JP2015215100A - Heat exchanging pipe, heat exchanger using heat exchanging pipe and heat exchanging device - Google Patents
Heat exchanging pipe, heat exchanger using heat exchanging pipe and heat exchanging device Download PDFInfo
- Publication number
- JP2015215100A JP2015215100A JP2014096596A JP2014096596A JP2015215100A JP 2015215100 A JP2015215100 A JP 2015215100A JP 2014096596 A JP2014096596 A JP 2014096596A JP 2014096596 A JP2014096596 A JP 2014096596A JP 2015215100 A JP2015215100 A JP 2015215100A
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- heat exchange
- tube
- heat
- inner pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Abstract
Description
この発明は、異なる質(性状)の熱交換媒体と被熱交換媒体との間の熱交換を行う熱交換管及びその熱交換管からなる熱交換器並びにその熱交換器からなる熱交換装置に関するものである。 The present invention relates to a heat exchange pipe for performing heat exchange between a heat exchange medium of different qualities (characteristics) and a heat exchange medium, a heat exchanger comprising the heat exchange pipe, and a heat exchange apparatus comprising the heat exchanger. Is.
例えば、給湯装置として、圧縮機、給湯用熱交換器、膨張弁、及び外気を熱源とする熱源側熱交換器からなる冷凍サイクルと、給湯用熱交換器、給水ポンプ、及び給湯タンクからなる給湯サイクルとから構成されるものがある。この給湯装置は、給湯用熱交換器で、圧縮機からの高温冷媒によって給水ポンプからの水を加熱して湯とし、この湯を給湯タンクに貯蔵して台所や湯槽等に供給する(特許文献1、段落0002、図6参照)。 For example, as a hot water supply apparatus, a hot water supply comprising a compressor, a hot water supply heat exchanger, an expansion valve, and a heat source side heat exchanger using outside air as a heat source, a hot water supply heat exchanger, a water supply pump, and a hot water supply tank. Some are composed of cycles. This hot water supply device is a hot water supply heat exchanger that heats water from a water supply pump with hot refrigerant from a compressor to form hot water, stores this hot water in a hot water supply tank, and supplies it to a kitchen, a hot water bath, etc. (Patent Literature) 1, paragraph 0002, FIG. 6).
その給湯用熱交換器は、内管と外管とからなる二重管構造が一般的であり、一方の管に炭酸ガス等の冷媒を流通し、他方の管に水を流通させ、すなわち、内外管に異なる質の熱交換媒体と被熱交換媒体を流通させて熱交換する(特許文献1、段落0003)。
この熱交換器においては、内外管に異なる熱交換媒体(流体)を流通させることから、例えば、内管を二重管とし、その間の周囲長さ方向に漏洩検知溝を形成したものがある。この漏洩検知溝は、内管の破損などによってその内管内の媒体、例えば、冷媒が内管の破損等で内管外面に漏れると、その漏洩液が管端に至ることにより、内管の内外の媒体の混合を防止するとともにその漏洩を検知するようになっている(特許文献1、段落0006)。
The hot water supply heat exchanger generally has a double-pipe structure composed of an inner pipe and an outer pipe. A refrigerant such as carbon dioxide gas is circulated through one pipe, and water is circulated through the other pipe. The heat exchange medium and the heat exchange medium of different qualities are circulated through the inner and outer tubes to exchange heat (Patent Document 1, paragraph 0003).
In this heat exchanger, since different heat exchange media (fluids) are circulated in the inner and outer pipes, for example, there is one in which the inner pipe is a double pipe and a leak detection groove is formed in the peripheral length direction therebetween. This leakage detection groove is used to prevent the leakage of the medium in the inner pipe due to damage to the inner pipe, for example, the refrigerant leaking to the outer surface of the inner pipe due to damage to the inner pipe. The medium is prevented from mixing and the leakage is detected (Patent Document 1, Paragraph 0006).
