CN108168329A - A kind of condensate recycling device - Google Patents
A kind of condensate recycling device Download PDFInfo
- Publication number
- CN108168329A CN108168329A CN201711469709.6A CN201711469709A CN108168329A CN 108168329 A CN108168329 A CN 108168329A CN 201711469709 A CN201711469709 A CN 201711469709A CN 108168329 A CN108168329 A CN 108168329A
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- CN
- China
- Prior art keywords
- pipe
- purification
- collecting chamber
- air collecting
- liquid storage
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B9/00—Auxiliary systems, arrangements, or devices
- F28B9/08—Auxiliary systems, arrangements, or devices for collecting and removing condensate
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The invention discloses a kind of condensate recycling devices, including air collecting chamber and liquid storage cylinder, the liquid storage cylinder is set on air collecting chamber side, the air collecting chamber both sides are equipped with gas collecting tube, the air collecting chamber is internally provided with nozzle, the air collecting chamber bottom is pumped equipped with first pressure, and the first pressure pump side face is equipped with first circulation pipe, and the first circulation pipe side is equipped with the first purification pipe and is managed with the second purification.The present invention passes through gas collecting tube and nozzle, when being entered in air collecting chamber by gas collecting tube in order to water vapour, the gas collecting tube being obliquely installed can cause water vapour spiral to move upwards, second pressure pump is by third circulation pipe by the water pump in liquid storage cylinder to nozzle, water is trickled down by nozzle, and the low temperature water mist that nozzle sprays can have the contact area of bigger compared to common heat exchanger tube with the higher water vapour of temperature, so that liquefaction efficiency is faster, organic efficiency higher has higher practicability.
Description
Technical field
The present invention relates to refrigeration technology field, more particularly to a kind of condensate recycling device.
Background technology
Condenser is the parts of refrigeration system, belongs to one kind of heat exchanger, gas or steam can be transformed into liquid, will
Heat in pipe is passed in a manner of quickly in the air near pipe, and condenser working process is an exothermic process, institute
All it is higher with condenser temperature, power plant is condensed with the steam that many condensers discharge turbine, is being freezed
With condenser come the refrigerant vapor of condensate ammonia and freon etc in factory, in petro chemical industry with condenser make hydro carbons and other
Chemical evapn condenses, and in distillation process, the device for steam being transformed into liquid is also referred to as condenser.
Condenser can generate a large amount of water vapours at work, these water vapours generally all can directly drift in air, this
Sample will result in certain waste of water resource, if condenser is for some chemical industry aspect, also having in the water vapour of generation can
It can thus be likely to result in the pollution of environment containing some industrial chemicals, be unfavorable for environmental protection.
Therefore, it is necessary to solve the above problems to invent a kind of condensate recycling device.
Invention content
The purpose of the present invention is to provide a kind of condensate recycling device, to solve the problems mentioned in the above background technology.
To achieve the above object, the present invention provides following technical solution：A kind of condensate recycling device, including air collecting chamber and storage
Sap cavity, the liquid storage cylinder are set on air collecting chamber side, and the air collecting chamber both sides are equipped with gas collecting tube, and the air collecting chamber is internally provided with spray
Head, the air collecting chamber bottom are pumped equipped with first pressure, and the first pressure pump side face is equipped with first circulation pipe, the first circulation
Pipe side is equipped with the first purification pipe and is managed with the second purification, and the second purification pipe is set on the first purification bottom of the tube, and described first is net
Change pipe with being equipped with circulating electromagnetic valve and water-purifying cavity on the second purification pipe, the water-purifying cavity is set on circulating electromagnetic valve side, described
Water-purifying cavity is internally provided with adsorption filtration chamber and deep layer purify cavity, and the end of the first purification pipe and the second purification pipe is equipped with second
Circulation pipe, the second circulation pipe is at the top of liquid storage cylinder and extends to inside liquid storage cylinder, and the liquid storage cylinder is internally provided with magnetic and floats
Sub- liquid level gauge, the magnetic float liquidlevel meter side are equipped with third circulation pipe, and the third circulation pipe is pumped equipped with second pressure, institute
It states second pressure pump side and is equipped with controller, the liquid storage cylinder side is equipped with drain pipe, and the drain pipe is equipped with drain electromagnetism
Valve.
