Patent Application
20210018281
The invention refers to a heat exchanger element and a method for manufacturing a heat exchanger element.
Heat transfer enhancement between solid surfaces and fluids is relevant for heat exchangers, which are applied in all kind of technical applications and their performance has a large impact on the overall efficiency. Heat exchangers transfer thermal energy (heat) from a solid heat source to a cooling fluid, from a warm fluid to a solid heat sink, or between several fluids that are separated by a solid heat exchanger wall. Classical heat transfer enhancement techniques incorporate one or a combination of either increase of heat exchanger surface, increase of fluid velocities and promotion of turbulence in the fluid-side thermal boundary layer or influencing surface wettability and nucleation site activity in case of boiling and condensation (R. L. Webb, “Principals of enhanced heat transfer”, Wiley, 1994).
For an increase of heat exchanger surface, surface extensions with fins are used. Most designs also promote turbulence in the boundary layer by segmenting the enhanced surfaces.
Another enhancement technique is to increase fluid velocities: Insert devices provide a periodic acceleration/deceleration of the fluid as well as turbulence in the fluid-side thermal boundary layer by periodically changing the flow cross-section. Swirl flow devices, for example, increase the fluid velocity by forcing the fluid on a swirling or helical streamline. In addition, some active techniques such as acoustic or electric fields and surface vibration are used to promote turbulence in the fluid. The artificial increase of the surface roughness mainly effects the formation of a thermal boundary layer, but has negligible influence on the surface area. The increase of roughness may be achieved by surface coatings incorporating relatively large particles.
Influencing surface wettability and nucleation site activity in case of boiling and condensation is yet another enhancement possibility. This can be achieved by surface coatings that change the surface energy of the heat exchanger wall. The surface energy influences the wetting angle, which has a significant influence on two-phase heat transfer in both boiling and condensation. Porous surfaces are also used to enhance nucleate boiling by providing artificial nucleation sites.
In Connor et al. “A dielectric surface coating technique to enhance boiling heat transfer from high power microelectronics”, IEEE Transactions on Components, Part A:, 18(3), 1995, an example for enhancement of boiling heat transfer in power micro-electronic devices by surface coatings with solid particles is disclosed: Al2O3 particles and diamond particles of 1 to 12 μm size are bonded to the surface with paint in layers up to 50 μm thickness. The microporous surface provides additional nucleation sites and enhances the nucleate boiling heat transfer by approximately factor two. Also, US 2007/0230128 A1 contains a method for two-phase cooling of heat generating electronic elements. It describes the microporous surface coating of a submerged heater surface with nickel particles of 30 to 50 μm size. The porous surface increases the density of boiling nucleation sites. Coatings with solid particles are also proposed in DE10 2012 108 602 A1, wherein coatings with a 10-500 μm thickness are shown, wherein the coating is made out of sand fixed to the surface with a polymer binder. The sand is an aggregate of solid particles of mineral origin as given in EN 12620 and EN 13139 with D50≥300 μm particle size.
Further, in Rahman et al., “Increasing Boiling Heat Transfer using Low Conductivity Materials”, Scientific Reports 5, 13145, 2015 a micro-structured matrix of insulating material is embedded on the surface of a good thermal conductor, which yields different surface temperatures during nucleate boiling and distinct areas of liquid and vapour flows. The micro-convection and the bubble dynamics increase the nucleate boiling heat transfer.
Also, influence of surface treatments on the heat flux from copper samples to liquid nitrogen is investigated in Hellmann et al., “Influence of Different Surface Treatments on the Heat Flux from Solids to Liquid Nitrogen”, IEEE Transactions on Applied Superconductivity, 24(3), 1-5, 2014. The cool-down of samples from room-temperature to liquid nitrogen temperature (78 K) show an improved cooling with Kapton coating. The effect is explained by the lower thermal conductivity of Kapton, which reduces the surface temperature and yields a better boiling heat transfer regime to the liquid nitrogen in this transient cool-down process.
In an embodiment, the present invention provides a heat exchanger element for being in contact with a gas. The heat exchanger element includes a solid surface coated with a layer of a predetermined material. The layer is configured to enhance the heat transfer between the solid surface and the gas by thermo-acoustic impedance matching.
The present invention will be described in even greater detail below based on the exemplary figures. The invention is not limited to the exemplary embodiments. All features described and/or illustrated herein can be used alone or combined in different combinations in embodiments of the invention. The features and advantages of various embodiments of the present invention will become apparent by reading the following detailed description with reference to the attached drawings which illustrate the following:
The known heat transfer enhancement techniques of the state of the art in case of heat transfer to single-phase flow have the general disadvantage of an increased pressure drop, which foils the energetic benefit of heat transfer enhancement—particularly in case of gas flow.
