1 meter per second；The nozzle diameter of the liquid flow increasing pipe (3-8) is straight for the mouth of pipe of liquid pipe conveying fluid (3-6)
The 1/2 to 3/4 of footpath.
Embodiment 6.With reference to Figure 14, the utility model proposes one kind be based on follow-on full-automatic hypochlorite generator
The implementation method of system, comprises the following specific steps that：
Step 1, networking control of starting shooting：The operation Job readiness of full-automatic hypochlorite generator's equipment of user side is just
Thread, user open the user equipment logon account of on-line customer's station terminal (8), and the startup information of input correspondence user side refers to
Make each control unit of PLC control stations 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 on-line customer's station terminal (8) correspondence user side simultaneously
Information reporting is to outer net monitoring system (9) and completes the reception to feedback command, until the full-automatic sodium hypochlorite of user side is sent out
The networking success of raw device device power-up simultaneously enters running status；
Step 2, networking operation control：Full-automatic hypochlorite generator's device power-up networking of user side described in step 1
Success into after running status, dissolved salt device (1), automatic matching device (2), electrolysis unit (3) and throwing device (4) it is each
Control unit receives PLC control stations (7) instruction issued the control for implementing each functional unit device respectively, while on-line customer
Station terminal (8) reports outer net monitoring system the operation and control information of PLC control stations (7) integrated Intranet operation control system
System (9) backup；
Step 3, networking troubleshooting control：In networking operation control described in step 2, if there is full-automatic time of correspondence user side
Sodium chlorate generator apparatus run not normal situation, then outer net monitoring system (9) can be according to on-line customer's work of correspondence user side
The operation and control information that position terminal (8) reports provides instruction on-line customer's station terminal (8) and carries out the information of failture evacuation operation
Prompting, until correspondence user side full-automatic hypochlorite generator's equipment by run it is not normal switch to normal operation, while networking
User's station terminal (8) backs up troubleshooting information reporting to outer net monitoring system (9)；
Step 4, networking control of shutting down：When full-automatic hypochlorite generator's equipment of correspondence user side need it is 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 side
Information reporting outer net monitoring system (9), the outer net monitoring system (9) then provide correspondence according to the shutdown stop information for reporting
On-line customer's station terminal (8) of user side shuts down and subsequently carries out cleaning operation journey to full-automatic hypochlorite generator's equipment
The information alert of sequence, until full-automatic hypochlorite generator's equipment of correspondence user side completes cleaning operation program and reports clear
Reason operation information gives outer net monitoring system (9), is had been enter into the full-automatic hypochlorite generator's equipment for backing up correspondence user side
State out of service.
All explanations not related in specific embodiment of the present utility model belong to techniques known, refer to public affairs
Know that technology is carried out.
This utility model Jing validation trials, achieve satisfied trial effect.
Above specific embodiment and embodiment be to the utility model proposes one kind based on follow-on full-automatic time
The concrete support of sodium chlorate generator system technological thought, it is impossible to which protection domain of the present utility model is limited with this, it is every according to
The utility model proposes technological thought, any equivalent variations done on the basis of the technical program or equivalent change,
Still fall within the scope of technical solutions of the utility model protection.
Claims (9)
1. it is a kind of to be 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 with PLC control stations (7) signal by data wire (6) respectively, it is characterised in that also including networking
User's station terminal (8), on-line customer's station terminal (8) are connected with PLC control stations (7) signal by data wire (6), connection
Network users station terminal (8) also interact formula RFDC with outer net monitoring system (9)；Dissolved salt device (1) bag
Staged dissolved salt equipment, automatic matching device (2) are included including liquid constant-flow controller, electrolysis unit (3) including integrated form anti-caking
The electrolysis installation of dirt, wherein：
On-line customer's station terminal (8) including data processor respectively with signal conversion module, wireless data communication module,
The state data acquisition module of hypochlorite generator's equipment, the self-help operation routine data mould of hypochlorite generator's equipment
The connection of block, failture evacuation operation sequence data module and video and audio prompting apparatuss signal, and be on-line customer's station terminal
(8) power management module powered；The signal conversion module is included for changing on-line customer's station terminal (8) input
With the analog-to-digital conversion module and D/A converter module of output signal；
The staged dissolved salt equipment, including water inlet (1-1), liquid outlet (1-2), bung (1-3), ladle body (1-4), drum head
(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) have equally distributed hole for water spraying；The staged salt slot structure includes being provided with head
Layer salt bath (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
Groove (1-7.1) is structure as a whole；Bottom salt bath (1-7.2) is circular configuration, and drum head (1-5) and bottom salt bath (1-7.2) are one
Body structure；It is saturated salt tank, saturated salt tank and liquid outlet (1-2) phase between bottom salt bath (1-7.2) and ladle body (1-4)
Connection；
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 female thread (2-1.1), and the lower valve body (2-2) is provided with and is engaged with upper valve body (2-1)
External screw thread (2-2.1), upper valve body (2-1) and lower valve body (2-2) by internal and external threads connect and formed 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) with holes and mobilizable valve element (2-4), 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) set
There is 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 which 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 liquid flow increasing of the clean saline kettle by carrying liqs pipe conveying fluid (3-6)
Pump (3-5) is connected with formula electrolysis group (3-9) is separated；The clean saline kettle includes the saline heating kettle (3- with heater (3-3)
1) connection, the salt water temperature in the clean saline heating kettle (3-1) are adjoined with hot salt brine filtering kettle (3-2) with filter material (3-4)
Spend for 50-100 DEG C；The power of the liquid flow increasing pump (3-5) is 10-100w, lift is 25-35m；It is described to separate formula electrolysis group
(3-9) including 2 to N number of electrolysis kettle, wherein connected by liquid flow increasing pipe (3-8) between each electrolysis kettle；In each electrolysis kettle
Be equipped with the single pair of electrode (3-7) including plate and cathode plate, the single pair of electrode (3-7) be electrolysed it is straight outside kettle
Stream power supply connection；The flow stream velocity for separating the electrolyte in formula electrolysis group (3-9) is not less than the saline in clean saline kettle
Water velocity.