また、同質、例えば、水と温水との熱交換器として、扁平のコルゲート管を並列し、その並列したコルゲート管を内管としてその外周面に外筒(外管)を嵌めたものがある(特許文献2、図5〜図8参照)。 Moreover, the same quality, for example, as a heat exchanger of water and warm water, there is one in which flat corrugated pipes are arranged in parallel, and the parallel corrugated pipe is used as an inner pipe and an outer cylinder (outer pipe) is fitted on the outer peripheral surface thereof ( (See Patent Document 2 and FIGS. 5 to 8).
上記特許文献1の熱交換器は、その断面が円形であり、円筒形内管の中心部を流れる媒体は内管の外周面を流れる媒体との距離が長い(遠い)ため、その熱交換率が低いものとなっている。
一方、特許文献2の熱交換器はコルゲート管を並列してそのコルゲート管は細いもの(小径)となっている。このため、上記断面円形の内管に比べ、同一流量であれば、その各コルゲート管内を流れる媒体とその外周面を流れる媒体との距離が短く(接触面積が多く)、その熱交換率も高い。
しかし、この並列コルゲート管からなる熱交換器を、異なる質の熱交換媒体と被熱交換媒体との熱交換に使用した場合、そのコルゲート管が破損すると、その管の内外の媒体が混合してしまう。
The heat exchanger of Patent Document 1 has a circular cross section, and the medium flowing through the central portion of the cylindrical inner tube has a long (far) distance from the medium flowing through the outer peripheral surface of the inner tube. Is low.
On the other hand, the heat exchanger of Patent Document 2 has corrugated tubes arranged in parallel, and the corrugated tubes are thin (small diameter). For this reason, compared with the inner pipe having a circular cross section, if the flow rate is the same, the distance between the medium flowing in each corrugated pipe and the medium flowing on the outer peripheral surface thereof is short (the contact area is large), and the heat exchange rate is also high. .
However, when this heat exchanger composed of parallel corrugated tubes is used for heat exchange between a heat exchange medium of different quality and a heat exchange medium, if the corrugated tube breaks, the media inside and outside the tube will mix. End up.
この発明は、以上の実状の下、特許文献2の熱交換器を、異なる質の熱交換媒体と被熱交換媒体との熱交換に使用し得るようにすることを課題とする。 This invention makes it a subject to make it possible to use the heat exchanger of patent document 2 for the heat exchange of a heat exchange medium of different quality, and a heat exchange medium under the above actual condition.
上記課題を達成するため、この発明は、上記並列されたコルゲート管を保護管で被覆すると共に、その保護管をコルゲート管に密着された熱交換管としたのである。
このようにすれば、並列するコルゲート管の間と保護管との間に両管端に通じる空隙が生じ、その空隙が、上記漏洩検知溝と同等なものとなって、熱交換管の内外の媒体の混合を防止するとともにその漏洩を検知するようにすることができる。
また、保護管をコルゲート管に密着させるとともにコルゲート管の溝に入り込むようにすれば、保護管とコルゲート管の一体性が確保されてコルゲート管内面と保護管外面の熱伝導性も高くなるとともに、保護管の表面にコルゲート管外面に倣う凹凸が生じ、その表面を流れる流体が凹凸によって乱流となるため、熱交換率の高いものとなる。
In order to achieve the above object, the present invention covers the parallel corrugated tubes with a protective tube, and the protective tube is a heat exchange tube in close contact with the corrugated tube.
In this way, a gap is formed between the parallel corrugated pipes and between the protective pipes, leading to both pipe ends, and the gap is equivalent to the leakage detection groove, so that the inside and outside of the heat exchange pipe It is possible to prevent the medium from being mixed and to detect the leakage.
