JP6153458B2 - Heat exchanger - Google Patents

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JP6153458B2
JP6153458B2 JP2013254529A JP2013254529A JP6153458B2 JP 6153458 B2 JP6153458 B2 JP 6153458B2 JP 2013254529 A JP2013254529 A JP 2013254529A JP 2013254529 A JP2013254529 A JP 2013254529A JP 6153458 B2 JP6153458 B2 JP 6153458B2
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header
plate
heat exchanger
pipe
water
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JP2015114003A (en
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晃史 西野
晃史 西野
英克 成瀬
英克 成瀬
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Rinnai Corp
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]

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  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
  • Details Of Fluid Heaters (AREA)
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Description

本発明は、流入ヘッダと流出ヘッダとを介して吸熱管内に流す水を燃焼排気により熱交換加熱する熱交換器に関する。   The present invention relates to a heat exchanger that heats and heats water flowing into a heat absorption pipe via an inflow header and an outflow header by combustion exhaust.

高熱効率化のために吸熱管の細管化を図った場合でも、水抜き作業時に吸熱管の先端開口に水膜が張ることを防止し、円滑な水抜きが可能となるよう、図5及び図6に示すようなヘッダ160内に並設された複数のパイプ端開口152aに対して連続して対向配置される水抜き板170を有する熱交換器が本出願人によって先に提案されている。この熱交換器では、ヘッダ160内でのパイプ端開口152aと水抜き板170との間の隙間を、パイプ端開口152aに水の表面張力に起因して形成される水膜の盛り上がり量以下に設定することにより、パイプ端開口152aと水抜き板170との間に水抜き流路を形成し、水抜き時の流水方向下流部における水の残留を防止している(特許文献1)。   Even when the endothermic tube is narrowed for high thermal efficiency, the water film is prevented from being stretched at the end opening of the endothermic tube during the draining operation so that smooth drainage is possible. The present applicant has previously proposed a heat exchanger having a water draining plate 170 arranged continuously facing a plurality of pipe end openings 152a arranged in parallel in a header 160 as shown in FIG. In this heat exchanger, the gap between the pipe end opening 152a and the water draining plate 170 in the header 160 is less than or equal to the rising amount of the water film formed in the pipe end opening 152a due to the surface tension of water. By setting, a drain passage is formed between the pipe end opening 152a and the drain plate 170 to prevent water from remaining in the downstream portion in the flowing direction when draining (Patent Document 1).

特開2010−175103JP 2010-175103 A

しかしながら、上記熱交換器を工業的に生産するにあたっては、吸熱管152の長さの製造誤差や、吸熱管152とヘッダ160とを接合する際の組み付け誤差などが生じるため、複数の吸熱管152をヘッダ本体161に設けた差込口163に挿入したとき、図6に見られるようにヘッダ160内に突出する各吸熱管152の出寸法を完全に一致させることは難しい。従って、特許文献1のように複数のパイプ端開口152aに対して連続して対向配置される水抜き板170では、水抜き板170が吸熱管152の出寸法の相違に追随することができず、パイプ端開口152aと水抜き板170との間の隙間を水膜の盛り上がり量以下にできない部分が生じるという問題がある。また、組み立て時にはパイプ端開口152aと水抜き板170との間に所定の隙間が形成されていても、凍結時に大きな負荷がかかって水抜き板170のパイプ端開口152aと対向する部分が変形した場合、水抜き板170は元の形状に戻らないため、隙間が大きくなるという問題がある。しかも、上記水抜き流路を形成するためのパイプ端開口152aと水抜き板170との間の隙間は、ヘッダ本体161をヘッダ蓋162で閉塞することによって形成されるため、吸熱管152の出寸法の相違により所定の隙間が形成されているかどうかの確認や、所定の隙間が形成されていない場合の調整もできない。それゆえ、ヘッダ本体161とヘッダ蓋162との間の距離、及び水抜き板170の高さが設計通り形成されていたとしても、水抜き不良が生じる場合がある。   However, when the heat exchanger is industrially produced, a manufacturing error in the length of the heat absorption tube 152, an assembly error when the heat absorption tube 152 and the header 160 are joined, and the like occur. Is inserted into the insertion port 163 provided in the header body 161, it is difficult to completely match the outgoing dimensions of the respective heat absorption tubes 152 protruding into the header 160 as seen in FIG. Therefore, in the drainage plate 170 continuously arranged opposite to the plurality of pipe end openings 152a as in Patent Document 1, the drainage plate 170 cannot follow the difference in the protruding size of the heat absorption tube 152. In addition, there is a problem in that there is a portion where the gap between the pipe end opening 152a and the drain plate 170 cannot be reduced below the rising amount of the water film. Further, even when a predetermined gap is formed between the pipe end opening 152a and the drain plate 170 at the time of assembly, a large load is applied during freezing and the portion of the drain plate 170 facing the pipe end opening 152a is deformed. In this case, since the drain plate 170 does not return to its original shape, there is a problem that the gap becomes large. In addition, the gap between the pipe end opening 152a and the drain plate 170 for forming the drain channel is formed by closing the header body 161 with the header lid 162. It is impossible to confirm whether or not the predetermined gap is formed due to the difference in dimensions, and it is not possible to adjust when the predetermined gap is not formed. Therefore, even if the distance between the header body 161 and the header lid 162 and the height of the drainage plate 170 are formed as designed, a drainage failure may occur.

