CN205505826U - There is parallel connection inside, has high -efficient brazed plate type heat exchanger of polyphone - Google Patents
There is parallel connection inside, has high -efficient brazed plate type heat exchanger of polyphone Download PDFInfo
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- CN205505826U CN205505826U CN201620216198.1U CN201620216198U CN205505826U CN 205505826 U CN205505826 U CN 205505826U CN 201620216198 U CN201620216198 U CN 201620216198U CN 205505826 U CN205505826 U CN 205505826U
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Abstract
The utility model provides a there is parallel connection inside, has high -efficient brazed plate type heat exchanger of polyphone, including the end plate, slab no. 1, slab no. 2, slab no. 3, bottom plate no. 1 or bottom plate no. 2, slab no. 1 has 4 holes, closely weld to the parallel connection form between them, increase heat exchanger's runner sectional area, the end plate, slab no. 2, slab no. 3, the bottom plate is 2 holes only, slab no. 2 and slab no. 3 welds at the slab between one, make a slab evenly distributed, slab no. 2 and slab later no. 1 forms the polyphone with the front and back part, it is more to contact, runner length is long more, the temperature the when temperature only flowed into when the cryogen flowed out can be realized than the thermit powder and 0.5 degree is hanged down. The utility model discloses have smallly, the price is low, and waste heat recovery is more thorough, can extensively apply to place hot water waste heat recovery and the supporting uses of small -size water heater such as monomer shower room, the pond of washing hand of family and public place, wash the dishes vegetable sink and beauty salon shampoo bed, can reduce the power of water heater, and energy saving, economic benefits are showing, are convenient for generally use widely.
Description
Technical field
The utility model relates to hot swapping and afterheat of hot water recovery technology field, particularly to having inside one and connecting, have the efficient brazed-plate heat exchanger of series winding.
Background technology
At present, in daily hot water cleans, domestic hot-water's overwhelming majority after being used is directly discharged into sewer, the use hot water place that only minority is large-scale has used heat reclamation device to reclaim heat energy, and family and public place monomer use shower house, hand washing sink, washing bowls or vegetables pond and cosmetology is hair washing bed seldom reclaims heat energy.Main cause is that Small Scale Heat Recovery Plant heat recovery efficiency is low, and energy recovery is undesirable；Large-scale heat reclamation device heat recovery efficiency is high, but volume is big, and price is high, also cannot install in these occasions.Want distributing to reclaim family and public place and use the waste heat of hot water on a small quantity, need that a kind of volume is little, waste heat recovery ratio more thoroughly, the heat reclamation device that energy recovery efficiency is high.
Utility model content
For the problems referred to above, the purpose of this utility model is to provide inside to be had and connects, have the efficient brazed-plate heat exchanger of series winding.
For achieving the above object, this utility model is with answering techniques below scheme:
A kind of inside described in the utility model has and connects, having the efficient brazed-plate heat exchanger of series winding.Including end plate, plate one, plate two, plate three, base plate one or base plate two, it is characterised in that: between end plate and plate two, between plate two and plate three, the plate one of equal number is installed between plate three and next sheet plate two or base plate one or base plate two；Plate one and previous section series winding between plate two and plate two and plate three form a long runner；Plate one and previous section between plate three and plate three and next plate two are contacted again and are formed a longer runner；End plate and base plate one or between repeat mounting tile two and plate three, series winding can form a runner the longest successively.
Further, end plate only has 2 interface 11Q and 14Q, and plate one has 4 holes, plate two only 2 hole 12H and 13H, plate three only 2 hole 21Q and 24Q, base plate one only 2 interface 22H and 23H, base plate two only 2 interface 31Q and 34Q.When being even slice when using plate two and plate three, the base plate of use is base plate one；When being odd number sheet when using plate two and plate three, the base plate of use is base plate two.The interface of end plate and base plate can be to blurt out, it is also possible to is turned welt, it is also possible to is to connect pipe thread mouth.End plate interface 11Q is connected with the hole 12H of plate two by the runner of plate one, the hole 12H of plate two is connected with the hole 21Q of plate three by the runner of plate one, so being consecutively connected to base plate, rearmost end plate interface 11Q and base plate one interface 22H or base plate two interface 31Q communicates formation heat exchange runner.Same end plate interface 14Q and base plate one interface 23H or base plate two interface 34Q communicates formation heat exchange runner.