In addition, if the protective tube is closely attached to the corrugated tube and enters the groove of the corrugated tube, the integrity of the protective tube and the corrugated tube is ensured, and the thermal conductivity of the corrugated tube inner surface and the outer surface of the protective tube is increased, Unevenness following the corrugated tube outer surface is generated on the surface of the protective tube, and the fluid flowing on the surface becomes turbulent due to the unevenness, so that the heat exchange rate is high.
この発明に係わる熱交換管の構成としては、質の異なる熱交換媒体又は被熱交換媒体を内部に流通し、その媒体と外部の前記被熱交換媒体又は熱交換媒体との熱交換をする熱交換管において、複数のコルゲート管が並列され、その並列されたコルゲート管を保護管で被覆し、その保護管は、各コルゲート管の外面に密着されて、保護管の外面もコルゲート管の外面に倣って凹凸状となっている構成を採用することができる。
この熱交換管を外管内に装填し、その熱交換管に熱交換媒体又は被熱交換媒体の一方を、熱交換管と外管との間に熱交換媒体又は被熱交換媒体の他方をそれぞれ流通させて熱交換器とすることができる。
また、この熱交換器を並列し、その並列した各熱交換器の一方の側に位置する熱交換器の一端を一方の給排用ヘッドとし、他方の側に位置する熱交換器の一端を他方の給排用ヘッドとし、隣接する各熱交換器の熱交換管は一方の熱交換器の端を他方の熱交換器の端に屈曲させた連続管とした構成の熱交換装置とすることができる。
The heat exchange pipe according to the present invention has a heat exchange medium or a heat exchange medium having different qualities inside and heat exchange between the medium and the external heat exchange medium or heat exchange medium. In the exchange pipe, a plurality of corrugated pipes are arranged in parallel, and the parallel corrugated pipes are covered with a protective pipe, and the protective pipes are in close contact with the outer surface of each corrugated pipe, and the outer face of the protective pipe is also on the outer face of the corrugated pipe. It is possible to adopt a configuration in which the shape is concave and convex.
The heat exchange tube is loaded into the outer tube, and either the heat exchange medium or the heat exchange medium is placed in the heat exchange tube, and the other of the heat exchange medium or the heat exchange medium is placed between the heat exchange tube and the outer tube. It can be distributed and used as a heat exchanger.
Also, the heat exchangers are arranged in parallel, and one end of the heat exchanger located on one side of each of the parallel heat exchangers is used as one supply / discharge head, and one end of the heat exchanger located on the other side is used. The other heat supply head is a heat exchange device having a structure in which the heat exchange pipe of each adjacent heat exchanger is a continuous pipe in which the end of one heat exchanger is bent to the end of the other heat exchanger. Can do.
この発明は、以上のように構成したので、熱交換管の内外の媒体の混合を防止するとともにその漏洩を検知するようにすることができ、かつ、熱交換率の高いものとなる。 Since the present invention is configured as described above, it is possible to prevent the medium inside and outside the heat exchange tube from mixing and to detect the leakage thereof, and to achieve a high heat exchange rate.
この発明に係る熱交換装置の一実施形態を図1〜図7に示し、この実施形態の熱交換装置は、上記給湯装置の給湯用熱交換器として使用されるものであり、複数の熱交換器Aを組み合わせたものである。その熱交換器Aは、炭酸ガス等の熱交換媒体(冷媒b)を通す内管10となる熱交換管と、その内管10の外側に配置され、内管10との間に被熱交換媒体である水aを通す外管20とから成る。 1 to 7 show an embodiment of a heat exchange device according to the present invention. The heat exchange device of this embodiment is used as a heat exchanger for hot water supply of the hot water supply device, and has a plurality of heat exchanges. This is a combination of vessel A. The heat exchanger A is disposed between the heat exchange pipe serving as the inner pipe 10 through which a heat exchange medium (refrigerant b) such as carbon dioxide gas passes and the inner pipe 10 to exchange heat with the inner pipe 10. And an outer tube 20 through which water a as a medium passes.
