CN106799062A - Water vapor condensation system - Google Patents
Water vapor condensation system Download PDFInfo
- Publication number
- CN106799062A CN106799062A CN201611171670.5A CN201611171670A CN106799062A CN 106799062 A CN106799062 A CN 106799062A CN 201611171670 A CN201611171670 A CN 201611171670A CN 106799062 A CN106799062 A CN 106799062A
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- China
- Prior art keywords
- heat exchanger
- chamber
- air
- water vapor
- water
- Prior art date
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0003—Condensation of vapours; Recovering volatile solvents by condensation by using heat-exchange surfaces for indirect contact between gases or vapours and the cooling medium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0003—Condensation of vapours; Recovering volatile solvents by condensation by using heat-exchange surfaces for indirect contact between gases or vapours and the cooling medium
- B01D5/0015—Plates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0078—Condensation of vapours; Recovering volatile solvents by condensation characterised by auxiliary systems or arrangements
- B01D5/009—Collecting, removing and/or treatment of the condensate
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- E—FIXED CONSTRUCTIONS
- E03—WATER SUPPLY; SEWERAGE
- E03B—INSTALLATIONS OR METHODS FOR OBTAINING, COLLECTING, OR DISTRIBUTING WATER
- E03B3/00—Methods or installations for obtaining or collecting drinking water or tap water
- E03B3/28—Methods or installations for obtaining or collecting drinking water or tap water from humid air
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/05—Compression system with heat exchange between particular parts of the system
Abstract
The present invention relates to Refrigeration Technique, a kind of water vapor condensation system is provided, including compressor and condenser, the high-pressure outlet of the compressor is connected with the entrance of the condenser, the low pressure inlet that the outlet of the condenser passes through compressor described in pipeline communication, the restricting element of series connection is provided with the pipeline, also include condensing trapping heat exchanger and blower fan, the condensing trapping heat exchanger includes the housing with chamber, air intlet and air outlet slit are provided with the top of the chamber, the bottom of the chamber is provided with condensed water row's mouth, the gas outlet of the blower fan connects with the air intlet, and the pipeline runs through the chamber.In the present invention, compressor, condenser and restricting element form cooling assembly, such that it is able to will blast the solid ice that the humid air in chamber is separated into the dry air of gas phase, the aqueous water of liquid phase or solid phase, can realize to humid air reclaimed water.
Description
Technical field
The present invention relates to Refrigeration Technique, more particularly to a kind of water vapor condensation system.
Background technology
With the expansion of economic fast-developing and population, the mankind are added to the irrational utilization of water resource, many areas
All occur in that the problem of scarcity of fresh water resources.The freshwater resources that China can the develop per capita about world per capita water 1/4,
Belong to the big country of serious water shortage, and water pollution situation is serious, more exacerbates the shortage of water resource.
Current China takes the measures such as water saving, " south water to north " and sea, buck desalination to improve serious water shortage present situation, but
The water-saving consciousness of the common people has much room for improvement, and " south water to north " engineering and desalinization labor intensive material resources are huge, and cost is very high.
The vapor enriched containing quantity among air, it is the important means for alleviating shortage of water resources to extract the moisture in air.Its master
It is that the moisture in humid air is down to below dew-point temperature using refrigeration system to want principle, and part vapor is changing to condensate
And separate out.
Patent CN102733451A propose it is a kind of collect atmospheric water system, by compressor, condenser, expansion valve and
Capillary device, evaporator, bypass four-way valve current divider, at least one bypass valve, white sensor, controller and collection vessel group
Into cardinal principle is that will heat generation drinking water after moisture cooling frosting in humid air.But the system does not make full use of
The energy of cold air and condensed water is dried, the efficiency of trapping moisture has much room for improvement, extremely low for air humidity dries desert ground
Area is difficult to be applicable.
The content of the invention
It is an object of the invention to provide a kind of water vapor condensation system, it is intended to for solving catching for existing condenser system
The relatively low problem of water collection efficiency.
