Heat exchanger and cooling method
US-11994346-B2 · May 28, 2024 · US
US2016223274A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016223274-A1 |
| Application number | US-201514979404-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 27, 2015 |
| Priority date | Feb 4, 2015 |
| Publication date | Aug 4, 2016 |
| Grant date | — |
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A heat exchanger includes: a first flow passage where first liquid flows; a second flow passage where second liquid flows; and a heat exchanger main body configured to exchange heat between the first liquid and the second liquid. The heat exchanger main body includes a cross-sectional area adjuster configured to change a flow passage cross-sectional area of at least one of the first flow passage and the second flow passage by thermal deformation. The cross-sectional area adjuster adjusts a value of the flow passage cross-sectional area in a low temperature range to be larger than a value of the flow passage cross-sectional area in a high temperature range.
Opening claim text (preview).
What is claimed is: 1 . A heat exchanger, comprising: a first flow passage where first liquid flows; a second flow passage where second liquid flows; and a heat exchanger main body configured to exchange heat between the first liquid and the second liquid, the heat exchanger main body including a cross-sectional area adjuster configured to change a flow passage cross-sectional area of at least one of the first flow passage and the second flow passage by thermal deformation, the cross-sectional area adjuster adjusting a value of the flow passage cross-sectional area in a low temperature range to be larger than a value of the flow passage cross-sectional area in a high temperature range. 2 . The heat exchanger according to claim 1 , wherein a decrease rate of kinetic viscosity, which is a decrease rate of a value of kinetic viscosity in a high temperature range relative to a value of kinetic viscosity in a low temperature range of the second liquid, is smaller than the decrease rate of kinetic viscosity of the first liquid, the cross-sectional area adjuster changes at least the flow passage cross-sectional area of the first flow passage, and the cross-sectional area adjuster adjusts a value of a decrease rate of a cross-sectional area, which is a decrease rate of the flow passage cross-sectional area in a high temperature range relative to the flow passage cross-sectional area in a low temperature range of the first flow passage, to be larger than a value of the decrease rate of the cross-sectional area of the second flow passage. 3 . The heat exchanger according to claim 1 , further comprising: a bypass flow passage configured to flow the first liquid by bypassing the first flow passage; and a second cross-sectional area adjuster provided at the bypass flow passage, and configured to adjust a flow passage cross-sectional area of the bypass flow passage in a high temperature range to be smaller than a flow passage cross-sectional area of the bypass flow passage in a low temperature range. 4 . The heat exchanger according to claim 2 , further comprising: a bypass flow passage configured to flow the first liquid by bypassing the first flow passage; and a second cross-sectional area adjuster provided at the bypass flow passage, and configured to adjust a flow passage cross-sectional area of the bypass flow passage in a high temperature range to be smaller than a flow passage cross-sectional area of the bypass flow passage in a low temperature range. 5 . The heat exchanger according to claim 1 , wherein the cross-sectional area adjuster includes a first fin disposed in the first flow passage and a second fin disposed in the second flow passage, and at least one of the first fin and the second fin contains mercury or polyethylene as a material. 6 . The heat exchanger according to claim 2 , wherein the cross-sectional area adjuster includes a first fin disposed in the first flow passage and a second fin disposed in the second flow passage, and at least one of the first fin and the second fin contains mercury or polyethylene as a material. 7 . The heat exchanger according to claim 3 , wherein the cross-sectional area adjuster includes a first fin disposed in the first flow passage and a second fin disposed in the second flow passage, and at least one of the first fin and the second fin contains mercury or polyethylene as a material. 8 . The heat exchanger according to claim 4 , wherein the cross-sectional area adjuster includes a first fin disposed in the first flow passage and a second fin disposed in the second flow passage, and at least one of the first fin and the second fin contains mercury or polyethylene as a material.
Derivation channels, e.g. bypass · CPC title
Details · CPC title
Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations (F28F3/08 takes precedence) · CPC title
Oil coolers · CPC title
by preventing the formation of continuous films of condensate on heat-exchange surfaces, e.g. by promoting droplet formation {(F28F13/18 takes precedence)} · CPC title
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