CN110482755A - Subacidity hypochloric acid water production equipment - Google Patents
Subacidity hypochloric acid water production equipment Download PDFInfo
- Publication number
- CN110482755A CN110482755A CN201811407762.8A CN201811407762A CN110482755A CN 110482755 A CN110482755 A CN 110482755A CN 201811407762 A CN201811407762 A CN 201811407762A CN 110482755 A CN110482755 A CN 110482755A
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- China
- Prior art keywords
- water
- hypochloric acid
- purification device
- subacidity hypochloric
- outlet
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 404
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 title claims abstract description 103
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 41
- 238000000746 purification Methods 0.000 claims abstract description 54
- 239000012528 membrane Substances 0.000 claims description 72
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 42
- 238000000108 ultra-filtration Methods 0.000 claims description 37
- 239000012498 ultrapure water Substances 0.000 claims description 37
- 238000001223 reverse osmosis Methods 0.000 claims description 34
- 238000001914 filtration Methods 0.000 claims description 21
- 235000020188 drinking water Nutrition 0.000 claims description 19
- 239000003651 drinking water Substances 0.000 claims description 19
- 239000008367 deionised water Substances 0.000 claims description 18
- 229910021641 deionized water Inorganic materials 0.000 claims description 18
- 229910021642 ultra pure water Inorganic materials 0.000 claims description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 13
- 229910052799 carbon Inorganic materials 0.000 claims description 13
- 238000009287 sand filtration Methods 0.000 claims description 8
- 238000012545 processing Methods 0.000 claims description 6
- XTEGARKTQYYJKE-UHFFFAOYSA-N chloric acid Chemical compound OCl(=O)=O XTEGARKTQYYJKE-UHFFFAOYSA-N 0.000 claims description 3
- 229940005991 chloric acid Drugs 0.000 claims description 3
- 239000003643 water by type Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 12
- 238000004140 cleaning Methods 0.000 description 11
- 238000009296 electrodeionization Methods 0.000 description 11
- 239000007788 liquid Substances 0.000 description 9
- 238000004659 sterilization and disinfection Methods 0.000 description 8
- 239000004576 sand Substances 0.000 description 7
- 239000012153 distilled water Substances 0.000 description 6
- 238000011010 flushing procedure Methods 0.000 description 6
- 239000008399 tap water Substances 0.000 description 6
- 235000020679 tap water Nutrition 0.000 description 6
- 238000012546 transfer Methods 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 238000012544 monitoring process Methods 0.000 description 4
- 239000008213 purified water Substances 0.000 description 4
- 230000001954 sterilising effect Effects 0.000 description 4
- 230000000844 anti-bacterial effect Effects 0.000 description 3
- 239000008280 blood Substances 0.000 description 3
- 210000004369 blood Anatomy 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000005611 electricity Effects 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 2
- 241000700605 Viruses Species 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910001424 calcium ion Inorganic materials 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 239000000645 desinfectant Substances 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 230000006870 function Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 229910001425 magnesium ion Inorganic materials 0.000 description 2
- 210000004877 mucosa Anatomy 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000008400 supply water Substances 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 241000282412 Homo Species 0.000 description 1
- 206010020852 Hypertonia Diseases 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 206010053615 Thermal burn Diseases 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000000840 anti-viral effect Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000003385 bacteriostatic effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000002242 deionisation method Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007646 directional migration Effects 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 239000002384 drinking water standard Substances 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- -1 for injecting Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 235000019645 odor Nutrition 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
- C02F1/4693—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electrodialysis
- C02F1/4695—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electrodialysis electrodeionisation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The present invention discloses a kind of subacidity hypochloric acid water production equipment.The production equipment includes at least one level purification device, and the purification device is used to carry out purified treatment to the raw water from raw water supply system and every grade of purification device is provided with corresponding water outlet；Subacidity hypochloric acid water generator, the subacidity hypochloric acid water generator is located at the purification device downstream and selectively connect with wherein first class purification device, and the subacidity hypochloric acid water generator is used to the water from the purification device being processed into subacidity hypochloric acid water；And feed water inlet, the water outlet of the water outlet of the purification device and the subacidity hypochloric acid water generator are switchably coupled to the feed water inlet by corresponding pipeline.The equipment is capable of providing a variety of different grades of purified waters or subacidity hypochloric acid water, and can be by user demand switching water intaking type.
Description
Technical field
The present invention relates to water production devices, and in particular to a kind of subacidity hypochloric acid water production equipment.
Background technique
Water is the material base of Source of life and socio-economic development and social progress.With social division of labor is elaborate
Change, in different application scenarios, diversified trend is presented in the requirement to water quality.For example daily drinking water needs to control water
Risk of the hardness to reduce inside of human body calcium deposition, generate calculus, in addition, in optical instrument, Mobile phone film, mobile phone screen
Cleaning in use is needed using high purity water.
