CN2287283Y - Combined condensing and cooling device - Google Patents
Combined condensing and cooling device Download PDFInfo
- Publication number
- CN2287283Y CN2287283Y CN 96235134 CN96235134U CN2287283Y CN 2287283 Y CN2287283 Y CN 2287283Y CN 96235134 CN96235134 CN 96235134 CN 96235134 U CN96235134 U CN 96235134U CN 2287283 Y CN2287283 Y CN 2287283Y
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- CN
- China
- Prior art keywords
- cooling
- utility
- model
- chamber
- condensation
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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.)
- Expired - Fee Related
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model provides a combined condensing and cooling device for various kinds of vapor condensation and cooling, belonging to a heat-exchange device of two kinds of heat exchange medium. The utility model is composed of a shell-and-tube heat exchanger, a coiled pipe heat exchanger, a steam and liquid separation chamber and a collecting chamber in the mode of connection through a closed tube. The utility model can be used for the operation of normal pressure, and can also be used for the operation of depressurization; the utility model has high condensing and cooling speed, less cooling water consumption, convenient operation and high safety. The utility model can be widely used for various kinds of condensation and cooling of the steam in the medicine industry, the food industry, the chemical industry, etc.
Description
The utility model relates to a kind of heat-exchange apparatus, particularly a kind of combined type condensation cooler that is used for all kinds of steam condensation coolings.Existing condensate cooler, what have can only be used for atmospheric operation, and what have can only be used for decompression operation, the condensation effect that has is bad, has tail vapour to discharge, and the cooling effect that has is bad, coolant temperature is high and run material, and the condensation cooling velocity that has is slow, and the consumption of cooling-water that has is big.
The purpose of this utility model, be to provide a kind of atmospheric operation that both can be used for, can be used for decompression operation again, the condensation cooling effect is all good, and the condensation cooling velocity is fast, and consumption of cooling-water is little, anury vapour is discharged, do not run the combined type condensation cooler of material, satisfy safe in utilization, reliable, economic dispatch requirement, can adapt to the needs of industry-by-industries such as medicine, food, chemical industry.
The purpose of this utility model reaches with following mode: liquid collecting plate (4), vacuum tube (14), cooling coil (5), cooling water jecket (16), gas-liquid separation plate (8), following liquid pipe (9), wireway (18), air bleeding valve (19), liquid level gauge (20), baiting valve (21) lumps together with collecting tank (11) soldering group; Collecting tank (11) go up to connect shell and tube condenser (2), is welded with steam inlet pipe (1) on the end socket (13) of shell and tube condenser (2), is but device of a kind of combined type condensation that integrates functions such as condensation cooling, gas-liquid separation, collection cooling fluid.
Below in conjunction with implementing legend technical characterictic of the present utility model and advantage are described in further detail and illustrate.
Accompanying drawing is a complete section front view of the present utility model.
As seen from the figure, cooling water jecket (16) and gas-liquid separating plate (8) are divided into ring-type cooling chamber (15) to collecting tank (11), (12) three chambers of gas-liquid separation chamber (6) and collecting chamber; The built-in cooling coil of ring-type cooling chamber (15) (5); Gas-liquid separation chamber (6) communicates with collecting chamber (12) by steam guiding tube (18) and following liquid pipe (9); The top of gas-liquid separation chamber (6) is welded with liquid collecting plate (4), and collecting chamber (12) is provided with exhaust-valve (19) liquid level gauge (20) and bleeder valve (21); Weld mutually with cooling coil (5) at the bottom of the awl of liquid collecting plate (4); Gas-liquid separation chamber (6) is led in the bottom that cooling water jecket (6) is passed in the outlet (7) of cooling coil (5); The upper side of gas-liquid separation chamber (6) is welded with vacuum tube (14).Shell and tube condenser (2) place collecting tank (11) above, be welded with steam inlet pipe (1) on the end socket (13) of shell and tube condenser (2); The lower side of shell and tube condenser (2) links to each other with the cooling chamber (15) of collecting tank (11) by coolant guide pipe (3).