Preferably, there are two the adsorption filtration chamber and deep layer purify cavity are all provided with, described two adsorption filtration chambers and two
Deep layer purify cavity is respectively arranged on the first purification pipe and the second purification pipe, and the deep layer purify cavity is set on adsorption filtration chamber side.
Preferably, the adsorption filtration intracavitary portion is filled with activated carbon, and the deep layer purify cavity is internally provided with reverse osmosis membrane.
Preferably, the magnetic float liquidlevel meter model is set as UHZ-25.
Preferably, the circulating electromagnetic valve, magnetic float liquidlevel meter and draining solenoid valve are electrically connected with controller.
Preferably, the third circulation pipe runs through at the top of air collecting chamber and extends to inside air collecting chamber and connect with nozzle.
Preferably, the gas collecting tube is obliquely installed in air collecting chamber both sides.
Preferably, the first purification pipe and the second purification Guan Junyu first circulation pipes are detachably connected by screw thread, institute
It states the first purification pipe and the second purification Guan Junyu second circulation pipes is detachably connected by screw thread.
The technique effect and advantage of the present invention：The present invention by gas collecting tube and nozzle, in order to water vapour by gas collecting tube into
When entering in air collecting chamber, the gas collecting tube being obliquely installed can cause water vapour spiral to move upwards, and second pressure pump is recycled by third
Pipe by the water pump in liquid storage cylinder to nozzle, by nozzle trickled down by water, and the low temperature water mist that nozzle sprays can compared to common heat exchanger tube
To have the contact area of bigger with the higher water vapour of temperature, so that liquefaction efficiency is faster, organic efficiency higher has
Higher practicability is managed by being equipped with the first purification pipe and the second purification, in order to when the adsorption filtration chamber on the first purification pipe
With deep layer purify cavity after using for a longer period, clean-up effect will reduce, and close the circulating electromagnetic valve on the first purification pipe at this time,
The circulating electromagnetic valve on the second purification pipe is opened, water will be flowed by first circulation pipe in the second purification pipe, and user can be with
By first purification pipe removed between first circulation pipe and second circulation pipe, change it is new, have easy to operate, user
Just the characteristics of, by being equipped with magnetic float liquidlevel meter and draining solenoid valve, in order to which magnetic float liquidlevel meter is monitored in liquid storage cylinder in real time
Liquid level, when the liquid level in liquid storage cylinder be higher than setting value when, controller control drain pipe on draining solenoid valve beat
It opens, extra water is flowed out by drain pipe, so as to prevent leading to not continue to recycle happening for condensed water because liquid storage cylinder is full of,
It ensure that the normal work of the present invention.
Description of the drawings
Fig. 1 is the overall structure diagram of the present invention.
Fig. 2 is the air collecting chamber cross-sectional view of the present invention.
In figure：1 air collecting chamber, 2 gas collecting tubes, 3 nozzles, 4 first pressures pump, 5 circulating electromagnetic valves, 6 first purification pipes, 7 second
Purify pipe, 8 water-purifying cavities, 9 adsorption filtration chambers, 10 deep layer purify cavities, 11 second circulation pipes, 12 liquid storage cylinders, 13 magnetic float liquidlevel meters,
14 third circulation pipes, 15 second pressures pump, 16 controllers, 17 drain pipes, 18 draining solenoid valves, 19 first circulation pipes.
Specific embodiment
Below in conjunction with the attached drawing in the embodiment of the present invention, the technical solution in the embodiment of the present invention is carried out clear, complete
Site preparation describes, it is clear that described embodiment is only part of the embodiment of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, those of ordinary skill in the art are obtained every other without making creative work
Embodiment shall fall within the protection scope of the present invention.
