This application is based upon and claims the benefit of priority of the prior Japanese Patent Application Nos. 2017-150742, filed on Aug. 3, 2017, and 2016-246987, filed on Dec. 20, 2016, the entire contents of which are incorporated herein by reference.
The embodiment discussed herein is related to an information processing device and an electronic device cooling method.
In an information processing device such as a server device or the like, a coolant supply device supplies a coolant into the information processing device by using metal piping, resin hoses, and the like to cool electronic devices or the like included in the information processing device.
A related technology is disclosed in Japanese Laid-open Patent Publication No. 2001-343174.
According to an aspect of the embodiment, an information processing device includes: a first distributing layer distributer configured to distribute a coolant for cooling a plurality of electronic devices stacked in a height direction; and a second distributing layer distributer coupled to the first distributing layer distributer and configured to distribute the coolant, wherein the first distributing layer distributer includes a first distributing pipe which temporarily stores the coolant and a plurality of first distributing connecting pipes branched from the first distributing pipe, the first distributing pipe is disposed in such a manner that an axis of the first distributing pipe is parallel with the height direction, and the plurality of first distributing connecting pipes are arranged side by side in the height direction, wherein the second distributing layer distributer includes a plurality of second distributing pipes which are coupled to the respective first distributing connecting pipes and temporarily store the coolant, each of the plurality of second distributing pipes is disposed in such a manner that an axis of the second distributing pipe is parallel with the height direction, and the plurality of second distributing pipes are arranged in the height direction.
The object and advantages of the invention will be realized and attained by means of the elements and combinations particularly pointed out in the claims.
It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanatory and are not restrictive of the invention, as claimed.
In a server device, a coolant is distributed to cool each of a plurality of electronic devices that each include a central processing unit (hereinafter a CPU). The coolant is, for example, distributed by a distributing unit in which distribution paths such as a plurality of hoses or the like are coupled to one thick pipe (which distributing unit is referred to also as a multiple-branch pipe or a manifold).
As the number of electronic devices included in the server device is increased, for example, the piping length of the distributing unit is increased to evenly distribute the coolant to the electronic devices, and therefore the mounting space of the distributing unit may be enlarged.
An information processing device in which the whole of a distributing unit distributing a coolant is miniaturized, for example, may be provided.
In the following, the same or similar elements are identified by common reference symbols, and the scale of the drawings may be changed as appropriate in order to facilitate understanding.
The distributing unit 210 is coupled to the heat exchanger 33 by a feed pipe 34. The coolant flows from the heat exchanger 33 through the feed pipe 34 into the distributing unit 210. The heat exchanger 33 is also a coolant feeder, and has a function of a pump that sends the coolant to the distributing unit 210.
The distributing unit 210 is a device that distributes the coolant sent from the heat exchanger 33 to the electronic devices 40. The distributing unit 210 includes a distributing pipe 211 into which the coolant flows and distributing connecting pipes 212 as communication paths between the distributing pipe 211 and the electronic devices 40. In
The merging unit 220 includes a merging pipe 221 and merging connecting pipes 222 as communication paths between the electronic devices 40 and the merging pipe 221. In
The structure that distributes the coolant to the electronic devices 40 using the distributing pipe 211 branching into the plurality of distributing connecting pipes 212 supplies the plurality of electronic devices 40 with the coolant at substantially equal temperatures and substantially equal flow rates. As the performance of the server device 2 is enhanced, for example, more electronic devices 40 each including a CPU are incorporated, and the size of the server device 2 may be increased due to the following factors.
(1) Because one distributing pipe 211 branches so as to couple to the plurality of electronic devices 40, the length of the distributing pipe 211 is increased as the number of electronic devices 40 is increased. In order to reduce pressure losses caused by difference between distances from the inlet of the distributing pipe 211 to the electronic devices 40 (which distances may hereinafter be referred to as distribution paths), the distribution paths desirably have a same length. Therefore, the lengths of all of the distributing connecting pipes 212 are adjusted to the length of a longest distributing connecting pipe 212. Thus, a larger mounting space may be provided.
(2) Pressure losses due to increases in distance from the inlet of the distributing pipe 211 to the individual outlets of the distributing pipe 211 invite decreases in flow rate. Thus, in order to reduce difference between the pressure losses, the diameter of the distributing pipe 211 may be further increased.