At present the municipal water supplies water process of most domestic mainly in tap water suspended matter and micro- life such as bacterium
Object is handled, less to handle the originally water hardness, and may cause serious secondary dirt in tap water transportational process
Dye, such as high-rise water tank supply water, and very long tap water feed-line can all cause potential iron rust, scale and microorganism
Equal pollution problems.So the tap water of usually municipal water supplies can not be used directly, need using specific program to reach
Water purifying effect, to meet different production requirements.
In the industrial production common water purification processing method generally include sand filtration, carbon filtration, softening filtering, secondary filter,
Ultrafiltration, osmosis filtration (RO filtering) etc..Wherein sand filtration is that usually there are also manganese sand and anthracites as filtrate using natural siliceous sand
Water filtration treatment technical process, main function is macromolecular solid particle and colloid in trap water, makes clarification of water；Carbon filtration
It is similar with sand filtration, usually using active carbon as filtrate；Secondary filter can remove usual sand filtration and carbon filtration in water and cannot remove
Fine suspended matter or colloidal particle；Softening filtering refer to reduce the water hardness filtering technique, generally use highly acid sun from
Subtree rouge cements out the calcium and magnesium ion in raw water, and the water of softened filtration treatment is generally known as deionized water；Ultrafiltration
It is a kind of pressurization membrane separation technique, filter sizes can reach Nano grade, is usually used in separating macromolecular solute, can be used for producing
Drinking water；Osmosis filtration (RO filtering) membrane aperture is smaller, is usually used in separating small molecule solute, can be used for producing purified water.
Presently commercially available purifier generallys use above-mentioned one kind or a few method as method for treating water,
Certain certain types of purified water can only be generally provided, without the need being able to satisfy under different application environment for different quality
It asks.In addition, presently commercially available purifier cannot all produce subacidity hypochloric acid water.
Summary of the invention
The purpose of the application is to provide a kind of subacidity hypochloric acid water production equipment, is able to produce subacidity hypochlorous acid
Water, and be provided at least one feed water inlet, the feed water inlet can provide a user the purified water for reaching different brackets standard or
Subacidity hypochloric acid water, and can be by user demand switching water intaking type.
To achieve the goals above, the present invention proposes a kind of subacidity hypochloric acid water production equipment, comprising:
At least one level purification device, the purification device to from the raw water of raw water supply system for carrying out at purification
It manages and every grade of purification device is provided with corresponding water outlet；
Subacidity hypochloric acid water generator, the subacidity hypochloric acid water generator are located at the purification device downstream simultaneously
It is selectively connect with wherein first class purification device, the subacidity hypochloric acid water generator from the purification for that will fill
The water set is processed into subacidity hypochloric acid water；And
The water outlet of feed water inlet, the water outlet of the purification device and the subacidity hypochloric acid water generator by pair
The pipeline answered is switchably coupled to the feed water inlet.
In one embodiment, the subacidity hypochloric acid water production equipment further comprises at least one water tank, at least
The water outlet of purification device described in level-one is connected with corresponding water tank by pipeline and the subacidity hypochloric acid water is sent out
The water outlet of raw device is connected with corresponding water tank by pipeline, wherein the water outlet of each water tank is connected via pipeline
In the feed water inlet.
In one embodiment, there are two feed water inlets for the subacidity hypochloric acid water production equipment tool, with the purification device
The water outlet of water tank of water outlet connection be connected to one of feed water inlet, with the subacidity hypochloric acid water generator
The water outlet of water tank of water outlet connection be connected to another feed water inlet.
In one embodiment, the purification device includes:
First order purification device, the first order purification device carry out sand filtration, carbon filtration, softening and precision to the raw water
At least one of filtering processing, wherein the water outlet of the first order purification device is switchably coupled to institute by pipeline
State feed water inlet；And
Ultrafiltration membrane set filter, the ultrafiltration membrane set filter be located at first order purification device downstream and for into
One step filters the water from the first order purification device, wherein the water outlet of the ultrafiltration membrane set filter can by pipeline
It is connected to the feed water inlet to switching.
In one embodiment, the purification device further comprises reverse osmosis membrane filt, the reverse osmosis membrane filt
The water from the ultrafiltration membrane set filter is filtered positioned at ultrafiltration membrane set filter downstream and for further, wherein institute
The water outlet for stating reverse osmosis membrane filt is switchably coupled to the feed water inlet by pipeline.
In one embodiment, the subacidity hypochloric acid water production equipment further includes electric deionizer, the electricity go from
Sub-device is located at the reverse osmosis membrane filt downstream and for further filtering the water from the reverse osmosis membrane filt,
And the water outlet of the electric deionizer is switchably coupled to the feed water inlet by pipeline.
In one embodiment, the first order purification device includes softening filter, and the water tank includes deionized water
Water tank, the deionized water water tank are located at the softening filter downstream and for storing from the softening filter
Deionized water and the outlet of the deionized water water tank feed water inlet is switchably coupled to by pipeline.