内管(熱交換管)10は、熱伝導性の高い金属からなるコルゲート管11を複数本並列したものが本体となり、そのコルゲート管11は、図7に示すように、両端を除いてその外周面にコルゲート溝12が形成されている。このコルゲート溝12は、螺旋のような連続的でも間欠的でも良く、また、外周同一円形溝を長さ方向に所要間隔に形成したものでも良い。コルゲート管11の並列数は任意であり、この実施形態では4本としている。 The inner pipe (heat exchange pipe) 10 is a main body in which a plurality of corrugated pipes 11 made of a metal having high thermal conductivity are arranged in parallel, and the corrugated pipe 11 has an outer periphery excluding both ends as shown in FIG. A corrugated groove 12 is formed on the surface. The corrugated groove 12 may be continuous or intermittent, such as a spiral, or may be formed by forming circular grooves having the same outer periphery at a required interval in the length direction. The parallel number of the corrugated pipes 11 is arbitrary, and in this embodiment, it is four.
並列したコルゲート管11には、図5、図6に示すように、その両端を除いて外周面全長に亘ってコルゲート管11と同一材料からなる保護管13が被覆されて熱交換管(内管)10となっている。その保護管13のコルゲート管11への被覆は密着されている。
このとき、図6(c)、(d)に示すように、コルゲート管11の溝12に保護管13が入り込んでその表面に波状の凹凸14が生じ、その入り込みによって、両者11、13の一体性(密着性)が確保されてコルゲート管11の内面と保護管13外面の熱伝導性が高くなっているとともに、保護管13表面の凹凸14により、その表面を流れる流体(水)aが乱流となって、熱交換率の高いものとなる。
As shown in FIGS. 5 and 6, the parallel corrugated tubes 11 are covered with a protective tube 13 made of the same material as the corrugated tube 11 over the entire outer peripheral surface except for both ends thereof, so that heat exchange tubes (inner tubes) ) 10. The covering of the protective tube 13 to the corrugated tube 11 is in close contact.
At this time, as shown in FIGS. 6 (c) and 6 (d), the protective tube 13 enters the groove 12 of the corrugated tube 11, and a wavy unevenness 14 is generated on the surface thereof. Property (adhesion) is ensured and the inner surface of the corrugated tube 11 and the outer surface of the protective tube 13 are increased in thermal conductivity, and the irregularity 14 on the surface of the protective tube 13 disturbs the fluid (water) a flowing on the surface. As a result, the heat exchange rate is high.
なお、この凹凸14を有する内管10の部分は、熱交換管としては意匠的に新規なものであり、この熱交換管10は、その凹凸14を有する部分を適宜の長さとし、その両端に適宜に入口栓(給排用ヘッド)又は出口栓(給排用ヘッド)を設けた形状となり、直線状であったり、曲線状又は湾曲状であったり、その湾曲も複数回としたもの(図1、図2参照)となったりする。 The portion of the inner tube 10 having the projections and depressions 14 is a novel design as a heat exchange tube, and the heat exchange tube 10 has a portion having the projections and depressions 14 having an appropriate length and is provided at both ends thereof. Appropriately provided with an inlet plug (supply / discharge head) or an outlet plug (supply / discharge head), which is linear, curved or curved, and curved several times (Fig. 1 and FIG. 2).
外管20は、断熱性の高い材料からなり、金属や樹脂が考えられるが、この実施形態では、熱可塑性樹脂を使用した一体成形品である。この外管20は、図4に示すように、その外周面に補強用のリブ21が縦横に形成され、その内部が円状空間が並んだ(串団子状)空間となっており(図3参照)、この空間内に上記内管10が挿通される。その挿通状態は、図3に示すように、外管20の内周面と内管10(保護管13)の外周面との間に間隙(空隙)22が形成され、その間隙22内にその長さ方向に保護管13の凹凸14が間欠的に存在する。 The outer tube 20 is made of a highly heat-insulating material and may be a metal or a resin. In this embodiment, the outer tube 20 is an integrally molded product using a thermoplastic resin. As shown in FIG. 4, the outer pipe 20 has reinforcing ribs 21 formed vertically and horizontally on the outer peripheral surface thereof, and the inside thereof is a space in which circular spaces are arranged (skew dumpling shape) (FIG. 3). The inner tube 10 is inserted into this space. As shown in FIG. 3, a gap (gap) 22 is formed between the inner peripheral surface of the outer tube 20 and the outer peripheral surface of the inner tube 10 (protective tube 13). The unevenness 14 of the protective tube 13 is intermittently present in the length direction.
