Patent Application
20080054217
This application is based on Japanese Patent Application No. 2006-241582 filed on Sep. 6, 2006, the content of which is incorporated herein by reference in its entirety.
1. Field of the Invention
The present invention relates to a heat transport fluid, a heat transport structure, and a heat transport method.
2. Description of the Related Art
A heat transport fluid used for a heat exchanger is required to have a high heat transfer coefficient. Dr. Choi et al. discloses that a heat transfer coefficient of ethylene glycol is improved by adding a small amount of nano (submicron) cluster in “Anomalously increased effective thermal conductivities of ethyleneglycol-based nanofluids containing copper nanoparticles, Applied Physics Letters, 2001, vol. 78, pp. 718-720.” However, recently, the transport fluid is required to have a higher heat transfer coefficient.
In view of the foregoing problems, it is an object of the present invention to provide a heat transport fluid, a heat transport structure, and a heat transport method having a high heat transfer coefficient.
A heat transport fluid according to an aspect of the invention includes a solvent, particles dispersed in the solvent, coating agents attached to surfaces of the particles, and organic components dispersed in the solvent.
In this transport fluid, a change between a structured state and an unstructured state is a phase change, and an energy level of the unstructured state is higher than that of the structured state by an energy corresponding to the phase change. Thus, the heat transport fluid phase-changes in accordance with the temperature. Accordingly, this heat transport fluid has a high heat transfer coefficients.
For example, the organic components may include an organic substance having at least a sulfur atom, a straight-chain organic substance, a cyclic organic substance, an organic substance having a disulfide, an organic substance having a quaternary ammonium, or an organic substance having a primary amine. For example, the organic substance having a disulfide may have a straight-chain molecular structure or may have a carbon number in a range from 8 to 36. Alternatively, the organic substance having a disulfide may include octadecyl disulfide.
Alternatively, the coating agents may include an organic substance having at least a sulfur atom, a straight-chain organic substance, or a cyclic organic substance. For example, an average particle size of the particles may be 10 nm or smaller. The particles may be made of an inorganic material or a metal.
The solvent may be water. In this case, the particles are made of gold, and the coating agents are made of a compound having a hydrophilic group. Alternatively, the solvent may be toluene. In this case, the particles are made of gold, and the coating agents are made of a compound having a hydrophobic group.
The heat transport fluid may be used for a heat transport structure that includes a first member having a first temperature, a second member having a second temperature higher than the first temperature, and a circulation device for circulating the heat transport fluid through the first member and the second member.
Furthermore, the heat transport fluid may be used for a heat transport method that includes a step of preparing a first member having a first temperature, a step of preparing a second member having a second temperature higher than the first temperature, and a step of circulating the heat transport fluid through the first member and the second member, for transporting heat from the second member to the first member.
Additional objects and advantages of the present invention will be more readily apparent from the following detailed description of preferred embodiments when taken together with the accompanying drawings. In the drawings:
A heat transport fluid 19 according to a first embodiment of the invention includes a solvent, particles 1 dispersed in the solvent, coating agents 7 attached to surfaces of the particles 1, and organic components 3.
When a temperature of the heat transport fluid 19 is a first predetermined temperature or lower, the organic components 3 are structured. In contrast, when the temperature is equal to or higher than a second predetermined temperature, which is higher than the first temperature, the organic components 3 are unstructured. Thereby, the heat transport fluid 19 changes between a structured state and an unstructured state in accordance with the temperature of the heat transport fluid within a working temperature range.
Specifically, when the temperature is the first predetermined temperature or lower within the working temperature range (e.g., from about −30 to 150° C.), the organic components 3 are arranged on the surfaces of the particles 1, thereby solvent elements 5 (solvent molecules) are also arranged on the surfaces of the particles 1 (i.e., the structured state), as shown in
A change of the heat transport fluid 19 between the structured state and the unstructured state is a phase change, and an energy level of the unstructured state is higher than that of the structured state by an energy corresponding to the phase change. Thus, the heat transport fluid 19 phase-changes in accordance with the temperature.
