CN102471104A - An electrolytic cell - Google Patents

An electrolytic cell Download PDF

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Publication number
CN102471104A
CN102471104A CN2010800309284A CN201080030928A CN102471104A CN 102471104 A CN102471104 A CN 102471104A CN 2010800309284 A CN2010800309284 A CN 2010800309284A CN 201080030928 A CN201080030928 A CN 201080030928A CN 102471104 A CN102471104 A CN 102471104A
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CN
China
Prior art keywords
electrode
electrolyzer
passage
aforementioned
central module
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN2010800309284A
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Chinese (zh)
Inventor
罗斯·莱斯利·帕尔默
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Poolrite Research Pty Ltd
Original Assignee
Poolrite Research Pty Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from AU2009903424A external-priority patent/AU2009903424A0/en
Application filed by Poolrite Research Pty Ltd filed Critical Poolrite Research Pty Ltd
Publication of CN102471104A publication Critical patent/CN102471104A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4672Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
    • C02F1/4674Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation with halogen or compound of halogens, e.g. chlorine, bromine
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46128Bipolar electrodes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/42Nature of the water, waste water, sewage or sludge to be treated from bathing facilities, e.g. swimming pools
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • C02F2201/006Cartridges

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

The invention relates to an electrolytic cell comprising a housing having a channel extending there through; an inlet allowing water to pass into the channel; an outlet allowing water to pass from the channel; and a series of electrodes located within the channel; wherein the channel is a spiral.