What the present invention was realized in：
The embodiment of the present invention provides a kind of water vapor condensation system, including compressor and condenser, the height of the compressor
Extrude mouth to be connected with the entrance of the condenser, the outlet of the condenser is entered by the low pressure of compressor described in pipeline communication
Mouthful, the restricting element of series connection is provided with the pipeline, also including condensing trapping heat exchanger and blower fan, the condensing trapping is changed
Hot device includes the housing with chamber, and air intlet and air outlet slit, the bottom of the chamber are provided with the top of the chamber
Portion is provided with condensed water row's mouth, and the gas outlet of the blower fan connects with the air intlet, and the pipeline runs through the chamber.
Further, the condensing trapping heat exchanger also includes the condensation silk screen being horizontally placed in the chamber, institute
State and condensation water collection portion is formed between condensation silk screen and the bottom surface of the chamber.
Further, the condensing trapping heat exchanger also includes the heat exchanger plates being vertically arranged, and the heat exchanger plates are by the chamber
The top of room extends to the condensation silk screen, and the air intlet is with the air outlet slit respectively positioned at the two of the heat exchanger plates
Side.
Further, the pipeline has the side of the air intlet through the chamber vertically.
Further, the pipe level runs through the chamber, and the pipeline is located at the lower section of the condensation silk screen.
Further, also including the first Recuperative heat exchanger, the refrigerant inlet connection of first Recuperative heat exchanger is described
The outlet of condenser, the refrigerant outlet of first Recuperative heat exchanger connects the import of the restricting element.
Further, air outlet slit described in the heat exchanger tube inlet communication of first Recuperative heat exchanger.
Further, condensed water row mouth described in the heat exchanger tube inlet communication of first Recuperative heat exchanger.
Further, also including the second Recuperative heat exchanger, the refrigerant inlet connection of second Recuperative heat exchanger is described
The refrigerant outlet of the first Recuperative heat exchanger, the refrigerant outlet of second Recuperative heat exchanger connects the restricting element and enters
Mouthful, air outlet slit described in the heat exchanger tube inlet communication of first Recuperative heat exchanger, the heat exchanger tube of second Recuperative heat exchanger
Condensed water row mouth described in inlet communication；Or condensed water row mouth described in the heat exchanger tube inlet communication of first Recuperative heat exchanger,
Air outlet slit described in the heat exchanger tube inlet communication of second Recuperative heat exchanger.
Further, the lower end of the chamber is gradually-reducing shape structure, and the condensed water row mouth is located at the gradually-reducing shape structure
Necking at.
The invention has the advantages that：
In condenser system of the invention, compressor, condenser and restricting element cooperatively form refrigeration system, can cause
The reduction of pipeline inner refrigerant temperature, after be pumped into extraneous air in chamber by blower fan, air connects with the pipeline of chamber interior point
Touch, the vapor contained in air can be rapidly condensed into aqueous water or solid ice, while the air after heat exchange is dried,
Dried air can discharge chamber by air outlet slit, in can realizing rapid acquiring humid air by condensing trapping heat exchanger
Moisture, arresting efficiency is higher.
Brief description of the drawings
In order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
The accompanying drawing to be used needed for having technology description is briefly described, it should be apparent that, drawings in the following description are only this
Some embodiments of invention, for those of ordinary skill in the art, on the premise of not paying creative work, can be with
Other accompanying drawings are obtained according to these accompanying drawings.
Fig. 1 is the structural representation of water vapor condensation system provided in an embodiment of the present invention；
Fig. 2 is the structural representation of the condensing trapping heat exchanger of the water vapor condensation system of Fig. 1；
Fig. 3 is the horizontally disposed structural representation of conduit of the condensing trapping heat exchanger of the water vapor condensation system of Fig. 1；
Fig. 4 uses dry air as the knot of heat transferring medium for the first Recuperative heat exchanger of the water vapor condensation system of Fig. 1
Structure schematic diagram；
Fig. 5 uses aqueous water as the structure of heat transferring medium for the first Recuperative heat exchanger of the water vapor condensation system of Fig. 1
Schematic diagram.