In one embodiment, the water tank includes drinking water water tank and high purity water water tank, the drinking water water storage
Tank is located at the downstream of the ultrafiltration membrane set filter and connect with the water outlet of the ultrafiltration membrane set filter, comes for storing
From the drinking water of the ultrafiltration membrane set filter；The high purity water water tank is located at the downstream of the reverse osmosis membrane filt simultaneously
It is connect with the water outlet of the reverse osmosis membrane filt, for storing the high purity water from the reverse osmosis membrane filt；Wherein
The water outlet of the drinking water water tank and the high purity water water tank is switchably coupled to the feed water inlet by pipeline.
In one embodiment, the water tank further includes ultrapure water water tank, and the ultrapure water water tank is located at the electricity
Deionizer downstream is simultaneously connect with the water outlet of the electric deionizer, comes from the electric deionizer for storing
Ultrapure water；The outlet of the ultrapure water water tank is switchably coupled to the feed water inlet by pipeline.
In one embodiment, the subacidity hypochloric acid water production equipment further includes controller, and the controller is arranged to
Control the water outlet of the purification device and a water outlet and institute in the water outlet of the subacidity hypochloric acid water generator
State feed water inlet connection.
Bring of the present invention has the beneficial effect that
Subacidity hypochloric acid water production equipment utilizes hydrodynamics reaction method, can generate and is with subacidity hypochloric acid water
The acidic aqueous solution of major antibacterial ingredient.The subacidity hypochloric acid water solution shows stable subacidity, to bacterium and virus
Equal organic matters have high inhibition effect, and anti-fungistatic effect is harmless as the hypochlorous acid that human white blood ball generates,
It can be used for external application degerming.The subacidity hypochloric acid water can also be used in the air peculiar smell such as removing taste, musty, stink with perspiration.In addition, this
Invention subacidity hypochloric acid water production equipment has at least one feed water inlet, which can provide according to user demand reaches
To at least one of the purified water of different brackets standard or subacidity hypochloric acid water.
Detailed description of the invention
Fig. 1 is the system diagram of the subacidity hypochloric acid water production equipment of one embodiment of the invention.
Specific embodiment
Presently preferred embodiments of the present invention is described in detail below with reference to attached drawing, to be clearer to understand the present invention
Objects, features and advantages.It should be understood that embodiment shown in the drawings does not limit the scope of the present invention, and it is
In order to illustrate the connotation of technical solution of the present invention.
In the following description, elaborate certain details to mention for the purpose for illustrating various disclosed embodiments
For the thorough understanding to various open embodiments.But it one skilled in the relevant art will recognize that can be without these details
In one or more details the case where practice embodiment.Under other circumstances, well known dress associated with this application
It sets, structure and technology may not be illustrated in detail or describe to avoid unnecessarily obscuring the description of embodiment.
Unless context has other needs, and in the whole instruction and claim, word " comprising " and its modification, such as
"comprising" and " having " should be understood meaning that is open, including, that is, should be interpreted that " including, but are not limited to ".
Expression is in conjunction with the embodiments described to be referred to " one embodiment " or " embodiment " throughout the specification
Certain features, structure or feature are included at least one embodiment.Therefore, in each position of the whole instruction " at one
In embodiment " or " in an embodiment " in appearance without all referring to identical embodiment.In addition, certain features, structure or feature
It can combine in any way in one or more embodiments.
The singular as used in the specification and appended " one " and " described " include plural object,
Unless being clearly dictated otherwise in text.It should be noted that term "or" is usually used with the meaning that it includes "and/or", remove
It is clearly dictated otherwise in non-text.
In the following description, structure and working method of the invention in order to clearly demonstrate, will be by many Directional words
It is described, but should be by the words such as "front", "rear", "left", "right", "outside", "inner", " outside ", " inside ", "upper", "lower"
Language understands for convenience of term, and is not construed as word of limitation.
Subacidity hypochloric acid water production equipment 100 is integrally shown in Fig. 1.Subacidity hypochloric acid water production equipment 100 is wrapped
At least one level purification device is included, for carrying out purified treatment to the raw water from raw water supply system.Here, raw water refers to
The processed water of equipment without the application, such as the tap water from municipal water supplies.It is set in purification device downstreams at different levels
There is subacidity hypochloric acid water generator 106, for subacidity hypochlorous acid will to be processed into through the processed water of purification devices at different levels
Water.Here, subacidity hypochloric acid water refers to hypochloric acid water of the pH value range between 6.2~6.8, and under selected pH value,
Its pH variation range is within positive and negative 0.05.
Specifically, subacidity hypochloric acid water production equipment 100 includes fore filter 101 and raw water tank 102, preposition mistake
Filter 101 is connected to water source by pipeline 301.It is connected between fore filter 101 and raw water tank 102 by pipeline 302.Come
It is stored in raw water tank 102 after being filtered from the raw water of raw water supply system via fore filter 101.On fore filter 101
Trip position is provided with valve 303, can control raw water by valve switch and flow into subacidity hypochloric acid water production equipment 100.It should
Valve is set as hand-operated valve.Preferably, the valve may be alternatively provided as solenoid valve.
Also as shown in Figure 1, raw water tank 102 passes through piping connection to first order filter device 103.It is supplied from raw water and is
The raw water of system carries out at least one of sand filtration, carbon filtration, softening and secondary filter processing by first order filter device 103.Compared with
Goodly, the first order filter device 103 includes at least softening filtering, and forms deionized water.Specifically, the first order filters
Device 103 includes sand carbon filter 1031, softening filter 1032 and accurate filter 1033.But according to the water quality of raw water
Situation, first order filter device 103 may include sand carbon filter 1031, softening filter 1032 and accurate filter 1033
In any one or two combination.Sand carbon filter 1031 be used to remove large particulate matter in tap water and impurity and
Improve the mouthfeel of water.The calcium ions and magnesium ions that softening filter 1032 then is used to go in water removal, adjust the hardness of water.Secondary filter
Device 1033 can remove the fine suspended matter or colloidal particle that usual sand filtration and carbon filtration cannot remove in water.In addition, usually also setting
It sets for carrying out regenerated salt regenerating unit 10321 to softening filter 1032, for being carried out again to softening filter 1032
It is raw.
Two branches can be divided by the processed water of first order filter device 103, one of branch leads to a feed water inlet
(not shown), the feed water inlet can provide a user deionized water.It can by the processed deionized water of first order filter device 103
As laboratory, laboratory water, boiler feed water etc..Another branch then passes through pipeline 304 and is connected to ultrafiltration membrane set filter
And/or reverse osmosis membrane assembly 104.
Ultrafiltration membrane set filter has melt-blown filter, for further filtering the water from first order filter device 103.
It is ultrafiltration water through the processed water of ultrafiltration membrane set filter.The pore size filter of melt-blown filter is about 0.01 micron, quilt in ultrafiltration water
The impurity such as bacterium, iron rust, colloid and organic matter are further eliminated, but remain oxygen in water and the micro mine of needed by human body
The nutritional ingredients such as substance, water quality, which reaches the current direct drinking standard in China, can be used for kindergarten, hospital, home for destitute, hotel food and beverage etc.
Industry, specifically degerming is fresh-keeping, food processing, the antiviral, various aspects such as wash one's face and rinse one's mouth play a significant role.It is filtered by ultrafiltration membrane group
The processed water of device can be divided into two branches, and one of branch leads to the first feed water inlet 204, which reaches
The current drinking water standard in China.It is high purity water through the processed water of reverse osmosis membrane assembly, can reach high-purity water quality standard, it is basic
Do not retain the minerals in water, pH value between 6-7, be faintly acid, can be used as stoste or former material production amenities,
The products such as sterile products, skin mucosa disinfecting agent.
Reverse osmosis membrane assembly membrane aperture is smaller than ultrafiltration membrane, can be used for further filtering from first order filter device 103
Or the processed water of ultrafiltration membrane set filter.Two branches can be divided by the processed water of reverse osmosis membrane assembly, one of them
Branch leads to the first feed water inlet 204, which can provide a user high purity water, another branch leads to subacidity time chlorine
Sour water generator 106.
In one embodiment, electrodeionization (EDI) is connected to by another branch by the processed water of reverse osmosis membrane assembly
Device (not shown).In EDI device, the directional migration of water intermediate ion is realized under the action of electric field, to reach water
Deep purifying desalination, therefore, EDI water is known as ultrapure water (EDI water), can be widely applied to electric power, electronics, medicine, chemical industry,
Optical instrument and laboratory field.By the processed water of EDI device be mainly used for generate distilled water, for injecting, blood it is saturating
Analysis etc..Two branches can be divided by the processed water of EDI device, one of branch leads to an equipment feed water inlet, the feed water inlet
Ultrapure water can be provided a user, another branch leads to subacidity hypochloric acid water generator 106.
In one embodiment, another branch is also passed through by the processed ultrapure water of electrodeionization (EDI) device and (is not shown in figure
It is connected to distil(l) device (not shown) out).The water purity handled through distil(l) device is higher, can reach medicine
Distill water quality standard.Two branches can be divided by being distilled the processed water of purification device, and one of branch leads to the first water outlet
204, which can provide a user medical distilled water, another branch leads to hypochloric acid water processing unit (plant) 106,
For medical distilled water to be fabricated to subacidity hypochloric acid water；It can using the subacidity hypochloric acid water that the medicine distilled water makes
As the products such as stoste or former material production skin mucosa disinfecting agent, scald wound disinfection agent.
In the present embodiment, occur in ultrafiltration membrane set filter and/or reverse osmosis membrane assembly 104 and subacidity hypochloric acid water
Disinfection system 105 is provided between device 106, for carrying out sterilization treatment to water.Ultraviolet disinfection can be used in disinfection system 105
System.The ultraviolet disinfection system may include outer sleeve and the quartz ultraviolet tube that is arranged in outer sleeve, in outside
Annular channel is formed between casing and quartz ultraviolet tube, is passed through for pipeline water flow.It should be understood that sterilization method is unlimited
In aforesaid way, other sterilization methods can be used.
