CN213924172U

CN213924172U - PH physicochemical adjustment technical device for drinking water

Info

Publication number: CN213924172U
Application number: CN202021922257.XU
Authority: CN
Inventors: 池国正; 池文君; 戴璐; 诸葛芝; 汪星; 江兵; 柳枫琪; 池万青
Original assignee: Zhejiang Lianchi Water Equipment Stock Co ltd
Current assignee: Zhejiang Lianchi Water Equipment Stock Co ltd
Priority date: 2020-09-05
Filing date: 2020-09-05
Publication date: 2021-08-10
Anticipated expiration: 2030-09-05

Abstract

The utility model discloses a PH physicochemical adjusting technical device for drinking water, which comprises a tank body with a first cavity and a second cavity, a water conveying structure for conveying water in the second cavity into the first cavity, a water inlet piece communicated with the second cavity, and a water outlet structure communicated with the first cavity; and a PH adjusting medium capable of performing a neutralization reaction with acidic water is arranged in the first chamber. The utility model discloses an export orientation sets up down, when making the water source of acidity come in, the water source is by middle to both sides diffusion, make the direction more even of rivers through, secondly through aeration equipment's setting again, the activity between calcium carbonate and the calcium carbonate has been increased, reduce calcium carbonate and produce the phenomenon that hardens, set up for the flaring shape through first cavity from bottom to top again at last, make the velocity of flow of water slow down from fast, the water source that prevents overflow department drives calcium carbonate and spills over, make the pipeline be difficult for blockking up, cost of maintenance reduces, more labour saving and time saving.

Description

PH physicochemical adjustment technical device for drinking water

Technical Field

The utility model belongs to the technical field of drinking water treatment, especially, relate to a drinking water PH materialization regulation technology device.

Background

Water is the basis on which people rely for survival and is an important natural resource in the world. With the increasing serious water pollution, a large amount of organic matters and heavy metal substances enter a water source in different ways, and the drinking water source is seriously polluted. In recent years, the toxic and disease caused by drinking water source pollution is endless, such as the pollution of the purple gold mining, which seriously affects the drinking water and agricultural production of local residents, and the 'chromium residue pollution event' in the city of qujing, Yunnan province, which is disputed in recent years, is more and more concerned about the safety of drinking water, so that people are more and more conscious of drinking water health, and the requirement for improving water quality is more and more urgent. In such market environments, water quality purification equipment is also in increasing demand. As the application field of water purification equipment is expanding, professional manufacturers of water purification equipment are also confronted with problems such as ensuring quality of purified water and improving after-sales maintenance of water purification equipment while enjoying the benefits of such growth.

At present, the existing drinking water pH adjusting mode is to pump calcium carbonate liquid into drinking water according to a certain proportion through a water pump to neutralize the acidity of the drinking water, but in the mode, the pumping amount of the calcium carbonate liquid is difficult to accurately control, so that the effect of adjusting the drinking water pH is influenced, the water pump is easy to block, and the maintenance cost is high; the pumping proportion of the calcium carbonate liquid needs to be manually controlled and allocated, so that the labor consumption cost is high, and time and labor are wasted.

SUMMERY OF THE UTILITY MODEL

The utility model provides a drinking water adjusting device which can automatically adjust the PH value and has good adjusting effect to overcome the defects of the prior art.

In order to achieve the above purpose, the utility model adopts the following technical scheme: a PH physicochemical adjustment technical device for drinking water comprises a tank body with a first cavity and a second cavity, a water conveying structure for conveying water in the second cavity into the first cavity, a water inlet piece communicated with the second cavity, and a water outlet structure communicated with the first cavity; and a PH adjusting medium capable of performing a neutralization reaction with acidic water is arranged in the first chamber. The utility model discloses an inside adjusting medium drops into first cavity, acidic water can and adjusting medium automatic emergence neutralization reaction, after acidic water gradually becomes neutral quality of water, adjusting medium no longer reacts with water, thereby make more accurate that water was adjusted, thereby reduce the ingestion of cost of labor, again because adjusting medium directly drops into inside first cavity, make inside this medium has been deposited first cavity always, it is not direct to contact with any pipeline, cost of maintenance greatly reduced, more labour saving and time saving.