Specific embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is all other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
Referring to Fig. 1 and Fig. 2, the embodiment of the present invention provides a kind of water vapor condensation system, including compressor 1 and condenser
2, the high-pressure outlet of compressor 1 is connected with the entrance of condenser 2, and the outlet of condenser 2 passes through the low pressure of pipeline communication compressor 1
Import, and the restricting element 3 of series connection is provided with the pipeline, compressor 1, condenser 2 and the shape of restricting element 3 are passed through to this
Into cooling assembly, the stream internal circulation flow that refrigerant is formed in three, condenser system also includes condensing trapping heat exchanger 4
And blower fan 5, condensing trapping heat exchanger 4 include with chamber 411 housing 41, the top of chamber 411 is provided with air and enters
Mouth 412 and air outlet slit 413, and its bottom is provided with condensed water row's mouth 414, gas outlet and the air intlet 412 of blower fan 5 connect
It is logical, and above-mentioned pipeline then runs through chamber 411, specifically, the portion of the low pressure inlet of pipeline connection restricting element 3 and compressor 1
Divide and run through chamber 411.In the present embodiment, compressor 1, condenser 2 and the three of restricting element 3 composition cooling assembly work as compression
When machine 1 works, the refrigerant temperature that restricting element 3 is exported between the low pressure inlet of compressor 1 in corresponding pipeline is relatively low, that is, pass through
The pipe temperature of the part of transluminal room 411 is relatively low, can be blasted in chamber 411 and and chamber extraneous humid air by blower fan 5
Pipeline in 411 is exchanged heat, and then causes that the humid air temperature in chamber 411 is relatively low, and the vapor in humid air is quick
It is condensed into aqueous water or solid ice is collected in the bottom of chamber 411, while forming dry air, dry air is in chamber 411
Interior automatic rising and can be discharged by air outlet slit 413, and the aqueous water collected in chamber 411 then can arrange the row of mouth 414 by condensed water
Go out.In the above-mentioned course of work, humid air can be separated into the dry air of gas phase, liquid phase in the condensing trapping heat exchanger 4
The solid ice of aqueous water or solid phase, can realize that, to the vapor trapping in humid air, arresting efficiency is higher.In addition, can
The lower end of the chamber 411 of condensing trapping heat exchanger 4 is set to gradually-reducing shape structure, condensed water row's mouth 414 is located at gradually-reducing shape structure
Necking at, it can facilitate and for the aqueous water of trapping in chamber 411 to be completely exhausted out housing 41, and drainage effect is very good.
Referring to Fig. 2 and Fig. 3, optimize above-described embodiment, condensing trapping heat exchanger 4 also includes condensation silk screen 42, condensation
Silk screen 42 is horizontally placed in chamber 411, and condensation water collection portion is formed between condensation silk screen 42 and the bottom surface of chamber 411.This reality
Apply in example, being horizontally disposed near the position of bottom in chamber 411 has condensation silk screen 42, and it can be made of metal material, when
When compressor 1 works, acted on by the heat exchange of pipeline inner refrigerant and cause that the temperature of condensation silk screen 42 is relatively low, roused by blower fan 5
Enter the humid air in chamber 411 first to be exchanged heat with the cold air in chamber 411, then continue to exchange heat with condensation silk screen 42, that is, pass through
Condensation silk screen 42 can further trap the aqueous vapor in humid air, after improving the arresting efficiency of condensing trapping heat exchanger 4, and condensation
Aqueous water slid in condensation water collection portion by condensation silk screen 42, then by condensed water row mouth 414 discharge.
