CN102430257B - Steam condenser - Google Patents
Steam condenser Download PDFInfo
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- CN102430257B CN102430257B CN 201110275510 CN201110275510A CN102430257B CN 102430257 B CN102430257 B CN 102430257B CN 201110275510 CN201110275510 CN 201110275510 CN 201110275510 A CN201110275510 A CN 201110275510A CN 102430257 B CN102430257 B CN 102430257B
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Abstract
The invention discloses a steam condenser which comprises a steam inlet unit, a normal temperature air inlet unit, a plate-type heat exchanger, a water-collecting tray, a water outlet, an electric control cabin and a housing of the condenser, wherein, the steam inlet unit comprises a steam pipeline, a steam indrawing fan and a steam separator, the normal temperature air inlet unit comprises a normal temperature air pipeline, a condensation fan and an air side inlet air filter screen, and the plate-type heat exchanger comprises a steam inlet end, a dry air outlet end and a second water outlet. According to the invention, steam firstly passes through the steam separator and then flows to the plate-type heat exchanger; the central part of the plate-type heat exchanger is multipath branched plate-shaped sub-pipelines which are parallelly arranged at intervals; normal temperature air in the normal temperature air pipeline passes through gaps among the plate-shaped sub-pipelines at the central part of the plate-type heat exchanger so as to realize heat exchange, high temperature steam is discharged after condensation, and condensed water is collected into the water-collecting tray. The invention has the following advantages: electric energy is saved by about 60% compared to the prior art; the steam condenser has the advantages of high stability and low maintenance cost.
Description
Technical field
The present invention relates to a kind of water vapour condenser, particularly a kind of energy-saving water stram condenser.
Background technology
In existing mechanical manufacturing enterprise, usually need in the purge chamber, clean various parts, can produce a large amount of water vapours during cleaning, if directly being emitted in the workshop, water vapour can increase air humidity, accelerate the equipment corrosion in the workshop, this just need handle the water vapour that the purge chamber ejects, and ejects after becoming dry air again.
Existing steam treatment device generally adopts the refrigeration compressor unit to come condensed steam, such water vapour condenser working process is condenser peripheral air process condenser normally, the liquid refrigerant of HTHP will be cooled to from the high temperature and high pressure gaseous refrigerant of compressor in the condenser, this liquid refrigerant is through the capillary step-down, cooling, become the low-temp low-pressure liquid refrigerant that is easy to evaporate, to evaporimeter, evaporate heat absorption, to cool off from the steam that cleaning machine sucks through inhaling the nebelwind machine, make its steam condense into water droplet and collect in the ponding dish outside the outflow machine, dry air enters indoor.This liquid refrigerant becomes gaseous state through the evaporation heat absorption, returns compressor, finishes kind of refrigeration cycle one time.Through continuous kind of refrigeration cycle steam is condensed.
This water vapour condenser, power consumption is big, and stabilization of equipment performance is low, the maintenance cost height.
Summary of the invention
The object of the invention provides a kind of water vapour condenser, to overcome the shortcoming that power consumption is big in the prior art, stabilization of equipment performance is low, maintenance cost is high.
For achieving the above object, the present invention is achieved through the following technical solutions:
A kind of water vapour condenser comprises steam inlet unit, gas at normal temperature air inlet unit, heat-exchangers of the plate type, water-collecting tray, discharge outlet, electric appliance control box and device housings, wherein:
The steam inlet unit comprises that jet chimney, steam suck blower fan and steam-water separator.The entrance point of jet chimney is communicated with the sealing of purge chamber's steam outlet place, be convenient to collect the water vapour that comes out from the purge chamber like this, and set gradually steam at the pipeline of the inlet end of jet chimney and suck blower fan and steam-water separator, the steam-water separator bottom is provided with first discharge outlet of passing the jet chimney wall, the water vapour that comes out from the purge chamber is come by the preliminary separation water outlet of steam-water separator earlier, is discharged to the water-collecting tray from first discharge outlet; The port of export of jet chimney connects the entrance point of heat-exchangers of the plate type, and the water vapour after steam-water separator separates flows into heat-exchangers of the plate type from the port of export of jet chimney, again behind heat-exchangers of the plate type discharged to atmosphere.