It is described including air collecting chamber 1 and liquid storage cylinder 12 the present invention provides a kind of condensate recycling device as shown in Figs. 1-2
Liquid storage cylinder 12 is set on 1 side of air collecting chamber, and 1 both sides of air collecting chamber are equipped with gas collecting tube 2, and the air collecting chamber 1 is internally provided with nozzle
3, for spraying water, 1 bottom of air collecting chamber is equipped with first pressure and pumps 4, and the first pressure pumps 4 sides and is equipped with first circulation pipe
19,19 side of first circulation pipe is equipped with the first purification pipe 6 and second and purifies pipe 7, and it is net that the second purification pipe 7 is set on first
Change 6 bottom of pipe, the first purification pipe 6 and second purifies is equipped with circulating electromagnetic valve 5 and water-purifying cavity 8 on pipe 7, and water-purifying cavity 8 is used
In the purification to water, the water-purifying cavity 8 is set on 5 side of circulating electromagnetic valve, the water-purifying cavity 8 be internally provided with adsorption filtration chamber 9 with
Deep layer purify cavity 10, the end that the first purification pipe 6 and second purifies pipe 7 are equipped with second circulation pipe 11, the second circulation
Pipe 11 is through 12 top of liquid storage cylinder and extends to inside liquid storage cylinder 12, and the liquid storage cylinder 12 is internally provided with magnetic float liquidlevel meter 13,
For detecting liquid level, 13 side of magnetic float liquidlevel meter is equipped with third circulation pipe 14, is set on the third circulation pipe 14
There is second pressure to pump 15, the second pressure pumps 15 sides and is equipped with controller 16, and 12 side of liquid storage cylinder is equipped with drain pipe 17,
The drain pipe 17 is equipped with draining solenoid valve 18.
There are two the adsorption filtration chamber 9 and deep layer purify cavity 10 are all provided with, described two adsorption filtration chambers 9 and two deep layers
Purify cavity 10 is respectively arranged on the first purification pipe 6 and the second purification pipe 7, in order to when the adsorption filtration chamber 9 on the first purification pipe 6
With deep layer purify cavity 10 after using for a longer period, clean-up effect will reduce, and close the cycle electromagnetism on the first purification pipe 6 at this time
Valve 5, opens the circulating electromagnetic valve 5 on the second purification pipe 7, and water will be flowed into the second purification pipe 7 by first circulation pipe 19, be made
User can remove the first purification pipe 6 between first circulation pipe 19 and second circulation pipe 11, change new, the depth
Layer purify cavity 10 is set on 9 side of adsorption filtration chamber, and filled with activated carbon, activated carbon has relatively strong for 9 inside of adsorption filtration chamber
Suction-operated, can effectively remove the impurity in water, the deep layer purify cavity 10 is internally provided with reverse osmosis membrane, reverse osmosis membrane
Membrane aperture is very small, thus can effectively go water removal in dissolved salts, colloid, microorganism and organic matter, have consume energy it is low,
The advantages that pollution-free, simple for process, easy to operate, 13 model of magnetic float liquidlevel meter are set as UHZ-25, the cycle electricity
Magnet valve 5, magnetic float liquidlevel meter 13 and draining solenoid valve 18 are electrically connected with controller 16, in order to which magnetic float liquidlevel meter 13 is real
When monitoring liquid storage cylinder 12 in liquid level, when the liquid level in liquid storage cylinder 12 be higher than setting value when, controller 16 control row
Draining solenoid valve 18 in liquid pipe 17 is opened, and extra water is flowed out by drain pipe 17, and the third circulation pipe 14 runs through air collecting chamber 1
Top simultaneously extends to the inside of air collecting chamber 1 and is connect with nozzle 3, in order to which second pressure pumps 15 by third circulation pipe 14 by liquid storage cylinder
Water pump in 12 is to nozzle 3, and the gas collecting tube 2 is obliquely installed in 1 both sides of air collecting chamber, and water vapour enters air collecting chamber 1 by gas collecting tube 2
In, the gas collecting tube 2 being obliquely installed can cause water vapour spiral to move upwards, it is described first purification pipe 6 and second purify pipe 7 with
First circulation pipe 19 is detachably connected by screw thread, and it is logical with second circulation pipe 11 that the first purification pipe 6 and second purifies pipe 7
It crosses screw thread to be detachably connected, be convenient for dismantling and install.