Referring to Fig. 1 and Fig. 3, continue to optimize above-described embodiment, condensing trapping heat exchanger 4 also includes the heat exchange being vertically arranged
Plate 43, heat exchanger plates 43 are extended from the top of chamber 411 to condensation silk screen 42, and air intlet 412 is located at respectively with air outlet slit 413
The both sides of heat exchanger plates 43.In the present embodiment, heat exchanger plates 43 are divided into two portions by the condensation upper space of silk screen 42 is located in chamber 411
Point, air intlet 412 and air outlet slit 413 corresponding the two segment spaces respectively, humid air first enter it through air intlet 412
Exchanged heat in middle a part of space, the dry air after vapor separation then bypasses heat exchanger plates 43 and enters in another part space
And discharged by air outlet slit 413.In above process, humid air is separated with dry air by heat exchanger plates 43, can be with
It is prevented effectively from humid air to mix with dry air, reduces the arresting efficiency of condensing trapping heat exchanger 4, while passes through the heat exchanger plates
43, the humid air and dry air that can cause the both sides of heat exchanger plates 43 carry out heat exchange, i.e., because dry air is changed by humid air
Formed after heat drop temperature, temperature is far below the humid air entered in chamber 411 by air intlet 412, to this changing in heat exchanger plates 43
Under heat effect, can by dry air can to enter humid air carry out precooling, the humid air after precooling again with refrigeration train
Part carries out heat exchange, and continuing to lower the temperature separates out vapor, further strengthens the arresting efficiency of condensing trapping heat exchanger 4.For this
The condensing trapping heat exchanger 4 of structure, can have various arrangements through the pipeline of chamber 411, such as pipeline is by side vertically
To through chamber 411, and the pipeline is located in the corresponding segment space of air intlet 412, and the flow direction of pipeline inner refrigerant is perpendicular
It is straight upward, and in the presence of blower fan 5, humid air is moved straight down in chamber 411, and this is freezed in the segment space
Agent forms counter-flow arrangement with humid air, and heat transfer effect is very good, and in this configuration, heat exchanger plates 43 extend to condensation silk screen 42
Upper surface, and there is gap between the two, the dry air after heat exchange is empty by the gap 413 corresponding parts of air inlet outlet
It is interior；And in another arrangement, pipe level can be run through chamber 411, and it is located at the lower section of condensation silk screen 42,
Refrigerant in pipeline flows along the direction of air intlet 412 to air outlet slit 413, and certain pipeline should be located at condensation water collection portion
The water surface top of interior aqueous water, in this configuration, the lower end of heat exchanger plates 43 extends to upper surface and the contact of condensation silk screen 42,
Condensation silk screen 42 is needed guiding through to this humid air to enter in condensation water collection portion, and again passes through condensation silk after being exchanged heat with pipeline
The air inlet of net 42 exports 413 corresponding segment spaces, and in this fashion, humid air transfer path is more long, and condensing trapping is changed
The trapping effect of hot device 4 is also very good.
Referring to Fig. 4 and Fig. 5, further, condenser system also includes the first Recuperative heat exchanger 6, the heat exchange of the first backheat
The refrigerant inlet of device 6 connects the outlet of condenser 2, and the refrigerant outlet of the first Recuperative heat exchanger 6 connects entering for restricting element 3
Mouthful.In the present embodiment, the first Recuperative heat exchanger 6 is had additional in cooling assembly, and the first Recuperative heat exchanger 6 is series at condenser
On stream between 2 and restricting element 3, the first Recuperative heat exchanger 6 is mainly used for carrying out at supercooling the refrigerant before throttling
Reason so that the refrigerant entered in the chamber 411 of condensing trapping heat exchanger 4 is lower, and condensing trapping heat exchanger 4 steams to humid air reclaimed water
The arresting efficiency of gas is higher.Low-temperature receiver for the first Recuperative heat exchanger 6 can use various ways, such as the first Recuperative heat exchanger
Dry air after the air outlet slit 413 of 6 heat exchanger tube inlet communication chamber 411, i.e. vapor are captured is discharging chamber 411
Enter afterwards in the heat exchanger tube of the first Recuperative heat exchanger 6, the heat transferring medium of the first Recuperative heat exchanger 6 is dry air, due to wet sky
Gas carries out heat exchange in the chamber 411, then the drying air temperature discharged by air outlet slit 413 is also very low, and temperature is relatively low
Dry air carries out heat exchange again in the heat exchanger tube of the first Recuperative heat exchanger 6 with refrigerant, is formed to refrigerant before throttling
Cross cold treatment；In a further mode of operation, heat exchanger tube inlet communication condensed water row's mouth 414 of the first Recuperative heat exchanger 6, that is, condense
The aqueous water of the trapping trapping of heat exchanger 4 enters in the heat exchanger tube of the first Recuperative heat exchanger 6, and the heat exchange of the first Recuperative heat exchanger 6 is situated between
Matter is aqueous water, and because the liquid coolant-temperature gage for trapping is very low, then the aqueous water can also form the mistake to refrigerant before throttling
Cold treatment.In two kinds of above-mentioned implementation methods, by the dry air or aqueous water pair that are produced in condensing trapping heat exchanger 4
Refrigerant before throttling carries out precooling, can not only obtain water vapor condensation efficiency higher, and realizes cold energy is returned
Receive and utilize.