Further, plate one between end plate and plate two, between plate two and plate three, between plate three (8) and next sheet plate two or base plate one or base plate two, the sheet number that plate one is installed is the most, and cross section of fluid channel is long-pending the biggest, and cold and hot dose of metered flow is the biggest.
Further, mounting tile two and plate three is repeated between end plate and base plate one or base plate two, plate two and three numbers of plate of repeating installation are the most, about the cold and hot dose number of times flowed is the most, and the length of series winding is the longest, and runner is the longest, cold and hot dose of heat exchange is the most abundant, when temperature when cryogen flows out flows into thermit powder, temperature difference is the least, and waste heat recovery is the most thorough, and the efficiency of recuperation of heat is the highest.
Accompanying drawing explanation
Fig. 1 is this utility model structure odd number schematic flow sheet；
Fig. 2 is this utility model structure even number schematic flow sheet；
1, interface 11Q；2, interface 14Q；3, end plate；
4, plate one；5, hole 12H；6, hole 13H；
7, plate two；8, plate three；9, hole 21Q；
10, hole 24Q；11, base plate one；12, interface 22H；
13, interface 23H；14, base plate two；15, interface 31Q；
16, interface 34Q；
Detailed description of the invention
The utility model is described in further detail below in conjunction with the accompanying drawings.
Inside described in the utility model has and connects, having the efficient brazed-plate heat exchanger of series winding.Including end plate (3), plate one (4), plate two (7), plate three (8), base plate one (11) or base plate two (14), it is characterised in that: between end plate (3) and plate two (7), between plate two (7) and plate three (8), between plate two (7) or plate three (8) and base plate one (11) or base plate two (14) and connect install equal number plate one (4)；Plate one (4) and previous section series winding between plate two (7) and plate two (7) and plate three (8) form a long runner；Plate one (4) and previous section between plate three (8) and plate three (8) and next plate two (7) are contacted again and are formed a longer runner；Repeating mounting tile two (7) and plate three (8) between end plate (3) and base plate one (11) or (14), series winding can form a runner the longest successively.
Described end plate (3), plate one (4), plate two (7), plate three (8), base plate one (11) or base plate two (14), end plate (3) only 2 interface 11Q (1) and 14Q (2), plate one (4) has 4 holes, plate two (7) only 2 hole 12H (5) and 13H (6), plate three (8) only 2 hole 21Q (9) and 24Q (10), base plate one (11) only 2 interface 22H (12) and 23H (13), base plate two (14) only 2 interface 31Q (15) and 34Q (16).Using plate two (7) and plate three (8) sum is even slice, and the base plate of use is base plate one (11), forms Figure of description Fig. 1 structure；Using plate two (7) and plate three (8) sum is odd number sheet, and the base plate of use is base plate two (14), forms Figure of description Fig. 2 structure.The interface of end plate and base plate can be to blurt out, it is also possible to is turned welt, it is also possible to is to connect pipe thread mouth.End plate (3) interface 11Q (1) is connected with the hole 12H (5) of plate two (7) by the runner of plate one (4), the hole 12H (5) of plate two (7) is connected with the hole 21Q (9) of plate three (8) by the runner of plate one (4), so being consecutively connected to base plate, last end plate (3) interface 11Q (1) communicates formation heat exchange runner with base plate one (11) interface 22H (12) or base plate two (14) interface 31Q (15).Same end plate (3) interface 14Q (2) communicates formation heat exchange runner with base plate one (11) interface 23H (13) or base plate two (14) interface 34Q (16).
Between described end plate (3) and plate two (7), between plate two (7) and plate three (8), between plate two (7) or plate three (8) and base plate one (11) or base plate two (14) and connect install equal number plate one (4), the sheet number that plate one (4) is installed is the most, cross section of fluid channel is long-pending the biggest, and cold and hot dose of metered flow is the biggest.
Mounting tile two (7) and plate three (8) is repeated between described end plate (3) and base plate one (11) or base plate two (14), plate two (7) and plate three (8) the sheet number installed are the most, about the cold and hot dose number of times flowed is the most, the length of series winding is the longest, runner is the longest, cold and hot dose of heat exchange is the most abundant, and when temperature when cryogen flows out flows into thermit powder, temperature difference is the least, and the efficiency of recuperation of heat is the highest.
Experiment proves that, reclaim the heat energy of low discharge thermit powder, this utility model is compared with detachable plate type heat exchanger, there is volume little, price is low, waste heat recovery is more thorough, if the loop of this utility model series winding is long, it is possible to achieve temperature when temperature only flows into than thermit powder when cryogen flows out is low 0.5 degree.