Subacidity hypochloric acid water generator 106 be located at purification device downstreams at different levels and selectively with wherein first class purification
Device connection, for above-mentioned deionized water, high purity water, ultrapure water, medical distilled water to be processed into subacidity hypochloric acid water,
In the branch that is connect with first order filter device 103, EDI device and distil(l) device be not shown.The application's is micro-
Acid hypochloric acid water generator 106 is using injection streaming reaction method.The resulting secondary chlorine of subacidity hypochloric acid water generator 106
Stable subacidity is presented in sour water, and it is narrow positive and negative 0.05 that pH value can stablize any one numerical value between 6.20-6.80
In range, it can be stored 18 months or more in the condition of being protected from light.The hypochloric acid water only generates the organic matters such as bacterium and virus strong
Inhibiting effect, anti-effective bacteriostatic ingredients have very strong degerming ability as the hypochlorous acid that human white blood ball generates, and
It is non-toxic to humans.The hypochloric acid water, which can also remove space smoke, stink, food odors, stink with perspiration etc., improves air quality.
Subacidity hypochloric acid water generator 106 includes a reactor 1061, medicine-chest 1062 and medicine-chest 1063.Medicine-chest
1062 and medicine-chest 1063 be respectively used to accommodate NaClO and HCl.According to reaction needs, by a certain amount of NaClO and HCl be added to
In reactor 1061 with from upstream purification device water hybrid concurrency life react, with generate pH value range 6.2~6.8 it
Between hypochloric acid water, and under selected pH value, pH variation range is within positive and negative 0.05.
The water outlet of subacidity hypochloric acid water generator 106 is used for via piping connection to the second feed water inlet 205 to user
It supplies water.Subacidity hypochloric acid water water tank is provided between subacidity hypochloric acid water generator 106 and the second feed water inlet 205
108, for storing the subacidity hypochloric acid water from subacidity hypochloric acid water generator.Preferably, in subacidity hypochloric acid water
Subacidity hypochloric acid water transfer water tank 109, this time are provided between generator 106 and subacidity hypochloric acid water water tank 108
Chloric acid water transfer water tank 109 is used for the storage during hypochloric acid water transfer.
Further, in the illustrated embodiment, which is provided with bypass line
201.The entrance of bypass line 201 is connect by triple valve 305 with raw water supply system.The triple valve 305 is configured to raw water
Supply system is selectively connect with bypass line 201 or first order filter device 103.The outlet of bypass line 201 via
Another triple valve 306 is connected to the water supply line of subacidity hypochloric acid water production equipment 100.Here, triple valve is electromagnetic three-way
Valve.It should be understood that triple valve by the solenoid valve that is separately mounted on bypass line and can also be mounted on subacidity time
Another solenoid valve of the water outlet branch road of chloric acid water generator substitutes.
Subacidity hypochloric acid water production equipment 100 is further provided with controller (not shown go out), when purification device or micro-
When acid hypochloric acid water generator breaks down, controller receives failure alarm signal, sounds an alarm and controls threeway Vavle switching
To bypass line 201, to guarantee that daily water consumption stablizes supply.
Further, as shown, being provided with deionized water water tank (figure in 103 downstream pipe of first order filter device
In be not shown), the water outlet of the deionized water water tank is connected to equipment feed water inlet via pipeline.Preferably, in ultrafiltration membrane group
Filter downstream pipeline is provided with drinking water water tank, and reverse osmosis membrane assembly downstream pipe is provided with high purity water water tank, drink
The first feed water inlet of equipment 204 is connected to via pipeline with the water outlet of water water tank and high purity water water tank.Preferably, in electricity
Deionization (EDI) device downstream pipe is provided with ultrapure water water tank (not shown), the water outlet of the ultrapure water water tank
Mouth is connected to equipment feed water inlet via pipeline.
Preferably, the feed water inlet of the first feed water inlet 204, the second feed water inlet 205 and other possible settings connects as desired
It is connected to one of deionized water branch, drinking water branch, high purity water branch, ultrapure water branch, medical distilled water branch or several
Kind.Controller is arranged to switch the water supply type of feed water inlet according to user setting.
Further, subacidity hypochloric acid water production equipment is provided with discharge pipe line 202, which passes through phase
The valve answered is connect with the outlet of each water tank.Preferably, the valve is set as solenoid valve, is controlled by controller and open and close
It closes.Fig. 1 embodiment is set as three-way solenoid valve 4025, is controlled and is switched by controller.Each water tank downstream pipe is provided with conveying
Pump and pressure switch, when pipeline pressure is smaller, pressure switch controls the delivery pump and opens to increase the pressure downstream to supply water
Power, when pipeline pressure is excessive, pressure switch controls delivery pump and closes.Each water tank is provided with level sensor.The liquid level is visited
The height that device is surveyed along water tank extends to detect the liquid level in corresponding water tank.