The present invention includes an improved heat exchanger element, which has an enhanced heat transfer capability and where the pressure drop is not increased.
The present invention further includes a cost-effective method for manufacturing a heat exchanger element with enhanced heat transfer capability.
A heat exchanger element for being in contact with a gas according to the invention comprises one or more solid surface(s). Meaning as such, that a heat exchanger element can have areas, which are coated and areas without any coating. At least one of these areas, one which is in contact with the heat exchanger fluid, here a gas, can be coated. According to the invention, said solid surface is coated with one or more layer(s) of predetermined material, the layer being suitable to enhance the heat transfer between the solid surface and said fluid by thermo-acoustic impedance matching.
This layer is a homogeneous material layer, whereas such a consistent material layer works for a single-phase fluid, such as any gas, effectively. The gas as the heat exchanging fluid can be a pure gas, a mixture of gases or an aerosol, i.e. a suspension of particles and/or droplets in a gaseous phase. The physical basis for the layer can be explained as follows:
Classical heat transfer theory is based on the concept of a thermal (as well as hydrodynamic) boundary layer, whereby the temperature of the fluid in contact with the wall is equal to the wall temperature and a decline in temperature occurs as
A fundamentally different behaviour was discovered by P. L. Kapitza (“The study of Heat Transfer on Helium II”, Journal of Physics (USSR) 4, 181, 1941), who found a temperature step during heat transfer from a solid wall to the quantum fluid Helium II, as shown in
As a general consequence of the Kapitza resistance, the differences in both the thermo-acoustic impedances and other thermal properties of the solid and the gas are responsible for the thermal resistance and thus the temperature step at the interface.
The layers of predetermined materials and the layer thicknesses are chosen such that the heat transfer between the solid surface and the gas is enhanced by thermo-acoustic impedance matching between all the layers in contact with each other. With this implementation, the sum of thermal resistances and thus the overall temperature difference between the solid surface and the gas is smaller than in case of the uncoated solid surface. Candidates for the coating and therefore examples for the predetermined materials are materials with intermediate values of thermo-acoustic impedance. This promotes in particular non-metallic amorphous materials rather than crystalline materials, as the latter have impedances in the range of metals or beyond.
Further, according to the invention, said solid surface can have at least one flat section or at least one section with a predetermined structuring or topology or a combination of both. The heat transfer enhancement according to the invention can be applied on either side of said solid surface. Further, it can be combined with the other enhancement methods, in particular with surface enhancement methods.
The heat exchanger element and or its surface can be made out of any suitable solid, such as copper, aluminum, steel, silicon, graphene or diamond, for example.
According to the invention, the solid surface has either at least one section which has a tubular shape with an outer surface and/or an inner surface both with a curvature, either concave or convex, as for example a tube segment, or which has at least one section which has a cylindrical shape with an outer surface and/or an inner surface, as for example a cylindrical body with a bore. The heat transfer enhancement according to the invention can be applied on either side of said solid surface. Further, it can be combined with the other enhancement methods, in particular with surface enhancement methods. The heat exchanger element and or its surface can be made out of any suitable solid, such as copper, aluminum, steel, silicon, graphene or diamond, for example.
Heat transfer enhancement between solid surfaces and gases can be applied by means of thermo-acoustic impedance matching. Thermo-acoustic impedances depend on the speed of sound and the mass density. The values for solids and gases can differ by several orders of magnitude. The layer materials and the layer thicknesses might be chosen such that the heat transfer between the solid surface and the gas is enhanced by thermo-acoustic impedance matching between all the layers in contact with each other. If the layer is too thin for the phonon excitation, there will be no effect of the layer, if it is too thick, said layer will function as a thermal insulator.
With this, the sum of thermal resistances and thus the overall temperature difference between the solid surface and the gas is smaller than in case of the uncoated solid surface. This is counter-intuitive with regard to classical heat transfer theory, where such coating would act as thermal insulation and worsen the heat transfer due to the additional thermal resistance(s) of the layer(s). Candidates for the coating are materials with intermediate values of thermo-acoustic impedance. This promotes in particular non-metallic amorphous materials rather than crystalline materials, as the latter have impedances in the range of metals or beyond.
The values for solids, liquids and gases differ by orders of magnitude as shown by the example data in Tab. 1.
For instance, the implementation of a LD-PE coating on a steel surface would enhance the heat transfer to gaseous nitrogen (or air) at 293 K, because the impedance (1.8E+06) is in-between that of steel (4.6E+07) and that of nitrogen gas (4.0E+02). On the other hand, the same LD-PE coating would have a negligible or even negative effect in case of heat transfer to water at 293 K, because the impedances of water (1.5E+06) and LD-PE are nearly the same and the LD-PE layer would thus not improve the thermo-acoustic impedance matching and only act as an additional thermal insulator. Depending for which gas the heat transfer has to be enhanced, the best layer-coating can be chosen and used. The effect is very effective for the heat transfer enhancement between solids and gases, which show the largest mismatch in thermo-acoustic impedance.