2. 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 are carried out data respectively and are led to backstage cloud server and intelligent remote team control Self-Service device
Letter connection；The backstage cloud server supports intelligent cluster controlled Self-Service device and on-line customer by wireless data communication network
Station terminal (8) interacts formula RFDC.
3. 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 is additionally included between first floor salt bath (1-7.1) and bottom salt bath (1-7.2) and arranges loop configuration
Intermediate layer salt bath (1-7.3), the width of rebate of the intermediate layer salt bath (1-7.3) start in each from first floor salt bath (1-7.1)
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. according to claim 3 a kind of based on follow-on full-automatic hypochlorite generator's system, it is characterised in that
The gap (2-6) circulated for liquid, the gap are provided between the columnar guide part (2-4.2) and lower valve body (2-2)
(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。
5. 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 saline heating kettle (3-1) is arranged on the inside of saline heating kettle (3-1) or saline heating kettle (3-1)
Outside；Brine temp in the saline heating kettle (3-1) is 70 DEG C.
6. 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. 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 40w, lift is 30 meters.
8. 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 saline kettle in the electrolysis installation of the integrated form good antiscale property is electrolysed group (3- with the formula that separates
9) flow stream velocity of the electrolyte in is not less than 1 meter per second.
9. according to claim 8 a kind of based on follow-on full-automatic hypochlorite generator's system, it is characterised in that
Pipe of the nozzle diameter of liquid flow increasing pipe (3-8) in the electrolysis installation of the integrated form good antiscale property for liquid pipe conveying fluid (3-6)
The 1/2 to 3/4 of mouth diameter.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620992039.0U CN206127439U (en) | 2016-08-30 | 2016-08-30 | Full -automatic hypochlorite generator system based on improved generation |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620992039.0U CN206127439U (en) | 2016-08-30 | 2016-08-30 | Full -automatic hypochlorite generator system based on improved generation |
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| CN206127439U true CN206127439U (en) | 2017-04-26 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018041059A1 (en) * | 2016-08-30 | 2018-03-08 | 江苏永冠给排水设备有限公司 | Improved full-automatic sodium hypochlorite generator system and implementation method |
| CN108037697A (en) * | 2017-12-04 | 2018-05-15 | 山东省科学院能源研究所 | It is a kind of based on ARM microcontrollers can remote control debugging sodium hypochlorite preparation system and its method of work |
| CN108403018A (en) * | 2018-02-10 | 2018-08-17 | 山东大风能源科技有限公司 | A kind of cleaning and sterilizing all-in-one machine |
| CN111020620A (en) * | 2019-12-25 | 2020-04-17 | 苏州希克曼物联技术有限公司 | Online automatically cleaning sodium hypochlorite synthesis system |
| CN111286747A (en) * | 2018-12-10 | 2020-06-16 | 彭志军 | Built-in ultrasonic electrolysis system oxyhydrogen device |
-
2016
- 2016-08-30 CN CN201620992039.0U patent/CN206127439U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018041059A1 (en) * | 2016-08-30 | 2018-03-08 | 江苏永冠给排水设备有限公司 | Improved full-automatic sodium hypochlorite generator system and implementation method |
| CN108037697A (en) * | 2017-12-04 | 2018-05-15 | 山东省科学院能源研究所 | It is a kind of based on ARM microcontrollers can remote control debugging sodium hypochlorite preparation system and its method of work |
| CN108037697B (en) * | 2017-12-04 | 2020-01-10 | 山东省科学院能源研究所 | Sodium hypochlorite preparation system and working method thereof |
| CN108403018A (en) * | 2018-02-10 | 2018-08-17 | 山东大风能源科技有限公司 | A kind of cleaning and sterilizing all-in-one machine |
| CN111286747A (en) * | 2018-12-10 | 2020-06-16 | 彭志军 | Built-in ultrasonic electrolysis system oxyhydrogen device |
| CN111020620A (en) * | 2019-12-25 | 2020-04-17 | 苏州希克曼物联技术有限公司 | Online automatically cleaning sodium hypochlorite synthesis system |
| CN111020620B (en) * | 2019-12-25 | 2022-01-14 | 苏州希克曼物联技术有限公司 | Online automatically cleaning sodium hypochlorite synthesis system |
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