In the structured state, the organic components 3 and the solvent elements 5 may be arranged in an area surrounded by the particles 1, as shown in
Temperatures between which the heat transport fluid 19 phase-changes (i.e., the first predetermined temperature and the second predetermined temperature) may be controlled in accordance with the working temperature range. The temperature under which the phase change occurs is changed in accordance with materials and contents of the organic components 3, the particles 1, and the solvent, for example.
As the material of the organic components 3, an organic substance having at least a sulfur atom, a straight-chain organic substance, a cyclic organic substance, an organic substance having a quaternary ammonium, an organic substance having a primary amine, an organic substance having a disulfide (e.g., having a straight-chain molecular structure), n-octadecanoic thiol, or mercaptosuccinic acid may be used, for example. The organic substance having a disulfide includes octadecyl disulfide having a carbon number of 18, for example.
The heat transport fluid 19 includes the coating agents 7 attached to the surfaces of the particles 1, thereby the particles 1 can be stably dispersed in the solvent. As a material of the coating agents 7, an organic substance having at least a sulfur atom, a straight-chain organic substance, a cyclic organic substance, an organic substance having a quaternary ammonium, an organic substance having a primary amine, n-octadecanoic thiol, or a mercaptosuccinic acid may be used, for example. The organic components 3 and the coating agents 7 may be made of the same material or different materials. Alternatively, the organic components 3 may include the same material as the coating agents 7 and an additional material. When the organic components 3 and the coating agents 7 are made of the same material, a content of the material is set to be the sum of a content required for coating the surfaces of the particles 1 and functioning as the coating agents 7, and a content required for functioning as the organic components 3.
A preferred average particle size of the particles 1 is 10 nm or smaller. A lower limit of the average particle size is not determined but preferred to be a particle size corresponding to a few atoms. As the material of the particles 1, a metal such as Au, Ag, Cu, Fe, and Ni, an inorganic material such as Si and F, an oxide such as Al2O3, MgO, CuO, Fe2O3, and TiO, or a polymer made of a resin may be used, for example. The particles 1 may be made of two or more materials. Specifically, a part of the particles 1 may be made of different material with another part of the particles 1.
The material of the solvent includes at least one of water, toluene, and ethylene glycol, for example. An example of a combination of the solvent, the particles 1, and the coating agents 7 includes water as the solvent, the particles 1 made of Au, and the coating agents 7 made of a composition having a hydrophilic group such as mercaptosuccinic acid, for example. Another example of the combination includes toluene as the solvent, the particles 1 made of Au, and the coating agents 7 made of a composition having a hydrophobic group such as n-octadecanoic thiol. The heat transport fluid 19 may further include a freezing-point depressant such as potassium acetate.
A manufacturing method of a heat transport fluid FE according to an example of the first embodiment will be described below. At first, 50 ml of 30 mmol/L HAuCl4 aqueous solution is added to a solution, in which 3.75 mmol of tetraoctylammonium bromide is added to 100 ml of toluene, and is stirred sufficiently. Next, 4.5 mmol of octadecanoic thiol is added to the solution and is stirred sufficiently. Then, a solution including 15 mmol of NaBH4 is added, and is stirred sufficiently. At last, surplus tetraoctylammonium bromide and octadecanoic thiol are removed by using methanol or ethanol.
This manufacturing method is called a two-phase reduction method (Brust method). In this method, octadecanoic thiol is added to the solution by three times more than Au. The heat transport fluid FE formed by this method includes toluene as the solvent, the particles 1 made of Au, octadecanoic thiol as the coating agents 7, and octadecyl disulfide as the organic components 3. In the heat transport fluid FE, the particles 1 have the average particle size about 2 nm.
Next, a thermal quantity of the heat transport fluid FE is measured with a differential scanning calorimeter about in a range from −30 to 60° C. at a rate about 5° C./min. As a result, the thermal quantity of the heat transport fluid FE changes about in a range from 10 to 25° C. Here, the temperatures between which the thermal quantity changes correspond to the temperatures between which the heat transport fluid FE phase-changes.