Within the setting time limit, when the liquid level that the level sensor detects is higher than predetermined fluid level, then controller is controlled
Discharge pipe line inlet valve is opened to drain and close the corresponding delivery pump of water tank downstream pipe.The water in water tank is determined as a result,
Phase discharge.Further, each water tank downstream water supply pipeline is provided with flowmeter, can be calculated accordingly according to the flowmeter registration
Water tank water supply.In setting time interval, if the flowmeter net flow is less than preset flow, controller control is opened
Discharge pipe line inlet valve is opened to drain and close the corresponding delivery pump of water tank downstream pipe.Thus, it is possible to by the water in water tank
Periodically discharge, thereby guarantees that the quality of water.Preferably, controller, which has, adjusts predetermined fluid level according to corresponding water tank water consumption
Function.
Specifically, for example, the outlet of raw water water tank 102 is provided with three-way solenoid valve 4025a.One, the triple valve goes out
Mouth is connected with discharge pipe line 202, another outlet is connected by pipeline 307 with first order filter device 103.Raw water water tank
Water tank height is provided with level sensor 4021a in 102, delivery pump 4023a, pressure switch are provided on pipeline 307
4027a, flowmeter 4022a and pressure sensor 4024a.Wherein pressure sensor 4024a is set to sand carbon filter 1031 and enters
At mouthful, for monitoring the pressure of its water inlet.When work, three-way solenoid valve 4025a is switched to be connected with pipeline 307, by raw water
Water tank 102 supplies water to first order filter device 103, and pressure sensor 4024a detects pipeline inlet water flow pressure.Work as pressure
When power is too low, the pressure that pressure switch 4027a control delivery pump 4023a increases downstream transport water is stopped when hypertonia
Only delivery pump 4023a.Within the setting time limit, when the liquid level that level sensor 4021a is detected is higher than predetermined fluid level, then control
Device control processed closes the corresponding delivery pump 4023a of 102 downstream pipe 307 of raw water water tank and switches three-way solenoid valve 4025a extremely
Discharge pipe line 202 is drained.
In setting time interval, if the flowmeter net flow is less than preset flow, such as the three day time in setting
In interval, if unused water or water consumption are lower than expection, the delivery pump 4023a that controller control is closed on pipeline 307 simultaneously will
Three-way solenoid valve 4025a switches to discharge pipe line 202 and is drained, to guarantee water supply quality.In addition, controller is according to the section
Water consumption in time interval, which is recalculated and controlled, adds aqueous position, and accordingly changes other preset values, for example change predetermined liquid
Position and preset flow.
Sand carbon filter 1031 is connected by pipeline 308 with softening filter 1032, is provided with pressure on pipeline 308
Sensor 4024b, also settable delivery pump, pressure switch, flowmeter on pipeline 308.Softening filter 1032 passes through pipeline
309 are connected with accurate filter 1033, and delivery pump, pressure switch, flowmeter can also be arranged on pipeline 309, wherein accurate
Filter 1033 is additionally provided with pressure sensor 4024c, for monitoring water flow pressure at accurate filter 1033.
First order filter device 103 is connected by pipeline 304 and ultrafiltration membrane set filter and/or reverse osmosis membrane assembly 104
It connects.The bottom end outlet of ultrafiltration membrane set filter and/or reverse osmosis membrane assembly 104 is also connect with discharge pipe line 202, is gone out in bottom end
Mouth is provided with dense row's diaphragm hand-operated valve 4029 and flowmeter 4022i, can manually control concentrated water discharge.It is arranged on pipeline 304
There are delivery pump 4023c, pressure switch 4027c, flowmeter (not shown go out), pressure sensor 4024c, is additionally provided with hand-operated valve
4026c。
Preferably, deionized water water tank (not shown go out) is provided on pipeline 304, in deionized water water tank
Outlet setting three-way solenoid valve, the triple valve one outlet are connect with ultrafiltration membrane set filter and/or reverse osmosis membrane assembly 104,
Another outlet is connect with discharge pipe line 202.Ultrafiltration membrane set filter and/or reverse osmosis membrane assembly 104 can set up ultrafiltration membrane group
Ultrafiltration membrane set filter and reverse osmosis membrane assembly can also be arranged, wherein reverse osmosis in filter or reverse osmosis membrane assembly simultaneously
Membrane module is set to ultrafiltration membrane set filter downstream.
Ultrafiltration membrane set filter downstream may be provided with the drinking water water tank of savings drinking water.Reverse osmosis membrane assembly downstream
It may be provided with the high purity water water tank of savings high purity water.Drinking water water tank and the outlet of high purity water water tank are provided with electromagnetism
Triple valve.The triple valve one outlet is connect with discharge pipe line 202, another outlet is connect with downstream pipe, for water into
The processing of one step.
Ultrafiltration membrane set filter and/or reverse osmosis membrane assembly 104 pass through pipeline 310 and subacidity hypochloric acid water generator
106 connections, are provided with bactericidal unit 105 in pipeline 310, for sterilizing to water.It is arranged in 105 inlet of bactericidal unit
There is flowmeter 4022d.Pipeline 310 is additionally provided with drinking water/high purity water water tank 107.Drinking water/107 edge of high purity water water tank
Height is provided with liquid level sensor 4021e.