Description

Electrolyzer
Technical field
The present invention relates to a kind of electrolyzer.Especially, the present invention relates to a kind of be used for to salt solution swimming pool, watering place etc. similarly retention basin carry out the chlorating electrolyzer.
Background technology
The pond chlorination is necessary for the growth of unwanted bacterium in the anti-sealing.Electrolytic chlorination has become a kind of popular approach that realizes sterilized water.The salt that is arranged in the water in the pond is added in the electrolytic chlorination utilization to, and said pond combines with the electrolyzer that is used to produce chlorine.Said chlorine is discharged in the water, thereby kills any unwanted bacterium and mikrobe.Said process cost efficient is high, the low maintenance and damage to the environment not.
When adopting electrolyzer chlorination tank water, the article of reproducing of this process are hydrogen.Under the normal circumstances, hydrogen is sent in the pond along with the water that flows through electrolyzer and is dissipated in the atmosphere.But if pond pump shuts down, electrolyzer possibly remain in operation, and produces hydrogen.Hydrogen can continue to gather, rather than also discharges into the atmosphere subsequently along with water flows into the pond.Under extreme case,, said hydrogen can set off an explosion if being lighted.
USP (the patent No.: 4861451) described a kind of electrolyzer that is configured to reduce hydrogen explosion possibility in the electrolyzer.Dispose said electrolyzer, so that the import of electrolyzer and outlet are positioned at the electrode below, said electrode is positioned at the electrolyzer body.If hydrogen is in the electrolyzer accumulated, then hydrogen is limited in the electrolyzer, makes water level below said electrode.This makes electrolysis stop, and therefore stops to produce hydrogen.
Electrolyzer shown in the patent 4861451, very effective aspect the amounts of hydrogen of limit electrolysis pond generation.But, because the design of electrolyzer, so there are some inherent defects.When electrolyzer was in level attitude, flowing of water must be through the direction conversion of four 90 degree, so that the restriction to hydrogen in the electrolyzer is provided.This significantly reduces the hydraulic efficiency of pond chlorination system through increasing extra pressure, and it is equivalent to add six meters long pipelines to system in theory.When electrolyzer was in vertical position, the top of chlorination system needed the loop setting in the pond, so that the restriction to hydrogen to be provided once more.This has increased a large amount of extra pipe fittings again.This extra pipe fitting and the change of water (flow) direction need bigger pump usually, so that extract water through chlorination system effectively, make chlorination system expensive more.In addition, along with the change of duct orientation, the common more complicated of drawing water.
Summary of the invention
The objective of the invention is to overcome or alleviate one or more disclosed problems and to the user provide with or favourable selection.
Under a kind of form, although need not to be unique or form the most widely, the present invention relates to a kind of electrolyzer, said electrolyzer comprises:
Shell has the passage of the said shell of extend through;
Import allows the inflow of water into said passage;
Outlet allows water to flow out said passage; And
A series of electrodes are positioned at said passage;
Wherein, said passage is a volution.
Typically, said shell is formed by base and lid.Usually, said shell is made of plastics, and still, can be that other suitable material is processed.Said shell also can comprise the side cover that covers joint between said base and the lid.
Typically, said import and outlet alignment each other.But said import can be in other angles with outlet, such as 90 degree.
Typically, said electrode is positioned at said passage, said outlet than said import more near said electrode.Said electrode can be formed by any suitable material, such as, titanium.Said electrode has been supplied single-stage or twin-stage electric charge (charge).
Said electrode can be removed from said passage, and said electrode can singlely be replaced, and said electrode can be installed on the central module.Said central module can form the part of said passage.Said central module can be detachable.
Said electrode can form the part of electrode box.Said electrode box can be removed from said shell.Said electrode box can comprise: the said central module that is used to install said electrode.Said electrode is installed on the said central module through inner support.Said electrode is installed on the said central module through outer support.
Said electrode can be that what to put down also can be crooked.One or more limits of said electrode can be arc.
Description of drawings
Now, embodiment of the invention will be described with reference to drawings for the general, wherein:
Fig. 1 is the frontview according to the electrolyzer of the embodiment of the invention;
Fig. 2 is the rear view of electrolyzer as shown in Figure 1;
Fig. 3 is the skeleton view of electrolyzer as shown in Figure 1;
Fig. 4 is the decomposition diagram of electrolyzer as shown in Figure 1;
Fig. 5 is the skeleton view according to the electrode box of first embodiment of the invention;
Fig. 6 is the part skeleton view of electrode box shown in Figure 5;
Fig. 7 is the skeleton view of part electrode box shown in Figure 5; And
Fig. 8 is the decomposition diagram of part electrode box shown in Figure 5.
Embodiment
Fig. 1 shows the electrolyzer 10 that is used for the chlorination tank water to Fig. 4.Electrolyzer 10 comprises shell 20 and electrode box 30.
Shell 20 is made up of base 40,50 and two side covers 60 of lid.Lid 50 is through a series of cap bolts 51 and 40 dismountable connections of base, and cap bolt 51 extends around the periphery of lid 50.Bolt hole 41 is positioned at base 40, is used for cap bolt 51 positioned will cover 50 being connected to base 40.Sealing 70 between lid 50 and base 40, with guarantee to cover 50 and base 40 between the junction waterproof.
Side cover 60 be installed in cover 50 and base 40 between the top of junction, to cover cap bolt 51.Side cover 60 has a series of male part 61, and male part 61 is installed in the recessed web member (receiver) 42 that is associated that is positioned on the base 40, so that side cover 60 is fixed to base 40.Front side cap 60 also comprises: conductor casing lid 62 is positioned at the conductor box 52 that covers on 50 to cover.
Import 80 is positioned at an end of base 40, and outlet 90 is positioned at the other end of base 40.Import 80 all has the pipeline connection 100 that is associated so that shell 20 is connected to the pipeline (not shown) that is associated with outlet 90.Import 80 and outlet 90 alignment each other.But, should be realized that according to the design of pond chlorination system, this situation is not necessary.
Fig. 5 illustrates in greater detail electrode box 30 to Fig. 9, and electrode box 30 comprises detachable central module 110, inner support 120, outer support 130 and a series of electrode 140.Detachable central module 110 is made of plastics and through setting treatment, so that be installed in the shell 20, extend to base 40 and cover in 50.The side 111 of detachable central module 110 is through setting treatment, so that near lid 50 and base 40.
Outer support 130 is used to install said a series of electrode 140 with inner support 120.Inner support 120 utilizes the interconnecting piece 121 on inner support 120 internal surfaces 122, with detachable 110 dismountable connections of central module.The outside surface 123 of inner support 120 has a series of inner support recesses 125 that are used for installing electrodes 140.
Outer support 130 also has a series of outer support recesses 131 that are positioned on outer support 130 internal surfaces 132.The top 133 and the bottom 134 of outer support 130 has a plurality of seams 135 that pass outer support 130 tops 133 and bottom 134.This allows water to pass support 130 and process electrode 140.Outer support 130 utilizes interference fit (interference fit) to be connected with inner support 120.The top 133 of outer support 130 is through setting treatment, so that outer support 130 is installed near the internal surface 132 of lid 50.
Each electrode 140 all is tabular and has arc outside 141 and inner edge 142 in said a series of electrode.Electrode 140 is through setting treatment, so that electrode 140 can easily be installed in the crooked shell 20.Should be realized that, the size of electrode 140 and shape be can be provided with and electrode 140 can process by multiple conspicuous for a person skilled in the art material.
Electrode 140 utilizes two conductors 150 (that is, negative electrode or anode) to be electrically connected, and said conductor 150 passes via conductor box 52 and covers 50, and passes the hole that is associated in the electrode 140.Conductor 150 all is carved with screw thread at each end, so that conductor bolt 141 can be placed on arbitrary end of conductor 150, said a series of electrodes 140 are fixed to tightly inner support 120 and outer support 130.Should be realized that electrode 140 is known in the field with being connected to of conductor 150.It should further be appreciated that the electric current of use can change.Such as, can adopt single-stage electric current or twin-stage electric current.
When detachable central module 110 is positioned at shell 20, form spirality channel 160.Spirality channel 160 begins to extend from import 80, passes base 40, passes and covers 50, turns back in the base 40, and extends from exporting 90.Should be realized that according to the particular requirement of the pipeline that is associated of electrolyzer 10 and pond filtering system, the shape and size of spirality channel 160 can change.
In use, water is through import 80 flow channels 160.Water flows through the direction of passage 160 by 43 indications of the arrow on the base 40.Then, water passes base 40, gets into and covers 50, flows around detachable central module 110 arc limits 112.Because the shape of the side 111 of detachable central module 110 and shell 20 couplings are not so water can pass between the side 111 of shell 20 and detachable central module 110.
Then, water passes the seam 135 in the top 133 of outer support 130.Because the top 133 of outer support 130 is near the internal surface of lid 50, water must pass the seam 135 at the top 133 of outer support 130.This has reduced water can the mobile area.Therefore, because water passes seam 135 in the top 133 of outer support 130, through electrode 140, and flow out, so the speed of water increases through the seams in the bottom 134 of outer support 130 135.The increase of this water speed can reduce the gathering of calcium on the electrode 140 potentially.Then, water passes base 40 and flows out from exporting 90.
In use, on level and vertical position, electrolyzer 10 all can use.If pump breaks down, then any excess hydrogen of gathering all can be limited in covering in 50.Any further gathering all can make water level finally drop to electrode below 140, stops to produce dangerous hydrogen.
Spirality channel 160 allows import 80 and outlet 90 alignment.Because water need not pass the turning of any 90 degree, therefore increased hydraulic efficiency.On the contrary, water moves to outlet 90 via spirality channel 160 from import 80, and (patent No.: the electrolyzer 10 that 4861451) illustrates is compared, and spirality channel 160 has increased hydraulic efficiency like USP with traditional.
It should further be appreciated that, under the situation that does not deviate from spirit of the present invention and scope, can carry out various other changes and modification said embodiment.

