초록 ▼

In an internal heat exchanger, when a corresponding diameter of a high pressure passage 5a is Ψh, a passage length Lh of the high pressure passage (5a) is so set as to satisfy the relation 9.16/{LN(4.5-Ψh+1.03)}<Lh<46/{LN(4.5-Ψh+1. 03)}, and when a corresponding diameter of a l

In an internal heat exchanger, when a corresponding diameter of a high pressure passage 5a is Ψh, a passage length Lh of the high pressure passage (5a) is so set as to satisfy the relation 9.16/{LN(4.5-Ψh+1.03)}<Lh<46/{LN(4.5-Ψh+1. 03)}, and when a corresponding diameter of a low pressure passage 5c is Ψl, a passage length Ll of the low pressure passage 5c is so set as to satisfy the relation 9.16/{LN(0.56×6-Ψl+1.02)}<Ll<46/{LN(0.56×6-Ψl +1.02)}, a passage sectional area Ah of the high pressure passage 5a is so set as to satisfy the relation 100×(0.25×Ψh1.2)-1/(0.04×Ψh+1.7) ≧Ah≧100×(500×Ψh1.2)-1 (0.04×Ψh+1.7), and a passage sectional area Al of the low pressure passage 5c is so set as to satisfy the relation 1.65/Ψl0.67<Al<626/Ψl0.67.

대표청구항 ▼

What is claimed is: 1. An internal heat exchanger applied to a vapor compression type refrigerator using carbon dioxide as a refrigerant, having a high pressure passage (5a) through which a high pressure refrigerant flows and a low pressure passage (5c) through which a low pressure side refrigerant

What is claimed is: 1. An internal heat exchanger applied to a vapor compression type refrigerator using carbon dioxide as a refrigerant, having a high pressure passage (5a) through which a high pressure refrigerant flows and a low pressure passage (5c) through which a low pressure side refrigerant flows, and conducting heat exchange between said high pressure side refrigerant and said low pressure side refrigerant while the flow of said high pressure side refrigerant and the flow of said low pressure side refrigerant constitute counter-flows, wherein: when the length units are millimeters and a corresponding diameter of said high pressure passage (5a) is Ψh, a passage length (Lh) of said high pressure passage (5a) is greater than 9.16/{LN(4.5-Ψh+1.03)} and smaller than 46/{LN(4.5-Ψh+1.03)}, and when a length unit is millimeter and a corresponding diameter of said low pressure passage (5c) is Ψl, a passage length (Ll) of said low pressure passage (5c) is greater than 9.16/{LN(0.56×6-Ψl+1.02)} and smaller than 46/{LN(0.56×6-Ψl+1.02)}. 2. An internal heat exchanger according to claim 1, wherein said high pressure passage (5a) and said low pressure passage (5c) are aligned on the same axis and constitute a double tube structure. 3. An internal heat exchanger according to claim 1, wherein tubular members constituting said high pressure passage (5a) and said low pressure passage (5c) are shaped into a flat shape. 4. An internal heat exchanger applied to a vapor compression type refrigerator using carbon dioxide as a refrigerant, having a high pressure passage (5a) through which a high pressure refrigerant flows and a low pressure passage (5c) through which a low pressure side refrigerant flows, and conducting heat exchange between said high pressure side refrigerant and said low pressure side refrigerant while the flow of said high pressure side refrigerant and the flow of said low pressure side refrigerant constitute counter-flows, wherein: when the length units are millimeters and a corresponding diameter of said high pressure passage (5a) is Ψh, a passage sectional area (Ah) of said high pressure passage (5a) is smaller than 100×(0.25×Ψh1.2)-1/(0.04×Ψh+1.7) and greater than 100×(500×Ψh1.2)-1(0.04×Ψh+1.7), and when a length unit is millimeter and a corresponding diameter of said low pressure passage (5c) is Ψl, a passage sectional area (Al) of said low pressure passage (5c) is greater than 1.65/Ψl0.67 and smaller than 626/Ψl0.67. 5. An internal heat exchanger according to claim 4, wherein both of said high pressure passage and said low pressure passage (5c) are constituted by a plurality of passages, and wherein the number (Nh) of said high pressure passages (5a) is smaller than 400/(π×Ψh2)×(0.25×Ψh1.2)-1/(0.04×Ψ h+1.7) and greater than 400/(π×Ψh2)×(500×Ψh1.2)-1/(0.04×Ψh+1. 7), and the number (Nl) of said low pressure passages (5c) is greater than 2.1/Ψl2.67 and smaller than 797/Ψl2.67. 6. An internal heat exchanger according to claim 4, wherein said high pressure passage (5a) and said low pressure passage (5c) are aligned on the same axis and constitute a double tube structure. 7. An internal heat exchanger according to claim 4, wherein tubular members constituting said high pressure passage (5a) and said low pressure passage (5c) are shaped into a flat shape.