CN205442891U - Open purification degasification water treatment facilities - Google Patents
Open purification degasification water treatment facilities Download PDFInfo
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- CN205442891U CN205442891U CN201620231032.7U CN201620231032U CN205442891U CN 205442891 U CN205442891 U CN 205442891U CN 201620231032 U CN201620231032 U CN 201620231032U CN 205442891 U CN205442891 U CN 205442891U
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- water inlet
- degasification
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Abstract
The utility model discloses an open purification degasification water treatment facilities, including purifying degasification mechanism, salt solution mechanism and anticorrosive mechanism, purify degasification mechanism and include water inlet, delivery port, discharge valve, purification chamber and devolatilizing chamber, salt solution mechanism and anticorrosive mechanism connect in parallel in water inlet department, and the water inlet setting is on the lateral wall that purifies the chamber, and the delivery port setting is purifying the chamber bottom, and discharge valve sets up at the devolatilizing chamber top, and the devolatilizing chamber is located and purifies the chamber top. The utility model discloses an open purification degasification water treatment facilities can get rid of warm impurity and the air that contains the systemic circulation aquatic that lead to through purifying degasification mechanism, makes water pressure stable, has reduced the cavitation and the noise pollution of water pump, has improved end -equipment's heat exchange efficiency and dehumidification function, cooperate salt solution mechanism and anticorrosive mechanism simultaneously, get rid of the calcium magnesium ion of aquatic, make the quality of water acid base balance, prevent that the pipeline from corroding and little biological pollution, reduced the running cost of system, prolonged life.
Description
Technical field
This utility model relates to a kind of HVAC system water treatment facilities, particularly to a kind of open purification de aerated water processing means.
Background technology
At present, the heating of more than 90% and air conditioner water circulating system, being often subject to the puzzlement of air problem, present in water system, large quantity of air (free gas in water and dissolved gas) will cause the appearance of series of problems: cavitation (in, the heat exchange efficiency affecting end-equipment and dehumidification function, corrosion and the harm of microorganism, sound pollution etc..
The mode solving the problems referred to above at present is to use limit pressure water feeding equipment, its mode many employings high expansion water box or pressurized tank realize with electro connecting pressure gauge, but it has that volume is big, level pressure inaccuracy, do not have degassing function, can not 100% absorption system swell increment, tank body be the shortcomings such as pressure vessel；Simultaneously because containing more calcium ions and magnesium ions in water, there will be the problem such as fouling, corrosion after temperature influence, system operation cost is caused to increase, operational efficiency reduces, service life shortens.
Utility model content
For solving above-mentioned technical problem, the utility model discloses a kind of open purification de aerated water processing means, including purifying deaerating mechanism, saline mechanism and anticorrosion mechanism, described purification deaerating mechanism includes water inlet, outlet, air bleeding valve, purification chamber and devolatilizing chamber, described saline mechanism and anticorrosion mechanism are connected in parallel on described water inlet, described water inlet is arranged on the sidewall in described purification chamber, described outlet is arranged on bottom described purification chamber, described air bleeding valve is arranged on described devolatilizing chamber top, and described devolatilizing chamber is positioned at above described purification chamber.
As further improvement of the utility model, described purification intracavity is provided with vortex stirrer and absorption filter bowl, it is provided with filter bottom described purification chamber, described vortex stirrer is vertically set on described purification intracavity, described absorption filter bowl is set in outside described vortex stirrer, and described filter is positioned at below described vortex stirrer and connects with described outlet.
As further improvement of the utility model, described saline mechanism includes brine tank and saltwater replenishment valve, and described brine tank is connected with described purification water inlet by saltwater replenishment valve.
As further improvement of the utility model, described anticorrosion mechanism includes preservative case and preservative replenishment valve, and described preservative case is connected with described purification water inlet by preservative replenishment valve.
As further improvement of the utility model, described water outlet is additionally provided with water quality testing meter.
The beneficial effects of the utility model are:
Open purification de aerated water processing means of the present utility model can remove impurity contained in HVAC system recirculated water and air by purifying deaerating mechanism, make stable water pressure, decrease cavitation and the noise pollution of water pump, improve heat exchange efficiency and the dehumidification function of end-equipment；Coordinate saline mechanism and anticorrosion mechanism simultaneously, remove the calcium ions and magnesium ions in water, make water quality acid-base balance, prevent corrosion of piping from polluting with microorganism, reduce the operating cost of system, extend service life.
Accompanying drawing explanation
In order to be illustrated more clearly that the technical scheme in this utility model embodiment, the accompanying drawing used required in embodiment will be briefly described below, apparently, accompanying drawing in describing below is only embodiments more of the present utility model, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is structural principle schematic diagram of the present utility model.
Labelling in figure: 1-purifies deaerating mechanism；11-water inlet；12-outlet；13-air bleeding valve；14-purifies chamber；141-vortex stirrer；142-adsorbs filter bowl；143-filter；15-devolatilizing chamber；16-water quality testing meter；2-saline mechanism；21-brine tank；22-saltwater replenishment valve；3-anticorrosion mechanism；31-preservative case；32-preservative replenishment valve.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is clearly and completely described, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole embodiments.
As shown in Figure 1, a kind of open purification de aerated water processing means, including purifying deaerating mechanism 1, saline mechanism 2 and anticorrosion mechanism 3, purify deaerating mechanism 1 and include that water inlet 11, outlet 12, air bleeding valve 13, purification chamber 14 and devolatilizing chamber 15, saline mechanism 2 and anticorrosion mechanism 3 are connected in parallel at water inlet 11.