Claims (18)

1. an electrolyzer is characterized in that, said electrolyzer comprises:
Shell has the passage of the said shell of extend through;
Import allows the inflow of water into said passage;
Outlet allows water to flow out said passage; And
A series of electrodes are positioned at said passage;
Wherein, said passage is a volution.
2. electrolyzer according to claim 1 is characterized in that, said shell is formed by base and lid.
3. electrolyzer according to claim 2 is characterized in that, said shell also comprises the side cover that covers joint between said base and the lid.
4. according to the described electrolyzer of aforementioned each claim, it is characterized in that said import and outlet alignment each other.
5. according to the described electrolyzer of aforementioned each claim, it is characterized in that said electrode is positioned at said passage, said outlet than said import more near said electrode.
6. according to the described electrolyzer of aforementioned each claim, it is characterized in that said electrode has been supplied single-stage or twin-stage electric charge.
7. according to the described electrolyzer of aforementioned each claim, it is characterized in that said electrode can be removed from said passage.
8. according to the described electrolyzer of aforementioned each claim, it is characterized in that said electrode can singlely be replaced.
9. according to the described electrolyzer of aforementioned each claim, it is characterized in that said electrode is installed on the central module.
10. electrolyzer according to claim 10 is characterized in that said central module forms the part of said passage.
11., it is characterized in that said central module is detachable according to claim 9 or 10 described electrolyzers.
12., it is characterized in that said electrode forms the part of electrode box according to the described electrolyzer of aforementioned each claim.
13. electrolyzer according to claim 12 is characterized in that, said electrode box can be removed from said shell.
14. according to claim 12 or 13 described electrolyzers, it is characterized in that said electrode box comprises: the said central module that is used to install said electrode.
15. electrolyzer according to claim 14 is characterized in that, said electrode is installed on the said central module through inner support.
16., it is characterized in that said electrode is installed on the said central module through exterior part according to claim 14 or 15 described electrolyzers.
17., it is characterized in that said electrode is that put down or crooked according to the described electrolyzer of aforementioned each claim.
18., it is characterized in that one or more limits of said electrode are arc according to the described electrolyzer of aforementioned each claim.
CN2010800309284A 2009-07-22 2010-07-22 An electrolytic cell Pending CN102471104A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
AU2009903424A AU2009903424A0 (en) 2009-07-22 An electrolytic cell
AU2009903424 2009-07-22
PCT/AU2010/000931 WO2011009170A1 (en) 2009-07-22 2010-07-22 An electrolytic cell