本発明は、上記課題を解決するためになされたものであり、ヘッダ内に吸熱管の水抜き板を設ける場合に、ヘッダ内での吸熱管の出寸法が異なる場合でも確実に水抜きが可能な熱交換器を生産性よく製造することにある。   The present invention has been made to solve the above-described problems. When a drain plate of the heat absorption pipe is provided in the header, the water can be reliably drained even when the end dimensions of the heat absorption pipe in the header are different. Is to manufacture a simple heat exchanger with high productivity.

本発明は、
燃焼排気が流れるケースと、
前記ケース内に配置された複数の吸熱管と、
前記ケースの側板に配置され、各吸熱管の一端部及び他端部がそれぞれ挿入されて接続される流入ヘッダ及び流出ヘッダと、
高さ位置が低位置側のヘッダ内に配置され、前記吸熱管内の水抜き時に並設された複数のパイプ端開口に達した水を水抜きするための水抜き板と、を備える熱交換器であって、
前記水抜き板は、複数のパイプ端開口のそれぞれに弾性的な付勢力を有して当接するように分離された分離板を有する熱交換器である。
The present invention
A case where combustion exhaust flows,
A plurality of endothermic tubes disposed in the case;
An inflow header and an outflow header which are arranged on the side plate of the case, and are connected by inserting one end and the other end of each heat absorption tube,
A heat exchanger comprising: a drain plate for draining water that has been arranged in a header at a low position on the low position side and drains water that has reached a plurality of pipe end openings arranged in parallel when draining water in the heat absorption pipe Because
The drainage plate is a heat exchanger having a separation plate separated so as to come into contact with each of a plurality of pipe end openings with an elastic biasing force.

上記水抜き板は、複数の吸熱管のパイプ端開口のそれぞれに弾性的な付勢力を有して当接するように分離された分離板を備えるから、ヘッダ内での吸熱管の出寸法が異なる場合でも、分離板が出寸法の相違を吸収でき、いずれのパイプ端開口にも分離板の少なくとも一部を当接させた状態で水抜き板を配置することができる。それゆえ、パイプ端開口と分離板との間の隙間を狭くできるから、いずれのパイプ端開口からも確実に水抜き流路を形成することができる。また、分離板がパイプ端開口に弾性的な付勢力でもって当接しているから、凍結時に分離板に負荷がかかっても、パイプ端開口と分離板との間の隙間が大きくなるのを防ぐことができる。   Since the water draining plate includes a separation plate that is separated so as to come into contact with each of the pipe end openings of the plurality of heat absorption tubes with an elastic biasing force, the dimensions of the heat absorption tubes in the header are different. Even in this case, the separation plate can absorb the difference in the protruding size, and the drain plate can be arranged in a state where at least a part of the separation plate is brought into contact with any of the pipe end openings. Therefore, since the gap between the pipe end opening and the separation plate can be narrowed, the drainage channel can be reliably formed from any pipe end opening. In addition, since the separation plate abuts the pipe end opening with an elastic biasing force, even if a load is applied to the separation plate during freezing, the gap between the pipe end opening and the separation plate is prevented from becoming large. be able to.

好ましくは、上記熱交換器において、
上記水抜き板は、複数の分離板を支持する支持部を備え、
前記各分離板は、ヘッダ内に配置される前の状態で支持部が下方になるように水抜き板を設置したとき、分離板の自由端が支持部側の固定端よりも高くなるように傾斜して設けられる。
Preferably, in the heat exchanger,
The drainage plate includes a support portion that supports a plurality of separation plates,
Each separation plate is arranged such that when the drainage plate is installed so that the support portion is in the lower state before being arranged in the header, the free end of the separation plate is higher than the fixed end on the support portion side. Inclined.

最も出寸法の大きな吸熱管と最も出寸法の小さい吸熱管とでパイプ端開口の位置が大きく異なる場合、分離板の固定端と自由端とが同一高さに形成されていると、弾性変形可能な分離板を形成しても、パイプ端開口の全てに分離板を当接させることが難しい。
しかしながら、上記水抜き板は、複数の分離板を支持する支持部を備えており、各分離板は、ヘッダ内に配置される前の状態において、自由端が固定端よりも高くなるように傾斜しているから、各分離板の自由端が固定端よりもヘッダ内でパイプ端開口に近接する傾斜面で形成されるとともに、各分離板がパイプ端開口に当接したときの弾性変形可能な範囲が大きくなる。その結果、各吸熱管の出寸法が大きく異なる場合でも、これに分離板を追随させることができ、全てのパイプ端開口に分離板を確実に弾性的な付勢力をもって当接させることができる。
If the position of the pipe end opening differs greatly between the endothermic pipe with the largest output dimension and the endothermic pipe with the smallest output dimension, it can be elastically deformed if the fixed end and free end of the separation plate are formed at the same height. Even if a separate separator plate is formed, it is difficult to bring the separator plate into contact with all the pipe end openings.
However, the drain plate includes a support portion that supports a plurality of separation plates, and each separation plate is inclined so that the free end is higher than the fixed end before being disposed in the header. Therefore, the free end of each separation plate is formed with an inclined surface closer to the pipe end opening in the header than the fixed end, and is elastically deformable when each separation plate abuts on the pipe end opening. The range becomes larger. As a result, even if the projecting dimensions of the respective heat absorption tubes are greatly different, the separation plate can be followed, and the separation plate can be reliably brought into contact with all the pipe end openings with an elastic biasing force.

以上のように、本発明に係る熱交換器によれば、ヘッダ内に水抜き板を配置させた熱交換器を工業的に生産する場合に、吸熱管の長さの製造誤差や吸熱管とヘッダとの取り付け誤差などでヘッダ内での吸熱管の出寸法が相違していても、水抜き板により出寸法の相違を吸収できるから、いずれの吸熱管のパイプ端開口にも水抜き板を当接させることができ、確実に水抜きを行うことができる。従って、水抜きを考慮して吸熱管の長さや取り付け時の吸熱管の位置決めを高精度に管理する必要がない。また、凍結によって分離板に負荷がかかってもパイプ端開口と分離板との間の隙間が大きくなるのを防ぐこともできる。よって、水抜き不良の生じ難い熱交換器を効率よく生産することが可能となる。   As described above, according to the heat exchanger according to the present invention, when industrially producing a heat exchanger in which a drainage plate is arranged in the header, the manufacturing error of the length of the heat absorption tube and the heat absorption tube Even if the heat sink tube exit dimensions in the header are different due to mounting errors with the header, etc., the difference in the output dimension can be absorbed by the water drain plate. It can be made to contact, and it can drain reliably. Therefore, it is not necessary to manage the length of the heat absorption tube and the positioning of the heat absorption tube at the time of attachment with high accuracy in consideration of drainage. Further, even when a load is applied to the separation plate due to freezing, it is possible to prevent the gap between the pipe end opening and the separation plate from becoming large. Therefore, it is possible to efficiently produce a heat exchanger that is unlikely to cause water drainage failure.

本発明の実施の形態に係る熱交換器を備えた給湯装置の構成を示す概略断面図である。It is a schematic sectional drawing which shows the structure of the hot water supply apparatus provided with the heat exchanger which concerns on embodiment of this invention. 本発明の実施の形態に係る副熱交換器の流入ヘッダの部分を分解した概略斜視図である。It is the schematic perspective view which decomposed | disassembled the part of the inflow header of the subheat exchanger which concerns on embodiment of this invention. 本発明の実施の形態に係る水抜き板を示す概略構成図であり、(A)は正面図を、(B)は断面図を示す。It is a schematic block diagram which shows the water draining plate which concerns on embodiment of this invention, (A) shows a front view, (B) shows sectional drawing. 本発明の実施の形態に係る流入ヘッダの内部構成を示す概略横断面図である。It is a schematic cross-sectional view which shows the internal structure of the inflow header which concerns on embodiment of this invention. 従来の水抜き板を示す概略構成図である。It is a schematic block diagram which shows the conventional water draining board. 従来の水抜き板を配置した流入ヘッダの内部構成を示す概略横断面図である。It is a schematic cross-sectional view which shows the internal structure of the inflow header which has arrange | positioned the conventional water draining board.

以下に、本発明の実施形態について添付図面を参照しながら説明する。
図1に示す給湯装置1は、潜熱回収型給湯装置であり、外装ケース2内に、ガスバーナ31を内蔵する燃焼筐3と、燃焼筐3の上方の主熱交換器4と、主熱交換器4の上方の副熱交換器5とを備えている。燃焼筐3の下側には、燃焼筐3内に燃焼用空気を供給する給気ファン11が設置されている。
Embodiments of the present invention will be described below with reference to the accompanying drawings.
A hot water supply apparatus 1 shown in FIG. 1 is a latent heat recovery type hot water supply apparatus, and includes a combustion housing 3 containing a gas burner 31 in an outer case 2, a main heat exchanger 4 above the combustion housing 3, and a main heat exchanger. 4 and an auxiliary heat exchanger 5 above. An air supply fan 11 that supplies combustion air into the combustion housing 3 is installed below the combustion housing 3.

主熱交換器4は、ガスバーナ31の燃焼排気が流れる胴部40内に間隔を存して並設した多数の吸熱フィン41と、これら吸熱フィン41を蛇行形状に貫通する吸熱管42とを備えている。副熱交換器5は、潜熱熱交換器であり、ケース50内に横向き蛇行形状に配置した複数本の吸熱管52を備えている。吸熱管52は、耐食性金属、例えば、ステンレス製、チタン製等のコルゲート管を蛇行形状に曲げ加工して形成される。ケース50の横方向一側の側板51には、流入ヘッダ6aと流出ヘッダ6bとが設けられ、複数本の吸熱管52の一端部が流入ヘッダ6aに接続され、他端部が流出ヘッダ6bに接続されている。流入ヘッダ6aには給水管81が接続され、流出ヘッダ6bには主熱交換器4の吸熱管42の上流端に繋がる接続管83が接続されている。主熱交換器4の吸熱管42の下流端には出湯管82が接続されている。副熱交換器5は、底板53の後部には主熱交換器4を通過した燃焼排気の排気導入口54が開設され、ケース50の前面には副熱交換器5を通過した燃焼排気を排出する排気口55が設けられる。   The main heat exchanger 4 includes a large number of endothermic fins 41 arranged in parallel in the body 40 through which the combustion exhaust gas of the gas burner 31 flows, and an endothermic pipe 42 penetrating the endothermic fins 41 in a meandering shape. ing. The auxiliary heat exchanger 5 is a latent heat exchanger, and includes a plurality of heat absorption tubes 52 arranged in a meandering manner in the case 50. The endothermic tube 52 is formed by bending a corrugated tube made of a corrosion-resistant metal such as stainless steel or titanium into a meandering shape. The side plate 51 on one side of the case 50 is provided with an inflow header 6a and an outflow header 6b. One end of a plurality of heat absorption tubes 52 is connected to the inflow header 6a, and the other end is connected to the outflow header 6b. It is connected. A water supply pipe 81 is connected to the inflow header 6a, and a connection pipe 83 connected to the upstream end of the heat absorption pipe 42 of the main heat exchanger 4 is connected to the outflow header 6b. A tapping pipe 82 is connected to the downstream end of the heat absorption pipe 42 of the main heat exchanger 4. The auxiliary heat exchanger 5 has an exhaust inlet 54 for combustion exhaust that has passed through the main heat exchanger 4 at the rear of the bottom plate 53, and exhausts the combustion exhaust that has passed through the auxiliary heat exchanger 5 on the front surface of the case 50. An exhaust port 55 is provided.

そして、出湯管82の下流端の出湯栓が開かれると給水管81から副熱交換器5の吸熱管52、主熱交換器4の吸熱管42へと通水され、また、ガスバーナ31が燃焼される。主熱交換器4では、ガスバーナ31の燃焼による燃焼排気中から主に顕熱を吸収して吸熱管42内を流れる水を熱交換加熱する。副熱交換器5では、燃焼排気中の水蒸気を凝縮して潜熱を吸収して吸熱管52内の水を熱交換加熱する。これにより、副熱交換器5及び主熱交換器4で加熱された温水が出湯管82から出湯される。   When the outlet tap at the downstream end of the hot water pipe 82 is opened, water is passed from the water supply pipe 81 to the heat absorption pipe 52 of the auxiliary heat exchanger 5 and the heat absorption pipe 42 of the main heat exchanger 4, and the gas burner 31 is combusted. Is done. In the main heat exchanger 4, sensible heat is mainly absorbed from the combustion exhaust gas generated by the combustion of the gas burner 31, and the water flowing in the heat absorption pipe 42 is heat exchange heated. The auxiliary heat exchanger 5 condenses the water vapor in the combustion exhaust and absorbs latent heat to heat and heat the water in the heat absorption pipe 52. As a result, the hot water heated by the sub heat exchanger 5 and the main heat exchanger 4 is discharged from the hot water discharge pipe 82.

なお、副熱交換器5は、後上がりに僅か傾斜(約5°)して設置されている。副熱交換器5において燃焼排気中の水蒸気の凝縮により発生した酸性のドレン水は、傾斜した底板53に滴下され、低位置のドレン回収部56からドレン排水管57を通り中和器58で中和された後、下水に排水される。   The auxiliary heat exchanger 5 is installed with a slight inclination (about 5 °) in the rearward direction. Acidic drain water generated by the condensation of water vapor in the combustion exhaust gas in the auxiliary heat exchanger 5 is dropped on the inclined bottom plate 53, and passes through the drain drain pipe 57 from the drain recovery portion 56 at the lower position and is neutralized in the neutralizer 58. After being summed, it is drained into sewage.

図2、及び図4に示すように、副熱交換器5における流入ヘッダ6aと流出ヘッダ6bは、側板51の所定位置を絞り加工することによりケース50の内方へ凹ませた凹部よりなるヘッダ本体61と、ケース50の外側から配設されてヘッダ本体61との間に閉鎖空間60を画成するヘッダ蓋62とを備えている。ヘッダ本体61には、吸熱管52用の差込口63が複数本の吸熱管52に対応して左右2列で千鳥状に複数開設され、ヘッダ蓋62には、給水管81や接続管83用の単一のジョイント部64が設けられている。ヘッダ蓋62は、ジョイント部64を設けない裏側が全周囲に周壁65を形成する浅い器状に形成されている。ヘッダ蓋62の裏側をヘッダ本体61の凹部に向けてヘッダ本体61の凹部内にヘッダ蓋62を嵌め込み、ヘッダ本体61の凹部内壁68とヘッダ蓋62の周壁65の外面とを重ね合わせた状態でロウ付けして各ヘッダ6a,6bが形成される。   As shown in FIGS. 2 and 4, the inflow header 6 a and the outflow header 6 b in the auxiliary heat exchanger 5 are headers formed by recesses recessed inward of the case 50 by drawing a predetermined position of the side plate 51. A main body 61 and a header lid 62 that is disposed from the outside of the case 50 and defines a closed space 60 between the main body 61 and the header main body 61 are provided. In the header main body 61, a plurality of insertion ports 63 for the heat absorption pipes 52 are provided in a staggered manner in two rows on the left and right sides corresponding to the plurality of heat absorption pipes 52, and a water supply pipe 81 and a connection pipe 83 are provided in the header lid 62. A single joint portion 64 is provided. The header lid 62 is formed in a shallow vessel shape in which the back side where the joint portion 64 is not provided forms a peripheral wall 65 on the entire periphery. The header lid 62 is fitted into the recess of the header body 61 with the back side of the header lid 62 facing the recess of the header body 61, and the recess inner wall 68 of the header body 61 and the outer surface of the peripheral wall 65 of the header lid 62 are overlapped. Each header 6a, 6b is formed by brazing.

流入ヘッダ6aのジョイント部64の位置は、下側に設けられており、流出ヘッダ6bにおけるジョイント部64の位置は、上側に設けられている。そして、副熱交換器5を傾けて設置することから、高さ位置は、流入ヘッダ6aの方が低位置に配置されている。   The position of the joint portion 64 of the inflow header 6a is provided on the lower side, and the position of the joint portion 64 in the outflow header 6b is provided on the upper side. And since the sub heat exchanger 5 is installed inclining, the inflow header 6a is arrange | positioned in the lower position in the height position.

本実施形態における副熱交換器5は、ケース50内に細管化された吸熱管52(例えば、口径:φ10mm)が8本配設されている。これにより、限られたスペース内に多くの吸熱管52を配置し、小型化が図られ且つ吸熱管52の伝熱面積が増して高熱効率化が達成される。これらの吸熱管52の一端部及び他端部はそれぞれ、流入ヘッダ6a及び流出ヘッダ6bのヘッダ本体61の差込口63に挿入されており、ヘッダ本体61の凹部内に突出させた吸熱管52のパイプ端開口52aは、左右2列で千鳥状に並設されている。   In the sub heat exchanger 5 in the present embodiment, eight heat absorption tubes 52 (for example, caliber: φ10 mm) are arranged in a case 50. Thereby, many heat absorption pipes 52 are arranged in a limited space, the size is reduced, and the heat transfer area of the heat absorption pipes 52 is increased, thereby achieving high thermal efficiency. One end portion and the other end portion of these heat absorption tubes 52 are respectively inserted into the insertion ports 63 of the header main body 61 of the inflow header 6a and the outflow header 6b, and the heat absorption tubes 52 protruded into the recesses of the header main body 61. The pipe end openings 52a are arranged in a staggered manner in two rows on the left and right.

図2〜図4に示すように、低位置側に配置された流入ヘッダ6a内には、水抜き時にパイプ端開口52aとの間で水抜き流路を形成するための水抜き板7が配設されている。本実施の形態の水抜き板7は、一枚の金属板(例えば、SUS304製、厚さ:約0.5mm)を成形加工することにより形成されており、支持部71と、支持部71の左右両下縁に支持された複数の分離板70(本実施の形態では、8枚)とを備えている。支持部71は、金属板を折り曲げて溝部を間に有する板状に形成されており、各分離板70は、流入ヘッダ6a内に水抜き板7が配置されたとき、パイプ端開口52aに弾性的な付勢力をもって当接可能なように、支持部71に支持される固定端76と、支持部71と反対側で自由端75を有する薄板状に形成されている。なお、支持部71は、左右の分離板70それぞれを支持するように形成してもよい。   As shown in FIGS. 2 to 4, in the inflow header 6 a arranged on the low position side, a drain plate 7 for forming a drain channel with the pipe end opening 52 a at the time of draining is arranged. It is installed. The drain plate 7 according to the present embodiment is formed by molding a single metal plate (for example, made of SUS304, thickness: about 0.5 mm). A plurality of separation plates 70 (eight in the present embodiment) supported by the left and right lower edges are provided. The support portion 71 is formed in a plate shape having a groove portion formed by bending a metal plate, and each separation plate 70 is elastic to the pipe end opening 52a when the drainage plate 7 is disposed in the inflow header 6a. It is formed in a thin plate shape having a fixed end 76 supported by the support portion 71 and a free end 75 on the opposite side to the support portion 71 so as to be able to come into contact with a specific urging force. The support portion 71 may be formed to support the left and right separation plates 70.

分離板70は、ヘッダ本体61の凹部内に突出させたパイプ端開口52aの配設位置に合わせて、支持部71を中心として左右2列で千鳥状に設けられている。また、千鳥状に配置された分離板70の最上位及び最下位以外に位置する分離板70はいずれも、固定端76と自由端75が同幅の略矩形状に形成されているが、最上位及び最下位に位置する分離板70はそれぞれ、ヘッダ本体61の内壁68の形状に合わせて、上縁及び下縁を傾斜させた略台形状に形成されている。   The separation plates 70 are provided in a staggered manner in two rows on the left and right sides around the support portion 71 in accordance with the arrangement position of the pipe end opening 52 a protruding into the recess of the header body 61. In addition, the separation plate 70 positioned in a staggered manner other than the uppermost and lowermost separation plates 70 has a fixed end 76 and a free end 75 formed in a substantially rectangular shape having the same width. The separation plates 70 positioned at the upper and lowermost positions are each formed in a substantially trapezoidal shape with the upper and lower edges inclined according to the shape of the inner wall 68 of the header body 61.

水抜き板7は、パイプ端開口52aと分離板70とを位置決め状態で対向させるために、ヘッダ本体61の底部に略沿った大きさを有している。各分離板70は、水抜き時に水が残留しやすいパイプ端開口52aの少なくとも一部を覆う大きさであれば特に限定されないが、好ましくは、分離板70がパイプ端開口52aと正対したときに、パイプ端開口52a全体が分離板70で覆われるように、対向配置されるパイプ端開口52aの口径よりも若干大きく形成される。なお、各分離板70を分離する切れ込み部77の幅は、分離板70の大きさと上下で隣接するパイプ端開口52aの間隔に合わせて適宜設定することができる。   The drain plate 7 has a size substantially along the bottom of the header body 61 so that the pipe end opening 52a and the separation plate 70 face each other in a positioned state. Each separation plate 70 is not particularly limited as long as it covers at least a part of the pipe end opening 52a where water tends to remain when draining, but preferably, when the separation plate 70 faces the pipe end opening 52a. In addition, the pipe end opening 52 a is formed to be slightly larger than the diameter of the opposed pipe end opening 52 a so that the entire pipe end opening 52 a is covered with the separation plate 70. Note that the width of the notch 77 that separates the separation plates 70 can be set as appropriate according to the size of the separation plate 70 and the interval between the pipe end openings 52a adjacent in the vertical direction.

また、図3に示すように、本実施の形態の分離板70は、流入ヘッダ6a内に配置される前の状態で支持部71が下方になるように水抜き板7を設置したとき、自由端75が支持部71と接続されている固定端76よりも高くなるように形成されている。すなわち、分離板70は、分離板70に負荷が加えられていない状態では、90°より大きな鈍角で支持部71と連接されており、左右の分離板70は、支持部71を鼎の中心として扇状に広がるように形成されている。これにより、固定端76と自由端75とが支持部71に対して略同一高さに形成されている場合よりも、自由端75をパイプ端開口52aに近接させることができるとともに、分離板70の弾性変形可能な許容範囲を広げることができる。   Moreover, as shown in FIG. 3, the separation plate 70 of the present embodiment is free when the drain plate 7 is installed so that the support portion 71 is positioned downward in the state before being arranged in the inflow header 6a. The end 75 is formed to be higher than the fixed end 76 connected to the support portion 71. That is, the separation plate 70 is connected to the support portion 71 at an obtuse angle larger than 90 ° in a state where no load is applied to the separation plate 70, and the left and right separation plates 70 have the support portion 71 as the center of the bag. It is formed to spread in a fan shape. As a result, the free end 75 can be brought closer to the pipe end opening 52 a than the case where the fixed end 76 and the free end 75 are formed at substantially the same height with respect to the support portion 71, and the separation plate 70. The permissible range of elastic deformation can be expanded.

さらに、分離板70の自由端75側には、支持部71側に折り曲げられた曲げ部73が形成されている。この曲げ部73の先端は、後述するように、流入ヘッダ6a内に水抜き板7が配置されたとき、出寸法の大きな吸熱管52のパイプ端開口52aと対向するヘッダ蓋62の周壁65の上端面と当接するように設けられている(図4)。   Further, a bent portion 73 that is bent toward the support portion 71 is formed on the free end 75 side of the separation plate 70. As will be described later, the bent portion 73 has a distal end of a peripheral wall 65 of the header lid 62 facing the pipe end opening 52a of the heat absorption pipe 52 having a large output dimension when the drain plate 7 is disposed in the inflow header 6a. It is provided in contact with the upper end surface (FIG. 4).

分離板70は、中央部に開設された口径の大きな4つの大孔部74aと、その上下に開設された口径の小さな2つの小孔部74bとを有している。これらの孔部74a,74bの口径は、パイプ端開口52aのそれよりも小径であり、分離板70がパイプ端開口52aと正対したときに、大孔部74aの全てと、小孔部74bの一部がパイプ端開口52a内に位置している。これにより、分離板70の略全面がパイプ端開口52aに当接しても、水が円滑に分離板70を通過でき、副熱交換器5の通常使用時に流入ヘッダ6aを介した吸熱管52への水の円滑な流通を確保できる。   The separation plate 70 has four large hole portions 74a having a large diameter opened at the central portion, and two small hole portions 74b having a small diameter opened at the top and bottom thereof. The diameters of these holes 74a and 74b are smaller than that of the pipe end opening 52a. When the separating plate 70 faces the pipe end opening 52a, all of the large holes 74a and the small holes 74b are formed. Is located in the pipe end opening 52a. Thereby, even if substantially the entire surface of the separation plate 70 abuts on the pipe end opening 52a, water can smoothly pass through the separation plate 70, and to the heat absorption pipe 52 via the inflow header 6a during normal use of the auxiliary heat exchanger 5. Smooth distribution of water.

本実施の形態において、支持部71は、流入ヘッダ6a内に水抜き板7が配置されたとき、左右に並列されたパイプ端開口52aの間に位置するように設けられている。支持部71の高さは、ヘッダ本体61の凹部に水抜き板7を配置してヘッダ蓋62をヘッダ本体61に嵌め込み、分離板70の少なくとも一部がパイプ端開口52aに当接したとき、支持部71の頂点がヘッダ蓋62の底面67に当接するように形成されている。なお、支持部71には、開孔が形成されていないが、分離板70と同様に開孔を設けてもよい。   In the present embodiment, the support portion 71 is provided so as to be positioned between the pipe end openings 52a juxtaposed side by side when the drain plate 7 is disposed in the inflow header 6a. The height of the support portion 71 is such that when the drain plate 7 is disposed in the concave portion of the header body 61 and the header lid 62 is fitted into the header body 61 and at least a part of the separation plate 70 contacts the pipe end opening 52a, The apex of the support portion 71 is formed so as to contact the bottom surface 67 of the header lid 62. In addition, although the opening is not formed in the support part 71, you may provide an opening similarly to the separating plate 70. FIG.

水抜き板7を流入ヘッダ6a内に配置するにあたっては、ヘッダ本体61の差込口63を介してヘッダ本体61の凹部内に吸熱管52のパイプ端開口52aを導出させ、差込口63と吸熱管52の外周面との境界にロウ材を塗布して仮固定する。次いで、ヘッダ本体61の凹部に水抜き板7を配置し、ヘッダ蓋62の周壁65がヘッダ本体61の内壁68に当接するまで嵌め込んでいく。このとき、吸熱管52の長さの製造誤差や、上記した吸熱管52とヘッダ本体61とを接合する際の導出させる吸熱管52の組み付け誤差により、例えば、図4に示すように、流入ヘッダ6a内では隣接する吸熱管52の出寸法が異なって形成される。それゆえ、複数のパイプ端開口52aに対して上下に連続して対向配置された従来の水抜き板170のように、剛直な一枚の金属板の場合、出寸法の少ない一部の吸熱管52のパイプ端開口52aと水抜き板170との間の隙間が大きくなる。さらに、残留した少量の水が凍結して水抜き板170に大きな負荷がかかり塑性変形した場合、水抜き板170は元の形状に戻らないため、組み立て時よりも隙間が大きくなる。その結果、水抜き時にパイプ端開口52aと水抜き板170との間で水の表面張力に起因した水膜が形成され、吸熱管52の水抜き時の流水方向下流部に水がさらに残留しやすくなる。   In disposing the drain plate 7 in the inflow header 6 a, the pipe end opening 52 a of the heat absorption pipe 52 is led out into the recess of the header body 61 through the insertion port 63 of the header body 61, A brazing material is applied to the boundary with the outer peripheral surface of the heat absorption tube 52 and temporarily fixed. Next, the drainage plate 7 is disposed in the recess of the header body 61 and is fitted until the peripheral wall 65 of the header lid 62 contacts the inner wall 68 of the header body 61. At this time, due to a manufacturing error in the length of the endothermic tube 52 or an assembly error of the endothermic tube 52 to be derived when the endothermic tube 52 and the header body 61 are joined together, for example, as shown in FIG. In 6a, the heat sink tubes 52 adjacent to each other are formed with different projecting dimensions. Therefore, in the case of a rigid single metal plate, such as the conventional water drain plate 170 that is continuously disposed vertically opposite to the plurality of pipe end openings 52a, a part of the endothermic tubes with a small output dimension. The clearance gap between the pipe end opening 52a of 52 and the drainage plate 170 becomes large. Further, when a small amount of remaining water is frozen and a large load is applied to the drainage plate 170 to cause plastic deformation, the drainage plate 170 does not return to its original shape, and therefore the gap becomes larger than that during assembly. As a result, a water film due to the surface tension of water is formed between the pipe end opening 52a and the drain plate 170 during drainage, and water further remains in the downstream portion in the flowing direction when draining the heat absorption pipe 52. It becomes easy.

しかしながら、本実施の形態では、水抜き板7が、各パイプ端開口52aに対向するように支持部71の左右に支持された分離板70を有しているから、ヘッダ本体61に水抜き板7を配置した状態でヘッダ蓋62をヘッダ本体61に嵌め込むと、図4に示すように、出寸法の大きな吸熱管52が配設されている箇所では、分離板70がパイプ端開口52aに押圧されて弾性変形していき、パイプ端開口52aの略全面に分離板70が当接し、曲げ部73がヘッダ蓋62の周壁65の上端面に当接する。また、出寸法の小さな吸熱管52が配設されている箇所では、同様に分離板70がパイプ端開口52aに押圧されて弾性変形するが、変形量は少ないから、自由端75側の一部のみがパイプ端開口52aに当接し、曲げ部73はヘッダ蓋62の周壁65の上端面から離間して、自由端75が固定端76よりもパイプ端開口52a側に位置するように配置される。このとき、支持部71の頂点はヘッダ蓋62の底面に当接し、ヘッダ本体61とヘッダ蓋62とが対向する方向で支持部71は固定されるから、出寸法の大きな吸熱管52のパイプ端開口52a及び出寸法の小さな吸熱管52のパイプ端開口52aのいずれにも、分離板70の少なくとも一部が弾性的な付勢力をもって当接する。これにより、いずれのパイプ端開口52aと分離板70との間の隙間も狭くすることができる。従って、水抜き作業中に吸熱管52の高低差による水の水頭圧が小さくなっても、パイプ端開口52aには水の表面張力に起因した水膜が形成され難くなり、パイプ端開口52aに達した水は分離板70を伝って水抜き板7の下方に流れていき、吸熱管52の水抜き時の流水方向下流部の水を円滑に排水することができる。このように、本実施の形態によれば、吸熱管52の長さに製造誤差が生じていたり、吸熱管52の流入ヘッダ6aへの取り付け時に取り付け誤差が生じたりしても、それらの誤差を水抜き板7で吸収することができる。さらに、少量の水が残留して凍結時に分離板70に大きな負荷がかかっても、分離板70は弾性変形可能であるため、凍結によってパイプ端開口52aと分離板70との間の隙間が大きくなるのを防ぐことができる。それゆえ、吸熱管52の長さやその出寸法について厳しい製造管理を行う必要がなく、確実に水抜きが可能な副熱交換器5を生産性良く製造することができる。   However, in the present embodiment, the drain plate 7 has the separation plates 70 supported on the left and right of the support portion 71 so as to face each pipe end opening 52a. When the header lid 62 is fitted into the header main body 61 in a state where the 7 is disposed, as shown in FIG. 4, the separation plate 70 is inserted into the pipe end opening 52a at the location where the heat absorption pipe 52 having a large output dimension is disposed. The separator 70 is pressed and elastically deformed so that the separation plate 70 comes into contact with substantially the entire surface of the pipe end opening 52 a, and the bent portion 73 comes into contact with the upper end surface of the peripheral wall 65 of the header lid 62. Further, at the place where the heat absorption tube 52 with a small projecting dimension is disposed, the separation plate 70 is similarly elastically deformed by being pressed by the pipe end opening 52a. However, since the deformation amount is small, a part on the free end 75 side is provided. Only the pipe end opening 52a abuts, and the bent portion 73 is spaced from the upper end surface of the peripheral wall 65 of the header lid 62 so that the free end 75 is positioned closer to the pipe end opening 52a than the fixed end 76. . At this time, the apex of the support portion 71 is in contact with the bottom surface of the header lid 62, and the support portion 71 is fixed in a direction in which the header body 61 and the header lid 62 face each other. At least a part of the separation plate 70 is brought into contact with both the opening 52a and the pipe end opening 52a of the heat absorption pipe 52 having a small projecting dimension with an elastic biasing force. Thereby, the clearance gap between any pipe end opening 52a and the separating plate 70 can also be narrowed. Therefore, even if the water head pressure due to the height difference of the heat absorption pipe 52 is reduced during the water draining operation, it is difficult to form a water film due to the surface tension of the water at the pipe end opening 52a. The reached water flows along the separation plate 70 and flows below the drain plate 7, and the water in the downstream direction in the flowing direction when draining the heat absorption pipe 52 can be smoothly drained. Thus, according to the present embodiment, even if a manufacturing error occurs in the length of the heat absorption pipe 52 or an attachment error occurs when the heat absorption pipe 52 is attached to the inflow header 6a, those errors are reduced. It can be absorbed by the drain plate 7. Furthermore, even if a small amount of water remains and a large load is applied to the separation plate 70 during freezing, the separation plate 70 can be elastically deformed, so that a gap between the pipe end opening 52a and the separation plate 70 becomes large due to freezing. Can be prevented. Therefore, it is not necessary to carry out strict production management with respect to the length of the heat absorption pipe 52 and its output dimension, and the auxiliary heat exchanger 5 capable of reliably draining water can be manufactured with high productivity.

特に、本実施の形態における分離板70は、分離板70に負荷がかけられていない状態で、自由端75が固定端76よりも高くなるように傾斜面で形成され、自由端75がパイプ端開口52aに近接して設けられているとともに、分離板70の弾性変形可能な許容範囲が広げられているから、吸熱管52の出寸法の相違が大きな場合でも、確実に分離板70の少なくとも一部をパイプ端開口52aに当接させることができる。   In particular, the separation plate 70 in the present embodiment is formed with an inclined surface so that the free end 75 is higher than the fixed end 76 in a state where no load is applied to the separation plate 70, and the free end 75 is the pipe end. Since it is provided close to the opening 52a and the allowable range in which the separation plate 70 can be elastically deformed is widened, it is ensured that at least one of the separation plates 70 is ensured even when the difference in the projecting dimensions of the heat absorption tubes 52 is large. The portion can be brought into contact with the pipe end opening 52a.

さらに、本実施の形態では、分離板70が対向するパイプ端開口52aに弾性的に付勢力をもって当接しているから、通常使用時に流入ヘッダ6a内を水が流通したときの水抜き板7のガタツキも防止できる。   Furthermore, in this embodiment, since the separating plate 70 is elastically abutted against the opposing pipe end opening 52a, the drain plate 7 when the water flows through the inflow header 6a during normal use. It can also prevent rattling.

なお、本発明は、上記実施形態のみに限定されず、本発明の範囲内で種々の変更を施すことが可能である。
例えば、吸熱管のパイプ端開口52aは、ヘッダ内で一列に配置されていてもよい。また、吸熱管52は、横置き蛇行形状でなく、渦巻状、螺旋状等に配設されるものでもよい。
さらに、熱交換器は、給湯装置に限らず、各種の熱交換装置に用いられるものでもよい。
In addition, this invention is not limited only to the said embodiment, A various change is possible within the scope of the present invention.
For example, the pipe end openings 52a of the heat absorption tubes may be arranged in a line in the header. Further, the endothermic tube 52 may be arranged in a spiral shape, a spiral shape, or the like instead of the horizontal meandering shape.
Further, the heat exchanger is not limited to the hot water supply device, and may be used for various heat exchange devices.

1 給湯装置
2 外装ケース
3 燃焼筐
4 主熱交換器
5 副熱交換器
6a 流入ヘッダ
6b 流出ヘッダ
7 水抜き板
42 吸熱管
50 ケース
51 側板
52 吸熱管
52a パイプ端開口
61 ヘッダ本体
60 閉鎖空間
62 ヘッダ蓋
63 差込口
70 分離板
71 支持部
75 自由端
76 固定端
DESCRIPTION OF SYMBOLS 1 Hot-water supply apparatus 2 Exterior case 3 Combustion housing 4 Main heat exchanger 5 Sub heat exchanger 6a Inflow header 6b Outflow header 7 Drain plate 42 Heat absorption pipe 50 Case 51 Side plate 52 Heat absorption pipe 52a Pipe end opening 61 Header main body 60 Closed space 62 Header lid 63 Insert port 70 Separation plate 71 Support part 75 Free end 76 Fixed end

Claims (2)

燃焼排気が流れるケースと、
前記ケース内に配置された複数の吸熱管と、
前記ケースの側板に配置され、各吸熱管の一端部及び他端部がそれぞれ挿入されて接続される流入ヘッダ及び流出ヘッダと、
高さ位置が低位置側のヘッダ内に配置され、前記吸熱管内の水抜き時に並設された複数のパイプ端開口に達した水を水抜きするための水抜き板と、を備える熱交換器であって、
前記水抜き板は、複数のパイプ端開口のそれぞれに弾性的な付勢力を有して当接するように分離された分離板を有する熱交換器。
A case where combustion exhaust flows,
A plurality of endothermic tubes disposed in the case;
An inflow header and an outflow header which are arranged on the side plate of the case, and are connected by inserting one end and the other end of each heat absorption tube,
A heat exchanger comprising: a drain plate for draining water that has been arranged in a header at a low position on the low position side and drains water that has reached a plurality of pipe end openings arranged in parallel when draining water in the heat absorption pipe Because
The water draining plate is a heat exchanger having a separating plate separated so as to abut each of the plurality of pipe end openings with an elastic biasing force.
請求項1に記載の熱交換器において、
前記水抜き板は、複数の分離板を支持する支持部を有し、
前記各分離板は、ヘッダ内に配置される前の状態で支持部が下方になるように水抜き板を設置したとき、分離板の自由端が支持部側の固定端よりも高くなるように傾斜して設けられている熱交換器。


The heat exchanger according to claim 1,
The drain plate has a support portion for supporting a plurality of separation plates,
Each separation plate is arranged such that when the drainage plate is installed so that the support portion is in the lower state before being arranged in the header, the free end of the separation plate is higher than the fixed end on the support portion side. An inclined heat exchanger.


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JP7241595B2 (en) * 2019-04-23 2023-03-17 リンナイ株式会社 Heat exchanger, combustion device provided with the same, and drain aid

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