外管20の両端は一方がオス部23、他方がメス部24となっており、メス部24にオス部23をパッキン25を介在し、ビス26によって締結することによって所要の数の外管20を連結し得る(図1、図2、図4参照)。この実施形態では二本を連結しているが、その連結を止めたり、任意の連結数としたりすることによって任意の長さの熱交換器Aとし得る。 One end of the outer tube 20 is a male part 23 and the other is a female part 24. The male part 23 is interposed in the female part 24 with a packing 25 and fastened with screws 26, so that the required number of outer pipes 20 are obtained. Can be connected (see FIGS. 1, 2, and 4). Although two are connected in this embodiment, it can be set as the heat exchanger A of arbitrary length by stopping the connection or making it the arbitrary number of connections.
この熱交換器Aによってコンパクトな所要容量の熱交換装置とするには、真っ直ぐな所要長さの内管10を用意し、その一端から外管20を挿し込み、その突出した前記内管10を円弧状に折り返して外管20に沿わせる。つぎに、その沿わせた内管10に新たに外管20を挿し込み、その突出した前記内管10を円弧状に折り返して外管20に沿わせる。以後、同様にして、所要段数の熱交換器Aが並列した状態とする(図1、図2参照)。この実施形態では、四列(四段)とした。この並列時、内管10はその列数に応じた長さとし、その両端は、各コルゲート管11を纏めて高温冷媒bの入口栓(給排用ヘッド)27a又は出口栓(給排用ヘッド)27bを設ける。 In order to obtain a heat exchange apparatus having a compact required capacity by this heat exchanger A, an inner tube 10 having a straight required length is prepared, an outer tube 20 is inserted from one end thereof, and the protruding inner tube 10 is attached to the inner tube 10. It folds in an arc shape and runs along the outer tube 20. Next, the outer tube 20 is newly inserted into the aligned inner tube 10, and the protruding inner tube 10 is folded back into an arc shape so as to be along the outer tube 20. Thereafter, similarly, the required number of stages of heat exchangers A are in parallel (see FIGS. 1 and 2). In this embodiment, there are four rows (four stages). At the time of this parallel, the inner pipe 10 has a length corresponding to the number of rows, and both ends of the inner pipe 10 are combined with the corrugated pipes 11 and the inlet plug (supply / discharge head) 27a or outlet plug (supply / discharge head) of the high-temperature refrigerant b 27b is provided.
その熱交換器Aの並列した内管10の折り返し部には外管20と同一材料からなるキャップ28を嵌め込む。このキャップ28は、両端が開口した筒状のものとしたり、一端面を閉じた有蓋筒状のものとしたりすることができる。前者の筒状であると、この熱交換装置の左又は右から水aが外管20内に入って右又は左から出る流れとなり(図1のa矢印参照)、後者の有蓋筒状であると、一の栓27a又は27b側から外管20に水aが入り、並列した一の外管20の端から他の外管20の他端に流れ込むように蛇行して他の栓27b又は27a側から出る流れとなる(図2のa矢印参照)。何れにしても、内管10内を流れる冷媒bと水aの流れ方向はできる限り逆方向となるようにする。 A cap 28 made of the same material as that of the outer tube 20 is fitted into the folded portion of the inner tube 10 in parallel with the heat exchanger A. The cap 28 can be a cylinder with both ends open, or a covered cylinder with one end face closed. In the former cylindrical shape, water a enters the outer tube 20 from the left or right of the heat exchange device and flows out from the right or left (see arrow a in FIG. 1), and the latter is a covered cylindrical shape. Then, water a enters the outer tube 20 from the side of the one plug 27a or 27b, meanders so as to flow from the end of the one outer tube 20 in parallel to the other end of the other outer tube 20, and the other plug 27b or 27a. The flow comes out from the side (see arrow a in FIG. 2). In any case, the flow direction of the refrigerant b and the water a flowing in the inner pipe 10 is made to be as opposite as possible.