Gas at normal temperature air inlet unit comprises gas at normal temperature pipeline, condensation fan, air side air intake air filter screen.The entrance point of gas at normal temperature pipeline is met to atmosphere by the air admission hole of equipment both sides, and air side air intake air filter screen is installed; The port of export of gas at normal temperature pipeline is provided with condensation fan, meet to atmosphere the gas outlet of condensation fan, insert heat-exchangers of the plate type on the intermediate conduit of gas at normal temperature pipeline, after condensation fan starts like this, after gas at normal temperature in the outer atmosphere of equipment is filtered through air side air intake air filter screen, be inhaled in the gas at normal temperature pipeline, finally from the condensation fan device for transferring, form the gas at normal temperature circulation.
Heat-exchangers of the plate type comprises steam inlet end, the dry air port of export, second discharge outlet.The intermediate portion presents the tabular sub-pipeline parallel interval of multiple branches and arranges, heat exchange is carried out in the gap that the ducted gas at normal temperature of gas at normal temperature is passed between the tabular sub-pipeline of heat-exchangers of the plate type mid portion, the heat on tabular sub-pipeline surface is taken away, such heat exchange characteristics are that water vapour and the gas at normal temperature of high temperature do not mixed mutually, the water vapour of heat is met and to be condensed into water after cold in heat-exchangers of the plate type, dry air after the cooling is met to atmosphere from the dry air port of export and is discharged, the water that condenses is discharged from second discharge outlet, and the dry air that second discharge outlet is positioned at heat-exchangers of the plate type exports distolateral.
Water-collecting tray is positioned at the bottom of equipment, collects the water of first discharge outlet, the discharge of second discharge outlet.The bottom of water-collecting tray is provided with the 3rd discharge outlet, is used for the water of water-collecting tray is discharged.
Electric appliance control box is positioned at the side of equipment, by the electricity consumption device in lead connection and the control appliance.
The quantity of described heat-exchangers of the plate type can be a plurality of, a plurality of heat-exchangerss of the plate type can be together in series from beginning to end, has increased the path-length of water vapour in heat-exchangers of the plate type like this, more is conducive to the drying of water vapour.
Described electric appliance control box inside also is provided with anxious stop breaker, temperature controller, suddenly stop breaker and be used in emergency circumstances the control of opening circuit, control when temperature controller is too high for the equipment operation temperature specifically can be carried out program setting and control operation by the computer control panel in the electric appliance control box.
The beneficial effect of a kind of water vapour condenser of the present invention is: energy-conserving and environment-protective, reaching under the prerequisite of same condensation effect, and save electric energy about 60% than prior art; While stabilization of equipment performance height, maintenance cost is low.
Description of drawings
Fig. 1 is the Facad structure simplified schematic diagram of water vapour condenser of the present invention.
Fig. 2 is the side structure simplified schematic diagram of water vapour condenser of the present invention.
Wherein the symbol description of Fig. 1 to Fig. 2 is as follows:
11, jet chimney, 111, the jet chimney entrance point, 112, the jet chimney port of export, 12, steam sucks blower fan, 13, steam-water separator, 21, the gas at normal temperature pipeline, 211, the gas at normal temperature pipe head, 212, the gas at normal temperature pipe outlet, 22, condensation fan, 23, air filter screen, 3, heat-exchangers of the plate type, 31, the steam inlet end, 32, the dry air port of export, 4, water-collecting tray, 51, first discharge outlet, 52, second discharge outlet, 53, the 3rd discharge outlet, 6, electric appliance control box, 61, suddenly stop breaker, 62, temperature controller, 7, device housings, 8, the purge chamber, 91, water vapour, 92, gas at normal temperature.
The specific embodiment
As shown in Figure 1 and Figure 2, be Facad structure simplified schematic diagram and the side structure simplified schematic diagram of water vapour condenser of the present invention.
A kind of water vapour condenser comprises steam inlet unit, gas at normal temperature air inlet unit, heat-exchangers of the plate type 3, water-collecting tray 4, discharge outlet, electric appliance control box 6 and device housings 7, wherein:
The steam inlet unit comprises that jet chimney 11, steam suck blower fan 12 and steam-water separator 13.Jet chimney entrance point 111 is communicated with the sealing of 8 steam outlet places, purge chamber, be convenient to collect 8 water vapours that come out 91 from the purge chamber like this, and set gradually steam at the pipeline of 111 ones of jet chimney entrance points and suck blower fan 12 and steam-water separator 13, steam-water separator 13 bottoms are provided with first discharge outlet 51 of passing jet chimney 11 walls, 8 water vapours that come out 91 are come by steam-water separator 13 preliminary separation water outlets earlier from the purge chamber, are discharged to the water-collecting tray 4 from first discharge outlet 51; The jet chimney port of export 112 connects the steam inlet end 31 of heat-exchangerss of the plate type 3, and the water vapour 91 after steam-water separator 13 separates flows into heat-exchangerss of the plate type 3 from the jet chimney port of export 112, again behind heat-exchangers of the plate type 3 discharged to atmosphere.
Gas at normal temperature air inlet unit comprises gas at normal temperature pipeline 21, condensation fan 22, air side air intake air filter screen 23.Gas at normal temperature pipe head 211 is met to atmosphere by the air admission hole of equipment both sides, and air side air intake air filter screen 23 is installed; Gas at normal temperature pipe outlet 212 is provided with condensation fan 22, meet to atmosphere the gas outlet of condensation fan 22, insert heat-exchangers of the plate type 3 on the intermediate conduit of gas at normal temperature pipeline 21, after condensation fan 22 starts like this, after gas at normal temperature 92 in the outer atmosphere of equipment is filtered through air side air intake air filter screen 23, be inhaled in the gas at normal temperature pipeline 21, finally from condensation fan 22 device for transferring, form gas at normal temperature 92 circulations.
Heat-exchangers of the plate type 3 comprises steam inlet end 31, the dry air port of export 32, second discharge outlet 52.The intermediate portion presents the tabular sub-pipeline parallel interval of multiple branches and arranges, heat exchange is carried out in the gap that gas at normal temperature 92 in the gas at normal temperature pipeline 21 is passed between the tabular sub-pipeline of heat-exchangers of the plate type 3 mid portions, the heat on tabular sub-pipeline surface is taken away, such heat exchange characteristics are that water vapour 91 and the gas at normal temperature 92 of high temperature do not mixed mutually, the water vapour 91 of heat is met and is condensed into water after cold in model formula heat exchanger 3, dry air after the cooling is met to atmosphere from the dry air port of export 32 and is discharged, the water that condenses is discharged from second discharge outlet 52, and second discharge outlet 52 is positioned at the dry air port of export 32 sides of heat-exchangers of the plate type 3.
Water-collecting tray 4 is positioned at the bottom of equipment, collects the water of first discharge outlet 51,52 discharges of second discharge outlet.The bottom of water-collecting tray 4 is provided with the 3rd discharge outlet 53, is used for the water of water-collecting tray 4 is discharged.
Electric appliance control box 6 is positioned at the side of equipment, by the electricity consumption device in lead connection and the control appliance.
The quantity of described heat-exchangers of the plate type 3 can be a plurality of, a plurality of heat-exchangers of the plate type 3 head and the tail can be together in series, and has increased the path-length of water vapour 91 in heat-exchangers of the plate type 3 like this, more is conducive to the drying of water vapour 91.
Described electric appliance control box 6 inside also are provided with anxious stop breaker 61, temperature controller 62, suddenly stop the control of opening circuit that breaker 61 is used in emergency circumstances, control when temperature controller 62 is too high for the equipment operation temperature specifically can be carried out program setting and control operation by the computer control panel in the electric appliance control box 6.
