CN1982236A - Method for electrolyzing water - Google Patents

Method for electrolyzing water Download PDF

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Publication number
CN1982236A
CN1982236A CN 200510111565 CN200510111565A CN1982236A CN 1982236 A CN1982236 A CN 1982236A CN 200510111565 CN200510111565 CN 200510111565 CN 200510111565 A CN200510111565 A CN 200510111565A CN 1982236 A CN1982236 A CN 1982236A
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CN
China
Prior art keywords
water
inner core
urceolus
filter
mixing device
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Pending
Application number
CN 200510111565
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Chinese (zh)
Inventor
刘新志
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.)
SITAINUO SCIENCE AND TRADE CO Ltd SHANGHAI
Original Assignee
SITAINUO SCIENCE AND TRADE CO Ltd SHANGHAI
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
Application filed by SITAINUO SCIENCE AND TRADE CO Ltd SHANGHAI filed Critical SITAINUO SCIENCE AND TRADE CO Ltd SHANGHAI
Priority to CN 200510111565 priority Critical patent/CN1982236A/en
Publication of CN1982236A publication Critical patent/CN1982236A/en
Pending legal-status Critical Current

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Abstract

A method for electrolyzing water is carried out by multi-stage filtering for raw water, filtering by sodium-filter or RO film filter, entering filtered water into mixer, mixing, entering mixed water into electrolyzer and electrolyzing. The device consists of internal cylinder and external cylinder, regulating valve is set at inlet of internal cylinder, a hole opposite to outlet of internal cylinder is set at external cylinder wall. It has stable and reliable water-quality.

Description

Be used for water is carried out electrolytic method
Technical field
The present invention relates to a kind of being used for carries out electrolytic method to water, by this method TDS in the electrolytic water of needs and the specific conductivity content amount of carrying out ratio are controlled, make TDS and specific conductivity in the water too high can not electrolysis or the electrolysis of bad electrolytic water become possibility, be applicable to that one is essential to the Application Areas of water electrolysis.
Background technology
In the process of electrolytic process treating water, because of TDS great disparity in the former water very big, specific conductivity difference is also very big, electrolyzer is in very among the difficulty the electrolysis of water, the Faradaic current of this moment is very huge, electrolyzer will suffer damage, and electrolytic water quality of while is extreme difference because the TDS too high levels will become.
According to the World Health Organization good water is defined as weakly alkaline, unharmful substance contains certain useful mineral substance, be the subset structure, water active, safety and sanitation have been water.The technology of a kind of electrolytic ionic water of Japan is introduced and is promoted in market before more than ten years, promptly former water is carried out electrolysis after the sterilising treatment after filtration, and its molecular grouping structure is changed, and pH value is weakly alkaline, and the ORP value improves, and this water becomes the healthy drinking water of a new generation.
Traditional method is, former water is carried out cascade filtration, carries out sterilising treatment after the electrolysis, and is hygienic to guarantee, sees that technical process is:
Former water------cascade filtration is drunk by electrolysis---sterilization---
But because the solvent thing solid amount TDS in the water can not be effectively dispeled in general filtration, therefore do not change electrical conductivity of water substantially, and very big difference will take place former electrical conductivity of water because of the variation of former water, former electrical conductivity of water is too high, can't carry out electrolysis, and the quality of brine electrolysis can descend.
China vast in territory, the water quality of the former water in various places is different, and electrolysis has a basic demand to electrical conductivity of water, good water notion according to the World Health Organization is weakly alkaline pH value>7, certain rigidity 170mg/L is arranged, and TDS is 300mg/L, then the electrolytic electrical conductivity of water of need is required to remain on about 150 Ц s/m, at this moment, the quality of brine electrolysis is best.
Because various places water quality differs, how the electrolysis of water is controlled its specific conductivity becomes the most thorny in an industry technical problem.
Summary of the invention
The purpose of this invention is to provide a kind of electrical conductivity of water that enters electrolyzer that makes and remain on a stable scope, guaranteed the water conditioning of brine electrolysis and be used for water is carried out electrolytic method reliably.
For realizing above purpose, technical scheme of the present invention provides a kind of being used for water is carried out electrolytic method,
Its method is:
The first step: Jiang Yuanshui carries out cascade filtration;
It is characterized in that,
Second step: the water of cascade filtration is filtered filter or the filtration of RO film filter through sodium again;
The 3rd step: with the water of cascade filtration with filter filter or the filtering water of RO film filter through sodium and enter mixing device and mix;
The 4th step: the water that will mix carries out after the electrolytic sterilizing processing promptly drinkable.
Described being used for carried out the used mixing device of electrolytic method to water, it is characterized in that, be made up of inner core and urceolus, inner core is located in the urceolus, is provided with variable valve in the ingress of inner core, and the wall of urceolus is provided with a hole facing to the inner core exit.
The present invention adopts nanofiltration device or RO membrane filtration to handle former water, by the mixing device of the present invention design, can carry out quantified controlling to TDS in the electrolytic water of need and specific conductivity simultaneously, can regulate arbitrarily, makes water after the electrolysis reach the technical requirements of setting smoothly.
Present method increases nanofiltration device or RO membrane filtration behind traditional cascade filtration, electrical conductivity of water is dispeled substantially, simultaneously, water inlet port at sodium filter device or RO filtering membrane picks out a mixing device, water after the certain proportion specific conductivity handled than higher water purification and nanofiltration device or RO film filter mixes, mixed water guarantees within the required range its specific conductivity, hardness, TDS all remain on an optimality criterion, this mixing device has setting device, can carry out ratio according to former electrical conductivity of water and regulate.
Advantage of the present invention is by to sodium filter or RO film filter treated water with through the smart water of coming that filters, and the mixing tank through adjustable apparatus is housed is handled adjusting arbitrarily to water quality, guarantees the consistence and the reliability of specific conductivity before its electrolysis.Simultaneously, a large amount of impurity in the water, objectionable impurities are all handled by sodium filter or RO film filter, eliminate fully, drawing by front end again needs electrolytic water (water purification behind the cascade filtration contains a large amount of mineral substance), has guaranteed that the former useful mineral substance in the water can not lose; Guaranteed that simultaneously electrolyzer carries out best electrolysis state to water, made the brine electrolysis of this moment reach the good water quality standard that the World Health Organization defines.
Description of drawings
Fig. 1 is the mixing device structural representation;
Fig. 2 is the inner tube structure synoptic diagram;
Fig. 3 is the outer tube structure synoptic diagram;
Fig. 4 carries out electrolytic method flow diagram for being used for to water.
Embodiment
The invention will be further described below in conjunction with drawings and Examples.
Embodiment
As shown in Figure 1, be the used mixing device of mixing device structural representation, described mixing device is made up of inner core 1 and urceolus 2, and inner core 1 is located in the urceolus 2, ingress at inner core 1 is provided with variable valve 3, and the wall of urceolus 2 is provided with a hole 4 facing to inner core 1 exit.
As shown in Figure 2, be the inner tube structure synoptic diagram, the outer end of described inner core 1 is a round tube type, in the middle of be provided with a circle can with the flange 5 of urceolus 2 nozzles sealings, the inner is a cone.
As shown in Figure 3, described urceolus 2 is the notch cuttype cylinder, and the internal diameter of the flange 5 of its internal diameter and inner core 1 coincide.
With pack into 2 li of urceolus of inner core 1, make the flange 5 and the sealing of urceolus 2 nozzles of inner core 1.
As shown in Figure 4, for being used for that water is carried out electrolytic method flow diagram, its method is:
The first step: Jiang Yuanshui carries out cascade filtration;
Second step: the water of cascade filtration is filtered filter or RO film filter through sodium again;
The 3rd step: with the water of cascade filtration with filter filter or the filtering water of RO film filter through sodium and enter mixing device and mix, water through cascade filtration enters from inner core 1 ingress, filtering filter or the filtering water of R film filter through sodium enters from the hole 4 of urceolus 2, in urceolus 2, mix, because inner core 1 ingress is provided with variable valve, available specific conductivity is tested or online detection immediately, carry out the adjusting of suitable proportion according to the former electrical conductivity of water of different situations, the water after making it and sodium filter or RO film filter being handled mixes the back specific conductivity and remains in certain required scope;
The 4th step: the water that will mix carries out after the electrolytic sterilizing processing promptly drinkable.