Fig. 4 and Fig. 5 is referred again to, further, condenser system also includes the second Recuperative heat exchanger and (do not show in figure
Go out), the refrigerant inlet of the second Recuperative heat exchanger connects the refrigerant outlet of the first Recuperative heat exchanger 6, the second Recuperative heat exchanger
Refrigerant outlet connect restricting element 3 import, i.e., on the basis of above-mentioned first Recuperative heat exchanger 6, condenser 2 with throttling
The second Recuperative heat exchanger is also in series with refrigerant flow path between element 3, refrigerant is successively through the first Recuperative heat exchanger 6 and
Two Recuperative heat exchangers pass through restricting element 3, and the refrigerant before this throttling is exchanged heat by the first Recuperative heat exchanger 6 and the second backheat
Device forms two-stage and crosses cold treatment, can further strengthen the water vapor condensation efficiency of condensing trapping heat exchanger 4.And for first time
The low-temperature receiver of the Recuperative heat exchanger of heat exchanger 6 and second is using the dry air or liquid produced in condensing trapping heat exchanger 4
The air outlet slit 413 of the heat exchanger tube inlet communication chamber 411 of water, such as the first Recuperative heat exchanger 6, the second Recuperative heat exchanger is changed
Heat pipe inlet communication chamber 411 condensed water row mouth 414, or the first Recuperative heat exchanger 6 heat exchanger tube inlet communication condensed water
Row's mouth 414, the heat exchanger tube inlet communication air outlet slit 413 of the second Recuperative heat exchanger, i.e. the first Recuperative heat exchanger 6 are empty using drying
Used as heat transferring medium, the second Recuperative heat exchanger uses aqueous water as heat transferring medium to gas, or the first Recuperative heat exchanger 6 uses liquid
, used as heat transferring medium, the second Recuperative heat exchanger is using dry air as heat transferring medium, and the utilization rate of cold energy is very high for state water.When
So in this configuration, the outlet of the heat exchanger tube of the first Recuperative heat exchanger 6 and the outlet of the heat exchanger tube of the second Recuperative heat exchanger
Connect extraneous.
Presently preferred embodiments of the present invention is the foregoing is only, is not intended to limit the invention, it is all in essence of the invention
Within god and principle, any modification, equivalent substitution and improvements made etc. should be included within the scope of the present invention.
Claims (10)
1. a kind of water vapor condensation system, including compressor and condenser, the high-pressure outlet of the compressor and the condenser
Entrance connection, the outlet of the condenser is provided with by the low pressure inlet of compressor described in pipeline communication on the pipeline
The restricting element of series connection, it is characterised in that：Also include condensing trapping heat exchanger and blower fan, the condensing trapping heat exchanger includes
Housing with chamber, is provided with air intlet and air outlet slit at the top of the chamber, and the bottom of the chamber is provided with
Condensed water arranges mouth, and the gas outlet of the blower fan connects with the air intlet, and the pipeline runs through the chamber.
2. water vapor condensation system as claimed in claim 1, it is characterised in that：The condensing trapping heat exchanger also includes water
The flat condensation silk screen being arranged in the chamber, condensation water collection is formed between the condensation silk screen and the bottom surface of the chamber
Portion.
3. water vapor condensation system as claimed in claim 2, it is characterised in that：It is vertical that the condensing trapping heat exchanger also includes
The heat exchanger plates of setting, the heat exchanger plates from the top of the chamber to it is described condensation silk screen extend, the air intlet with it is described
Air outlet slit is respectively positioned at the both sides of the heat exchanger plates.
4. water vapor condensation system as claimed in claim 3, it is characterised in that：The pipeline has through the chamber vertically
The side of the air intlet.