The above is only better embodiment of the present utility model, therefore all equivalence changes done according to structure, feature and the principle described in this utility model patent claim or modification, all it is included in this utility model patent claim.
Claims (4)
1. an inside has and connects, having the efficient brazed-plate heat exchanger of series winding, including end plate (3), plate one (4), plate two (7), plate three (8), base plate one (11) or base plate two (14), it is characterised in that: between end plate (3) and plate two (7), between plate two (7) and plate three (8), between plate two (7) or plate three (8) and base plate one (11) or base plate two (14) and connect install equal number plate one (4)；Plate one (4) and previous section series winding between plate two (7) and plate two (7) and plate three (8) form a long runner；Plate one (4) and previous section between plate three (8) and plate three (8) and next plate two (7) are contacted again and are formed a longer runner；Repeating mounting tile two (7) and plate three (8) between end plate (3) and base plate one (11) or base plate two (14), series winding can form a runner the longest successively.
Inside the most according to claim 1 has and connects, having the efficient brazed-plate heat exchanger of series winding, it is characterized in that: end plate (3) only 2 interface 11Q (1) and 14Q (2), plate one (4) has 4 holes, plate two (7) only 2 hole 12H (5) and 13H (6), plate three (8) only 2 hole 21Q (9) and 24Q (10), base plate one (11) only 2 interface 22H (12) and 23H (13), base plate two (14) only 2 interface 31Q (15) and 34Q (16)；When being even slice when using plate two (7) and plate three (8), the base plate of use is base plate one (11)；When being odd number sheet when using plate two (7) and plate three (8), the base plate of use is base plate two (14)；The interface of end plate and base plate can be to blurt out, it is also possible to is turned welt, it is also possible to is to connect pipe thread mouth；End plate (3) interface 11Q (1) is connected with the hole 12H (5) of plate two (7) by the runner of plate one (4), the hole 12H (5) of plate two (7) is connected with the hole 21Q (9) of plate three (8) by the runner of plate one (4), so being consecutively connected to base plate, last end plate (3) interface 11Q (1) communicates formation heat exchange runner with base plate one (11) interface 22H (12) or base plate two (14) interface 31Q (15)；Same end plate (3) interface 14Q (2) communicates formation heat exchange runner with base plate one (11) interface 23H (13) or base plate two (14) interface 34Q (16).
Inside the most according to claim 1 has and connects, having the efficient brazed-plate heat exchanger of series winding, it is characterized in that: between end plate (3) and plate two (7), between plate two (7) and plate three (8), between plate two (7) or plate three (8) and base plate one (11) or base plate two (14) and connect install equal number plate one (4), the sheet number that plate one (4) is installed is the most, cross section of fluid channel is long-pending the biggest, and cold and hot dose of metered flow is the biggest.
Inside the most according to claim 1 has and connects, having the efficient brazed-plate heat exchanger of series winding, it is characterized in that: between end plate (3) and base plate, repeat mounting tile two (7) and plate three (8), plate two (7) and plate three (8) the sheet number installed are the most, about the cold and hot dose number of times flowed is the most, the length of series winding is the longest, runner is the longest, cold and hot dose of heat exchange is the most abundant, when temperature when cryogen flows out flows into thermit powder, temperature difference is the least, and the efficiency of recuperation of heat is the highest.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620216198.1U CN205505826U (en) | 2016-03-15 | 2016-03-15 | There is parallel connection inside, has high -efficient brazed plate type heat exchanger of polyphone |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620216198.1U CN205505826U (en) | 2016-03-15 | 2016-03-15 | There is parallel connection inside, has high -efficient brazed plate type heat exchanger of polyphone |
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| Publication Number | Publication Date |
|---|---|
| CN205505826U true CN205505826U (en) | 2016-08-24 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620216198.1U Expired - Fee Related CN205505826U (en) | 2016-03-15 | 2016-03-15 | There is parallel connection inside, has high -efficient brazed plate type heat exchanger of polyphone |
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| CN (1) | CN205505826U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105674787A (en) * | 2016-03-15 | 2016-06-15 | 刘洋豪 | Efficient brazing plate type heat exchanger capable of achieving parallel and series connection insides |
-
2016
- 2016-03-15 CN CN201620216198.1U patent/CN205505826U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105674787A (en) * | 2016-03-15 | 2016-06-15 | 刘洋豪 | Efficient brazing plate type heat exchanger capable of achieving parallel and series connection insides |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160824 Termination date: 20180315 |