CN201561682U - Vertical condenser with double inclined baffle plates - Google Patents
Vertical condenser with double inclined baffle plates Download PDFInfo
- Publication number
- CN201561682U CN201561682U CN2009202804327U CN200920280432U CN201561682U CN 201561682 U CN201561682 U CN 201561682U CN 2009202804327 U CN2009202804327 U CN 2009202804327U CN 200920280432 U CN200920280432 U CN 200920280432U CN 201561682 U CN201561682 U CN 201561682U
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- China
- Prior art keywords
- deflection plate
- baffle plates
- heat exchange
- condenser
- heat exchanger
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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 - Lifetime
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Abstract
The utility model relates to a vertical condenser with double inclined baffle plates, which belongs to condensing heat exchange equipment. The vertical condenser is provided with a casing, heat exchange tubes and baffle plates, the heat exchange tubes are placed inside an inner cavity of the casing, and the baffle plates are arranged inside the inner cavity of the casing relative to the heat exchange tubes. The vertical condenser is characterized in that the baffle plates and axial lines of the heat exchange tubes are in inclination angle design, and further, by utilizing a center surface of the casing as a boundary, the baffle plates are symmetrically downwards inclined to two sides. The vertical condenser is simple and reasonable in structure and convenient in manufacturing, the inclined baffle plates can rapidly discharge condensing fluid flowing from the upper heat exchange tube, eliminates shortages that a lower heat exchange tube of a traditional vertical condenser is poor in condensing effect and even can not exchange heat fundamentally, greatly improves condensing effect, and increases condensing efficiency. The double inclined baffle plates can be respectively flexibly combined with condensing tubes with various structural forms so as to form high-efficient condenser with various structural forms.
Description
Technical field
The utility model relates to a kind of pair of inclination deflection plate vertical (type) condenser, belongs to heat transmission equipment.
Background technology
Vertical (type) condenser, housing, heat exchanger tube, deflection plate are arranged, heat exchanger tube places the housing inner chamber, relative heat exchanger tube is provided with deflection plate in the housing inner chamber, the mobility status of heat transferring medium in the deflection plate adjustment housings inner chamber, deflection plate can in time be drained the condensate liquid on the heat exchanger tube again simultaneously, improves condensation effect greatly, is mainly used in fields such as the energy, chemical industry, oil.Traditional vertical (type) condenser, its deflection plate is horizontally disposed with, condensate film on the heat exchanger tube is behind certain thickness, flow downward at gravity and air-flow effect lower edge heat exchanger tube, after running into deflection plate, a small part condensate liquid continues to flow downward along baffle hole, and remaining is flocked on the deflection plate, baffle hole gap location from deflection plate edge and lower under the gravity effect flows down along heat exchanger tube, repeats the process of front during to next piece deflection plate again.Liquid film on the heat exchanger tube is from top to bottom more and more thicker, and condensation effect worse and worse.
The utility model content
The purpose of this utility model is to provide a kind of pair of inclination deflection plate vertical (type) condenser, and simple in structure, cost is low, the condensation efficiency height.
Described in the utility model pair of inclination deflection plate vertical (type) condenser, housing, heat exchanger tube, deflection plate are arranged, heat exchanger tube places the housing inner chamber, relative heat exchanger tube is provided with deflection plate in the housing inner chamber, it is characterized in that deflection plate and heat exchanger tube axis are the angle of inclination design, can in time drain the condensate liquid that flows down from heat exchanger tube, guarantee to continue good condensation effect.
Deflection plate is that the boundary is downward-sloping to bilateral symmetry with the housing median plane, and the angle that the angle of inclination is controlled at horizontal plane is 5-45 degree angle, that is: deflection plate is not a plane, and each deflection plate has two angled planes, and the condensate liquid water conservancy diversion is effective.
Deflection plate is fixed in the housing by distance sink tube, and is safe and reliable, stable performance.
