CN202078828U - Steam-water separating device of refrigerated type dryer - Google Patents
Steam-water separating device of refrigerated type dryer Download PDFInfo
- Publication number
- CN202078828U CN202078828U CN2011201686674U CN201120168667U CN202078828U CN 202078828 U CN202078828 U CN 202078828U CN 2011201686674 U CN2011201686674 U CN 2011201686674U CN 201120168667 U CN201120168667 U CN 201120168667U CN 202078828 U CN202078828 U CN 202078828U
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- separating cavity
- water
- disengagement chamber
- housing
- chamber
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Abstract
The utility model relates to a refrigerated type dryer, and particularly relates to and discloses a steam-water separating device of the refrigerated type dryer, which comprises a housing; the housing internally comprises a primary separating cavity, a secondary separating cavity and a final separating cavity from bottom to top, the primary separating cavity is an enclosed cavity formed by a vertical baffle, a top right sloping baffle and the housing, the lower part of the vertical baffle is provided with a primary separating cavity outlet, the primary separating cavity is provided with an air inlet port, the final separating cavity is formed by a lower shelf positioned above the top right sloping baffle, an upper shelf and the housing, a stainless steel screen is arranged in the final separating cavity, an air outlet port is arranged above the final separating cavity, the secondary separating cavity is formed between the primary separating cavity and the final separating cavity, a water collecting tank is arranged at the bottom of the secondary separating cavity, and a water drainage port is connected below the water collecting tank. In the steam-water separating device of the refrigerated type dryer, water can be removed by three cavities in a grading manner so as to effectively remove liquid water in compressed air, ensure outlet air with low dew point and realize high-efficiency steam-water separation in smaller space.
Description
Technical field
The utility model relates to a kind of freezing type drier, particularly a kind of water separator of freezing type drier.
Background technology
Freezing type drier mainly is made up of refrigeration system, heat-exchange system, carbonated drink piece-rate system and corresponding electric control system four parts.Saturated compressed air is in cooling procedure, can in heat exchanger, gather a large amount of condensation waters, also there are a large amount of more tiny water droplet water smokes to be suspended in and enter the precool heat exchanger device in the compressed air, after these water droplet water smokes enter the precooling regenerator, along with the part " double evaporation-cooling " of carrying out of heat exchange is returned gas phase, make in the finished product gas moisture increase cause dew point to rise, the aqueous water that another part has little time to evaporate then enters user pipe with air-flow, make in the gas equipment of downstream aqueous water to occur, certainly will influence the quality of product like this.For the aqueous water that condenses in the heat transfer process can well be separated from finished product gas, thereby guarantee the quality of finished product gas, it is essential that water separator is set, and is obligato vitals in the freezing type drier.
Domestic manufacturer generally adopts baffle plate or silk screen isolating construction, compressed air enters separator along air inlet pipe in the baffle separator, air-flow is subjected to stopping of baffle plate, be mixed in just can the adhere surface that is trapped in baffle plate and be accumulated into the bigger drop of particle diameter at baffle edge and fall into separator bottom of airborne water droplet, though it is simple in structure, cheap, but domestic process for machining and manufacturing is relatively poor relatively, and baffle plate is to soldering angle, distribute bits is equipped with strict requirement, therefore can only separate the drop of the above greater particle size of 10 μ m, and the drop that can't separate than small particle diameter causes finished product gas dew point to rise.Because the fluctuation situation that throughput may exist also can cause the decline of separating effect, compressed air enters involute formula silk screen agglomeration separation after entering the vulgar centrifugation in bottom in the domestic silk screen separate mode simultaneously.The problem that this frame mode exists is that causing separating barrel diameter increases greatly, influences the compactedness of equipment owing to there is the separation of low speed.And interior rolling silk screen simple installation, but being easy to cause silk screen loose, separating effect is had a greatly reduced quality simultaneously.And cylindrical shell adopts carbon steel to make, and is easy to get rusty in saturated compressed air, and equipment uses the later stage to cause silk screen to stop up, and the pressure loss heightens, the terminal supply gas pressure of the system that influences.External product is because of its machining accuracy height, and verifies repeatedly that by emulation experiment separating effect of the same type will be much higher than home products.