この実施形態の熱交換装置は以上の構成であり、この熱交換装置を上記給湯装置の給湯用熱交換器とすると、圧縮機からの高温冷媒bが内管10内を流通し、給水ポンプからの水aが外管20内の空隙22内を流通する。このとき、保護管13が内管10に一体となって両者の熱伝導性が高いものとなっており、また、外管20の内周面と内管10(保護管13)の外周面との間の間隙22内の保護管13の凹凸14によって流通する水aが乱流となるため、内管10内の高温冷媒bと水aとの熱交換は円滑になされる。 The heat exchange device of this embodiment has the above-described configuration, and when this heat exchange device is a hot water supply heat exchanger of the hot water supply device, the high-temperature refrigerant b from the compressor circulates in the inner pipe 10 and is supplied from the water supply pump. Water a flows through the gap 22 in the outer tube 20. At this time, the protective tube 13 is integrated with the inner tube 10 to have high thermal conductivity between them, and the inner peripheral surface of the outer tube 20 and the outer peripheral surface of the inner tube 10 (protective tube 13). Since the water a flowing through the irregularities 14 of the protective tube 13 in the gap 22 between them becomes a turbulent flow, heat exchange between the high-temperature refrigerant b and the water a in the inner tube 10 is performed smoothly.
なお、コルゲート管11と保護管13との空隙内に漏液検知線を設けたり、その空隙の長さ方向一端に漏液検知器を設けたりすることによって、コルゲート管11や保護管13が破損してその空隙に漏液した場合、その漏液を検出し得るようにすることができる。 The corrugated tube 11 and the protective tube 13 are damaged by providing a leak detection line in the gap between the corrugated tube 11 and the protective tube 13 or by providing a leak detector at one end in the length direction of the gap. If the liquid leaks into the gap, the liquid leakage can be detected.
上記実施形態は、水aと冷媒bとによる熱交換の場合であったが、この発明は、質の異なる熱交換媒体と被熱交換媒体との熱交換であれば、何れの態様においても採用し得ることは勿論である。また、コルゲート管11は円管(円状パイプ)でなくても、扁平管とすることができる(特許文献2図5〜図7参照)。さらに、内管10に被熱交換媒体(例えば、水a)、内外管間に熱交換媒体(例えば、冷媒b)を流通させることもできる。
このように、今回開示された実施の形態はすべての点で例示であって制限的なものではないと考えられるべきである。この発明の範囲は、特許請求の範囲によって示され、特許請求の範囲と均等の意味および範囲内でのすべての変更が含まれることが意図される。
The above embodiment is a case of heat exchange between the water a and the refrigerant b, but the present invention is adopted in any aspect as long as heat exchange is performed between the heat exchange medium and the heat exchange medium having different qualities. Of course you can. Moreover, the corrugated pipe | tube 11 can be made into a flat tube even if it is not a circular pipe (circular pipe) (refer patent document 2 FIGS. 5-7). Furthermore, a heat exchange medium (for example, water a) can be circulated through the inner pipe 10 and a heat exchange medium (for example, refrigerant b) can be circulated between the inner and outer pipes.
Thus, it should be thought that embodiment disclosed this time is an illustration and restrictive at no points. The scope of the present invention is defined by the terms of the claims, and is intended to include any modifications within the scope and meaning equivalent to the terms of the claims.