Further, the pH adjusting medium is calcium carbonate particles. Through setting up PH conditioning medium and being the calcium carbonate granule, through the setting of granule, when water when flowing, can drive the mutual collision between granule and the granule, and then make mutually scattering between the granule be powdered, the powdery calcium carbonate can be better with the acidic quality of water take place neutralization reaction.

Further, the first chamber is in a flaring structure from bottom to top. Through the setting of flaring shape, the water source of acidity flows in from the flaring lower part earlier, at this moment, the velocity of flow of water becomes fast, rivers become fast and drive the calcium carbonate granule of subsiding lower part in the cell body and stir, can drive the friction of colliding with each other between calcium carbonate and the calcium carbonate when stirring, thereby effectually prevent that calcium carbonate from producing the phenomenon that hardens, flow into flaring upper portion from the flaring lower part when the water source afterwards, at this moment, the velocity of flow of water becomes slow gradually, thereby rivers become slow and make heavier calcium carbonate granule sink downwards, simultaneously the velocity of flow of water slows down and is difficult to drive calcium carbonate overflow together, thereby make the pipeline be difficult for plugging up, the cost of labor intakes lowly, and labour saving and time saving.

Further, the water inlet part is provided with an inlet and an outlet, and the outlet is arranged in a downward direction. Set up downwards through the export direction, make the water source when acidity get into from the import, it is inside to advance water spare to flow through, spout downwards again by the export, make the water source by middle diffusion to around, and can be in the second chamber bottom at utmost disperse, make the more even of water source distribution, secondly the bottom contact in spun water source and the second chamber, when the bottom in the contact storage second chamber, water can carry out the clash of water impact power to the bottom in the second chamber, with the help of the impact force, water is to the more wide of diffusion around, the inside water of cell body can mix with water more even, the water source mixes the phenomenon that produces the stirring in the cell body, also drive calcium carbonate simultaneously and stir, take place neutralization reaction with the quality of water of acidity, make the neutralization reaction effect of water better.

Furthermore, one end of the water inlet piece extends into the second chamber, and the outlet is formed in the end part of the water inlet extending into the second chamber. Through the setting of the piece that intakes, with the utility model discloses in, the central point in the pond is located to this piece best selection that intakes, through the setting at central point for the water source can be fully even by middle to both sides diffusion, the effect of mixing between water and the water is better, and the water source of each department can carry out fully and react with calcium carbonate.

Further, the device also comprises an aeration device used for conveying gas into the first chamber. Through setting up aeration equipment, when great granule subsides the bottom in the cell body, aeration equipment starts for calcium carbonate in the cell body and calcium carbonate produce the phenomenon of floating the collision, increase the activity of calcium carbonate, make calcium carbonate be difficult for piling up, and can not produce the phenomenon that hardens, the usefulness of full play calcium carbonate, thereby the powder that calcium carbonate collision friction goes out can take place the neutralization reaction with the water source of acidity is automatic, it is better to have guaranteed that water source reaction effect.

Further, the aeration device comprises an aeration pipe communicated with the second chamber and an aeration piece connected with the aeration pipe. Through setting up the piece of exposing to the sun, can produce the phenomenon of the stirring of floating to the accumulational calcium carbonate that sinks for take place the friction each other between calcium carbonate and the calcium carbonate, increase the activity of calcium carbonate, the phenomenon that prevents to harden produces, calcium carbonate activeness increases simultaneously, make the area of calcium carbonate and water mutual contact big more, make the water source of each department can both take place abundant reaction with calcium carbonate, make the effect of water regulation better, moreover, the steam generator is simple in structure, the intake of cost is reduced.

Furthermore, the water delivery structure comprises a filter plate arranged in the tank body and a plurality of filter heads arranged on the filter plate. Through the setting of filter for first cavity and second cavity keep apart relatively, prevent simultaneously that the calcium carbonate granule from piling up the bottom in the second cavity, make the water source can't spout from the export, secondly when gas gets into the time from the filter head, owing to be provided with a plurality of filter heads, make more even that gas can diffuse, thereby the calcium carbonate that has driven each department can float, reduces the accumulational phenomenon of calcium carbonate.