Publications (1)

Publication Number Publication Date
CN102471104A true CN102471104A (en) 2012-05-23

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CN2010800309284A Pending CN102471104A (en) 2009-07-22 2010-07-22 An electrolytic cell

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US (1) US20120181169A1 (en)
EP (1) EP2456720A4 (en)
CN (1) CN102471104A (en)
AU (1) AU2010276087A1 (en)
WO (1) WO2011009170A1 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8007653B2 (en) * 2004-09-15 2011-08-30 Aquatron, Inc. Method and appartus for operation of pool cleaner with integral chlorine generator
WO2013019750A1 (en) 2011-07-29 2013-02-07 Hayward Industries, Inc. Systems and methods for controlling chlorinators
EP2736849A4 (en) * 2011-07-29 2015-07-29 Hayward Ind Inc Systems and methods for user-installable chlorinators
AU2012290292B2 (en) 2011-07-29 2017-08-17 Hayward Industries, Inc. Chlorinators and replaceable cell cartridges therefor
WO2013044315A1 (en) * 2011-09-27 2013-04-04 Poolrite Research Pty Ltd An electrolytic cell
EP3602024A4 (en) 2017-03-21 2020-11-18 Hayward Industries, Inc. Systems and methods for sanitizing pool and spa water
US11407661B2 (en) * 2017-07-17 2022-08-09 Watkins Manufacturing Corporation Chlorine generator system
FR3141457A1 (en) * 2022-10-31 2024-05-03 Pool Technologie sodium hypochlorite production device

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3751351A (en) * 1971-03-15 1973-08-07 Eastman Kodak Co Electrolytic cell for recovering metal from a solution containing ions thereof,and method for operating same
US3840455A (en) * 1972-02-24 1974-10-08 Eastman Kodak Co Electrolytic cell for recovering metals from solution
US6051118A (en) * 1994-12-30 2000-04-18 Ishifuku Metal Industry Co., Ltd. Compound electrode for electrolysis

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19928071A1 (en) * 1999-06-14 2000-12-21 Gehlert Wassertechnik Gmbh Water supply pipe electrode insert kills germs and minimizes deposit of limestone scale
US7211176B2 (en) * 2004-11-02 2007-05-01 Zodiac Pool Care, Inc. Replaceable chlorinator electrode assembly
WO2006110799A1 (en) * 2005-04-12 2006-10-19 Zodiac Pool Care, Inc. Vessel and method for water treatment
RU2367614C1 (en) * 2008-07-28 2009-09-20 Федеральное государственное образовательное учреждение высшего профессионального образования Волгоградская государственная сельскохозяйственная академия Water electric activator

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3751351A (en) * 1971-03-15 1973-08-07 Eastman Kodak Co Electrolytic cell for recovering metal from a solution containing ions thereof,and method for operating same
US3840455A (en) * 1972-02-24 1974-10-08 Eastman Kodak Co Electrolytic cell for recovering metals from solution
US6051118A (en) * 1994-12-30 2000-04-18 Ishifuku Metal Industry Co., Ltd. Compound electrode for electrolysis

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Publication number Publication date
AU2010276087A1 (en) 2011-12-22
WO2011009170A1 (en) 2011-01-27
US20120181169A1 (en) 2012-07-19
EP2456720A4 (en) 2013-02-27
EP2456720A1 (en) 2012-05-30

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Application publication date: 20120523