5. water vapor condensation system as claimed in claim 3, it is characterised in that：The pipe level runs through the chamber, and
The pipeline is located at the lower section of the condensation silk screen.
6. the water vapor condensation system as described in claim any one of 1-5, it is characterised in that：Also exchanged heat including the first backheat
Device, the refrigerant inlet of first Recuperative heat exchanger connects the outlet of the condenser, the system of first Recuperative heat exchanger
The import of restricting element described in cryogen outlet.
7. water vapor condensation system as claimed in claim 6, it is characterised in that：The heat exchanger tube of first Recuperative heat exchanger enters
The mouth connection air outlet slit.
8. water vapor condensation system as claimed in claim 6, it is characterised in that：The heat exchanger tube of first Recuperative heat exchanger enters
The mouth connection condensed water row mouth.
9. water vapor condensation system as claimed in claim 6, it is characterised in that：Also include the second Recuperative heat exchanger, described the
The refrigerant inlet of two Recuperative heat exchangers connects the refrigerant outlet of first Recuperative heat exchanger, second Recuperative heat exchanger
Refrigerant outlet connect the restricting element import, air described in the heat exchanger tube inlet communication of first Recuperative heat exchanger goes out
Mouthful, condensed water row mouth described in the heat exchanger tube inlet communication of second Recuperative heat exchanger；Or first Recuperative heat exchanger
Condensed water row mouth, air outlet slit described in the heat exchanger tube inlet communication of second Recuperative heat exchanger described in heat exchanger tube inlet communication.
10. water vapor condensation system as claimed in claim 1, it is characterised in that：The lower end of the chamber is gradually-reducing shape structure,
The condensed water row mouth is located at the necking of the gradually-reducing shape structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611171670.5A CN106799062B (en) | 2016-12-17 | 2016-12-17 | Vapor condenser system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611171670.5A CN106799062B (en) | 2016-12-17 | 2016-12-17 | Vapor condenser system |
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| Publication Number | Publication Date |
|---|---|
| CN106799062A true CN106799062A (en) | 2017-06-06 |
| CN106799062B CN106799062B (en) | 2019-05-28 |
Family
ID=58984545
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611171670.5A Active CN106799062B (en) | 2016-12-17 | 2016-12-17 | Vapor condenser system |
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| Country | Link |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109331494A (en) * | 2018-09-12 | 2019-02-15 | 杭州轩辉环境设备有限公司 | A kind of effluent purifying system and purification method |
| CN111365875A (en) * | 2020-05-26 | 2020-07-03 | 华东交通大学 | Pharmaceutical factory sewage source mechanical refrigeration cold-trap system |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1999043990A1 (en) * | 1998-02-27 | 1999-09-02 | Watermaster Technologies Limited | Water making apparatus |
| CN203160322U (en) * | 2013-04-02 | 2013-08-28 | 苏州必信空调有限公司 | Device for fetching water from air |
| CN204703227U (en) * | 2015-04-16 | 2015-10-14 | 北京星达科技发展有限公司广东分公司 | Captation |
| CN205742354U (en) * | 2016-05-12 | 2016-11-30 | 张萍 | A kind of intelligent high-efficiency air water machine |
-
2016
- 2016-12-17 CN CN201611171670.5A patent/CN106799062B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1999043990A1 (en) * | 1998-02-27 | 1999-09-02 | Watermaster Technologies Limited | Water making apparatus |
| CN203160322U (en) * | 2013-04-02 | 2013-08-28 | 苏州必信空调有限公司 | Device for fetching water from air |
| CN204703227U (en) * | 2015-04-16 | 2015-10-14 | 北京星达科技发展有限公司广东分公司 | Captation |
| CN205742354U (en) * | 2016-05-12 | 2016-11-30 | 张萍 | A kind of intelligent high-efficiency air water machine |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109331494A (en) * | 2018-09-12 | 2019-02-15 | 杭州轩辉环境设备有限公司 | A kind of effluent purifying system and purification method |
| CN111365875A (en) * | 2020-05-26 | 2020-07-03 | 华东交通大学 | Pharmaceutical factory sewage source mechanical refrigeration cold-trap system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106799062B (en) | 2019-05-28 |
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