Summary of the invention
Have at the water separator of prior art freezing type drier that equipment is not compact, the defective of inferior separating effect, the utility model provides a kind of water separator that can realize the efficient freezing type drier that separates of carbonated drink in less space.
For achieving the above object, the utility model adopts following technical scheme:
The water separator of freezing type drier, comprise housing, described enclosure interior comprises the primary separation chamber from down to up, secondary disengagement chamber, the final stage disengagement chamber, described primary separation chamber is by perpendicular baffle plate, the enclosed cavity that upper right slanting baffle and housing form, perpendicular baffle plate bottom has the outlet of primary separation chamber, the primary separation chamber is provided with intake interface, be positioned at the following shelf of upper right slanting baffle top, last shelf and housing form the final stage disengagement chamber, in the final stage disengagement chamber stainless steel cloth is set, final stage disengagement chamber top is provided with the interface of giving vent to anger, form secondary disengagement chamber between primary separation chamber and the final stage disengagement chamber, secondary disengagement chamber bottom has water leg, and the water leg below connects drainage interface.
As preferably, described stainless steel cloth comprises first silk screen layer, second silk screen layer, the 3rd silk screen layer from down to up, and described meshcount successively decreases from top to bottom successively.
As preferably, bottom, described primary separation chamber is provided with the first upper left slanting baffle, the second upper left slanting baffle, is obliquely installed the lower-left slanting baffle with upper right slanting baffle.
As preferably, high speed honeycomb duct and low-speed centrifugal device are set in the described secondary disengagement chamber.
Adopt the baffle plate of forming certain angle in the primary separation chamber, separate big liquid water droplets by compressed air direct collision baffle plate, a part is escaped the annular gyration of the fine droplets of baffle plate seizure with air motion direction generation decline earlier, back rising, gathering increases and separates with compressed air mutually in this process, separate by efficient centrifugal after the good tangential velocity of the honeycomb duct rectification acquisition of secondary disengagement chamber again, remove the drop of the above particle diameter of 10 μ m substantially; The final stage disengagement chamber adopts compound stainless steel cloth, by the silk screen combination layer by layer from low to high of different meshes, effectively removes little aqueous water to the compressed air of 5 μ m.Combination by above three chambers dewaters, and guarantees the outlet air of low dew point.
The water separator of freezing type drier of the present utility model dewaters by three chamber classifications, effectively removes the aqueous water in the compressed air, guarantees the outlet air of low dew point, can realize in less space that carbonated drink efficiently separates.
Description of drawings
Fig. 1 is the structural representation of the water separator embodiment of freezing type drier described in the utility model.
Fig. 2 is the cutaway view of A-A direction among Fig. 1.
Specific embodiment
Below in conjunction with the accompanying drawing 1,2 and the specific embodiment the utility model is described in further detail:
The water separator of freezing type drier, as Fig. 1, shown in Figure 2, comprise housing 1, housing (1) inside comprises primary separation chamber 7 from down to up, secondary disengagement chamber 8, final stage disengagement chamber 9, primary separation chamber 7 is by perpendicular baffle plate 61, the enclosed cavity that upper right slanting baffle 62 and housing 1 form, described perpendicular baffle plate 61 bottoms have primary separation chamber outlet 9, primary separation chamber 7 is provided with intake interface 2, be positioned at the following shelf 10 of upper right slanting baffle 62 tops, last shelf 11 forms final stage disengagement chamber 9 with housing 1, stainless steel cloth 4 is set in the final stage disengagement chamber 8, final stage disengagement chamber 9 tops are provided with the interface 3 of giving vent to anger, form secondary disengagement chamber 8 between primary separation chamber 7 and the final stage disengagement chamber 9, secondary disengagement chamber 8 bottoms have water leg 12, and water leg 12 belows connect drainage interface 13.Described stainless steel cloth 4 comprises first silk screen layer 41, second silk screen layer 42, the 3rd silk screen layer 43 from down to up, the order number of described first silk screen layer 41 is the 30-40 order, the order number of second silk screen layer 42 is the 10-15 order, and the order number of the 3rd silk screen layer 43 is the 2-5 order.7 bottoms, described primary separation chamber are provided with first upper left slanting baffle 63, the second upper left slanting baffle 64, are obliquely installed lower-left slanting baffle 65 with upper right slanting baffle 62.High speed honeycomb duct 5 and low-speed centrifugal device 14 are set in the described secondary disengagement chamber 8.