Operation principle of the present invention：During work, water vapour is entered by gas collecting tube 2 in air collecting chamber 1, the gas collecting tube 2 being obliquely installed
Water vapour spiral can be caused to move upwards, second pressure pump 15 is by third circulation pipe 14 by the water pump in liquid storage cylinder 12 to nozzle
3, water is trickled down by nozzle 3, and water vapour is liquefied and is pumped in first circulation pipe 19 by first pressure pump 4, on the second purification pipe 7
Circulating electromagnetic valve 5 it is flat when be closed, water cannot be introduced into the second purification pipe 7, the circulating electromagnetic valve on the first purification pipe 6
5 be in opening, water by first purification pipe 6 enter first purification pipe 6 on water-purifying cavity 8 inside adsorption filtration chamber 9 and deeply
In layer purify cavity 10, activated carbon in adsorption filtration chamber 9 carries out water adsorption filtration, the reverse osmosis membrane pair in deep layer purify cavity 10
Water carries out deep layer purification, and treated water is flowed by second circulation pipe 11 in liquid storage cylinder 12, and magnetic float liquidlevel meter 13 is supervised in real time
The liquid level in liquid storage cylinder 12 is surveyed, when the liquid level in liquid storage cylinder 12 is higher than setting value, controller 16 controls drain pipe
Draining solenoid valve 18 on 17 is opened, and extra water is flowed out by drain pipe 17,9 He of adsorption filtration chamber on the first purification pipe 6
After using for a longer period, clean-up effect will reduce deep layer purify cavity 10, close the circulating electromagnetic valve on the first purification pipe 6 at this time
5, the circulating electromagnetic valve 5 on the second purification pipe 7 is opened, will be flowed by first circulation pipe 19 in second purification pipe 7, user
First purification pipe 6 between first circulation pipe 19 and second circulation pipe 11 can be removed, changed new.
Finally it should be noted that：The foregoing is only a preferred embodiment of the present invention, is not intended to restrict the invention,
Although the present invention is described in detail referring to the foregoing embodiments, for those skilled in the art, still may be used
To modify to the technical solution recorded in foregoing embodiments or carry out equivalent replacement to which part technical characteristic,
All within the spirits and principles of the present invention, any modification, equivalent replacement, improvement and so on should be included in the present invention's
Within protection domain.
Claims (8)
1. a kind of condensate recycling device, including air collecting chamber（1）And liquid storage cylinder（12）, it is characterised in that：The liquid storage cylinder（12）If
In air collecting chamber（1）Side, the air collecting chamber（1）Both sides are equipped with gas collecting tube（2）, the air collecting chamber（1）It is internally provided with nozzle
（3）, the air collecting chamber（1）Bottom is pumped equipped with first pressure（4）, the first pressure pump（4）Side is equipped with first circulation pipe
（19）, the first circulation pipe（19）Side is equipped with the first purification and manages（6）It is managed with the second purification（7）, the second purification pipe（7）
Set on the first purification pipe（6）Bottom, the first purification pipe（6）It is managed with the second purification（7）On be equipped with circulating electromagnetic valve（5）With
Water-purifying cavity（8）, the water-purifying cavity（8）Set on circulating electromagnetic valve（5）Side, the water-purifying cavity（8）It is internally provided with adsorption filtration chamber
（9）With deep layer purify cavity（10）, the first purification pipe（6）It is managed with the second purification（7）End be equipped with second circulation pipe（11）,
The second circulation pipe（11）Through liquid storage cylinder（12）Top simultaneously extends to liquid storage cylinder（12）Inside, the liquid storage cylinder（12）It is internal
Equipped with magnetic float liquidlevel meter（13）, the magnetic float liquidlevel meter（13）Side is equipped with third circulation pipe（14）, the third cycle
Pipe（14）Second pressure is equipped with to pump（15）, the second pressure pump（15）Side is equipped with controller（16）, the liquid storage cylinder
（12）Side is equipped with drain pipe（17）, the drain pipe（17）It is equipped with draining solenoid valve（18）.
2. a kind of condensate recycling device according to claim 1, it is characterised in that：The adsorption filtration chamber（9）With deep layer
Purify cavity（10）There are two being all provided with, described two adsorption filtration chambers（9）With two deep layer purify cavities（10）It is net to be respectively arranged on first
Change pipe（6）It is managed with the second purification（7）On, the deep layer purify cavity（10）Set on adsorption filtration chamber（9）Side.
3. a kind of condensate recycling device according to claim 1, it is characterised in that：The adsorption filtration chamber（9）Inside is filled out
Filled with activated carbon, the deep layer purify cavity（10）It is internally provided with reverse osmosis membrane.
