CN202229479U - Evaporator provided with elliptical flat spiral heat exchange tube - Google Patents
Evaporator provided with elliptical flat spiral heat exchange tube Download PDFInfo
- Publication number
- CN202229479U CN202229479U CN 201120241604 CN201120241604U CN202229479U CN 202229479 U CN202229479 U CN 202229479U CN 201120241604 CN201120241604 CN 201120241604 CN 201120241604 U CN201120241604 U CN 201120241604U CN 202229479 U CN202229479 U CN 202229479U
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- Prior art keywords
- heat exchange
- flat spiral
- spiral heat
- exchange tube
- evaporimeter
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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.)
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Abstract
The utility model discloses an evaporator provided with an elliptical flat spiral heat exchange tube. The evaporator includes an evaporator body and at least one elliptical flat spiral heat exchange tube, the elliptical flat spiral heat exchange tube is provided with a medium inlet and a medium outlet; the elliptical flat spiral heat exchange tube at least includes a tube body, the tube body is composed of a special-shaped tube section, and a first straight tube section and a second straight tube section which are respectively arranged at the two ends of the special-shaped tube section; the special-shaped tube section is provided with an elliptical flat cross section, the long axis and the short axis of the ellipse are arranged at an rotating included angle relative to the axis of the tube body. The evaporator provided adopted the elliptical flat spiral heat exchange tube greatly improves the heat exchange efficiency, and the whole heat exchange efficiency of the evaporator provided is greatly higher than that of the evaporator in the prior art, therefore, the evaporator provided has the advantages of low cost and convenient manufacturing. The evaporator provided is suitable to be applied to the industries of petroleum, chemicals, fertilizers, boilers, pharmacy, foodstuffs, electric power, nuclear energy, environmental protection, heat supply, household electrical appliances etc.
Description
Technical field
The utility model relates to the heat-exchange apparatus technical field, relates in particular to a kind of evaporimeter.
Background technology
The application of evaporimeter in industrial, civilian is very universal.The main effect of evaporimeter is exactly the high temperature refrigerant steam after cooling is compressed through refrigeration compressor and makes it liquefaction.Evaporimeter is different by its cooling medium, can be divided into water-cooled, air-cooled type, vaporation-type three major types.
Though evaporimeter of the prior art is of a great variety, all be to have used existing various heat exchanger tube.As everyone knows, heat exchanger tube is the critical component of heat transmission equipment, and the heat exchange efficiency of heat exchanger tube directly has influence on the operating efficiency of heat transmission equipment.The efficient of evaporimeter and energy-conservation core are heat exchanger tube.
Therefore, those skilled in the art is devoted to develop the evaporimeter that a kind of heat exchange efficiency is high, manufacturing is novel easily always.
The utility model content
Because the above-mentioned defective of prior art, the utility model technical problem to be solved provides the evaporimeter that a kind of heat exchange efficiency is high, oval flat spiral heat exchange tube is used in manufacturing easily.
For realizing above-mentioned purpose, the utility model provides a kind of evaporimeter of using oval flat spiral heat exchange tube, comprises device body and the flat spiral heat exchange tube of at least one ellipse; The flat spiral heat exchange tube of said ellipse has medium inlet and media outlet; The flat spiral heat exchange tube of said ellipse comprises body at least, and said body is made up of special-shaped pipeline section that is positioned at the middle part and first straight length, the second straight length one that lay respectively at said special-shaped pipeline section two ends; Said special-shaped pipeline section has oval flat cross section, and this long axis of ellipse has a rotation angle with the axis of the said relatively body of minor axis.
Preferably, the length of said major axis is greater than the diameter of said body.
Preferably, said first straight length and said second straight length be not for isometric or isometric.
Preferably, said body is a welded tube.
Preferably, said body is metal straight collimator or seamless straight collimator.
Preferably, said rotation angle is clockwise or counterclockwise.
Preferably, said rotation angle is 1 °-75 °.