Water inlet 11 is arranged on the sidewall purifying chamber 14, and outlet 12 is arranged on bottom purification chamber 14, and air bleeding valve 13 is arranged on devolatilizing chamber 15 top, and devolatilizing chamber 15 is positioned at above purification chamber 14, is additionally provided with the water quality testing meter 16 for detecting effluent quality at outlet 12.
Saline mechanism 2 includes brine tank 21 and saltwater replenishment valve 22, brine tank 21 is connected with water inlet 11 by saltwater replenishment valve 22, in purifying deaerating mechanism 1, saline is supplemented by saltwater replenishment valve 22, according to sodium form ion exchange principle, sodium ion exchanges with calcium ions and magnesium ions in water, calcium and magnesium is got rid of, makes water demineralization and less scaling.
Anticorrosion mechanism 3 includes that preservative case 31 and preservative replenishment valve 32, preservative case 31 are connected with water inlet 11 by preservative replenishment valve 32, supplements preservative by preservative replenishment valve 32 in purifying deaerating mechanism 1, prevents corrosion of piping from polluting with microorganism.
Vortex stirrer 141 and absorption filter bowl 142 it is provided with in purifying chamber 14, purify and be provided with filter 143 bottom chamber 14, vortex stirrer 141 is vertically set in purification chamber 14, absorption filter bowl 142 is set in outside vortex stirrer 141, and filter 143 is positioned at below vortex stirrer 141 and connects with outlet 12.
During work, vortex stirrer 141 rotarily drives the water purified in chamber 14 and rotates formation vortex, according to centripetal force formula F=mv2/ r, wherein: m be mass of object (kg), v be object linear velocity (m/s), r be the moving radius (m) of object.As shown from the above formula, the impurity in water is moved closer to vortex core by centripetal force effect in rotary course, and radius constantly reduces, and this pulling force is also continuing to increase, so object can be with elliptical orbit close to whirlpool center.The most heavier impurity will be inhaled in the filter 143 below vortex stirrer 141, and lighter float is then attracted to adsorb on filter bowl 142, thus realizes the purification of impurities in water.
Opening the outside aerofluxus of air bleeding valve 13, according to Henry's law, gas is dissolubility and water temperature and pressure correlation in water, at a certain temperature, is directly proportional to the pressure of gas.When air bleeding valve 13 is outwards bled, the pressure of the intracavity water surface reduces, and makes gas evolution soluble in water, makes stable water pressure, decrease cavitation and the noise pollution of water pump, improves heat exchange efficiency and the dehumidification function of end-equipment.
Open purification de aerated water processing means of the present utility model can remove impurity contained in HVAC system recirculated water and air by purifying deaerating mechanism 1；Coordinate saline mechanism 2 and anticorrosion mechanism 3 simultaneously, remove the calcium ions and magnesium ions in water, make water quality acid-base balance, prevent corrosion of piping from polluting with microorganism, reduce the operating cost of system, extend service life.
The foregoing is only preferred embodiment of the present utility model; not in order to limit this utility model; all within spirit of the present utility model and principle, any modification, equivalent substitution and improvement etc. made, within should be included in protection domain of the present utility model.
Claims (5)
1. an open purification de aerated water processing means, it is characterized in that, including purifying deaerating mechanism, saline mechanism and anticorrosion mechanism, described purification deaerating mechanism includes water inlet, outlet, air bleeding valve, purification chamber and devolatilizing chamber, described saline mechanism and anticorrosion mechanism are connected in parallel on described water inlet, described water inlet is arranged on the sidewall in described purification chamber, described outlet is arranged on bottom described purification chamber, described air bleeding valve is arranged on described devolatilizing chamber top, and described devolatilizing chamber is positioned at above described purification chamber.
Open purification de aerated water processing means the most according to claim 1, it is characterized in that, described purification intracavity is provided with vortex stirrer and absorption filter bowl, it is provided with filter bottom described purification chamber, described vortex stirrer is vertically set on described purification intracavity, described absorption filter bowl is set in outside described vortex stirrer, and described filter is positioned at below described vortex stirrer and connects with described outlet.
Open purification de aerated water processing means the most according to claim 1, it is characterised in that described saline mechanism includes brine tank and saltwater replenishment valve, described brine tank is connected with described purification water inlet by saltwater replenishment valve.
4., according to the open purification de aerated water processing means described in claim 1 or 3, it is characterised in that described anticorrosion mechanism includes preservative case and preservative replenishment valve, described preservative case is connected with described purification water inlet by preservative replenishment valve.
Open purification de aerated water processing means the most according to claim 1, it is characterised in that described water outlet is additionally provided with water quality testing meter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620231032.7U CN205442891U (en) | 2016-03-24 | 2016-03-24 | Open purification degasification water treatment facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620231032.7U CN205442891U (en) | 2016-03-24 | 2016-03-24 | Open purification degasification water treatment facilities |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205442891U true CN205442891U (en) | 2016-08-10 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620231032.7U Expired - Fee Related CN205442891U (en) | 2016-03-24 | 2016-03-24 | Open purification degasification water treatment facilities |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109160574A (en) * | 2018-11-13 | 2019-01-08 | 开平市狮山林场松香厂 | A kind of resin purification machine |
-
2016
- 2016-03-24 CN CN201620231032.7U patent/CN205442891U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109160574A (en) * | 2018-11-13 | 2019-01-08 | 开平市狮山林场松香厂 | A kind of resin purification machine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160810 Termination date: 20200324 |