The same with common deflection plate, deflection plate has single breach and two kinds of two breach, and the breach of single breach deflection plate is made up of single-piece in a side, is staggered successively in housing.Every group of two breach deflection plate are made up of two of A, B, and A spare breach is in both sides, and B spare breach is in the centre.No matter be single breach deflection plate or two breach deflection plate, all can convince liquid bath by patient analysis at the low side of deflection plate, be beneficial to drawing of condensate liquid.Single breach deflection plate and two breach deflection plates can adapt to the condenser of different disposal amount or different inlet form (as the strap clamp cover that enters the mouth).
The utility model compared with prior art has following beneficial effect:
Simple and reasonable, easily manufactured, skewed deflection plate can be drained the condensate liquid that flows down on the heat exchanger tube of top rapidly, the defective of having eliminated traditional vertical condenser heat exchanger tube condensation effect difference even can't having carried out heat exchange at all, improve condensation effect greatly, improved condensation efficiency.
Two inclination deflection plates respectively with the condenser pipe flexible combination of multiple version, can derive the efficient condenser of multiple version.
Description of drawings
The structural representation of Fig. 1, existing common vertical (type) condenser.
Baffle arrangement schematic diagram among Fig. 2, Fig. 1.
Another baffle arrangement schematic diagram among Fig. 3, Fig. 1.
Fig. 4, the utility model one example structure schematic diagram.
Baffle arrangement schematic diagram among Fig. 5, Fig. 4.
Another baffle arrangement schematic diagram among Fig. 6, Fig. 4.
Fig. 7, another example structure schematic diagram of the utility model.
Baffle arrangement schematic diagram among Fig. 8, Fig. 7.
Another baffle arrangement schematic diagram among Fig. 9, Fig. 7.
Among the figure: 1, housing 2, heat exchanger tube 3, distance sink tube 4, pull bar 5,6, deflection plate 7, housing 8, heat exchanger tube 9, distance sink tube 10, pull bar 11,12, deflection plate 13,14, guiding gutter 15, housing 16, heat exchanger tube 17, distance sink tube 18, pull bar 19,20, deflection plate 21, guiding gutter.
The specific embodiment
The utility model is described in further detail below in conjunction with the embodiment accompanying drawing.
As Fig. 1, Fig. 2, shown in Figure 3, in existing single bow plate vertical (type) condenser, the deflection plate 5,6 of single bow formula is horizontally disposed, and deflection plate 6 is fixed in the housing 1 by distance sink tube 3 and pull bar 4, and deflection plate 5,6 is single bow formula deflection plate of interlaced arrangement.
As Fig. 4, Fig. 5, shown in Figure 6, described in the utility model pair of inclination deflection plate vertical (type) condenser, housing 7 is arranged, heat exchanger tube 8, deflection plate 11,12, heat exchanger tube 8 places housing 1 inner chamber, deflection plate 11,12 is single gap type deflection plate, deflection plate 11,12 are angle of inclination design with the heat exchanger tube axis, deflection plate 11,12 is that the boundary is downward-sloping to bilateral symmetry with the housing median plane, the angle that the angle of inclination is controlled at horizontal plane is 5-45 degree angle, the convenient condensate liquid that flows down from heat exchanger tube 8 of in time draining, prevent that condensed water from accumulating, guarantee to continue good condensation effect, deflection plate 11,12 are fixed in the housing 1 deflection plate 11 by distance sink tube 9 and pull bar 10,12 low side has intake chute 13,14, be beneficial to the unimpeded of condensed water and flow.
As Fig. 7, Fig. 8, shown in Figure 9, described in the utility model pair of inclination deflection plate vertical (type) condenser, by housing 15, heat exchanger tube 16, deflection plate 19,20, heat exchanger tube 16 places housing 15 inner chambers, deflection plate 19,20 is two breach deflection plates, deflection plate 19 is the two breach deflection plates of breach in both sides, and deflection plate 20 is the two breach deflection plates of two breach in the centre
Claims (4)
1. a two inclination deflection plate vertical (type) condenser has housing, heat exchanger tube, deflection plate, and heat exchanger tube places the housing inner chamber, and relative heat exchanger tube is provided with deflection plate in the housing inner chamber, it is characterized in that deflection plate and heat exchanger tube axis are the angle of inclination design.