Drinking water/107 exit of high purity water water tank is provided with triple valve 4025e.The triple valve one outlet and row
Water lines 202 connect.The triple valve another outlet branch road be provided with delivery pump 4023e, pressure switch 4027e with
And another triple valve 4025f.The one outlet of the triple valve is connect with subacidity hypochloric acid water generator 106, another goes out
Mouth is connect with the first feed water inlet 204, and branch road is provided with flowmeter 4022e, for monitoring pipeline flow.On the branch road
Equipped with flowmeter 4022f, for monitoring pipeline flow.
Subacidity hypochloric acid water generator 106 is connect by pipeline 311 with subacidity hypochloric acid water transfer water tank 109,
Subacidity hypochloric acid water transfer water tank 109 is along being highly provided with liquid level sensor 4021g.In subacidity hypochloric acid water transfer
109 exit of water tank is provided with three-way solenoid valve 4025g.The one of outlet of the triple valve is connect with discharge pipe line 202,
Another outlet is connect by pipeline 312 with subacidity hypochloric acid water water tank 108.Subacidity hypochloric acid water water tank 108 is set
It is equipped with liquid level sensor 4021h.Delivery pump 4023g is provided on pipeline 312.The outlet of subacidity hypochloric acid water water tank 108 is set
It is equipped with three-way solenoid valve 4025h, which connect with discharge pipe line 202, another outlet passes through pipeline 313
It is connect with the second feed water inlet 205.Delivery pump 4023h, pressure switch 4027h and flowmeter are provided on pipeline 313
4022h to monitor pressure, flow, and controls according to pressure and flow the movement of delivery pump and three-way solenoid valve.
Further, corresponding water tank entrance is provided with solenoid valve, when water tank emptying adds water again, works as liquid level
When higher than predetermined fluid level, controller closes the solenoid valve of the entrance.Preferably, corresponding water tank entrance also sets up a hand-operated valve
4026, the water inlet of water tank can be turned off manually.
Further, subacidity hypochloric acid water production equipment is provided with detergent line, which includes cleaning total road
203 and cleaning branch 206.Wherein, clean total road 203 at least one entrance and at least one outlet, each entrance via
Pipeline can open and close to connect with the water outlet of corresponding water tank, and each outlet is able to turn on or off via pipeline and corresponding purification device
Ground connection.It cleans 203 1, total road entrance in figure to connect with subacidity hypochloric acid water water tank, another entrance and drinking water
And/or the connection of high purity water water tank, one exports the entrance for being connected to first order filter device 103.
Another entrance for cleaning total road 203 is connect with raw water water tank 102, and outlet is connected to super by a pipeline
Filter membrane set filter and/or reverse osmosis membrane assembly 104, for ultrafiltration membrane set filter and/or reverse osmosis membrane assembly 104 into
Row rinses.The pipeline is provided with solenoid valve 4031.
Cleaning branch 206 is for cleaning water tank.Delivery pump is provided on the pipeline of water tank water outlet connection
4023.The entrance of cleaning branch 206 is connect with the outlet of delivery pump 4023, and outlet is connected to water tank entrance.Controller energy
It enough controls the unlatching of delivery pump 4023 and forms the flushing pressure of cleaning pipeline.The outlet for cleaning branch 206 is connected by pipeline
Flushing nozzle (not shown go out) inside to water tank, Flushing nozzle and the angled setting of water storage top tank structure.Controller is arranged to
Flushing nozzle rotation can be controlled, comprehensive flushing is carried out to water tank.It should be appreciated that Flushing nozzle as needed may be used
More than one is set, is merged into water tank water inlet with cleaning the outlet property of can choose of branch 206 same.In addition, clear
The road Xi Zong 203 and cleaning branch 206 are provided with solenoid valve, are opened or closed by controller control.
Presently preferred embodiments of the present invention has already been described in detail above, it is understood that if desired, embodiment can be modified
Aspect provides other embodiment to use the aspect, feature and design of various patents, application and publication.
In view of detailed descriptions above, these and other variation can be made to embodiment.In general, being wanted in right
In asking, term used should not be construed as limited to specific embodiment disclosed in description and claims, but should be managed
Solution be include whole equivalency ranges that all possible embodiment is enjoyed together with these claims.
Claims (10)
1. a kind of subacidity hypochloric acid water production equipment, which is characterized in that the subacidity hypochloric acid water production equipment includes:
At least one level purification device, the purification device is for the raw water progress purified treatment from raw water supply system and often
Grade purification device is provided with corresponding water outlet；
Subacidity hypochloric acid water generator, the subacidity hypochloric acid water generator are located at the purification device downstream and selective
Ground is connect with wherein first class purification device, and the subacidity hypochloric acid water generator is for adding the water from the purification device
Work is at subacidity hypochloric acid water；And
The water outlet of feed water inlet, the water outlet of the purification device and the subacidity hypochloric acid water generator passes through corresponding pipe
Road is switchably coupled to the feed water inlet.