4. a kind of condensate recycling device according to claim 1, it is characterised in that：The magnetic float liquidlevel meter（13）Model
It is set as UHZ-25.
5. a kind of condensate recycling device according to claim 1, it is characterised in that：The circulating electromagnetic valve（5）, magnetic float
Liquid level gauge（13）And draining solenoid valve（18）And controller（16）It is electrically connected.
6. a kind of condensate recycling device according to claim 1, it is characterised in that：The third circulation pipe（14）Through collection
Air cavity（1）Top simultaneously extends to air collecting chamber（1）Internal and nozzle（3）Connection.
7. a kind of condensate recycling device according to claim 1, it is characterised in that：The gas collecting tube（2）Be obliquely installed in
Air collecting chamber（1）Both sides.
8. a kind of condensate recycling device according to claim 1, it is characterised in that：The first purification pipe（6）With second
Purification pipe（7）With first circulation pipe（19）It is detachably connected by screw thread, the first purification pipe（6）With the second purification pipe
（7）With second circulation pipe（11）It is detachably connected by screw thread.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711469709.6A CN108168329A (en) | 2017-12-29 | 2017-12-29 | A kind of condensate recycling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711469709.6A CN108168329A (en) | 2017-12-29 | 2017-12-29 | A kind of condensate recycling device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108168329A true CN108168329A (en) | 2018-06-15 |
Family
ID=62519838
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711469709.6A Pending CN108168329A (en) | 2017-12-29 | 2017-12-29 | A kind of condensate recycling device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108168329A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112082224A (en) * | 2020-09-21 | 2020-12-15 | 谢亚凤 | Negative ion air purifier |
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| CN1935675A (en) * | 2006-09-05 | 2007-03-28 | 葫芦岛北方膜技术工业有限公司 | Drinking water emergency purifying process and its apparatus |
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| CN101825360A (en) * | 2010-05-10 | 2010-09-08 | 贵阳铝镁设计研究院 | Method and device for recycling high-pressure dissolved steam exhaust of diluting tank in alumina production |
| CN203274539U (en) * | 2013-02-21 | 2013-11-06 | 山东中德设备有限公司 | Movable waste heat steam recycling device |
| CN204365069U (en) * | 2014-12-19 | 2015-06-03 | 辽宁华孚环境工程股份有限公司 | Oily sludge pyrolysis air-breathing gas condenser |
-
2017
- 2017-12-29 CN CN201711469709.6A patent/CN108168329A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3022985A (en) * | 1958-06-06 | 1962-02-27 | Chicago Bridge & Iron Co | Silencer and heat recovery system |
| CN1045174A (en) * | 1990-03-22 | 1990-09-05 | 魏仕英 | Jet-type mixing condenser |
| CN1935675A (en) * | 2006-09-05 | 2007-03-28 | 葫芦岛北方膜技术工业有限公司 | Drinking water emergency purifying process and its apparatus |
| CN201110536Y (en) * | 2007-09-24 | 2008-09-03 | 广州德上能源技术有限公司 | Flue gas waste heat recovery energy-saving system |
| CN201470220U (en) * | 2009-08-25 | 2010-05-19 | 南宁市维威制药有限公司 | Tap water chloridion removing device |
| CN101825360A (en) * | 2010-05-10 | 2010-09-08 | 贵阳铝镁设计研究院 | Method and device for recycling high-pressure dissolved steam exhaust of diluting tank in alumina production |
| CN203274539U (en) * | 2013-02-21 | 2013-11-06 | 山东中德设备有限公司 | Movable waste heat steam recycling device |
| CN204365069U (en) * | 2014-12-19 | 2015-06-03 | 辽宁华孚环境工程股份有限公司 | Oily sludge pyrolysis air-breathing gas condenser |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112082224A (en) * | 2020-09-21 | 2020-12-15 | 谢亚凤 | Negative ion air purifier |
| CN112082224B (en) * | 2020-09-21 | 2021-11-26 | 淮北雷德机电科技有限公司 | Negative ion air purifier |
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| PB01 | Publication | ||
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| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180615 |
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| RJ01 | Rejection of invention patent application after publication |