2. according to claim 1 pair of inclination deflection plate vertical (type) condenser is characterized in that deflection plate is that the boundary is downward-sloping to bilateral symmetry with the housing median plane.
3. according to claim 2 pair of inclination deflection plate vertical (type) condenser is characterized in that deflection plate is fixed in the housing by distance sink tube.
4. according to claim 1,2 or 3 described pairs of inclination deflection plate vertical (type) condensers, it is characterized in that the low side of deflection plate has intake chute.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2009202804327U CN201561682U (en) | 2009-12-04 | 2009-12-04 | Vertical condenser with double inclined baffle plates |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2009202804327U CN201561682U (en) | 2009-12-04 | 2009-12-04 | Vertical condenser with double inclined baffle plates |
Publications (1)
Publication Number | Publication Date |
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CN201561682U true CN201561682U (en) | 2010-08-25 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN2009202804327U Expired - Lifetime CN201561682U (en) | 2009-12-04 | 2009-12-04 | Vertical condenser with double inclined baffle plates |
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CN (1) | CN201561682U (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102538511A (en) * | 2012-02-27 | 2012-07-04 | 景立秋 | Laminated type condenser |
CN103673679A (en) * | 2013-12-19 | 2014-03-26 | 江阴江顺铝型材成套设备制造有限公司 | Heat exchanger for hot shearing furnace |
CN105202948A (en) * | 2015-10-14 | 2015-12-30 | 东南大学 | Reverse flow type spiral baffle plate U-shaped pipe bundle heat exchanger |
CN105841543A (en) * | 2016-05-31 | 2016-08-10 | 郑州大学 | Oblique rod baffle type oblique flow heat exchanger |
CN106017136A (en) * | 2016-05-13 | 2016-10-12 | 中国海洋石油总公司 | Vertical type shell-and-tube heat exchanger |
CN106215531A (en) * | 2016-08-26 | 2016-12-14 | 海洲环保集团有限公司 | A kind of panel type steam water separator |
CN107308676A (en) * | 2017-07-24 | 2017-11-03 | 辽宁清道夫环保工程有限公司 | Vertical condensation device |
CN107726897A (en) * | 2017-11-17 | 2018-02-23 | 四川沃姆斯科技有限公司 | A kind of shell side formula condenser |
-
2009
- 2009-12-04 CN CN2009202804327U patent/CN201561682U/en not_active Expired - Lifetime
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102538511A (en) * | 2012-02-27 | 2012-07-04 | 景立秋 | Laminated type condenser |
CN103673679A (en) * | 2013-12-19 | 2014-03-26 | 江阴江顺铝型材成套设备制造有限公司 | Heat exchanger for hot shearing furnace |
CN105202948A (en) * | 2015-10-14 | 2015-12-30 | 东南大学 | Reverse flow type spiral baffle plate U-shaped pipe bundle heat exchanger |
CN105202948B (en) * | 2015-10-14 | 2017-11-03 | 东南大学 | A kind of adverse current type helical baffles U-tube bundle heat exchanger |
CN106017136A (en) * | 2016-05-13 | 2016-10-12 | 中国海洋石油总公司 | Vertical type shell-and-tube heat exchanger |
CN106017136B (en) * | 2016-05-13 | 2018-04-24 | 中国海洋石油总公司 | A kind of vertical shell-and-tube heat exchanger |
CN105841543A (en) * | 2016-05-31 | 2016-08-10 | 郑州大学 | Oblique rod baffle type oblique flow heat exchanger |
CN105841543B (en) * | 2016-05-31 | 2018-09-21 | 郑州大学 | Tilt the oblique stream heat exchanger of baffling grating |
CN106215531A (en) * | 2016-08-26 | 2016-12-14 | 海洲环保集团有限公司 | A kind of panel type steam water separator |
CN107308676A (en) * | 2017-07-24 | 2017-11-03 | 辽宁清道夫环保工程有限公司 | Vertical condensation device |
CN107726897A (en) * | 2017-11-17 | 2018-02-23 | 四川沃姆斯科技有限公司 | A kind of shell side formula condenser |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CX01 | Expiry of patent term |
Granted publication date: 20100825 |
|
CX01 | Expiry of patent term |