Preferably, said body is the U type.
Preferably, said body is the S type.
Preferably, said evaporimeter is horizontal-type evaporator, vertical-type evaporator, spiral tube evaporator, cooling coil, air-cooler.
The evaporimeter of the utility model will be much higher than existing evaporimeter owing to adopted oval flat spiral heat exchange tube on the whole heat exchange efficiency of evaporimeter.
The utility model especially is suitable for the raw material of welded tube as heat exchanger tube; And the cost of welded tube is lower at least by about 20% than the cost that is used as the raw-material seamless straight collimator of heat exchanger tube (like copper pipe, stainless steel tube etc.) in the prior art, thereby the utility model has reduced the manufacturing cost of evaporimeter significantly.
And; The evaporimeter of the oval flat spiral heat exchange tube of the application of the utility model; Because oval flat spiral heat exchange tube can also have straight length, when making evaporimeter, the good sealing effect of straight length and device body; Be more suitable for the manufacturing technology of existing evaporimeter, be much higher than existing evaporimeter in its projected life and service life.
Further; Because first straight length and second straight length of the oval flat spiral heat exchange tube of the utility model can be not isometric, when making evaporimeter, borrow is installed easily like this; Greatly reduce limited space property, improved the utilization rate of the device space.
The oval flat spiral heat exchange tube that the utility model uses is more suitable for the manufacturing process of conventional evaporator, and it both is connected with the device body that expansible pastes, also can weld, but the while also expanded and welded tube joint be used in combination.
The oval flat spiral heat exchange tube that the utility model adopts, body can also be U type or S type, has greatly expanded application, goes for the evaporimeter of various kinds, model, specification.
The evaporimeter of the oval flat spiral heat exchange tube of the application of the utility model; Can be applied in the existing various evaporimeter; Like horizontal-type evaporator, vertical-type evaporator, spiral tube evaporator, cooling coil, air-cooler etc., have good effect of heat exchange, simple in structure, cost is low; Make beneficial effects such as facility, be applicable in the multiple industries such as oil, chemical industry, chemical fertilizer, boiler, pharmacy, food, electric power, nuclear energy, environmental protection, heat supply, household electrical appliances.
Description of drawings
Fig. 1 is the structural representation of embodiment 1 of the evaporimeter of the utility model.
Fig. 2 is the perspective view of the oval flat spiral heat exchange tube in embodiment illustrated in fig. 1.
Fig. 3 is the local structure for amplifying sketch map of A-A portion among Fig. 2.
The specific embodiment
Below will combine accompanying drawing that the technique effect of design, concrete structure and the generation of the utility model is described further, with purpose, characteristic and the effect of understanding the utility model fully.
Evaporimeter mainly partly is made up of device body, heat exchanger tube etc.As shown in Figure 1, a kind of evaporimeter of using oval flat spiral heat exchange tube of present embodiment mainly comprises device body and at least one heat exchanger tube, evaporating liquid steam-gas inlet 4, evaporating liquid vapor outlet port 5, and other associated conduit.
The special feature of the utility model is that heat exchanger tube is oval flat spiral heat exchange tube 1.Like Fig. 2, shown in Figure 3, the oval flat spiral heat exchange tube 1 in the utility model, its main body is the body of a metal, especially, is the metal welded tube in the present embodiment.Body surrounds and forms the medium channel that a confession heat transferring medium circulates therein, with the heat exchange of medium inside and outside the realization body.
In the utility model, body is by the special-shaped pipeline section 10 that is positioned at the middle part, and first straight length 11, second straight length, 12 one that lay respectively at special-shaped pipeline section 10 two ends constitute.
Abnormity pipeline section 10 has oval flat cross section, and this long axis of ellipse has a rotation angle with the axis of the relative body of minor axis.
In the present embodiment, the length of the major axis of special-shaped pipeline section 10 is greater than the diameter of body.