10 内管
11 コルゲート管
12 コルゲート管表面の溝
13 保護管
14 保護管表面の凹凸
20 外管
21 リブ
22 間隙
A 熱交換器
a 水(被熱交換媒体)
b 冷媒(熱交換媒体)
DESCRIPTION OF SYMBOLS 10 Inner pipe | tube 11 Corrugated pipe | tube 12 The groove | channel 13 of the corrugated pipe surface 13 Protective pipe 14 The unevenness | corrugation 20 of the protective pipe surface Outer pipe | tube 21 Rib 22 Gap | interval A Heat exchanger a Water (heat exchange medium)
b Refrigerant (heat exchange medium)
Claims (3)
複数のコルゲート管(11)が並列され、その並列されたコルゲート管(11)を保護管(13)で被覆し、その保護管(13)は、各コルゲート管(11)の外面に密着されて、保護管(13)の外面もコルゲート管(11)の外面に倣って凹凸状(14)となっていることを特徴とする熱交換管。 The heat exchange medium (b) or the heat exchange medium (a) of different quality is circulated inside, and the medium (a, b) and the external heat exchange medium (a) or heat exchange medium (b) A heat exchange pipe (10) for performing heat exchange,
A plurality of corrugated pipes (11) are arranged in parallel, the parallel corrugated pipes (11) are covered with a protective pipe (13), and the protective pipes (13) are in close contact with the outer surface of each corrugated pipe (11). The heat exchange tube is characterized in that the outer surface of the protective tube (13) is also uneven (14) following the outer surface of the corrugated tube (11).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2014096596A JP6321442B2 (en) | 2014-05-08 | 2014-05-08 | HEAT EXCHANGE TUBE, HEAT EXCHANGER USING SAME, AND HEAT EXCHANGE DEVICE |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2014096596A JP6321442B2 (en) | 2014-05-08 | 2014-05-08 | HEAT EXCHANGE TUBE, HEAT EXCHANGER USING SAME, AND HEAT EXCHANGE DEVICE |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2015215100A true JP2015215100A (en) | 2015-12-03 |
JP6321442B2 JP6321442B2 (en) | 2018-05-09 |
Family
ID=54752145
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2014096596A Active JP6321442B2 (en) | 2014-05-08 | 2014-05-08 | HEAT EXCHANGE TUBE, HEAT EXCHANGER USING SAME, AND HEAT EXCHANGE DEVICE |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP6321442B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2019158228A (en) * | 2018-03-13 | 2019-09-19 | 株式会社ワイ・ジェー・エス. | Heat exchanger |
CN111006396A (en) * | 2019-12-30 | 2020-04-14 | 四川昊宇龙星科技有限公司 | Dual-purpose double-layer sleeve heat exchanger |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60103295A (en) * | 1983-11-10 | 1985-06-07 | Fuji Electric Co Ltd | Double pipe type heat exchanger |
JP2004340555A (en) * | 2003-05-19 | 2004-12-02 | Furukawa Electric Co Ltd:The | Heat exchanger |
JP2005009832A (en) * | 2003-06-20 | 2005-01-13 | Hitachi Cable Ltd | Double pipe type heat exchanger |
JP2008196792A (en) * | 2007-02-14 | 2008-08-28 | Matsushita Electric Ind Co Ltd | Heat exchanger |
JP2012002495A (en) * | 2010-05-18 | 2012-01-05 | Yjs:Kk | Heat exchanger |
US20120055660A1 (en) * | 2010-09-02 | 2012-03-08 | Cerro Flow Products Llc | Flattened fluid conduits for use in heat exchangers and other systems, and associated methods of manufacture and use |
JP2012112556A (en) * | 2010-11-22 | 2012-06-14 | Nippon Itomic Co Ltd | Heat exchanger and method of connecting the same |
-
2014
- 2014-05-08 JP JP2014096596A patent/JP6321442B2/en active Active
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60103295A (en) * | 1983-11-10 | 1985-06-07 | Fuji Electric Co Ltd | Double pipe type heat exchanger |