Furthermore, a first switch is arranged on the water inlet piece, and a second switch is arranged on the aerator pipe. Through setting up first switch and second switch, played certain guide effect to water source and gas, prevented the phenomenon of water source and gas reflux, guaranteed the stability that whole equipment goes on, it is better to realize the water reaction effect.

Furthermore, the water outlet structure comprises a water collecting tank arranged on the upper part of the tank body in a covering manner and a water outlet pipe connected with the water collecting tank. Through the setting of header tank for water after the reaction can be collected from the inside overflow of cell body to the header tank in, the mode that adopts the overflow carries out a effect of slowing down to the water source of overflow, makes the water source that flows more steady, and rivers slow down also to be difficult for flowing calcium carbonate simultaneously.

To sum up the utility model has the advantages of it is following: set up downwards through the export direction, when making the water source of acidity come in, the water source is by middle to both sides diffusion, make the direction that the water flows through more even, secondly through aeration equipment's setting again, the activity between calcium carbonate and the calcium carbonate has been increased, reduce calcium carbonate and produce the phenomenon that hardens, set up for the flaring shape through first cavity from bottom to top again at last, make the velocity of flow of water from fast slowing down, the water source that prevents the overflow department drives the calcium carbonate and spills over, make the pipeline be difficult for blockking up, cost of maintenance reduces, more labour saving and time saving.

Drawings

Fig. 1 is a schematic structural diagram of the present invention.

Fig. 2 is a left side view of the present invention.

Fig. 3 is a first cross-sectional perspective view taken along a-a in fig. 2.

Fig. 4 is a second sectional perspective view taken along a-a in fig. 2.

Detailed Description

As shown in fig. 1-4, a PH physicochemical adjustment technical device for drinking water comprises a first chamber 1, a second chamber 2, a water delivery structure 4, a water inlet member 5 and a water outlet structure 6; the pool body 3 is provided with a first cavity 1 and a second cavity 2, a PH adjusting medium capable of performing a neutralization reaction with acidic water is arranged in the first cavity 1, the PH adjusting medium is calcium carbonate particles 7, the water sending piece is made of stainless steel, the quality of flowing water is pure, lead-free and harmless to human bodies is ensured by adopting the stainless steel, and the stainless steel is low temperature resistant, non-cracking and high in durability; the water feeding piece is communicated with the second chamber 2; the water outlet structure 6 is communicated with the first chamber 1.

Specifically, the first chamber 1 is in a flaring shape from bottom to top, the water source flows from fast to slow in flow speed through the flaring shape, the fast place of the flow speed accelerates the mutual collision and friction of calcium carbonate and calcium carbonate in the water storage tank, so that the powder which is rubbed out is released in water and reacts and dissolves with the water, and the water reaction effect is better; the water conveying structure 4 is used for conveying water in the second chamber 2 into the first chamber 1;

specifically, the water feeding member is communicated with the second chamber 2, the water feeding member is provided with a first switch 52, further, the water feeding member is provided with an inlet 50 and an outlet 51, the outlet 51 is arranged downwards, and the outlet 51 is arranged downwards, so that when an acidic water source enters from the inlet 50, flows through the inside of the water inlet piece 5 and is sprayed downwards from the outlet 51, the water source is diffused from the middle to the periphery, the water flows more uniformly, the second water source is contacted with the bottom of the second chamber 2, and when the second water source is contacted with the bottom of the second chamber 2, the water will impact the bottom of the second chamber 2 with the impact force of the water, so that the water flow speed is accelerated by the impact force, meanwhile, the neutralization reaction of water and calcium carbonate is accelerated, so that the neutralization reaction effect of water is better, one end of the water feeding piece extends into the second chamber 2, and the outlet 51 extends into the end part of the second chamber 2; the water inlet part 5 is provided with a first switch 52.

Specifically, the device further comprises an aeration device 8 for conveying gas into the first chamber 1, wherein the aeration device 8 comprises an aeration pipe 80 and an aeration piece 81; the aeration pipe 80 is communicated with the second chamber 2; a second switch 82 is arranged on the aeration pipe 80; aeration spare 81 links to each other with this aeration pipe 80, this aeration spare 81 is prior art, for the air-blower that can purchase on the market, when the velocity of flow at the water source was slower through setting up of aeration spare 81, aeration spare 81 carries out the impact of wind-force to the water source, the velocity of flow of rivers has been accelerated, the velocity of flow accelerates to make the reaction with water more high-efficient, carry out the effect of stirring to water simultaneously, make the rivers of each department can both react, avoid the water source at dead angle play, make the effect of water regulation better.