Further, first straight length 11 and second straight length 12 are isometric for not.Its beneficial effect is; The oval flat spiral heat exchange tube of the utility model is when being used to assemble evaporation equipment; Because the pitch space of tube sheet is limited, adopt the not isometric straight length in two ends, when assembling just in the past an end by means of size; To make full use of the space between the tube sheet, improved the convenience that evaporation equipment is installed.
Certainly, in the ordinary course of things, also can adopt first straight length 11 and second straight length 12 for isometric.
Particularly, in different embodiment, above-mentioned rotation angle can be for clockwise, also can be for counterclockwise.
The rotation angle can be chosen according to actual conditions in 75 ° at 1 °.Generally speaking, the size of rotation angle is relevant with the length of body, and the length of body is long more, and the rotation angle that can take is also just big more.Selecting for use of above-mentioned various rotation angles, also relevant with the hydrodynamics attribute of heat transferring medium, be not restriction to the utility model.
The technique scheme of the utility model applicable to stainless steel straight collimator (seamless steel pipe), is particularly useful for the metal welded tube.
Oval flat spiral heat exchange tube in the utility model is not also owing to have cold working after the tubulation moulding, so internal structure stress eliminates basically, and anti-fouling tendency, corrosion resistance are better.The utility model also has simple in structure, and cost is low, makes more beneficial effect such as facility.
According to client's needs, the entire length of the oval flat spiral heat exchange tube in the utility model can be chosen between tens of rice at 0 meter.Certainly, if the reasonable disposition heat-treatment furnace, the entire length of the oval flat spiral heat exchange tube in the utility model can also be in random length, and is not subject to the specification of cold working equipment.
Process conditions, the structural safety that perfect evaporimeter should satisfy reasonably to realize defined when design or type selecting be reliable, be convenient to make, installation, Operation and maintenance and economically rationally.Therefore, in the design process of evaporimeter, give one's full attention to the harmony of each parameter.
Oval flat spiral heat exchange tube has constituted the heat-transfer area of evaporimeter, and the size and dimension heat exchanging of oval flat spiral heat exchange tube has very big influence.When adopting the heat exchanger tube of minor diameter, the heat exchange area of evaporimeter unit volume is big, and equipment is compact, and the metal wastage of unit heat transfer area is few, and heat transfer coefficient is also higher.Therefore, to the large diameter heat exchanger tube of the general selection of the big perhaps dirty fluid of viscosity, the fluid that cleans is generally selected the heat exchanger tube of minor diameter.
The parameter of the material of heat exchanger tube is selected and should be confirmed according to pressure, temperature and the corrosivity of medium.
The arrangement of heat exchanger tube on the device body singly will do not considered the compactedness of equipment, also will consider the situation of character, structural design and the processing and manufacturing aspect of fluid.
The selection of heat exchanger tube centre-to-centre spacing should be considered the compactedness of structure on the device body, and heat-transfer effect is considered the intensity and the required space of scavenging duct outer surface of device body again.
In addition, also need consider the fixing means of heat exchanger tube on the device body.If spacing is too little, when employing was welded to connect, the weld seam of adjacent two heat exchanger tubes was too near, and weldquality is influenced by heat and is difficult to obtain assurance; If adopt expanded joint, extruding force possibly cause the device body that excessive distortion takes place, and loses the adhesion between heat exchanger tube and device body.The centre-to-centre spacing of the general heat exchanger tube that adopts is not less than 1.25 times of heat exchanger tube external diameter.
In other embodiments, oval flat spiral heat exchange tube also can be made U type or S type as required.
A kind of heat transferring medium that only circulates in the evaporimeter of the oval flat spiral heat exchange tube of above-mentioned various application of the utility model, with other outer Medium Exchange heats of evaporimeter.
The oval flat spiral heat exchange tube that the utility model uses is compared with other structure heat exchanger tubes of equivalent diameter in the prior art; Though cross-sectional area is identical; But the flow-disturbing effect is obvious in the oval flat spiral heat exchange tube, and its heat exchange efficiency greatly improves, and has also further reduced the energy consumption of evaporimeter.