With the structure of the distributing unit 210 and the merging unit 220 illustrated in
As illustrated in
For example, the distributing unit 10 includes the first distributing layer distributing unit 131 that distributes the coolant from the feed pipe 34, and the second distributing layer distributing unit 132 that is coupled to the first distributing layer distributing unit 131 and further distributes the coolant. The first distributing layer distributing unit 131 includes a distributing pipe 111 that temporarily stores the coolant, and a plurality of distributing connecting pipes 121 branched from the distributing pipe 111. The distributing connecting pipes 121 are indicated by solid line arrows in
The heat exchanger 33 is coupled to the distributing pipe 111 present in the first distributing layer 131 via the feed pipe 34. The distributing pipe 111 branches into four distributing connecting pipes 121. The distributing pipe 111 is provided with a plurality of outlets for one inlet. The distributing connecting pipes 121 of the first distributing layer distributing unit 131 on an upstream side are each coupled to the distributing pipe 112 of the second distributing layer distributing unit 132 on a downstream side. The distributing connecting pipe 121 is provided with one outlet for one inlet. The distributing pipe 112 of the second distributing layer distributing unit 132 branches into a plurality of distributing connecting pipes 122. The distributing connecting pipes 122 are individually coupled to inlets 47 (see
As illustrated in
When a single distributing pipe is used as in the server device 2 illustrated in
Therefore, a space occupying rate of the distributing connecting pipes 12 may be reduced. Because a flow rate per distributing pipe 11 is decreased, the diameter SD of the distributing pipes 11 may be reduced. Therefore, the distributing unit 10 as a whole may be more miniaturized, and parts cost may be reduced.
As with the distributing unit 10, the merging unit 20 has a hierarchical structure as illustrated in
As illustrated in
The size of the distributing unit 210 and the merging unit 220 of the server device 2 illustrated in
The diameter SD1 of the distributing pipe 111 of the first distributing layer distributing unit 131 is set at 45 mm. A length SL1 in a longitudinal direction of the distributing pipe 111 of the first distributing layer distributing unit 131 is set at 400 mm. The following Equation is used to set the diameter SD2 of the distributing pipes 112 of the second distributing layer distributing unit 132.
SD
2
=SD
1
/√{square root over ( )}SN
1
where SD2 denotes the diameter of the distributing pipes 112 of the second distributing layer distributing unit 132, SD1 denotes the diameter of the distributing pipe 111 of the first distributing layer distributing unit 131, and SN1 denotes the number of branches from the distributing pipe 111 of the first distributing layer distributing unit 131 to the distributing pipes 112 of the second distributing layer distributing unit 132.
Because the distributing pipe 111 of the first distributing layer distributing unit 131 branches into eight pipes of the second distributing layer distributing unit 132, for example, a flow rate at which the coolant passes through each of the distributing pipes 112 of the second distributing layer distributing unit 132 is ⅛ of a flow rate at which the coolant passes through the distributing pipe 111 of the first distributing layer distributing unit 131. In order to suppress pressure losses in the distributing pipes 112 of the second distributing layer distributing unit 132 to a similar level to that of the distributing pipe 111 of the first distributing layer distributing unit 131, a cross-sectional area of the distributing pipes 112 of the second distributing layer distributing unit 132 is set at approximately ⅛ of a cross-sectional area of the distributing pipe of the first distributing layer distributing unit 131, as in the case of the flow rates. For example, the cross-sectional area ratio is ⅛, and an inside diameter ratio is √(⅛). When distribution and cost aspects are considered while the above is taken into consideration, the diameter SD2 of the distributing pipes 112 in a second layer is set at 20 mm, and a pipe length SL2 of the distributing pipes 112 is set at 400 mm. A diameter of the distributing connecting pipes 121 (hoses) coupling the distributing pipe 111 of the first distributing layer distributing unit to the distributing pipes 112 of the second distributing layer distributing unit is set at 15 mm, and a length of the distributing connecting pipes 121 is set at 1500 mm. The merging unit 20 is formed with similar dimensions because the merging unit 20 collects the cooling water fed into each of the electronic devices 40 by the distributing unit 10. For example, the diameter CD1 of the merging pipe 211 of the first merging layer merging unit 231 is set at 20 mm, a pipe length CL1 of the merging pipe 211 of the first merging layer merging unit 231 is set at 400 mm, the diameter CD2 of the merging pipe 212 of the second merging layer merging unit 232 is set at 45 mm, and a pipe length CL2 of the merging pipe 212 of the second merging layer merging unit 232 is set at 400 mm. A diameter of the merging connecting pipes 222 is set at 15 mm, and a length of the merging connecting pipes 222 is set at 1500 mm.
A volume in a case where the distributing unit 10 and the merging unit 20 are fabricated with the above-described dimensions is illustrated in Table 1.
When the distributing unit 210 illustrated in
A volume in a case where the distributing unit and the merging unit are fabricated with the above-described dimensions is illustrated in Table 2.
A comparison of the volume of the distributing unit 10 and the merging unit 20 of the server device 1 which volume is illustrated in Table 1 with the volume of the distributing unit 210 and the merging unit 220 of the server device 2 which volume is illustrated in Table 2 indicates that a volume reduction to approximately ⅓ may be achieved. Therefore, for example, when the server device 1 illustrated in
In the server device 2 illustrated in
The distributing unit 10 and the merging unit 20 illustrated in
When the layers of the distributing layer distributing units are generalized, and, for example, referred to as N layers (N is a layer number and an integer of one or more, and increases from the upstream side, from which the coolant flows, to the downstream side), a distributing layer distributing unit 13N includes a distributing pipe 11N that stores the coolant temporarily and a plurality of distributing connecting pipes 12N coupled to distributing pipes 11N+1 or electronic devices 40 on the downstream side.