Due to the mechanism of phonon propagation, the thickness(es) of the coating layer(s) is one design parameter for thermo-acoustic impedance matching, beside the choice of the layer material. Preferably, said layer can have a thickness in a range between 1 μm to 100 μm. Thinner layers of non-matching material might therefore be applied on the surface next to the gas, without disturbing the thermo-acoustic impedance matching. An example are sub-micron metallic layers for UV or corrosion protection, for the prevention of fouling or for optical reasons. The thickness can be adapted according to phonon propagation properties of specific materials.
In a further embodiment, said solid surface can be coated with several layers out of different predetermined materials and having different thicknesses.
In a preferred embodiment, said heat exchanger element can be manufactured according to the method described according to the invention. This enables a simple and cost-efficient manufacturing of an enhanced heat exchanger element. For being in contact with a gas, said heat exchanger element comprises one or more solid surface(s). The manufacturing comprises the step of coating said solid surface with one or more layer(s) of predetermined material, wherein said layer is suitable to enhance the heat transfer between the solid surface and said gas by thermo-acoustic impedance matching.
In another embodiment of the invention, coating of said layer is performed onto the solid surface by slot-die coating, doctor blading, dip coating, spray painting or alternatively by the lamination of films. These methods can be used continuously (roll-to-roll).
In
Onto the solid surface 2 a layer 4 is coated, so that the layer 4 is part of the heat exchanger element 1.
The heat transfer direction is represented by arrow 5 and the generated temperature profile is depicted by curve 6. The temperature profile results from the consideration of both Kapitza conductance and thermal boundary theory in case of a gas 3 flowing along a heat exchanger element 1. The total temperature difference results from the first and second temperature steps 6a, 6b, a temperature gradient 6c and a thermal boundary layer 6d (shown by curve 6). Due to thermo-acoustic impedance matching, the total temperature difference 7b between the surface 2 and the gas 3 is smaller than the temperature difference of the uncoated wall, which would result in a larger temperature difference 7a (indicated by the dashed lines). As the layer 4 does not influence the thermal boundary layer by the promotion of turbulence, the heat transfer enhancement is due to thermo-acoustic impedance matching.
In
Further, in
While the invention has been illustrated and described in detail in the drawings and foregoing description, such illustration and description are to be considered illustrative or exemplary and not restrictive. It will be understood that changes and modifications may be made by those of ordinary skill within the scope of the following claims. In particular, the present invention covers further embodiments with any combination of features from different embodiments described above and below.
The terms used in the claims should be construed to have the broadest reasonable interpretation consistent with the foregoing description. For example, the use of the article “a” or “the” in introducing an element should not be interpreted as being exclusive of a plurality of elements. Likewise, the recitation of “or” should be interpreted as being inclusive, such that the recitation of “A or B” is not exclusive of “A and B,” unless it is clear from the context or the foregoing description that only one of A and B is intended. Further, the recitation of “at least one of A, B and C” should be interpreted as one or more of a group of elements consisting of A, B and C, and should not be interpreted as requiring at least one of each of the listed elements A, B and C, regardless of whether A, B and C are related as categories or otherwise. Moreover, the recitation of “A, B and/or C” or “at least one of A, B or C” should be interpreted as including any singular entity from the listed elements, e.g., A, any subset from the listed elements, e.g., A and B, or the entire list of elements A, B and C.
1 Heat exchanger element
2 Solid Surface
3, 3′ Gas
4, 4′, 4″ Layer
5 Heat flux
6 Temperature profile
6
a,
6
a′ First temperature step
6
b,
6
b′ Second temperature step
6
c,
6
c′ Temperature gradient in the layer
6
d,
6
d′ Temperature gradient in the boundary layer
7 Overall temperature difference
7
a Temperature difference of an uncoated surface
7
b Temperature difference of a surface coated with one layer
7
c Temperature difference of a surface coated with more than one layer
| Number | Date | Country | Kind |
|---|---|---|---|
| 17401041.3 | Apr 2017 | EP | regional |
This application is a U.S. National Phase Application under 35 U.S.C. § 371 of International Application No. PCT/EP2018/000057, filed on Feb. 13, 2018, and claims benefit to European Patent Application No. EP 17401041.3, filed on Apr. 7, 2017. The International Application was published in English on Oct. 11, 2018 as WO 2018/184712 under PCT Article 21(2).
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2018/000057 | 2/13/2018 | WO | 00 |
