Heat exchange – With coated – roughened or polished surface
Reexamination Certificate
2002-07-23
2003-12-16
McKinnon, Terrell (Department: 3743)
Heat exchange
With coated, roughened or polished surface
C165S184000, C138S038000
Reexamination Certificate
active
06662860
ABSTRACT:
The present application is based on Japanese Patent Application No. 2001-223636, which is incorporated herein by reference.
BACKGROUND OF THE INVENTION
1. Field of the Invention
The present invention relates to a heat transfer pipe for a liquid medium having a grooved inner surface into which the liquid medium is introduced to conduct heat exchange between the liquid medium, and gas, liquid and solid substance outside the pipe, and also relates to a heat exchanger employing the heat transfer pipe.
2. Related Art
Such a heat transfer pipe for a liquid medium having a grooved inner surface into which the liquid medium flows to conduct heat exchange between the liquid medium, and gas, liquid and solid substance outside the pipe has been conventionally incorporated in a heat exchanger as a part of the heat exchanger. Material selection and shape design of the heat transfer pipe have been made so that favorable heat exchanging efficiency can be obtained. As one of the examples, there has been a proposal for enhancing the heat transferring efficiency between the pipe and the liquid medium by forming lead grooves or ribs on an inner surface of the heat transfer pipe so as to give agitating action to the liquid medium.
For example, in case of a grooved pipe which has been usually used, there are formed grooves having a lead angle of ten degree or more.
In Japanese Publication No. JP-A-59-84093 of an unexamined patent application, there is proposed a heat transfer pipe in which ribs formed on an inner surface of the pipe are in a trapezoidal shape having a standing plane on a face opposed to a flow of the liquid medium which stands at a right angle with respect to an axis of the pipe, and an inclined plane on a face in a direction of the flow, so that a turbulent flow may be created and agitating performance of the liquid medium may be enhanced thereby improving heat transfer.
However, in the aforesaid grooved pipe, effect of improving the heat exchanging efficiency has been insufficient, because when the liquid medium flows on an inner surface of the pipe provided with grooves having a groove pitch of 1.5 mm and a lead angle of 15 degree, remarkable improvement in heat transferring efficiency can not be obtained, as shown in
FIG. 10
, as compared with a smooth inner surfaced pipe. Moreover, in many cases, the heat transfer pipe is inserted into plate fins and widened for use. When the pipe is widened with a mandrel having a spherical projection, there is a problem that projected portions of the pipe are liable to be crushed, because the projected portions pressed with the mandrel are decreased in number, as the lead angle of the grooves becomes larger.
Further, in the heat transfer pipe provided with the trapezoidal ribs on the inner surface of the pipe, it has been difficult to form the standing plane of the right angle with high molding accuracy, due to a complicated sectional shape of the rib. This will lead to an increase of production cost. Specifically, it has been difficult to keep the angle of the standing plane at 90° while sufficiently maintaining a height required for creation of the turbulent flow. It has been also difficult to fully mold up to a tip end portion of the rib, and there has been a probability that a corner part may be molded in a smooth curve. Hence, there has been a problem that it would be difficult to obtain required performance with reliability.
SUMMARY OF THE INVENTION
The present invention has been made on a background of the above described circumstances, and an object of the present invention is to provide a heat transfer pipe for a liquid medium provided with grooves in which heat exchanging performance can be remarkably enhanced, with relatively small pressure loss and least collapse of the grooves when the pipe is widened, and also a heat exchanger employing this heat transfer pipe.
(1) In order to solve the above described problems, according to the invention, there is provided a heat transfer pipe for a liquid medium having a grooved inner surface, there is provided the heat transfer pipe for a liquid medium having a grooved inner surface in which heat exchange is conducted with movement of the liquid medium in the pipe, characterized in that there are formed, on an inner surface of the heat transfer pipe, annular or spiral grooves in a direction inclined at an angle of 45° to 90° with respect to an axis of the pipe, and that the annular or spiral grooves are continuously formed at a predetermined interval in a longitudinal direction of the pipe.
(2) The invention of the heat transfer pipe for a liquid medium having a grooved inner surface according to the above (1) is characterized in that the annular or spiral grooves have a groove depth of 0.20 mm or more, and a groove pitch of two to five times larger than the groove depth.
(3) The invention of the heat transfer pipe for a liquid medium having a grooved inner surface according to (1) or (2) is characterized in that a ratio W/P of a bottom width W of a projection formed between the annular or spiral grooves to the groove pitch P is 0.1 to 0.9.
(4) The invention of the heat transfer pipe for a liquid medium having a grooved inner surface according to any one of (1) to (3) is characterized in that the heat transfer pipe is a welded pipe having a welded portion.
(5) The invention of the heat exchanger is characterized by including the heat transfer pipe for a liquid medium having a grooved inner surface according to any one of (1) to (4).
(6) The invention of the heat exchanger according to (S) is characterized in that the heat transfer pipe for a liquid medium having a grooved inner surface is inserted into a plurality of plate fins which are arranged in parallel, and widened so as to be tightly fitted to the plate fins.
(7) The heat transfer pipe according to (1) is characterized in that the projection has an inclined surface with respect to the flow of the liquid medium on a side where the liquid medium flows in.
(8) The heat transfer pipe according to (7) is characterized in the said projection has a shape of crest.
Specifically, according to the heat transfer pipe for a liquid medium having a grooved inner surface as described (1), the liquid medium flowing inside the pipe will be appropriately agitated by means of the annular or spiral grooves having an adequate angle difference with respect to the pipe axis, and heat transfer to the pipe can be effectively improved. Pressure loss on this occasion is small and efficiency in general will be remarkably increased. In addition, when the pipe is widened, there is little collapse of the projection between the grooves, and deterioration of the efficiency will be avoided. In case where the angle difference with respect to the pipe axis is less than 40°, sufficient improvement of the heat transfer cannot be obtained, since flows along the grooves are liable to occur, and agitating action of the liquid medium becomes insufficient. Moreover, even though the above mentioned angle difference is larger than 90° in a particular rotation direction, an angle difference in a reverse rotation direction can be regarded as less than 90°. Therefore, the direction of the grooves with respect to the pipe axis is limited to be 45° to 90°.
Moreover, it is desirable that the annular or spiral grooves may have a groove depth of 0.20 mm or more, and a groove pitch of two to five times larger than the groove depth, as described in (2). Generally, the heat transfer pipe of the heat exchanger has a diameter of 7 mm to 20 mm, and so, the depth of the groove may desirably be 0.20 mm or more. With the depth less than 0.20 mm, sufficient agitating action of the liquid medium cannot he obtained. Further, the depth of the groove is desirably less than 1 mm. This is because with too large depth of the groove, the turbulent flow becomes violent, causing a larger pressure loss. By making the groove pitch two to five times larger than the groove depth, the agitating action of the liquid medium will be more effective. In case where the groove has the groove pitch less than twice a
Iwamoto Takashi
Kawai Masayuki
Nagahara Kohtaroh
Ono Shin-ichi
Owaki Yasushi
McKinnon Terrell
Sughrue & Mion, PLLC
The Japan Steel Works Ltd.
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