The oval flat spiral heat exchange tube that the utility model uses because the flow-disturbing effect in the pipe, less scaling, the anti-tartar performance is good, so the evaporimeter of the utility model also have less scaling, the characteristics that the anti-tartar performance is good.
In sum, the just several kinds of preferred embodiment of the utility model described in this specification, above embodiment is only unrestricted in order to the technical scheme of explanation the utility model.All technical staff in the art according to the design of the utility model on the basis of existing technology through the available technical scheme of logical analysis, reasoning, or a limited experiment, all should be within the claim protection domain of the utility model.
Claims (10)
1. an evaporimeter of using oval flat spiral heat exchange tube is characterized in that: comprise device body and the flat spiral heat exchange tube of at least one ellipse; The flat spiral heat exchange tube of said ellipse has medium inlet and media outlet; The flat spiral heat exchange tube of said ellipse comprises body at least, and said body is made up of special-shaped pipeline section that is positioned at the middle part and first straight length, the second straight length one that lay respectively at said special-shaped pipeline section two ends; Said special-shaped pipeline section has oval flat cross section, and this long axis of ellipse has a rotation angle with the axis of the said relatively body of minor axis.
2. use the evaporimeter of oval flat spiral heat exchange tube according to claim 1, it is characterized in that: the length of said major axis is greater than the diameter of said body.
3. use the evaporimeter of oval flat spiral heat exchange tube according to claim 1, it is characterized in that: said first straight length and said second straight length be not for isometric or isometric.
4. use the evaporimeter of oval flat spiral heat exchange tube according to claim 1, it is characterized in that: said body is a welded tube.
5. use the evaporimeter of oval flat spiral heat exchange tube according to claim 1, it is characterized in that: said body is the metal straight collimator.
6. use the evaporimeter of oval flat spiral heat exchange tube according to claim 1, it is characterized in that: said rotation angle is clockwise or counterclockwise.
7. use the evaporimeter of oval flat spiral heat exchange tube according to claim 1, it is characterized in that: said rotation angle is 1 °-75 °.
8. use the evaporimeter of oval flat spiral heat exchange tube according to claim 1, it is characterized in that: said body is the U type.
9. use the evaporimeter of oval flat spiral heat exchange tube according to claim 1, it is characterized in that: said body is the S type.
10. use the evaporimeter of oval flat spiral heat exchange tube according to claim 1, it is characterized in that: said evaporimeter is horizontal-type evaporator, vertical-type evaporator, spiral tube evaporator, cooling coil, air-cooler.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201120241604 CN202229479U (en) | 2011-07-11 | 2011-07-11 | Evaporator provided with elliptical flat spiral heat exchange tube |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN 201120241604 CN202229479U (en) | 2011-07-11 | 2011-07-11 | Evaporator provided with elliptical flat spiral heat exchange tube |
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CN202229479U true CN202229479U (en) | 2012-05-23 |
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CN 201120241604 Expired - Fee Related CN202229479U (en) | 2011-07-11 | 2011-07-11 | Evaporator provided with elliptical flat spiral heat exchange tube |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102331114A (en) * | 2011-07-11 | 2012-01-25 | 上海科米钢管有限公司 | Evaporator applying elliptical flat spiral heat exchange pipe |
CN103245227A (en) * | 2013-04-28 | 2013-08-14 | 王云清 | Flue gas waste heat recovery element and device capable of breaking through low temperature dew point |
-
2011
- 2011-07-11 CN CN 201120241604 patent/CN202229479U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102331114A (en) * | 2011-07-11 | 2012-01-25 | 上海科米钢管有限公司 | Evaporator applying elliptical flat spiral heat exchange pipe |
CN103245227A (en) * | 2013-04-28 | 2013-08-14 | 王云清 | Flue gas waste heat recovery element and device capable of breaking through low temperature dew point |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120523 Termination date: 20120711 |