Claims (4)
1. the water separator of freezing type drier, comprise housing (1), it is characterized in that: described housing (1) inside comprises primary separation chamber (7) from down to up, secondary disengagement chamber (8), final stage disengagement chamber (9), described primary separation chamber (7) is by perpendicular baffle plate (61), the enclosed cavity that upper right slanting baffle (62) and housing (1) form, described perpendicular baffle plate (61) bottom has primary separation chamber outlet (9), primary separation chamber (7) is provided with intake interface (2), be positioned at the following shelf (10) of upper right slanting baffle (62) top, last shelf (11) forms final stage disengagement chamber (9) with housing (1), stainless steel cloth (4) is set in the final stage disengagement chamber (8), final stage disengagement chamber (9) top is provided with the interface (3) of giving vent to anger, form secondary disengagement chamber (8) between primary separation chamber (7) and the final stage disengagement chamber (9), secondary disengagement chamber (8) bottom has water leg (12), and water leg (12) below connects drainage interface (13).
2. the water separator of freezing type drier according to claim 1, it is characterized in that: described stainless steel cloth (4) comprises first silk screen layer (41), second silk screen layer (42), the 3rd silk screen layer (43) from down to up, and described meshcount successively decreases from top to bottom successively.
3. the water separator of freezing type drier according to claim 2, it is characterized in that: bottom, described primary separation chamber (7) is provided with the first upper left slanting baffle (63), the second upper left slanting baffle (64), is obliquely installed lower-left slanting baffle (65) with upper right slanting baffle (62).
4. the water separator of freezing type drier according to claim 3 is characterized in that: high speed honeycomb duct (5) and low-speed centrifugal device (14) are set in the described secondary disengagement chamber (8).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011201686674U CN202078828U (en) | 2011-05-25 | 2011-05-25 | Steam-water separating device of refrigerated type dryer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011201686674U CN202078828U (en) | 2011-05-25 | 2011-05-25 | Steam-water separating device of refrigerated type dryer |
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CN202078828U true CN202078828U (en) | 2011-12-21 |
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CN2011201686674U Expired - Fee Related CN202078828U (en) | 2011-05-25 | 2011-05-25 | Steam-water separating device of refrigerated type dryer |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107983103A (en) * | 2017-12-29 | 2018-05-04 | 无锡海悦生化装备有限公司 | Air dehumidifier |
CN108379985A (en) * | 2018-04-19 | 2018-08-10 | 北京京诚科林环保科技有限公司 | Steam releasing mouth self-cleaning device |
-
2011
- 2011-05-25 CN CN2011201686674U patent/CN202078828U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107983103A (en) * | 2017-12-29 | 2018-05-04 | 无锡海悦生化装备有限公司 | Air dehumidifier |
CN107983103B (en) * | 2017-12-29 | 2024-05-17 | 无锡海悦生化装备有限公司 | Air dehumidifier |
CN108379985A (en) * | 2018-04-19 | 2018-08-10 | 北京京诚科林环保科技有限公司 | Steam releasing mouth self-cleaning device |
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Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111221 Termination date: 20150525 |
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EXPY | Termination of patent right or utility model |