Additionally, thermal conductivities of the heat transport fluid FE and toluene as a reference are measured by a thin wire method. At first, a metal thin wire (e.g., a Pt wire having a diameter about 50 μm) is strained in a sufficiently large measuring medium (e.g., about 20 mm in diameter). Then, a predetermined amount of a thermal flow is generated by current heating from a time t=0 and flows out from a surface of the thin wire. The predetermined thermal flow is set so that a temperature of the thin wire increases about by 1° C. during a measurement (i.e., from about 0.3 to 0.6 A in current value). The temperature of the thin wire increases with time in accordance with a formula including thermal properties of the measuring medium such as the thermal conductivity and a specific heat. Thus, the thermal conductivity can be obtained by measuring an increase of the temperature and applying the measured value to the formula.
A thermal conductivity ratio (λ1/λ2) of the heat transport fluid FE to toluene is calculated based on a thermal conductivity (λ1) of the heat transport fluid FE and a thermal conductivity (λ2) of toluene measured by the above-described method. As shown in
Next, a heat transport fluid CE according to a comparative example is manufactured as described below. At first, Au nano particles coated by polyvinylpyrrolidone are prepared. Next, polyvinylpyrrolidone as a ligand is exchanged for octadecanoic thiol. Then, surplus octadecanoic thiol is removed by using methanol or ethanol.
The heat transport fluid CE includes toluene as the solvent, the particles 1 made of Au, and octadecanoic thiol as the coating agents 7, but does not include the organic components 3, which is included in the heat transport fluid FE. Therefore, an organic content of the heat transport fluid CE is lower than that of the heat transport fluid FE by the content of the organic components 3, as shown in
A thermal quantity of the heat transport fluid CE is measured with the differential scanning calorimeter. A change of the thermal quantity is smaller than that of the heat transport fluid FE. Thus, the heat transport fluid CE does not phase-change even when the temperature changes.
Additionally, a thermal conductivity (λ3) of the heat transport fluid CE and the thermal conductivity (λ2) of toluene as the reference are measured, and a thermal conductivity ratio (λ3/λ2) of the heat transport fluid CE to toluene is calculated. As shown in
A heat transport structure according to a second embodiment of the invention includes a first member having a first temperature and a second member having a second temperature higher than first temperature, and circulation device for circulating a heat transport fluid through the first member and the second member. When the first temperature is lower than the first predetermined temperature of the first embodiment, and the second temperature is higher than the second predetermined temperature of the first embodiment, a heat transfer coefficient of the heat transport structure is improved by using the heat transport fluid 19 according to the first embodiment.
Specifically, when the heat transport fluid 19 in the structured state flows into the second member having the second temperature higher than the second predetermined temperature, the heat transport fluid 19 receives a heat corresponding to the phase change in addition to a heat due to a normal thermal conduction, thereby the heat transport fluid becomes the unstructured state having a high energy level, as shown in
This heat transport structure can be used for a cooling device 11 for a vehicular engine, for example. As shown in
The cylinder block 15 and the cylinder head 17 have temperatures higher than a temperature under which the phase change of the heat transport fluid 19 occurs, and the radiator 13 has a temperature lower than the temperature under which the phase change occurs. Therefore, when the heat transport fluid 19 flows into the cylinder block 15 and the cylinder head 17, the heat transport fluid 19 receives the heat corresponding to the phase change in addition to heat due to a normal thermal conduction, thereby the heat transport fluid 19 is in a high energy level and becomes the unstructured state. In contrast, when the heat transport fluid 19 flows into the radiator 13, the heat transport fluid 19 releases the heat corresponding to the phase change in addition to the heat due to the normal thermal conduction, thereby the heat transport fluid 19 becomes the structured state. Thus, the heat transport fluid 19 has the pseudo latent heat transport effect, thereby the heat transfer coefficient of the heat transport fluid 19 increases. As a result, the cooling device 11 has a high heat transfer coefficient.
Such changes and modifications are to be understood as being within the scope of the present invention as defined by the appended claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2006-241582 | Sep 2006 | JP | national |
