HEAT EXCHANGER

PROBLEM TO BE SOLVED: To provide a heat exchanger capable of reducing bulk in a thickness direction of a heat exchanger by forming a pipe member in a single stage, being satisfactorily mounted under the floor of an automobile, and preventing breakage of the pipe member by fly rock in running. SOLUTI...

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Hauptverfasser: USUI SHOICHIRO, SEGAWA HISASHI, KONDO KEIMEI
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creator USUI SHOICHIRO
SEGAWA HISASHI
KONDO KEIMEI
description PROBLEM TO BE SOLVED: To provide a heat exchanger capable of reducing bulk in a thickness direction of a heat exchanger by forming a pipe member in a single stage, being satisfactorily mounted under the floor of an automobile, and preventing breakage of the pipe member by fly rock in running. SOLUTION: This heat exchanger includes a plurality of fin members 3 formed as corrugated fins and having engagement recesses 8 on a curved sections 6, and the pipe member 1 formed by connecting straight pipe sections 2 disposed through the fin members 3 by U-shaped bent sections 5. An outer diameter of the pipe member 1 is 8-12 mm, and a facing distance 17 of the fin members 3 is 0.5-5.0 mm in a state that the straight pipe sections 2 are engaged with the engagement recesses 8 of the fin members 3. Formula of y≥2.46x-0.29(y is protrusion height of fin members 3 from surface of pipe member 1/facing distance 17 of curved top sections 15, and x is facing interval 17 of curved top sections 15), is satisfied when the protrusion height of the fin members 3 is 11 mm or less, and the facing interval 17 is within a range of 0.5-5.00 mm. COPYRIGHT: (C)2011,JPO&INPIT
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SOLUTION: This heat exchanger includes a plurality of fin members 3 formed as corrugated fins and having engagement recesses 8 on a curved sections 6, and the pipe member 1 formed by connecting straight pipe sections 2 disposed through the fin members 3 by U-shaped bent sections 5. An outer diameter of the pipe member 1 is 8-12 mm, and a facing distance 17 of the fin members 3 is 0.5-5.0 mm in a state that the straight pipe sections 2 are engaged with the engagement recesses 8 of the fin members 3. Formula of y≥2.46x-0.29(y is protrusion height of fin members 3 from surface of pipe member 1/facing distance 17 of curved top sections 15, and x is facing interval 17 of curved top sections 15), is satisfied when the protrusion height of the fin members 3 is 11 mm or less, and the facing interval 17 is within a range of 0.5-5.00 mm. 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SOLUTION: This heat exchanger includes a plurality of fin members 3 formed as corrugated fins and having engagement recesses 8 on a curved sections 6, and the pipe member 1 formed by connecting straight pipe sections 2 disposed through the fin members 3 by U-shaped bent sections 5. An outer diameter of the pipe member 1 is 8-12 mm, and a facing distance 17 of the fin members 3 is 0.5-5.0 mm in a state that the straight pipe sections 2 are engaged with the engagement recesses 8 of the fin members 3. Formula of y≥2.46x-0.29(y is protrusion height of fin members 3 from surface of pipe member 1/facing distance 17 of curved top sections 15, and x is facing interval 17 of curved top sections 15), is satisfied when the protrusion height of the fin members 3 is 11 mm or less, and the facing interval 17 is within a range of 0.5-5.00 mm. 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subjects BLASTING
DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OFGENERAL APPLICATION
HEAT EXCHANGE IN GENERAL
HEATING
LIGHTING
MECHANICAL ENGINEERING
WEAPONS
title HEAT EXCHANGER
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