Claims (4)

1. one kind is used for water is carried out electrolytic method, and its method is:
The first step: Jiang Yuanshui carries out cascade filtration;
It is characterized in that,
Second step: the water of cascade filtration is filtered filter or RO film filter through sodium again;
The 3rd step: with the water of cascade filtration with filter filter or the filtering water of RO film filter through sodium and enter mixing device and mix;
The 4th step: the water that will mix carries out after the electrolytic sterilizing processing promptly drinkable.
2. according to claim 1 being used for carried out the used mixing device of electrolytic method to water, it is characterized in that, form by inner core (1) and urceolus (2), inner core (1) is located in the urceolus (2), ingress at inner core (1) is provided with variable valve (3), and the wall of urceolus (2) is provided with a hole (4) facing to inner core (1) exit.
3. according to claim 2 being used for carried out the used mixing device of electrolytic method to water, it is characterized in that, the outer end of described inner core (1) is a round tube type, in the middle of be provided with a circle can with the flange (5) of urceolus (2) nozzle sealing, the inner is a cone.
4. according to claim 2 being used for carried out the used mixing device of electrolytic method to water, it is characterized in that, described urceolus (2) is the notch cuttype cylinder, and the internal diameter of the flange (5) of its internal diameter and inner core (1) coincide.
CN 200510111565 2005-12-15 2005-12-15 Method for electrolyzing water Pending CN1982236A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200510111565 CN1982236A (en) 2005-12-15 2005-12-15 Method for electrolyzing water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200510111565 CN1982236A (en) 2005-12-15 2005-12-15 Method for electrolyzing water

Publications (1)

Publication Number Publication Date
CN1982236A true CN1982236A (en) 2007-06-20

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Application Number Title Priority Date Filing Date
CN 200510111565 Pending CN1982236A (en) 2005-12-15 2005-12-15 Method for electrolyzing water

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CN (1) CN1982236A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102452754A (en) * 2010-10-28 2012-05-16 四川久大制盐有限责任公司 A method for preparing alkaline ionized water by electroreduction
CN104030498A (en) * 2014-05-21 2014-09-10 国家电网公司 By-pass flow treatment method for circulating water from power plant
CN110590026A (en) * 2019-09-02 2019-12-20 深圳市深创环境工程技术有限公司 Dehydration method for deep conditioning of fecal sewage and sludge and dehydration device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102452754A (en) * 2010-10-28 2012-05-16 四川久大制盐有限责任公司 A method for preparing alkaline ionized water by electroreduction
CN102452754B (en) * 2010-10-28 2014-02-05 四川久大制盐有限责任公司 Method for preparing alkaline ionized water by electroreduction
CN104030498A (en) * 2014-05-21 2014-09-10 国家电网公司 By-pass flow treatment method for circulating water from power plant
CN104030498B (en) * 2014-05-21 2016-08-24 国家电网公司 A kind of electric power plant circulating water parallel seismic method method
CN110590026A (en) * 2019-09-02 2019-12-20 深圳市深创环境工程技术有限公司 Dehydration method for deep conditioning of fecal sewage and sludge and dehydration device

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