Specifically, the water delivery structure 4 comprises a filter plate 40 and a filter head 41; the filter plate 40 is fixedly connected with the inside of the tank body 3; the number of the filter heads 41 is a plurality, and the filter heads 41 can be arranged according to specific situations, and the filter heads 41 are uniformly arranged on the filter plate 40 at intervals.

Specifically, the water outlet structure 6 comprises a water collecting tank 10 and a water outlet pipe 11; the water collecting tank 10 is covered on the upper part of the tank body 3; the water outlet pipe 11 is connected with the bottom of the water collecting tank 10, and the water outlet pipe 11 is made of stainless steel pipes.

The utility model discloses a concrete work flow as follows: firstly, acidic water enters from an inlet 50, the acidic water passes through the inside of the water inlet piece 5 and then flows into the second chamber 2 from an outlet 51, the acidic water drives calcium carbonate in the second chamber 2 to collide under the action of flow velocity, the calcium carbonate and the calcium carbonate rub with each other, powder generated by the friction is combined with the acidic water, the acidic water and the calcium carbonate are subjected to neutralization reaction, then the water flows out from the filter head 41 and enters the first chamber 1, the acidic water continues to react with the calcium carbonate, after the reaction regulation is finished, the water is neutral, and the neutral water overflows into the water collecting tank 10 and then flows out from the water outlet pipe 11.

When the acidic water flows out from the outlet 51, the acidic water has a slow flow rate, so that the calcium carbonate and the calcium carbonate cannot react, the aeration piece 81 is started, the air flows through the aeration pipe 80, flows out from the aeration pipe 80, the flow rate of the water is accelerated under the driving of the wind power, the calcium carbonate and the calcium carbonate are driven to collide with each other, and the acidic water is subjected to a neutralization reaction, wherein the reaction process is the same as the above.

Claims

1. A PH physicochemical adjustment technical device for drinking water comprises a tank body (3) provided with a first chamber (1) and a second chamber (2), a water conveying structure (4) used for conveying water in the second chamber (2) into the first chamber (1), a water inlet piece (5) communicated with the second chamber (2), and a water outlet structure (6) communicated with the first chamber (1); the method is characterized in that: a PH adjusting medium capable of generating a neutralization reaction with acidic water is arranged in the first chamber (1).

2. The drinking water PH physicochemical regulating technical device according to claim 1, characterized in that: the pH adjusting medium is calcium carbonate particles (7).

3. The drinking water PH physicochemical regulating technical device according to claim 1, characterized in that: the first chamber (1) is of a flaring-shaped structure from bottom to top.

4. The drinking water PH physicochemical regulating technical device according to claim 1, characterized in that: the water inlet part (5) is provided with an inlet (50) and an outlet (51), and the outlet (51) is arranged downwards.

5. A drinking water PH materialization adjustment technical device according to claim 4, characterized in that: one end of the water inlet piece (5) extends into the second chamber (2), and the outlet (51) extends into the end part of the second chamber (2).

6. The drinking water PH physicochemical regulating technical device according to claim 1, characterized in that: also comprises an aeration device (8) used for conveying gas into the first chamber (1).

7. The PH physicochemical regulating technical device for drinking water is characterized in that the aeration device (8) comprises an aeration pipe (80) communicated with the second chamber (2) and an aeration piece (81) connected with the aeration pipe (80).

8. The PH physicochemical regulating technical device for drinking water is characterized in that the water conveying structure (4) comprises a filter plate (40) arranged in the tank body (3) and a plurality of filter heads (41) arranged on the filter plate (40).

9. The PH physicochemical regulating technical device for drinking water is characterized in that a first switch (52) is arranged on the water inlet piece (5), and a second switch (82) is arranged on the aeration pipe (80).

10. The drinking water PH physicochemical regulating technical device according to claim 1, characterized in that: the water outlet structure (6) comprises a water collecting tank (10) which is covered on the upper part of the tank body (3) and a water outlet pipe (11) which is connected with the water collecting tank (10).