The operation beginning: material steam enters shell and tube condenser (2) along steam inlet pipe (1) and obtains condensation, condensate liquid enters cooling coil by liquid collecting plate (4) and obtains cooling, cooling fluid enters gas-liquid separation chamber (6) along outlet (7), enter collecting chamber (12) by following liquid pipe (9) again, liquid level juice (20) shows when liquid level has expired, close down liquid valve (10), lead steam valve (17), open air bleeding valve (19) and bleeder valve (21) is emitted liquid.During atmospheric operation, open air bleeding valve (19), on-condensible gas is discharged; During decompression operation, on-condensible gas is taken away by vacuum tube (14), this shows, the utility model both can be used for atmospheric operation, can be used for decompression operation again.Because cooling water by the ring-type cooling chamber, enters shell and tube condenser (2) by coolant guide pipe (3) earlier again, therefore, forms the countercurrent flow of cold and hot two media long period, heat transfer coefficient is big, and cooling velocity is fast, and cooling water heats up high, and consumption of cooling-water is little.Because collecting tank (11) integrates cooling, gas-liquid separation and collection three functions, thereby compact conformation, and is easy to operate, safe in utilization, economical, reliable, can be widely used in all kinds of steam condensation coolings of industries such as medicine, food, chemical industry.
Claims (2)
1, a kind of combined type condensation cooler that is used for all kinds of steam condensation coolings, by shell and tube condenser, cooling coil and collecting tank are main formation, its characteristic is that taper liquid collecting plate (4) is arranged in the collecting tank (11), cooling water jecket (16) and taper gas-liquid separation plate (8), weld mutually with cooling coil (5) at the bottom of the awl of taper liquid collecting plate (4), the outlet (7) of cooling coil (5) is passed cooling water jecket (16) and is led to gas-liquid separation chamber (6).
2, a kind of combined type condensation cooler that is used for all kinds of steam condensation coolings, its feature also is, one cooling chamber (15) is arranged in the collecting tank (11), cooling coil (5) is arranged in the cooling chamber (15), the top of cooling chamber (5) has coolant guide pipe (3) to communicate with shell and tube condenser (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96235134 CN2287283Y (en) | 1996-06-25 | 1996-06-25 | Combined condensing and cooling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96235134 CN2287283Y (en) | 1996-06-25 | 1996-06-25 | Combined condensing and cooling device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2287283Y true CN2287283Y (en) | 1998-08-05 |
Family
ID=33911286
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 96235134 Expired - Fee Related CN2287283Y (en) | 1996-06-25 | 1996-06-25 | Combined condensing and cooling device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2287283Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100414220C (en) * | 2005-11-22 | 2008-08-27 | 淄博创尔沃中央空调有限公司 | Automatic gas-liquid separation condenser for central air conditioning unit |
| WO2009009928A1 (en) * | 2007-07-18 | 2009-01-22 | Tsinghua University | Condensing and heat transferring method having automatic liquid dividing function and apparatus thereof |
| CN102225244A (en) * | 2011-05-13 | 2011-10-26 | 安徽禾盛生物能源有限公司 | Grading type condensing device for coal/biomass pyrolysis equipment |
| CN102698460A (en) * | 2012-05-31 | 2012-10-03 | 东营市冠森绝缘制品有限公司 | Condensation recoverer |
| CN104422300A (en) * | 2013-08-30 | 2015-03-18 | 程长青 | Vacuum condenser |
-
1996
- 1996-06-25 CN CN 96235134 patent/CN2287283Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100414220C (en) * | 2005-11-22 | 2008-08-27 | 淄博创尔沃中央空调有限公司 | Automatic gas-liquid separation condenser for central air conditioning unit |
| WO2009009928A1 (en) * | 2007-07-18 | 2009-01-22 | Tsinghua University | Condensing and heat transferring method having automatic liquid dividing function and apparatus thereof |
| CN102225244A (en) * | 2011-05-13 | 2011-10-26 | 安徽禾盛生物能源有限公司 | Grading type condensing device for coal/biomass pyrolysis equipment |
| CN102698460A (en) * | 2012-05-31 | 2012-10-03 | 东营市冠森绝缘制品有限公司 | Condensation recoverer |
| CN104422300A (en) * | 2013-08-30 | 2015-03-18 | 程长青 | Vacuum condenser |
| CN104422300B (en) * | 2013-08-30 | 2017-05-31 | 程长青 | A kind of vacuum condenser |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |