CN202315380U - Steam condenser - Google Patents
Steam condenser Download PDFInfo
- Publication number
- CN202315380U CN202315380U CN2011203480623U CN201120348062U CN202315380U CN 202315380 U CN202315380 U CN 202315380U CN 2011203480623 U CN2011203480623 U CN 2011203480623U CN 201120348062 U CN201120348062 U CN 201120348062U CN 202315380 U CN202315380 U CN 202315380U
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- steam
- water
- plate type
- gas
- heat
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Abstract
The utility model discloses a steam condenser which comprises a steam inlet unit, a normal-temperature gas inlet unit, a plate type heat exchanger, a water collecting disc, a water outlet, an electrical appliance control box and an equipment housing, wherein the steam inlet unit comprises a steam pipeline, a steam absorbing fan and a steam/water separator; the normal-temperature gas inlet unit comprises a normal-temperature gas pipeline, a condensing fan and an air filter mesh for filtering side inlet air; and the plate type heat exchanger comprises a steam inlet end, a dry air outlet end and a second water outlet. The steam flows into the plate type heat exchanger through the steam/water separator, the plate type heat exchanger,is internally provided with a plurality of branch plate-shaped pipelines which are arranged in parallel and at intervals, and the normal-temperature gas in the normal-temperature gas pipeline passes through gaps among the branch plate-shaped pipelines in the middle of the plate type heat exchanger to carry out heat exchange, so that the high-temperature steam is condensed and discharged, and the condensate water is collected in the water collecting disc. The steam condenser has the advantages that compared with the prior art, about 60% of electric energy can be saved by adopting the steam condenser; and the steam condenser is high in stability and low in maintenance cost.
Description
Technical field
The utility model 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, can increase air humidity, quicken the equipment corrosion in the workshop if water vapour directly is emitted 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; With the liquid refrigerant that is cooled to HTHP in the condenser from the high temperature and high pressure gaseous refrigerant of compressor, this liquid refrigerant becomes the low-temp low-pressure liquid refrigerant that is easy to evaporate through capillary step-down, cooling; To evaporimeter, evaporate heat absorption; To pass through and inhale the nebelwind machine and cool off from the steam that cleaning machine sucks, and 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, accomplishes one time kind of refrigeration cycle.Through continuous kind of refrigeration cycle steam is condensed.
This water vapour condenser, power consumption is big, and stabilization of equipment performance is low, and maintenance cost is high.
The utility model content
The utility model purpose 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 realizing above-mentioned purpose, the utility model is realized through following technical scheme:
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 on the pipeline of the inlet end of jet chimney, set gradually steam 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, and 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, behind heat-exchangers of the plate type, arranges to atmosphere again.
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, inserts 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,, form the gas at normal temperature circulation finally from the condensation fan device for transferring.
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 each other, and the water vapour of heat is met and condensed into water after cold in heat-exchangers of the plate type, and the dry air after the cooling is met to atmosphere from the dry air port of export and 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, through the electricity consumption device in lead connection and the control appliance.
The quantity of said heat-exchangers of the plate type can be a plurality of, can a plurality of heat-exchangerss of the plate type 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 helps the drying of water vapour.
Said electric appliance control box inside also is provided with one or both that suddenly stop breaker, temperature controller; Suddenly stopping breaker is used for the control of opening circuit in emergency circumstances; Temperature controller is used for the control of equipment operation temperature when too high, specifically can carry out program setting and control operation through the computer control panel in the electric appliance control box.
The beneficial effect of the described a kind of water vapour condenser of the utility model is: energy-conserving and environment-protective, reaching under the prerequisite of same condensation effect, and save electric energy about 60% than prior art; Stabilization of equipment performance is high simultaneously, and maintenance cost is low.
Description of drawings
Fig. 1 is the Facad structure simplified schematic diagram of the utility model water vapour condenser.
Fig. 2 is the side structure simplified schematic diagram of the utility model water vapour condenser.
Wherein the symbol description of Fig. 1 to Fig. 2 is following:
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, 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, the 53, the 3rd discharge outlet, 6, electric appliance control box, 61, the anxious breaker that stops, 62, temperature controller; 7, device housings, 8, the purge chamber, 91, water vapour, 92, gas at normal temperature.
The specific embodiment
Like Fig. 1, shown in Figure 2, be the Facad structure simplified schematic diagram and the side structure simplified schematic diagram of the utility model water vapour condenser.
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 from the purge chamber 8 water vapours 91 that come out like this; And on the pipeline of 111 ones of jet chimney entrance points, set gradually steam 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, and 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-exchangers of the plate type 3, and the water vapour 91 after steam-water separator 13 separates flows into heat-exchangers of the plate type 3 from the jet chimney port of export 112, behind heat-exchangers of the plate type 3, arranges to atmosphere again.
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, inserts 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,, form gas at normal temperature 92 circulations finally from condensation fan 22 device for transferring.
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 the water vapour 91 of high temperature does not mix with gas at normal temperature 92 each other, and the water vapour 91 of heat is met and condensed into water after cold in model formula heat exchanger 3, and the dry air after the cooling is met to atmosphere from the dry air port of export 32 and 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 that first discharge outlet 51, second discharge outlet 52 are discharged.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, through the electricity consumption device in lead connection and the control appliance.
The quantity of said heat-exchangers of the plate type 3 can be a plurality of, can a plurality of heat-exchangers of the plate type 3 head and the tail 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 helps the drying of water vapour 91.
Said electric appliance control box 6 inside also are provided with anxious stop breaker 61, temperature controller 62; Suddenly stopping breaker 61 is used for the control of opening circuit in emergency circumstances; Temperature controller 62 is used for the control of equipment operation temperature when too high, specifically can carry out program setting and control operation through 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 on the pipeline of jet chimney entrance point (111) portion, set gradually steam 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), and 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, through the electricity consumption device in lead connection and the control appliance.
2. water vapour condenser as claimed in claim 1 is characterized in that: the quantity of said heat-exchangers of the plate type (3) can be that a plurality of head and the tail are composed in series.
3. according to claim 1 or claim 2 water vapour condenser is characterized in that: said 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 |
|---|---|---|---|
| CN2011203480623U CN202315380U (en) | 2011-09-16 | 2011-09-16 | Steam condenser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203480623U CN202315380U (en) | 2011-09-16 | 2011-09-16 | Steam condenser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202315380U true CN202315380U (en) | 2012-07-11 |
Family
ID=46427383
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203480623U Withdrawn - After Issue CN202315380U (en) | 2011-09-16 | 2011-09-16 | Steam condenser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202315380U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102430257A (en) * | 2011-09-16 | 2012-05-02 | 无锡市迪昌制冷设备有限公司 | Water vapor condenser |
-
2011
- 2011-09-16 CN CN2011203480623U patent/CN202315380U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102430257A (en) * | 2011-09-16 | 2012-05-02 | 无锡市迪昌制冷设备有限公司 | Water vapor condenser |
| CN102430257B (en) * | 2011-09-16 | 2013-07-10 | 无锡市迪昌制冷设备有限公司 | Steam condenser |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20120711 Effective date of abandoning: 20130710 |
|
| RGAV | Abandon patent right to avoid regrant |