2. subacidity hypochloric acid water production equipment according to claim 1, which is characterized in that the subacidity hypochloric acid water
Production equipment further comprises at least one water tank, and the water outlet of purification device described at least one level is connected with pair by pipeline
The water outlet of the water tank and the subacidity hypochloric acid water generator answered is connected with corresponding water tank by pipeline,
In the water outlet of each water tank be connected to the feed water inlet via pipeline.
3. subacidity hypochloric acid water production equipment according to claim 2, which is characterized in that the subacidity hypochloric acid water
For production equipment tool there are two feed water inlet, the water outlet for the water tank connecting with the water outlet of the purification device is connected to wherein one
The water outlet of a feed water inlet, the water tank connecting with the water outlet of the subacidity hypochloric acid water generator is connected to another confession
The mouth of a river.
4. subacidity hypochloric acid water production equipment according to claim 2, which is characterized in that the purification device includes:
First order purification device, the first order purification device carry out in sand filtration, carbon filtration, softening and secondary filter the raw water
At least one processing, wherein the water outlet of the first order purification device is switchably coupled to the water supply by pipeline
Mouthful；And
Ultrafiltration membrane set filter, the ultrafiltration membrane set filter are located at first order purification device downstream and for further mistakes
The water from the first order purification device is filtered, wherein the water outlet of the ultrafiltration membrane set filter is switchably connected by pipeline
It is connected to the feed water inlet.
5. subacidity hypochloric acid water production equipment according to claim 4, which is characterized in that the purification device is further
Including reverse osmosis membrane filt, the reverse osmosis membrane filt is located at ultrafiltration membrane set filter downstream and for further mistake
The water from the ultrafiltration membrane set filter is filtered, wherein the water outlet of the reverse osmosis membrane filt is switchably connected by pipeline
It is connected to the feed water inlet.
6. subacidity hypochloric acid water production equipment according to claim 5, which is characterized in that the subacidity hypochloric acid water
Production equipment further includes electric deionizer, the electric deionizer be located at the reverse osmosis membrane filt downstream and for into
The water outlet that one step filters water and the electric deionizer from the reverse osmosis membrane filt is changeable by pipeline
Ground is connected to the feed water inlet.
7. subacidity hypochloric acid water production equipment according to claim 6, which is characterized in that the first order purification device
Including softening filter, the water tank includes deionized water water tank, and the deionized water water tank is located at described softened
Filter downstream and for store deionized water and the deionized water water tank from the softening filter outlet lead to
Piping is switchably coupled to the feed water inlet.
8. subacidity hypochloric acid water production equipment according to claim 7, which is characterized in that the water tank includes drinking
Water water tank and high purity water water tank, the drinking water water tank are located at the downstream of the ultrafiltration membrane set filter and surpass with described
The water outlet of filter membrane set filter connects, for storing the drinking water from the ultrafiltration membrane set filter；The high purity water stores
Water pot is located at the downstream of the reverse osmosis membrane filt and connect with the water outlet of the reverse osmosis membrane filt, comes for storing
From the high purity water of the reverse osmosis membrane filt；Wherein the water outlet of the drinking water water tank and the high purity water water tank is logical
Piping is switchably coupled to the feed water inlet.
9. subacidity hypochloric acid water production equipment according to claim 8, which is characterized in that the water tank further includes surpassing
Pure water water tank, the ultrapure water water tank are located at the electric deionizer downstream and the water outlet with the electric deionizer
Mouth connection, for storing the ultrapure water from the electric deionizer；It the outlet of the ultrapure water water tank can by pipeline
It is connected to the feed water inlet to switching.
10. subacidity hypochloric acid water production equipment according to claim 1, which is characterized in that the subacidity hypochlorous acid
Water production device further includes controller, and the controller is arranged to control the water outlet of the purification device and the subacidity time
A water outlet in the water outlet of chloric acid water generator is connected to the feed water inlet.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811407762.8A CN110482755A (en) | 2018-11-23 | 2018-11-23 | Subacidity hypochloric acid water production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811407762.8A CN110482755A (en) | 2018-11-23 | 2018-11-23 | Subacidity hypochloric acid water production equipment |
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| Publication Number | Publication Date |
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| CN110482755A true CN110482755A (en) | 2019-11-22 |
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|---|---|---|---|
| CN201811407762.8A Pending CN110482755A (en) | 2018-11-23 | 2018-11-23 | Subacidity hypochloric acid water production equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020244353A1 (en) * | 2019-06-06 | 2020-12-10 | 上海万籁环保科技股份有限公司 | Non-electrolytic slightly acidic hypochlorous water generation apparatus, and generation method |
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| CN206196781U (en) * | 2016-11-23 | 2017-05-31 | 沐康源科技（北京）有限公司 | A kind of subacidity hypochloric acid water preparation facilities |
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| CN209128238U (en) * | 2018-11-23 | 2019-07-19 | 上海万籁环保科技股份有限公司 | Subacidity hypochloric acid water production equipment |
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| CN203728676U (en) * | 2013-12-31 | 2014-07-23 | 青岛澳德龙电子科技有限公司 | Medical comprehensive water treatment system |
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