The merging unit 20 is not limited to two layers either, and may be formed in three layers or more according to the number of coupled electronic devices 40. A merging layer merging unit 23M (M is a layer number, and increases from the upstream side, from which the coolant flows, to the downstream side) includes a merging pipe 21M that stores the coolant temporarily and a plurality of merging connecting pipes 22M coupled to the electronic devices 40 or merging pipes 21M−1 of merging layer merging units on the upstream side. Each merging pipe 21M is provided with a plurality of inlets and one drain outlet.
The number of layers of the distributing unit 10 and the number of layers of the merging unit 20 may be the same, or may be different from each other. For example, the distributing unit 10 may be formed in three layers, and the merging unit 20 may be formed in two layers. For example, only the merging unit 20 may be formed in one layer.
When the distributing unit 10 is fabricated in a plurality of layers, a diameter SDN+1 of a distributing pipe 11N+1 of an (N+1)th distributing layer distributing unit on the downstream side is formed smaller than a diameter SDN of a distributing pipe 11N in an Nth distributing layer distributing unit. In the Nth distributing layer distributing unit, a diameter TDN of a distributing connecting pipe 12N is formed smaller than the diameter SDN of the distributing pipe 11N.
In consideration of pressure losses during distribution of the coolant, the diameter SDN+1 of the distributing pipe 11N+1 of the (N+1)th distributing layer distributing unit 13N+1 on the downstream side may be determined by the following Equation.
SD
N+1
=SD
N/√{square root over ( )}(SNN)
where SDN denotes the diameter of the distributing pipe 11 in the Nth distributing layer distributing unit, and SNN denotes the number of distributions in the Nth distributing layer distributing unit.
When the merging unit 20 is formed in a plurality of layers, a diameter CDM−1 (M is an integer of 2 or more, and increases from the upstream side of the coolant to the downstream side) of a merging pipe 21M−1 in an (M−1)th layer is formed smaller than a diameter CDM of a merging pipe 21M present in an Mth merging layer merging unit. For example, a diameter CDM+1 of a merging pipe 21M+1 in an (M+1)th layer (downstream side) is formed larger than the diameter CDM of the merging pipe 21M present in the Mth merging layer merging unit. In the Mth merging layer merging unit, a diameter UDM of a merging connecting pipe 22M is formed smaller than the diameter CDM of the merging pipe 21M.
The diameter CDM+1 of the merging pipe 21M+1 in the (M+1)th layer may be determined by the following Equation.
CD
M+1
=CD
M×√{square root over ( )}(CNM+1)
where CDM denotes the diameter of the pipe in the Mth merging layer merging unit (layer on the upstream side), and CNM+1 denotes the number of merging flows from which the coolant merges in the (M+1)th merging layer merging unit (layer on the downstream side).
Also in a merging unit 120 of the server device 1a illustrated in
Pipes having a same diameter are used as the first distributing pipe 111 and the second distributing pipe 112. However, a height SL1 of the first distributing pipe 111 and a height SL2 of the second distributing pipe 112 may be a same dimension, or may be different from each other. For example, one of the height SL1 of the first distributing pipe 111 and the height SL2 of the second distributing pipe 112 may be larger.
In addition, pipes having a same diameter are used as the first merging pipe 211 and the second merging pipe 212. However, a height CL1 of the first merging pipe 211 and a height CL2 of the second merging pipe 212 may be a same dimension, or may be different from each other. For example, one of the height CL2 of the second merging pipe 212 and the height CL1 of the first merging pipe 211 may be larger. This is because pressure losses of the coolant flowing in the distributing unit 110 or the merging unit 120 change depending on the diameters (CD1, CD2, SD1, and SD2) of the pipes, but are affected little by differences in length of those pipes, for example, differences in height (SL1, SL2, CL1, and CL2) of the pipes.
In the server device 1a illustrated in
Because the diameter SD1 of the first distributing pipe 111 and the diameter SD2 of the second distributing pipes 112 are essentially a same dimension, the first distributing pipe 111 and the second distributing pipes 112 are procured according to same specifications. Because the first distributing pipe 111 and the second distributing pipes 112 are procured according to the same specifications, a purchased quantity of pipe material used for the first distributing pipe 111 and the like is increased. Thus, unit cost may be decreased and procurement cost may be reduced. The first merging pipe 211 and the second merging pipe 212 of the merging unit 120 of the server device 1a may also provide similar effects.
All examples and conditional language recited herein are intended for pedagogical purposes to aid the reader in understanding the invention and the concepts contributed by the inventor to furthering the art, and are to be construed as being without limitation to such specifically recited examples and conditions, nor does the organization of such examples in the specification relate to a showing of the superiority and inferiority of the invention. Although the embodiment of the present invention has been described in detail, it should be understood that the various changes, substitutions, and alterations could be made hereto without departing from the spirit and scope of the invention.
Number | Date | Country | Kind |
---|---|---|---|
2016-246987 | Dec 2016 | JP | national |
2017-150742 | Aug 2017 | JP | national |