Claims (3)
1. water vapour condenser is characterized in that: comprise steam inlet unit, gas at normal temperature air inlet unit, heat-exchangers of the plate type (3), water-collecting tray (4), discharge outlet, electric appliance control box (6) and device housings (7), wherein:
The steam inlet unit comprises that jet chimney (11), steam suck blower fan (12) and steam-water separator (13), jet chimney entrance point (111) is communicated with the sealing of purge chamber (8) water vapour (91) exit, and set gradually steam at the pipeline of jet chimney entrance point (111) portion and suck blower fan (12) and steam-water separator (13), steam-water separator (13) bottom is provided with first discharge outlet (51) of passing jet chimney (11) wall, and the jet chimney port of export (112) connects the steam inlet end (31) of heat-exchangers of the plate type (3);
Gas at normal temperature air inlet unit comprises gas at normal temperature pipeline (21), condensation fan (22) and air side air intake air filter screen (23), gas at normal temperature pipe head (211) is met to atmosphere by the air admission hole of equipment both sides, and air side air intake air filter screen (23) is installed, gas at normal temperature pipe outlet (212) is provided with condensation fan (22), meet to atmosphere the gas outlet of condensation fan (22), inserts heat-exchangers of the plate type (3) on the intermediate conduit of gas at normal temperature pipeline (21);
Heat-exchangers of the plate type (3) comprises steam inlet end (31), the dry air port of export (32), second discharge outlet (52), the intermediate portion presents the tabular sub-pipeline parallel interval of multiple branches and arranges, heat exchange is carried out in the gap that gas at normal temperature (92) in the gas at normal temperature pipeline (21) is passed between the tabular sub-pipeline of heat-exchangers of the plate type (3) mid portion, the dry air port of export (32) is met to atmosphere, and second discharge outlet (52) is positioned at the dry air port of export (32) side of heat-exchangers of the plate type (3);
Water-collecting tray (4) is positioned at the bottom of equipment, collects the water of first discharge outlet (51), second discharge outlet (52) discharge, and the bottom of water-collecting tray (4) is provided with the 3rd discharge outlet (53);
Electric appliance control box (6) is positioned at the side of equipment, by the electricity consumption device in lead connection and the control appliance.
2. water vapour condenser as claimed in claim 1, it is characterized in that: the quantity of described heat-exchangers of the plate type (3) can be that a plurality of head and the tail are composed in series.
3. water vapour condenser as claimed in claim 1 or 2 is characterized in that: described electric appliance control box (6) inside also is provided with anxious one or both of breaker (61), temperature controller (62) of stopping.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110275510 CN102430257B (en) | 2011-09-16 | 2011-09-16 | Steam condenser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110275510 CN102430257B (en) | 2011-09-16 | 2011-09-16 | Steam condenser |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102430257A CN102430257A (en) | 2012-05-02 |
| CN102430257B true CN102430257B (en) | 2013-07-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201110275510 Expired - Fee Related CN102430257B (en) | 2011-09-16 | 2011-09-16 | Steam condenser |
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| CN (1) | CN102430257B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202860162U (en) * | 2012-07-25 | 2013-04-10 | 仁化县科信节能服务有限公司 | Cyclic steam recycling device |
| CN104043261A (en) * | 2013-03-14 | 2014-09-17 | 深圳市艾基科技有限公司 | Air purification system |
| CN105795951A (en) * | 2016-04-25 | 2016-07-27 | 广东长盈电器有限公司 | Oven steam cooling system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101099072A (en) * | 2005-01-07 | 2008-01-02 | 阿尔法拉瓦尔有限公司 | A heat exchanger device |
| CN101539375A (en) * | 2009-04-23 | 2009-09-23 | 吴植仁 | Spiral lamina fin type air cooler |
| CN201889096U (en) * | 2010-09-17 | 2011-07-06 | 中科合成油工程有限公司 | Heat exchanging separator |
| CN201906551U (en) * | 2010-09-30 | 2011-07-27 | 东莞信易电热机械有限公司 | Dehumidifier |
| CN202315380U (en) * | 2011-09-16 | 2012-07-11 | 无锡市迪昌制冷设备有限公司 | Steam condenser |
-
2011
- 2011-09-16 CN CN 201110275510 patent/CN102430257B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101099072A (en) * | 2005-01-07 | 2008-01-02 | 阿尔法拉瓦尔有限公司 | A heat exchanger device |
| CN101539375A (en) * | 2009-04-23 | 2009-09-23 | 吴植仁 | Spiral lamina fin type air cooler |
| CN201889096U (en) * | 2010-09-17 | 2011-07-06 | 中科合成油工程有限公司 | Heat exchanging separator |
| CN201906551U (en) * | 2010-09-30 | 2011-07-27 | 东莞信易电热机械有限公司 | Dehumidifier |
| CN202315380U (en) * | 2011-09-16 | 2012-07-11 | 无锡市迪昌制冷设备有限公司 | Steam condenser |
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| Publication number | Publication date |
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| CN102430257A (en) | 2012-05-02 |
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Granted publication date: 20130710 Termination date: 20160916 |
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| CF01 | Termination of patent right due to non-payment of annual fee |