JP2004340555A (en) * | 2003-05-19 | 2004-12-02 | Furukawa Electric Co Ltd:The | Heat exchanger |
JP2005009832A (en) * | 2003-06-20 | 2005-01-13 | Hitachi Cable Ltd | Double pipe type heat exchanger |
JP2008196792A (en) * | 2007-02-14 | 2008-08-28 | Matsushita Electric Ind Co Ltd | Heat exchanger |
JP2012002495A (en) * | 2010-05-18 | 2012-01-05 | Yjs:Kk | Heat exchanger |
US20120055660A1 (en) * | 2010-09-02 | 2012-03-08 | Cerro Flow Products Llc | Flattened fluid conduits for use in heat exchangers and other systems, and associated methods of manufacture and use |
JP2012112556A (en) * | 2010-11-22 | 2012-06-14 | Nippon Itomic Co Ltd | Heat exchanger and method of connecting the same |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2019158228A (en) * | 2018-03-13 | 2019-09-19 | 株式会社ワイ・ジェー・エス. | Heat exchanger |
JP7064908B2 (en) | 2018-03-13 | 2022-05-11 | 株式会社ワイ・ジェー・エス. | Heat exchanger |
CN111006396A (en) * | 2019-12-30 | 2020-04-14 | 四川昊宇龙星科技有限公司 | Dual-purpose double-layer sleeve heat exchanger |
Also Published As
Publication number | Publication date |
---|---|
JP6321442B2 (en) | 2018-05-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPWO2019176566A1 (en) | Plate heat exchanger, heat pump device including plate heat exchanger, and heat pump heating and hot water supply system including heat pump device | |
JP6321442B2 (en) | HEAT EXCHANGE TUBE, HEAT EXCHANGER USING SAME, AND HEAT EXCHANGE DEVICE | |
JP6211313B2 (en) | Triple tube heat exchanger | |
RU2019110262A (en) | PIPE ASSEMBLY FOR PIPE HEAT EXCHANGER AND TUBE HEAT EXCHANGER CONTAINING SUCH PIPE ASSEMBLY | |
KR101064630B1 (en) | Heat exchanger | |
JP2006078062A (en) | Heat exchanger | |
JPH08313177A (en) | Multi-tube type heat exchanger | |
JP2009264644A (en) | Heat exchanger | |
JP2005069620A (en) | Heat exchanger | |
JP2010255856A (en) | Heat exchanger and heat pump water heater using the same | |
JP2009264643A (en) | Heat exchanger | |
JP2013253710A (en) | Heat exchanger and heat pump water heater with the same | |
JP2005147567A (en) | Double pipe type heat exchanger | |
JP2008267631A (en) | Heat exchanger | |
JP6115375B2 (en) | Hot water storage unit and water heater | |
JP2012107768A (en) | Water refrigerant heat exchanger | |
KR102010156B1 (en) | shell in a shell and plate heat exchanger, and shell and plate heat exchanger having the same | |
JP2008175450A (en) | Heat exchanger | |
KR20150004531A (en) | Heat Exchanger | |
JP2010032183A (en) | Heat exchanger | |
JP2014005990A (en) | Heat exchanger and heat pump water heater including the same | |
JP2010255857A (en) | Heat exchanger and heat pump water heater using the same | |
KR101500064B1 (en) | Heat exchanging unit and plate type heat exchanger having thereof | |
CA2745590A1 (en) | Hybrid horizontal drainpipe heat exchanger | |
JP2014016058A (en) | Device for performing heat exchange between water and refrigerant, and heat pump hot water supply device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20170119 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20170822 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20170823 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20171020 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20180306 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20180405 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 6321442 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |