JP5835569B2 - Heat exchanger and hot water device provided with the same - Google Patents

Heat exchanger and hot water device provided with the same Download PDF

Info

Publication number
JP5835569B2
JP5835569B2 JP2011238066A JP2011238066A JP5835569B2 JP 5835569 B2 JP5835569 B2 JP 5835569B2 JP 2011238066 A JP2011238066 A JP 2011238066A JP 2011238066 A JP2011238066 A JP 2011238066A JP 5835569 B2 JP5835569 B2 JP 5835569B2
Authority
JP
Japan
Prior art keywords
hot water
portions
heat transfer
tube
water inlet
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.)
Active
Application number
JP2011238066A
Other languages
Japanese (ja)
Other versions
JP2013096609A (en
Inventor
健 大東
健 大東
誠 廣津
誠 廣津
由起子 野口
由起子 野口
濱田 哲郎
哲郎 濱田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Noritz Corp
Original Assignee
Noritz Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Noritz Corp filed Critical Noritz Corp
Priority to JP2011238066A priority Critical patent/JP5835569B2/en
Publication of JP2013096609A publication Critical patent/JP2013096609A/en
Application granted granted Critical
Publication of JP5835569B2 publication Critical patent/JP5835569B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

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

Description

本発明は、燃焼ガスなどの加熱用気体からフィンチューブタイプの伝熱管を用いて熱回収を行なうように構成された熱交換器、およびこの熱交換器を備えた給湯装置などの温水装置に関する。   The present invention relates to a heat exchanger configured to recover heat from a heating gas such as a combustion gas by using a fin tube type heat transfer tube, and a hot water apparatus such as a hot water supply apparatus provided with the heat exchanger.

ガス給湯装置などの温水装置に用いられている熱交換器としては、間隔を隔てて並んだ多数枚のプレート状のフィンに伝熱管を貫通させ、かつこの伝熱管やフィンの周囲を缶体によって囲んだ構造のものがよく用いられている。このような構造の熱交換器においては、熱回収量を多くするための手段として、伝熱管を上下複数段に設ける場合が多い。ただし、このような手段によれば、熱交換器の上下高さ方向のサイズが大きくなる。そこで、従来においては、伝熱管を蛇行状に形成し、かつこの伝熱管を缶体の上下高さにおいて単段(1段)に設ける手段がある(たとえば、特許文献1を参照)。このような構成によれば、熱交換器全体の上下高さ寸法を小さくし、製造コストを低減することができる利点が得られる。   As a heat exchanger used in a hot water device such as a gas hot water supply device, a heat transfer tube is passed through a large number of plate-like fins arranged at intervals, and the periphery of the heat transfer tube and fins is formed by a can body. The enclosed structure is often used. In a heat exchanger having such a structure, heat transfer tubes are often provided in a plurality of stages above and below as means for increasing the amount of heat recovery. However, according to such a means, the size of the heat exchanger in the vertical height direction is increased. Therefore, conventionally, there is means for forming the heat transfer tubes in a meandering manner and providing the heat transfer tubes in a single stage (one stage) at the vertical height of the can body (see, for example, Patent Document 1). According to such a configuration, there is an advantage that the vertical height dimension of the entire heat exchanger can be reduced and the manufacturing cost can be reduced.

しかしながら、前記したように伝熱管の単段化を図る場合には、次に述べるような不具合を生じる虞がある。   However, as described above, when the heat transfer tube is made to be a single stage, there is a possibility of causing the following problems.

すなわち、伝熱管を蛇行状に形成して単段に設けた場合において、この伝熱管の一端を入水口とし、かつ他端を出湯口として、伝熱管に通水を行なわせると、その通水方向は一方向となる。このような一方向の通水がなされる状態において、たとえば伝熱管の下方に配置されたバーナを燃焼駆動させて伝熱管を加熱すると、伝熱管の入水口寄り領域と出湯口寄り領域とでは、大きな温度差を生じる。具体的には、伝熱管の入水口寄り領域は、比較的低温の水が供給されたばかりであって、この水はバーナによって充分に加熱されていない状態にあるために、低温領域となる。これに対し、出湯口寄り領域では、入水口から出湯口に到達する迄の期間にわたってバーナにより充分に加熱された湯水が流通するために、高温領域となる。
このような現象を生じた場合、低温領域である入水口寄り領域においては、燃焼ガス中の水蒸気が凝縮し、燃焼ガス中の硫黄酸化物や窒素酸化物などを含んだ強酸性のドレイン(凝縮水)が発生し易い。強酸性のドレインが発生すると、伝熱管やフィンが耐酸性を有しないたとえば銅製とされているような場合において、これらが腐食し易くなる。一方、高温領域である出湯口寄り領域においては、伝熱管内を流通する湯水が過熱状態となって沸騰し、また伝熱管の高温酸化を生じるといったことが懸念される。したがって、これらの現象を適切に防止または抑制することが望まれる。
That is, in the case where the heat transfer tube is formed in a meandering shape and is provided in a single stage, when one end of the heat transfer tube is used as a water inlet and the other end is used as a hot water outlet, water is passed through the heat transfer tube. The direction is one direction. In such a state where water is unidirectionally passed, for example, when the heat transfer tube is heated by burning the burner disposed below the heat transfer tube, the heat transfer tube close region and the hot water discharge port close region A large temperature difference is generated. Specifically, the region close to the water inlet of the heat transfer tube has just been supplied with relatively low-temperature water, and this water is not sufficiently heated by the burner, so it becomes a low-temperature region. On the other hand, the hot water outlet region is a high temperature region because hot water sufficiently heated by the burner circulates over a period from the water inlet to the hot water outlet.
When such a phenomenon occurs, the water vapor in the combustion gas condenses in the region near the water inlet, which is a low temperature region, and a strongly acidic drain (condensation) containing sulfur oxides or nitrogen oxides in the combustion gas. Water) is likely to occur. When a strongly acidic drain is generated, the heat transfer tubes and fins are likely to corrode when they are made of, for example, copper which does not have acid resistance. On the other hand, in the region near the hot water outlet, which is a high temperature region, there is a concern that the hot water flowing through the heat transfer tube will boil in an overheated state and cause high temperature oxidation of the heat transfer tube. Therefore, it is desirable to appropriately prevent or suppress these phenomena.

実公平3−18874号公報Japanese Utility Model Publication No. 3-18874

本発明は、前記したような事情のもとで考え出されたものであり、伝熱管を単段化して全体の薄型化を図る場合において、入水側の領域においてドレインが発生することや、出湯側の領域において伝熱管内を流通する湯水が沸騰するといったことを適切に防止し、または抑制することが可能な熱交換器、およびこの熱交換器を備えた温水装置を提供することを、その課題としている。   The present invention has been conceived under the circumstances as described above, and in the case where a heat transfer tube is made into a single stage to reduce the overall thickness, a drain is generated in a region on the water inlet side, Providing a heat exchanger capable of appropriately preventing or suppressing boiling of hot water flowing through the heat transfer tube in the region on the side, and a hot water device including the heat exchanger, It is an issue.

上記の課題を解決するため、本発明では、次の技術的手段を講じている。   In order to solve the above problems, the present invention takes the following technical means.

本発明の第1の側面により提供される熱交換器は、プレート状の複数のフィンに貫通した複数の直状管体部を有する伝熱管と、前記複数の直状管体部および前記複数のフィンの周囲を囲む複数の側壁部を有し、かつ上下両面部が加熱用気体の流出入用の開口部とされる缶体と、を備えており、前記伝熱管は、前記複数の直状管体部が前記缶体の前後または左右の幅方向に間隔を隔てて並ぶとともに前記缶体の上下高さ方向に単段に設けられて連結用管体部を介して一連に接続された蛇行状に形成されており、前記伝熱管の前記幅方向の両端に位置する2つの直状管体部のうち、一方は入水側管体部とされ、かつ他方は出湯側管体部とされ、前記伝熱管における湯水の流通は、前記入水側管体部から前記出湯側管体部に向けて一方向になされるように構成された、熱交換器であって、前記入水側管体部とこれに対向接近する前記缶体の第1の側壁部との隙間の幅は、前記出湯側管体部とこれに対向接近する前記缶体の第2の側壁部との隙間の幅よりも大きくされていることを特徴としている。
ここで、缶体の側壁部(第1の側壁部,第2の側壁部)は、缶体の主要部材とは別体の部材(たとえば、後述する実施形態の仕切部材3)を用いて構成された側壁部をも含む概念である。
The heat exchanger provided by the first aspect of the present invention includes a heat transfer tube having a plurality of straight tube portions penetrating through a plurality of plate-like fins, the plurality of straight tube portions, and the plurality of tube portions. A can body having a plurality of side wall portions surrounding the periphery of the fins and having both upper and lower side portions as openings for the inflow and outflow of the heating gas, and the heat transfer tube has the plurality of straight shapes The meandering in which the tube portions are arranged at intervals in the front-rear or left-right width direction of the can body and are provided in a single stage in the vertical height direction of the can body and connected in series via the connecting tube portion Of the two straight tube portions located at both ends in the width direction of the heat transfer tube, one is a water inlet side tube portion, and the other is a hot water side tube portion, Distribution of hot water in the heat transfer pipe is made in one direction from the water inlet side pipe body part toward the hot water outlet side pipe body part. It is a heat exchanger comprised in this way, Comprising: The width | variety of the clearance gap between the said inflow side pipe body part and the 1st side wall part of the said can body which opposes and approaches this is the said hot water side pipe body part and this It is characterized by being larger than the width of the gap with the second side wall portion of the can body facing and approaching.
Here, the side wall portions (first side wall portion, second side wall portion) of the can body are configured by using a member separate from the main member of the can body (for example, a partition member 3 in an embodiment described later). This is a concept including the side wall portion.

このような構成によれば、伝熱管の入水側管体部と缶体の第1の側壁部との隙間を通過する加熱用気体の流量を多くする一方、出湯側管体部と缶体の第2の側壁部との隙間を通過する加熱用気体の流量を少なくすることができる。このため、伝熱管に低温の湯水が入水される場合であっても、入水側管体部およびその近傍部分に対する加熱量を多くして、これらの部分の温度を上昇させることができ、ドレインが発生することを防止または抑制することが可能となる。したがって、ドレインに起因して伝熱管やフィンが腐食し易くなるといった不具合を回避することができる。一方、伝熱管の出湯側管体部およびその近傍部分については、加熱用気体による加熱量を少なくすることができるために、伝熱管内を流通する湯水が過熱状態となって沸騰することや、伝熱管が高温酸化するといったことも適切に防止または抑制することが可能となる。   According to such a configuration, while increasing the flow rate of the heating gas passing through the gap between the water inlet side tube portion of the heat transfer tube and the first side wall portion of the can body, the outlet side tube portion and the can body The flow rate of the heating gas passing through the gap with the second side wall portion can be reduced. For this reason, even when low-temperature hot water is poured into the heat transfer pipe, the amount of heat applied to the water inlet side pipe body part and the vicinity thereof can be increased, and the temperature of these parts can be increased. It is possible to prevent or suppress the occurrence. Therefore, the trouble that the heat transfer tubes and the fins are easily corroded due to the drain can be avoided. On the other hand, about the outlet side tube portion of the heat transfer tube and the vicinity thereof, the amount of heating by the heating gas can be reduced, so that the hot water flowing through the heat transfer tube is boiled in an overheated state, It is possible to appropriately prevent or suppress the heat transfer tube from being oxidized at high temperature.

本発明の第2の側面により提供される熱交換器は、プレート状の複数のフィンに貫通した複数の直状管体部を有する伝熱管と、前記複数の直状管体部および前記複数のフィンの周囲を囲む側壁部を有し、かつ上下両面部が加熱用気体の流出入用の開口部とされる缶体と、を備えており、前記伝熱管は、前記複数の直状管体部が前記缶体の前後または左右の幅方向に間隔を隔てて並ぶとともに前記缶体の上下高さ方向に単段に設けられて連結用管体部を介して一連に接続された蛇行状に形成されており、前記伝熱管の前記幅方向の両端に位置する2つの直状管体部のうち、一方は入水側管体部とされ、かつ他方は出湯側管体部とされ、前記伝熱管における湯水の流通は、前記入水側管体部から前記出湯側管体部に向けて一方向になされるように構成された、熱交換器であって、前記複数のフィンには、これら複数のフィンどうしの間を前記加熱用気体が通過する際の抵抗となるように前記各フィンの表面の一部を突出させた加熱用気体の流れ規制部が複数設けられており、これら複数の流れ規制部として、前記出湯側管体部とこれに対向接近する前記缶体の第2の側壁部との間またはその上方もしくは下方に位置する最出湯側の流れ規制部が設けられている一方、前記入水側管体部とこれに対向接近する前記缶体の第1の側壁部との間およびその上下方の位置には、流れ規制部は設けられておらず、または前記最出湯側の流れ規制部よりも前記加熱用気体の流れに対する抵抗が小さい流れ規制部が設けられ、前記入水側管体部の周辺部分よりも前記出湯側管体部の周辺部分の方が前記加熱用気体の流れに対する抵抗が大きくなるように構成されていることを特徴としている。 The heat exchanger provided by the second aspect of the present invention includes a heat transfer tube having a plurality of straight tube portions penetrating through a plurality of plate-shaped fins, the plurality of straight tube portions, and the plurality of tube portions. A can body having a side wall portion surrounding the periphery of the fin and having both upper and lower surface portions as openings for inflow and outflow of heating gas, and the heat transfer tube includes the plurality of straight tube bodies Are arranged in a row in the width direction of the front and rear or left and right of the can body, and are provided in a single stage in the vertical height direction of the can body and connected in series through a connecting tube portion. Of the two straight tube portions that are formed at both ends in the width direction of the heat transfer tube, one is a water inlet side tube portion, and the other is a hot water discharge side tube portion. Circulation of hot water in the heat pipe is performed in one direction from the incoming water side pipe part toward the outgoing hot water side pipe part. In the heat exchanger, a part of the surface of each fin protrudes from the plurality of fins so as to provide resistance when the heating gas passes between the plurality of fins. A plurality of heating gas flow restricting portions provided as the plurality of flow restricting portions , or between the hot water side pipe body portion and the second side wall portion of the can body facing and approaching the hot water side pipe body portion; While a flow regulating portion on the most hot water side located above or below is provided, between the inlet side tube body portion and the first side wall portion of the can body facing and approaching the same, and above and below it The position is not provided with a flow restricting portion, or is provided with a flow restricting portion having a smaller resistance to the flow of the heating gas than the flow restricting portion on the outermost hot water side. The peripheral part of the tapping side tube part is more than the peripheral part. Is characterized by being configured so that the resistance to the flow of heat gas increases.

このような構成によれば、各ファンに加熱用気体の流れ規制部が所定の偏った状態に設けられていることに基づき、入水側管体部の周辺部には多くの加熱用気体が流れ易くなり、かつ出湯側管体部の周辺部には多くの加熱用気体が流れ難くなる作用が得られる。したがって、本発明の第1の側面によって提供される熱交換器と同様に、伝熱管の入水側管体
部およびその近傍部分の温度を高くし、この領域にドレインが発生することを適切に防止または抑制することができる。また、伝熱管の出湯側管体部およびその近傍部分が過当な高温領域にならないようにし、伝熱管内を流通する湯水が沸騰することや、伝熱管が高温酸化するといったことも適切に防止または抑制することができる。
According to such a configuration, based on the fact that the heating gas flow restricting portion is provided in a predetermined biased state in each fan, a large amount of heating gas flows in the peripheral portion of the water inlet side tube portion. It becomes easy and the effect | action which becomes difficult for many heating gas to flow to the peripheral part of the tapping hot water side pipe body part is acquired. Therefore, similarly to the heat exchanger provided by the first aspect of the present invention, the temperature of the water inlet side tube portion of the heat transfer tube and the vicinity thereof are raised to appropriately prevent the drain from being generated in this region. Or it can be suppressed. In addition, the outlet side tube portion of the heat transfer tube and the vicinity thereof are not excessively heated, and it is also possible to appropriately prevent the boiling of hot water flowing through the heat transfer tube and the high temperature oxidation of the heat transfer tube. Can be suppressed.

さらに、前記構成によれば、伝熱管の入水側管体部と缶体の第1の側壁部との間には、加熱用気体が多く流れ易くなり、出湯側管体部と缶体の第2の側壁部との間には、加熱用気体が多く流れないようにすることができる。したがって、入水側管体部およびその周辺部の温度を高め、また出湯側管体部およびその周辺部が過当な高温領域になることを抑制するのに好適である。 Furthermore, according to the said structure, it becomes easy to flow a lot of gas for heating between the water inlet side pipe | tube part of a heat exchanger tube, and the 1st side wall part of a can, and the hot water side pipe | tube part and the 1st of a can It is possible to prevent a large amount of heating gas from flowing between the two side walls. Therefore, it is suitable for increasing the temperature of the water inlet side pipe body part and its peripheral part and suppressing the hot water side pipe part and its peripheral part from becoming an excessively high temperature region.

本発明の第3の側面により提供される熱交換器は、プレート状の複数のフィンに貫通した複数の直状管体部を有する伝熱管と、前記複数の直状管体部および前記複数のフィンの周囲を囲む側壁部を有し、かつ上下両面部が加熱用気体の流出入用の開口部とされる缶体と、を備えており、前記伝熱管は、前記複数の直状管体部が前記缶体の前後または左右の幅方向に間隔を隔てて並ぶとともに前記缶体の上下高さ方向に単段に設けられて連結用管体部を介して一連に接続された蛇行状に形成されており、前記伝熱管の前記幅方向の両端に位置する2つの直状管体部のうち、一方は入水側管体部とされ、かつ他方は出湯側管体部とされ、前記伝熱管における湯水の流通は、前記入水側管体部から前記出湯側管体部に向けて一方向になされるように構成された、熱交換器であって、前記複数のフィンには、これら複数のフィンどうしの間を前記加熱用気体が通過する際の抵抗となるように前記各フィンの表面の一部を突出させた加熱用気体の流れ規制部が複数設けられており、これら複数の流れ規制部として、前記複数の直状管体部どうしの間に設けられた複数の流れ規制部があり、これら複数の直状管体部のうち、前記入水側管体部とこれに隣接する直状管体部との間およびその上下方の領域に設けられている流れ規制部は、他の直状管体部どうしの各間およびその上下方の領域に設けられている流れ規制部よりも前記加熱用気体の流れに対する抵抗が小さい構成とされ、前記入水側管体部の周辺部分よりも前記出湯側管体部の周辺部分の方が前記加熱用気体の流れに対する抵抗が大きくなるように構成されていることを特徴としている。 The heat exchanger provided by the third aspect of the present invention includes a heat transfer tube having a plurality of straight tube portions penetrating through a plurality of plate-shaped fins, the plurality of straight tube portions, and the plurality of tube portions. A can body having a side wall portion surrounding the periphery of the fin and having both upper and lower surface portions as openings for inflow and outflow of heating gas, and the heat transfer tube includes the plurality of straight tube bodies Are arranged in a row in the width direction of the front and rear or left and right of the can body, and are provided in a single stage in the vertical height direction of the can body and connected in series through a connecting tube portion. Of the two straight tube portions that are formed at both ends in the width direction of the heat transfer tube, one is a water inlet side tube portion, and the other is a hot water discharge side tube portion. Circulation of hot water in the heat pipe is performed in one direction from the incoming water side pipe part toward the outgoing hot water side pipe part. In the heat exchanger, a part of the surface of each fin protrudes from the plurality of fins so as to provide resistance when the heating gas passes between the plurality of fins. There are a plurality of heating gas flow restricting portions, and the plurality of flow restricting portions include a plurality of flow restricting portions provided between the plurality of straight tube portions. Among the straight tube portions, the flow restricting portion provided in the region between the water inlet side tube portion and the straight tube portion adjacent thereto and in the upper and lower regions thereof is another straight tube body. The resistance to the flow of the heating gas is smaller than that of the flow restricting portion provided between the portions and in the upper and lower regions, and the hot water side of the peripheral portion of the water inlet side tube portion. The resistance to the flow of the heating gas is greater in the peripheral part of the tube part It is characterized by being configured such that.

このような構成によれば、伝熱管の入水側管体部とこれに隣接する直状管体部との間を流れる加熱用気体の量を多くすることができる。したがって、入水側管体部およびその周辺領域の温度をより高めることが可能であり、ドレインの発生を防止する上で一層好ましい。   According to such a configuration, it is possible to increase the amount of the heating gas flowing between the water inlet side tube portion of the heat transfer tube and the straight tube portion adjacent thereto. Therefore, it is possible to further increase the temperature of the water inlet side pipe body part and the surrounding area, which is more preferable in preventing the generation of drain.

本発明においては、第1の側面により提供される熱交換器と、第2または第3の側面により提供される熱交換器とのそれぞれの特徴的な構成の双方を備えた構成とすることが可能である。
具体的には、第2または第3の側面により提供される熱交換器において、前記入水側管体部とこれに対向接近する前記缶体の第1の側壁部との隙間の幅は、前記出湯側管体部とこれに対向接近する前記缶体の第2の側壁部との隙間の幅よりも大きくされた構成とすることが可能である。
In this invention, it is set as the structure provided with both each characteristic structure of the heat exchanger provided by the 1st side surface, and the heat exchanger provided by the 2nd or 3rd side surface. Is possible.
Specifically, in the heat exchanger provided by the second or third side face, the width of the gap between the water inlet side pipe body part and the first side wall part of the can body facing and approaching the water inlet side pipe part is: It is possible to make it the structure made larger than the width | variety of the clearance gap between the said hot water side pipe body part and the 2nd side wall part of the said can body which opposes and approaches this.

このような構成によれば、入水側管体部およびその周辺部が低温領域となってドレインが発生することや、出湯側管体部およびその周辺部が過熱状態となることを、より徹底して防止することができる。   According to such a configuration, it is more thorough that the water inlet side pipe part and its peripheral part become a low temperature region and a drain is generated, and that the outlet side pipe part and its peripheral part are overheated. Can be prevented.

本発明の第の側面により提供される温水装置は、本発明の第1ないし第3の側面のいずれかにより提供される熱交換器を備えていることを特徴としている。 The hot water apparatus provided by the fourth aspect of the present invention includes the heat exchanger provided by any one of the first to third aspects of the present invention.

このような構成によれば、本発明の第1ないし第3の側面により提供される熱交換器について述べたのと同様な効果が得られる。 According to such a configuration, the same effect as described for the heat exchanger provided by the first to third aspects of the present invention can be obtained.

本発明のその他の特徴および利点は、添付図面を参照して以下に行なう発明の実施の形態の説明から、より明らかになるであろう。   Other features and advantages of the present invention will become more apparent from the following description of embodiments of the present invention with reference to the accompanying drawings.

本発明が適用された熱交換器(1次熱交換器)を備えた温水装置の一例を示す概略正面断面図である。It is a schematic front sectional view showing an example of a hot water apparatus provided with a heat exchanger (primary heat exchanger) to which the present invention is applied. 図1のII−II断面図である。It is II-II sectional drawing of FIG. 図1のIII−III断面図である。FIG. 3 is a sectional view taken along line III-III in FIG. 1. 図1に示す1次熱交換器の平面断面図である。It is a plane sectional view of the primary heat exchanger shown in FIG. 図1に示す温水装置の要部概略正面断面図である。It is a principal front schematic sectional drawing of the hot water apparatus shown in FIG. (a)は、図5のVIa−VIa断面図であり、(b)は、(a)のVIb−VIb断面図である。(A) is VIa-VIa sectional drawing of FIG. 5, (b) is VIb-VIb sectional drawing of (a). 図5のVII−VII断面図である。It is VII-VII sectional drawing of FIG. 図1に示す1次熱交換器に仕切部材を装着する状態を示す要部分解断面図である。It is a principal part disassembled sectional view which shows the state which attaches a partition member to the primary heat exchanger shown in FIG. 図1に示す温水装置の2次熱交換器を示す平面断面図である。It is a top sectional view showing the secondary heat exchanger of the hot water device shown in FIG. 本発明に係る温水装置の他の例を示す概略正面断面図である。It is a schematic front sectional drawing which shows the other example of the hot water apparatus which concerns on this invention.

以下、本発明の好ましい実施の形態について、図面を参照して具体的に説明する。   Hereinafter, preferred embodiments of the present invention will be specifically described with reference to the drawings.

図1〜図9は、本発明が適用された温水装置、およびこれに関連する構成の一例を示している。
図1によく表われているように、本実施形態の温水装置WH1は、バーナ5、1次熱交換器HE1、2次熱交換器HE2、およびこれら全体を囲む外装ケース90を備えている。この温水装置WH1は、一般給湯と、風呂給湯または暖房用給湯との2系統の給湯動作を独立して行なうことが可能であり、1次熱交換器HE1、および2次熱交換器HE2は、ともに1缶2回路方式である。
FIGS. 1-9 has shown an example of the hot water apparatus with which this invention was applied, and the structure relevant to this.
As clearly shown in FIG. 1, the hot water device WH1 of the present embodiment includes a burner 5, a primary heat exchanger HE1, a secondary heat exchanger HE2, and an outer case 90 surrounding them. This hot water device WH1 can independently perform two systems of hot water supply, general hot water supply and bath hot water supply or heating hot water supply. The primary heat exchanger HE1 and the secondary heat exchanger HE2 are: Both are one-can two-circuit systems.

1次熱交換器HE1は、本発明に係る熱交換器の一例に相当し、1つの缶体6内に、平面視蛇行状の第1および第2の伝熱管T1,T2が収容された構成である。2次熱交換器HE2は、1つのケース7内に、螺旋状に形成された複数の第3および第4の伝熱管T3,T4が収容された構成であり、本発明に係る熱交換器には相当しない。   The primary heat exchanger HE1 corresponds to an example of a heat exchanger according to the present invention, and has a configuration in which the first and second heat transfer tubes T1 and T2 having a serpentine shape in plan view are accommodated in one can body 6. It is. The secondary heat exchanger HE2 has a configuration in which a plurality of third and fourth heat transfer tubes T3 and T4 formed in a spiral shape are accommodated in one case 7, and is included in the heat exchanger according to the present invention. Is not equivalent.

バーナ5は、たとえばガスバーナであり、ファン51からバーナケース50内に上向きに送られてくる燃焼用空気を利用して燃料ガスを燃焼させる。ただし、このバーナ5は、燃料の燃焼動作を個別に制御可能な第1および第2の燃焼領域A1,A2を有している。第1および第2の燃焼領域A1,A2の上方領域は、仕切部材52によって仕切られ、第1および第2の燃焼領域A1,A2のそれぞれにおいて発生された燃焼ガスは第1および第2の伝熱管T1,T2に向けて個別に進行するようになっている。   The burner 5 is a gas burner, for example, and burns fuel gas by using combustion air sent upward from the fan 51 into the burner case 50. However, the burner 5 has first and second combustion regions A1 and A2 that can individually control the combustion operation of the fuel. The upper region of the first and second combustion regions A1, A2 is partitioned by a partition member 52, and the combustion gas generated in each of the first and second combustion regions A1, A2 is the first and second transmissions. It progresses individually toward the heat tubes T1 and T2.

1次熱交換器HE1は、燃焼ガスから顕熱を回収するためのものであり、この1次熱交換器HE1を構成する缶体6、第1および第2の伝熱管T1,T2、ならびに後述するフィン2A,2Bは、いずれも銅製である。この1次熱交換器HE1の缶体6は、上下方向に起立した側壁部60a〜60dを有する平面視略矩形の枠状である。ただし、本発明でいう「缶体の側壁部」の概念には、後述する仕切部材3の側壁部30aも含まれる。缶体6の上下両面部は、矩形状に開口しており、燃焼ガスの流出入口に相当する。バーナ5によって発生された燃焼ガスは、缶体6内をその下方から上方に向けて通過する。   The primary heat exchanger HE1 is for recovering sensible heat from the combustion gas. The can 6 constituting the primary heat exchanger HE1, first and second heat transfer tubes T1 and T2, and a later-described The fins 2A and 2B to be made are both made of copper. The can body 6 of the primary heat exchanger HE1 has a substantially rectangular frame shape in plan view having side wall portions 60a to 60d erected in the vertical direction. However, the concept of the “side wall portion of the can” in the present invention includes a side wall portion 30a of the partition member 3 described later. The upper and lower surfaces of the can 6 are opened in a rectangular shape and correspond to combustion gas inflow / outlet ports. The combustion gas generated by the burner 5 passes through the can 6 upward from below.

図4に示すように、第1の伝熱管T1は、フィン2Aに貫通する複数の直状管体部11aが略U字状の連結用管体部12aを介して一連に繋がった平面視蛇行状である。より具体的には、複数の直状管体部11aは、缶体6の前後方向に延びる向きとされて、缶体6の左右幅方向である水平方向に略一定間隔で並び、かつ上下高さ方向に単段に設けられた状態とされている。各直状管体部11aの両端部は、缶体6の側壁部60a,60bを貫
通し、かつこれら側壁部60a,60bにロウ付などの手段を用いて接合されている。互いに隣り合う直状管体部11aの端部どうしは、U字管を利用した連結用管体部12aを介して接続されている。第2の伝熱管T2は、フィン2Bに貫通して上下高さ方向に単段に設けられた複数の直状管体部11bと連結用管体部12bとを有しており、第1の伝熱管T1と同様に、それらは平面視蛇行状に繋がり、かつ側壁部60a,60bに支持されている。第1および第2の伝熱管T1,T2は、略同一高さに揃えられて、缶体6の左右幅方向に並んでいる。
As shown in FIG. 4, the first heat transfer tube T1 has a meandering in a plan view in which a plurality of straight tube portions 11a penetrating the fins 2A are connected in series via a substantially U-shaped connecting tube portion 12a. Is. More specifically, the plurality of straight tubular body portions 11 a are oriented in the front-rear direction of the can body 6, arranged in a horizontal direction that is the left-right width direction of the can body 6 at substantially constant intervals, and It is in a state of being provided in a single stage in the vertical direction. Both end portions of each straight tube portion 11a penetrate the side wall portions 60a and 60b of the can body 6 and are joined to the side wall portions 60a and 60b by means such as brazing. The ends of the straight tubular body portions 11a adjacent to each other are connected to each other via a coupling tubular body portion 12a using a U-shaped tube. The second heat transfer tube T2 has a plurality of straight tube portions 11b and connecting tube portions 12b that are provided in a single stage in the vertical height direction through the fins 2B. Similar to the heat transfer tube T1, they are connected in a serpentine shape in plan view and are supported by the side walls 60a and 60b. The first and second heat transfer tubes T <b> 1 and T <b> 2 are aligned at substantially the same height and are arranged in the left-right width direction of the can body 6.

第1および第2の伝熱管T1,T2の入水口15a,15bは、缶体6の側壁60c,60dに最も接近した位置の直状管体部11a,11bに、継手用管体12a',12b'を連結して設けられている。なお、継手用管体12a',12b'またはこれに相当する部材を用いることなく、入水側管体部11a',11b'の一端開口部をそのまま入水口とすることもできる。この点は、次の出湯口16a,16bも同様である。出湯口16a,16bは、後述する仕切部材3に最接近した直状管体部11a,11bの一端開口部である。このような構成により、入水口15a,15bに供給されたそれぞれの湯水は、第1および第2の伝熱管T1,T2に沿って蛇行して流れるものの、矢印N1,N2に示すように、缶体6の側壁60c,60dに接近した位置から仕切部材3側に向けて一方向に流れ、出湯口16a,16bに到達する。なお、本発明においては、前記湯水の流通方向を前記方向とは反対とすることもできる。   The water inlets 15a and 15b of the first and second heat transfer tubes T1 and T2 are connected to the straight tube portions 11a and 11b at positions closest to the side walls 60c and 60d of the can body 6 to the joint tubes 12a ′, 12b 'is connected. It should be noted that one end opening of the water inlet side pipe parts 11a 'and 11b' can be used as the water inlet without using the joint pipes 12a 'and 12b' or a member corresponding thereto. This also applies to the next outlets 16a and 16b. The hot water outlets 16a and 16b are one end openings of the straight tube portions 11a and 11b that are closest to the partition member 3 described later. With such a configuration, the hot water supplied to the water inlets 15a and 15b flows in a meandering manner along the first and second heat transfer tubes T1 and T2, but as shown by arrows N1 and N2, It flows in one direction from the position approaching the side walls 60c, 60d of the body 6 toward the partition member 3, and reaches the hot water outlets 16a, 16b. In the present invention, the flowing direction of the hot water may be opposite to the direction.

フィン2A,2Bは、燃焼ガスからの熱回収量を多くするためのものであり、缶体6の左右幅方向に延びた薄手のプレート状である。図5に示すように、フィン2A,2Bの一端部は、缶体6の側壁部60c,60dにロウ付けなどの手段を用いて接合されている。一方、図8に示すように、フィン2A,2Bの他端部は、缶体6には接合されておらず、これらの間に形成された隙間68には、フィン2A,2B間を仕切る仕切部材3が挿入して装着されている。仕切部材3は、たとえば耐熱性に優れた金属板が断面コ字状またはこれに類する形態に屈曲されて構成されたものであり、一側縁部(図面では下側縁部)どうしが繋がり、かつ互いに隙間を隔てて対向する一対の板状の側壁部30a,30bを有している。これら一対の側壁部30a,30bは、バネ性をもって撓み変形可能であり、このことにより仕切部材3は、その厚みが変更可能である。この仕切部材3は、厚みがやや小さくなるように圧縮された状態で隙間68に挿入されて保持されている。   The fins 2 </ b> A and 2 </ b> B are for increasing the amount of heat recovered from the combustion gas, and are thin plates extending in the left-right width direction of the can body 6. As shown in FIG. 5, one end portions of the fins 2 </ b> A and 2 </ b> B are joined to the side wall portions 60 c and 60 d of the can 6 using a means such as brazing. On the other hand, as shown in FIG. 8, the other end portions of the fins 2A and 2B are not joined to the can body 6, and a gap 68 formed between them is a partition that partitions the fins 2A and 2B. The member 3 is inserted and mounted. The partition member 3 is formed, for example, by bending a metal plate having excellent heat resistance into a U-shaped cross section or a form similar thereto, and one side edge portion (lower edge portion in the drawing) is connected, And it has a pair of plate-shaped side wall part 30a, 30b which mutually opposes through a clearance gap. The pair of side wall portions 30a and 30b can be bent and deformed with a spring property, whereby the thickness of the partition member 3 can be changed. The partition member 3 is inserted and held in the gap 68 in a compressed state so that the thickness is slightly reduced.

第1の伝熱管T1およびフィン2Aについては、缶体6の側壁部60cに対向接近する直状管体部11a(入水側管体部11a')寄りの領域が低温領域になることを抑制し、かつ仕切部材3の側壁部30aに対向接近する直状管体部11a(出湯側管体部11a")寄りの領域が過熱状態になることを抑制するための手段として、次のような手段が講じられている(なお、缶体6の側壁部60cは、本発明でいう第1の側壁部の一例に相当し、仕切部材3の側壁部30aは、本発明でいう第2の側壁部の一例に相当する。本発明でいう第1および第2の側壁部は、缶体自体が具備している側壁部に限らず、缶体とは別体に形成された部材であって、缶体に直接または間接的に取付けられた部材によって構成されたものであってもよい)。   About 1st heat exchanger tube T1 and fin 2A, it has controlled that the field near straight tube part 11a (incoming side tube part 11a ') facing and approaching side wall part 60c of can 6 becomes a low temperature area. In addition, as means for suppressing the region near the straight tubular body portion 11a (the tapping side tubular body portion 11a ") facing and approaching the side wall portion 30a of the partition member 3 from being overheated, the following means are provided. (Note that the side wall portion 60c of the can 6 corresponds to an example of the first side wall portion referred to in the present invention, and the side wall portion 30a of the partition member 3 corresponds to the second side wall portion referred to in the present invention. The first and second side wall portions referred to in the present invention are not limited to the side wall portions provided in the can body itself, but are members formed separately from the can body, It may be constituted by a member attached directly or indirectly to the body).

図5において、入水側管体部11a'と側壁部60cとの隙間C1の幅L1は、出湯側管体部11a"と側壁部30aとの隙間C2の幅L2よりも大きくされている。このことにより、後述するように、隙間C1を通過する燃焼ガスの量を多くする一方、隙間C2を通過する燃焼ガスの量を少なくすることができる。なお、複数の直状管体部11aの配列ピッチは、一定とされている(ただし、入水側管体部11a'に接近するほど直状管体部11aの配列ピッチを徐々に大きくし、入水側管体部11a'寄り領域を通過する燃料ガスの量を多くするように構成してもかまわない)。   In FIG. 5, the width L1 of the gap C1 between the water inlet side pipe body part 11a ′ and the side wall part 60c is made larger than the width L2 of the gap C2 between the hot water side pipe body part 11a ″ and the side wall part 30a. Thus, as will be described later, the amount of the combustion gas passing through the gap C1 can be increased while the amount of the combustion gas passing through the gap C2 can be reduced. The pitch is constant (provided that the arrangement pitch of the straight tubular portions 11a is gradually increased as the distance from the incoming water tubular portion 11a 'increases, and the fuel passes through the region closer to the incoming water tubular portion 11a'. It may be configured to increase the amount of gas).

フィン2Aには、燃焼ガスの流れ規制部20,21が設けられている。この流れ規制部20,21は、フィン2Aの複数箇所を部分的に突出させた部分であって、本来的には、フィン2Aと燃焼ガスとの接触度合いを高めて熱回収量を多くするためのものであるが、本実施形態においては、燃焼ガスの流通量制御にも利用されている。これら流れ規制部20,21は、缶体6の幅方向において均一な分布には設けられておらず、入水側管体部11a'の周辺部分よりも出湯側管体部11a"の周辺部分の方が、燃焼ガス流れに対する抵抗が大きくなるように設けられている。より具体的には、出湯側管体部11a"と側壁部30aとの隙間C2の上方には、流れ規制部20(本発明でいう最出湯側の流れ規制部)が設けられているのに対し、入水側管体部11a'と側壁部60cとの隙間C1およびその上下には、流れ規制部20に相当する流れ規制部は設けられていない。ただし、これに代えて、隙間C2およびその上下のいずれかに流れ規制部20よりも小サイズ(低抵抗)の流れ規制部を設けた構成とすることができる。流れ規制部20は、たとえば図7に示すように、フィン2Aの一部がフィン2Aの前方または後方に適当な寸法だけ突出するように押し出された形態である。   The fins 2 </ b> A are provided with combustion gas flow restricting portions 20 and 21. The flow restricting portions 20 and 21 are portions in which a plurality of portions of the fin 2A are partially protruded, and are essentially for increasing the degree of contact between the fin 2A and the combustion gas to increase the heat recovery amount. However, in the present embodiment, it is also used for controlling the flow rate of the combustion gas. These flow restricting portions 20 and 21 are not provided in a uniform distribution in the width direction of the can body 6, and are located closer to the peripheral portion of the tapping side tubular portion 11 a ″ than the peripheral portion of the water inlet side tubular portion 11 a ′. More specifically, the resistance to the combustion gas flow is increased. More specifically, the flow restricting portion 20 (main) is disposed above the gap C2 between the tapping side tube portion 11a "and the side wall portion 30a. The flow regulating portion on the most hot water side referred to in the invention is provided, whereas the flow regulating portion corresponding to the flow regulating portion 20 is provided above and below the gap C1 between the water inlet side pipe body portion 11a ′ and the side wall portion 60c. There is no section. However, instead of this, it is possible to adopt a configuration in which a flow restricting portion having a size (low resistance) smaller than that of the flow restricting portion 20 is provided in the gap C2 and above or below it. For example, as shown in FIG. 7, the flow restricting portion 20 has a form in which a part of the fin 2 </ b> A is pushed out so as to protrude by an appropriate dimension in front of or behind the fin 2 </ b> A.

隣り合う直状管体部11aの各間およびその上方領域には、複数の流れ規制部21が設けられている。これらのうち、入水側管体部11a'とこれに隣接する直状管体部11aどうしの間およびその上方領域に設けられた流れ規制部21(21a)は、これ以外の流れ規制部21よりも燃焼ガス流れに対する抵抗が小さくなるように構成されている。本実施形態では、そのための手段として、流れ規制部21aの数を、他の箇所に設けられた流れ規制部21の数よりも少なくしている。ただし、本発明においては、これに代えて、または加えて、流れ規制部21,21aのサイズを相違させるようにしてもかまわない。流れ規制部21(21aも含む)は、たとえば図6に示すような形態であり、切り起こしの手法を用いて形成されている。すなわち、流れ規制部21は、フィン2Aに略平行な2条の切り目を形成した後に、これら2条の切り目に挟まれた部分を断面コ字状に屈曲させるようにしてフィン2Aの前方または後方に突出させたものである。   A plurality of flow restricting portions 21 are provided between the adjacent straight tubular body portions 11a and in an upper region thereof. Among these, the flow restricting portion 21 (21a) provided between the water inlet side tube portion 11a ′ and the adjacent straight tube portion 11a and the upper region thereof is more than the other flow restricting portions 21. Also, the resistance to the combustion gas flow is reduced. In this embodiment, the number of the flow control parts 21a is made smaller than the number of the flow control parts 21 provided in another location as a means for that. However, in the present invention, instead of or in addition to this, the sizes of the flow restricting portions 21 and 21a may be different. The flow restricting portion 21 (including 21a) has a form as shown in FIG. 6, for example, and is formed using a cutting and raising method. That is, the flow restricting portion 21 forms two slits substantially parallel to the fin 2A, and then bends the portion sandwiched between the two slits in a U-shaped cross section in front or rear of the fin 2A. It protrudes into

フィン2Bには、熱回収量を多くするための凸状部(流れ規制部)が適宜設けられているものの、伝熱管T2の入水側部分への燃焼ガス通過量を出湯側部分の燃焼ガス通過量よりも積極的に多くするための手段はとくに講じられていない。これは、伝熱管T2は、風呂給湯用または暖房給湯用であって、伝熱管T1と比較すると、バーナ5による加熱量が少ないために、入水側においてドレインが発生し難く、また出湯側において過熱状態が生じ難いためである。ただし、本実施形態とは異なり、伝熱管T2についても、伝熱管T1と同様に、入水側部分への燃焼ガス通過量を多くし、かつ出湯側部分への燃焼ガス通過量を少なくするための手段を講じてもよい。   Although the fin 2B is appropriately provided with a convex portion (flow restricting portion) for increasing the amount of heat recovery, the amount of combustion gas passing to the water inlet side portion of the heat transfer tube T2 is determined as the amount of combustion gas passing through the hot water side portion. No special measures are taken to actively increase the quantity. This is because the heat transfer pipe T2 is used for bath hot water supply or heating hot water supply, and compared with the heat transfer pipe T1, the amount of heating by the burner 5 is small, so that it is difficult for drainage to occur on the incoming water side, and overheating on the outgoing hot water side. This is because the condition is difficult to occur. However, unlike this embodiment, the heat transfer tube T2 also has a similar structure to the heat transfer tube T1 in order to increase the amount of combustion gas passing to the incoming water side portion and to reduce the amount of combustion gas passing to the hot water side portion. Means may be taken.

図1において、2次熱交換器HE2は、1次熱交換器HE1を通過した燃焼ガスから潜熱を回収するためのものであり、1次熱交換器HE1上に載設されたケース7内に、複数の第3および第4の伝熱管T3,T4が収容され、かつそれらの間が仕切板74を介して仕切られた構成である。第3および第4の伝熱管T3,T4、ならびにケース7は、潜熱回収に伴って発生する強酸性のドレインに対する耐食性を有すべくその材質はたとえばステンレスである。図9に示すように、複数の第3の伝熱管T3は、サイズが相違する螺旋状管体として形成されて、重ね巻き状に配列されており、それらの上下両端部は、ケース7の外部に引き出されて通水用のヘッダ75a,75bと連結されている。複数の第4の伝熱管T4も、その基本的な形態は第3の伝熱管T3と同様であり、重ね巻き状に配列された螺旋状管体として形成され、かつその上下両端部には、通水用のヘッダ75c,75dが連結されている。   In FIG. 1, the secondary heat exchanger HE2 is for recovering latent heat from the combustion gas that has passed through the primary heat exchanger HE1, and is placed in a case 7 mounted on the primary heat exchanger HE1. The plurality of third and fourth heat transfer tubes T3 and T4 are accommodated and the space between them is partitioned via a partition plate 74. The third and fourth heat transfer tubes T3, T4 and the case 7 are made of, for example, stainless steel so as to have corrosion resistance against the strongly acidic drain generated along with the recovery of latent heat. As shown in FIG. 9, the plurality of third heat transfer tubes T <b> 3 are formed as spiral tubes having different sizes and are arranged in an overlapping manner, and their upper and lower ends are arranged outside the case 7. Is connected to headers 75a and 75b for passing water. The plurality of fourth heat transfer tubes T4 are also similar in basic form to the third heat transfer tube T3, and are formed as spiral tubes arranged in an overlapping manner, and at both upper and lower ends thereof, The headers 75c and 75d for water flow are connected.

2次熱交換器HE2のケース7は、底壁部70aに給気口71a,71bを有し、かつ前壁部70bに排気口72を有している。図2に示すように、1次熱交換器HE1の第1
の伝熱管T1が設けられた箇所を通過した燃焼ガスは、給気口71aからケース7内に進行し、第3の伝熱管T3どうしの隙間を通過した後に排気口72から外部に排出される。また、図3に示すように、1次熱交換器HE1の第2の伝熱管T2が設けられた箇所を通過した燃焼ガスは、給気口71bからケース7内に進行し、第4の伝熱管T4どうしの隙間を通過した後に排気口72から外部に排出される。このような過程において、燃焼ガスから第3および第4の伝熱管T3,T4により潜熱回収がなされる。潜熱回収に伴って発生した強酸性のドレインは、第3および第4の伝熱管T3,T4からケース7の底壁部70a上に流れ落ちてから、図示されていないドレイン排出口を通過してケース7の外部に排出されるようになっている。
The case 7 of the secondary heat exchanger HE2 has air supply ports 71a and 71b in the bottom wall portion 70a, and an exhaust port 72 in the front wall portion 70b. As shown in FIG. 2, the first heat exchanger HE1
The combustion gas that has passed through the portion where the heat transfer tube T1 is provided proceeds into the case 7 from the air supply port 71a, passes through the gap between the third heat transfer tubes T3, and is then discharged to the outside from the exhaust port 72. . In addition, as shown in FIG. 3, the combustion gas that has passed through the location where the second heat transfer tube T2 of the primary heat exchanger HE1 is provided proceeds into the case 7 from the air supply port 71b, and the fourth heat transfer. After passing through the gap between the heat pipes T4, it is discharged to the outside from the exhaust port 72. In such a process, latent heat is recovered from the combustion gas by the third and fourth heat transfer tubes T3 and T4. The strongly acidic drain generated by the latent heat recovery flows down from the third and fourth heat transfer tubes T3 and T4 onto the bottom wall portion 70a of the case 7 and then passes through a drain discharge port (not shown). 7 is discharged to the outside.

図1に示すように、外装ケース90の底部または側部には、給水管80a,80bが接続される外部入水口90a,90b、および出湯管81a,81bが接続される外部出湯口92a,92bが設けられている。外部入水口90aに供給された湯水は、配管部92aを介してヘッダ75bに供給されることにより、2次熱交換器HE2の第3の伝熱管T3内を流通する。その後、この湯水は、ヘッダ75aおよび配管部93aを介して1次熱交換器HE1の入水口15aに送られ、第1の伝熱管T1内を通過する。第1の伝熱管T1を通過して出湯口16aに到達した湯水は、その後に配管部94aを介して外部出湯口92aに到達する。外部出湯口92aに到達した湯水は、たとえば台所や洗面所などに供給される。   As shown in FIG. 1, external water inlets 90 a and 90 b to which water supply pipes 80 a and 80 b are connected and external hot water outlets 92 a and 92 b to which hot water discharge pipes 81 a and 81 b are connected to the bottom or side of the outer case 90. Is provided. The hot water supplied to the external water inlet 90a is supplied to the header 75b via the piping part 92a, thereby circulating in the third heat transfer tube T3 of the secondary heat exchanger HE2. Thereafter, the hot water is sent to the water inlet 15a of the primary heat exchanger HE1 through the header 75a and the piping portion 93a, and passes through the first heat transfer tube T1. The hot water that has passed through the first heat transfer tube T1 and has reached the hot water outlet 16a then reaches the external hot water outlet 92a through the piping portion 94a. The hot water reaching the external hot water outlet 92a is supplied to, for example, a kitchen or a washroom.

一方、外部入水口90bに供給された湯水は、配管部92bを介してヘッダ75dに供給されることにより、2次熱交換器HE2の第4の伝熱管T4内を流通する。その後、この湯水は、ヘッダ75cおよび配管部93bを介して1次熱交換器HE1の入水口15bに送られ、第2の伝熱管T2内を通過する。第2の伝熱管T2を通過して出湯口16bに到達した湯水は、その後に配管部94bを介して外部出湯口91bに到達し、風呂給湯用または暖房給湯用として所定の箇所に供給される。   On the other hand, the hot water supplied to the external water inlet 90b is supplied to the header 75d via the piping part 92b, thereby circulating in the fourth heat transfer pipe T4 of the secondary heat exchanger HE2. Thereafter, the hot water is sent to the water inlet 15b of the primary heat exchanger HE1 via the header 75c and the piping portion 93b, and passes through the second heat transfer tube T2. The hot water that has passed through the second heat transfer pipe T2 and has reached the hot water outlet 16b then reaches the external hot water outlet 91b through the piping portion 94b, and is supplied to a predetermined location for bath hot water supply or heating hot water supply. .

次に、前記した温水装置WH1の作用について説明する。   Next, the effect | action of above described hot water apparatus WH1 is demonstrated.

まず、1次熱交換器HE1の第1および第2の伝熱管T1,T2は、複数の直状管体部11a,11bが、上下方向に単段(1段)に設けられた構成である。このため、直状管体部11a,11bを上下複数段に設けた場合と比較して、1次熱交換器HE1を薄型化し、温水装置WH1全体の小型化、ならびに製造コストの低減を図ることができる。   First, the first and second heat transfer tubes T1 and T2 of the primary heat exchanger HE1 have a configuration in which a plurality of straight tube portions 11a and 11b are provided in a single stage (one stage) in the vertical direction. . For this reason, compared with the case where the straight tube parts 11a and 11b are provided in a plurality of upper and lower stages, the primary heat exchanger HE1 is made thinner, the entire hot water device WH1 is downsized, and the manufacturing cost is reduced. Can do.

バーナ5を燃焼駆動させて、燃焼ガスを1次熱交換器HE1に向けて進行させた場合、入水側管体部11a'の周辺部分には比較的多くの燃焼ガスを供給させることができるとともに、出湯側管体部11a"の周辺部分には余り多くの燃焼ガスが供給されないようにすることができる。これは、既述したように、隙間C1,C2の幅L1,L2が、L1>L2の関係にあることや、隙間C2についてはその上方に燃焼ガスの流れ規制部20が設けられて燃焼ガス流れに対する抵抗を生じるのに対し、隙間C1については流れ規制部20に相当する手段が設けられておらず、燃焼ガス流れに対する抵抗が小さくされていることによる。さらに、複数の流れ規制部21aは、他の流れ規制部21よりも燃焼ガス流れに対する抵抗が小さく、入水側管体部11a'とこれに隣接する直状管体部11aとの間にも燃焼ガスが流入し易いことにもよる。   When the burner 5 is driven to burn and the combustion gas is advanced toward the primary heat exchanger HE1, a relatively large amount of combustion gas can be supplied to the peripheral portion of the water inlet side pipe portion 11a ′. In addition, it is possible to prevent excessive combustion gas from being supplied to the peripheral portion of the hot water side pipe body portion 11a ". As described above, the widths L1 and L2 of the gaps C1 and C2 are L1>. The fact that there is a relationship of L2 and that the gap C2 is provided with a combustion gas flow restricting portion 20 above it to cause resistance to the combustion gas flow, while the gap C1 has means corresponding to the flow restricting portion 20 It is not provided, and the resistance to the combustion gas flow is reduced, and the plurality of flow restriction portions 21a have a smaller resistance to the combustion gas flow than the other flow restriction portions 21, and the water inlet side pipe body portion. This is also because the combustion gas easily flows between 11a ′ and the straight tubular body portion 11a adjacent thereto.

伝熱管T1には、2次熱交換器HE2の伝熱管T3を通過して加熱された湯水が供給されるものの、伝熱管T3への入水温度がかなり低い場合には、伝熱管T1への入水温度が比較的低くなる。これに対し、前記したように入水側管体部11a'の周辺部分に比較的多くの燃焼ガスが供給されると、伝熱管T1に低温の湯水が供給された場合であっても、入水側管体部11a'の周辺部分が低温状態に維持されることは適切に抑制される。その結果
、それらの部分に多くのドレインが発生しないようにし、ドレインに起因して入水側管体部11a'やフィン2Aが腐食し易くなる不具合を適切に抑制することができる。
Although the hot water heated by passing through the heat transfer tube T3 of the secondary heat exchanger HE2 is supplied to the heat transfer tube T1, when the temperature of the water input to the heat transfer tube T3 is considerably low, the water input to the heat transfer tube T1 The temperature is relatively low. On the other hand, as described above, when a relatively large amount of combustion gas is supplied to the peripheral portion of the water inlet side pipe body portion 11a ', even if cold hot water is supplied to the heat transfer pipe T1, the water inlet side It is suppressed appropriately that the peripheral part of tube part 11a 'is maintained at a low-temperature state. As a result, it is possible to prevent a large number of drains from being generated in those portions, and to appropriately suppress a problem that the water inlet side tube portion 11a ′ and the fins 2A are easily corroded due to the drains.

一方、伝熱管T1内の湯水温度は、この伝熱管T1の末端に相当する出湯側管体部11a"において最も高温となる。これに対し、この出湯側管体部11a"の周辺部分については、既述したように、燃焼ガス供給量が多くならないようにされる。したがって、出湯側管体部11a"およびその周辺部分において、湯水が加熱状態となって沸騰することを適切に防止することができる。湯水が沸騰すると、伝熱管T1内に気泡が生じ、円滑な湯水流通が行なわれなくなる他、伝熱管T1が湯水によって冷却されなくなって伝熱管T1が熱損傷するといった不具合を生じるが、本実施形態によれば、そのような不具合も適切に防止することが可能である。   On the other hand, the temperature of the hot water in the heat transfer tube T1 is the highest in the tapping side tube portion 11a "corresponding to the end of the heat transfer tube T1. On the other hand, the peripheral portion of this tapping side tube portion 11a" As described above, the combustion gas supply amount is not increased. Accordingly, it is possible to appropriately prevent hot water from being heated and boiling in the hot water side pipe body portion 11a "and its peripheral portion. When the hot water is boiled, bubbles are generated in the heat transfer tube T1 and smooth. In addition to the fact that the hot water circulation is not performed, the heat transfer tube T1 is not cooled by the hot water and the heat transfer tube T1 is thermally damaged. However, according to the present embodiment, such a problem can be appropriately prevented. It is.

図10は、本発明の他の実施形態を示している。同図において、前記実施形態と同一または類似の要素には、前記実施形態と同一の符号を付し、その説明は省略する。同図に示す温水装置WH2においては、1次熱交換器HE1および2次熱交換器HE2が、1缶2回路には構成されておらず、一系統のみの給湯機能を備えたものとして構成されている。本実施形態においては、前記実施形態の仕切部材3に相当する部材は用いられておらず、出湯側管体部11a"には、缶体6の側壁部60d'が対向接近している。したがって、この側壁部60d'が、本発明でいう第2の側壁部の他の具体例に相当する。   FIG. 10 shows another embodiment of the present invention. In the figure, the same or similar elements as those of the above embodiment are denoted by the same reference numerals as those of the above embodiment, and the description thereof is omitted. In the hot water apparatus WH2 shown in the figure, the primary heat exchanger HE1 and the secondary heat exchanger HE2 are not configured in one can two circuits, but are configured to have a hot water supply function of only one system. ing. In the present embodiment, a member corresponding to the partition member 3 of the above-described embodiment is not used, and the side wall 60d ′ of the can 6 is opposed to and close to the tapping side tube body portion 11a ″. The side wall portion 60d 'corresponds to another specific example of the second side wall portion in the present invention.

本発明は、上述した実施形態の内容に限定されない。本発明に係る熱交換器および温水装置の各部の具体的な構成は、本発明の意図する範囲内において種々に設計変更自在である。   The present invention is not limited to the contents of the above-described embodiment. The specific configuration of each part of the heat exchanger and the hot water apparatus according to the present invention can be variously modified within the range intended by the present invention.

入水側管体部11a'の周辺領域の燃焼ガス供給量を多くし、かつ出湯側管体部11a"の周辺領域の燃焼ガス供給量を少なくするための手段としては、隙間C1,C2の幅L1,L2を、L1>L2の関係に設定する手段のみを適用し、フィン2Aに設けられる燃焼ガス用の流れ規制部20,21を不均一に設ける手段を適用しない構成としてもよい。また、これとは反対に、燃焼ガス用の流れ規制部20,21を不均一に設ける手段を適用し、L1>L2の関係に設定する手段を適用しない構成とすることもできる。   As means for increasing the amount of combustion gas supply in the peripheral region of the water inlet side tube portion 11a 'and decreasing the amount of combustion gas supply in the peripheral region of the tapping water side tube portion 11a ", the width of the gaps C1 and C2 is used. Only a means for setting L1 and L2 to a relationship of L1> L2 may be applied, and a means for unevenly providing the flow regulating portions 20 and 21 for the combustion gas provided on the fin 2A may be omitted. On the contrary, it is also possible to adopt a configuration in which means for providing the combustion gas flow restricting portions 20 and 21 non-uniformly is applied, and means for setting the relationship of L1> L2 is not applied.

本発明でいう加熱用気体の流れ規制部は、複数のフィンどうしの間を加熱用気体が通過する際の抵抗となるように各フィンの表面の一部を突出させた形態を有するものであればよい。したがって、前記したようにフィンの一部を押し出したもの、きり起こし状に形成したものの他、たとえばバーリング孔(孔の周辺部分が凸状に起立)とすることもできる。   The heating gas flow restricting portion referred to in the present invention has a form in which a part of the surface of each fin is protruded so as to be a resistance when the heating gas passes between the plurality of fins. That's fine. Therefore, as described above, a part of the fin is extruded or formed to be raised, and for example, a burring hole (a peripheral part of the hole stands up in a convex shape) can be used.

本発明に係る温水装置は、必ずしも1次および2次の2つの熱交換器を備えたものとして構成されていなくてもよく、熱交換器として、本発明に係る熱交換器を1つのみ用いた温水装置とすることもできる。上述の実施形態では、バーナの上方に熱交換器が設けられて、燃焼ガスが熱交換器の下方から上方に向けて進行するいわゆる正燃方式とされているが、これとは反対に、バーナの下方に熱交換器が設けられて、燃焼ガスが上方から下方に向けて進行する逆燃方式とすることも可能である。本発明でいう加熱用気体としては、バーナを利用して発生させた燃焼ガスに限らず、たとえば燃料電池やガスエンジンなどから排出される高温の排ガスを利用することもできる。本発明でいう温水装置とは、湯を生成する機能を備えた装置の意であり、一般給湯用、風呂給湯用、暖房用、あるいは融雪用などの各種の給湯装置、および給湯以外に用いられる湯を生成する装置を広く含む。   The hot water apparatus according to the present invention does not necessarily have to be configured with two primary and secondary heat exchangers, and only one heat exchanger according to the present invention is used as the heat exchanger. It can also be a hot water device. In the above-described embodiment, a heat exchanger is provided above the burner so that the combustion gas proceeds from the lower side to the upper side of the heat exchanger. It is also possible to adopt a reverse combustion system in which a heat exchanger is provided below the gas and the combustion gas advances from the upper side to the lower side. The heating gas referred to in the present invention is not limited to the combustion gas generated using a burner, and high-temperature exhaust gas discharged from, for example, a fuel cell or a gas engine can also be used. The hot water device as used in the present invention means a device having a function of generating hot water, and is used for various types of hot water supply devices for general hot water supply, bath hot water supply, heating, snow melting, and the like, and hot water supply. Widely includes equipment for producing hot water.

WH1,WH2 温水装置
HE1 1次熱交換器(本発明に係る熱交換器)
HE2 2次熱交換器
T1 第1の伝熱管(伝熱管)
C1,C2 隙間
2A フィン
3 仕切部材
6 缶体
11a 直状管体部
11a' 入水側管体部
11a" 出湯側管体部
12a 連結用管体部
20,21 流れ規制部(加熱用気体の流れ規制部)
30a 側壁部(第2の側壁部)
60c 側壁部(第1の側壁部)
60d’ 側壁部(第2の側壁部)
WH1, WH2 water heater HE1 primary heat exchanger (heat exchanger according to the present invention)
HE2 secondary heat exchanger T1 first heat transfer tube (heat transfer tube)
C1, C2 Gap 2A Fin 3 Partition member 6 Can body 11a Straight tubular body portion 11a 'Incoming water tubular body portion 11a "Hot water outlet side tubular body portion 12a Connecting tubular body portions 20, 21 Flow regulating portion (flow of heating gas Regulatory Department)
30a Side wall (second side wall)
60c side wall (first side wall)
60d 'side wall (second side wall)

Claims (5)

プレート状の複数のフィンに貫通した複数の直状管体部を有する伝熱管と、
前記複数の直状管体部および前記複数のフィンの周囲を囲む複数の側壁部を有し、かつ上下両面部が加熱用気体の流出入用の開口部とされる缶体と、を備えており、
前記伝熱管は、前記複数の直状管体部が前記缶体の前後または左右の幅方向に間隔を隔てて並ぶとともに前記缶体の上下高さ方向に単段に設けられて連結用管体部を介して一連に接続された蛇行状に形成されており、
前記伝熱管の前記幅方向の両端に位置する2つの直状管体部のうち、一方は入水側管体部とされ、かつ他方は出湯側管体部とされ、前記伝熱管における湯水の流通は、前記入水側管体部から前記出湯側管体部に向けて一方向になされるように構成された、熱交換器であって、
前記入水側管体部とこれに対向接近する前記缶体の第1の側壁部との隙間の幅は、前記出湯側管体部とこれに対向接近する前記缶体の第2の側壁部との隙間の幅よりも大きくされていることを特徴とする、熱交換器。
A heat transfer tube having a plurality of straight tube sections penetrating through a plurality of plate-shaped fins;
A can body having a plurality of side wall portions surrounding the plurality of straight tubular body portions and the plurality of fins, and having both upper and lower side portions as openings for inflow and outflow of a heating gas. And
In the heat transfer tube, the plurality of straight tube portions are arranged at intervals in the front-rear or left-right width direction of the can body and are provided in a single stage in the vertical height direction of the can body. Formed in a serpentine shape connected in series through the section,
Of the two straight tube portions located at both ends of the heat transfer tube in the width direction, one is a water inlet tube portion and the other is a hot water discharge tube portion, and the flow of hot water in the heat transfer tube Is a heat exchanger configured to be made in one direction from the water inlet side pipe body part toward the hot water outlet side pipe body part,
The width of the gap between the water inlet side pipe body part and the first side wall part of the can body facing and approaching the water inlet side pipe body part is the second side wall part of the can body facing and approaching the hot water side pipe body part. The heat exchanger is characterized by being larger than the width of the gap.
プレート状の複数のフィンに貫通した複数の直状管体部を有する伝熱管と、
前記複数の直状管体部および前記複数のフィンの周囲を囲む側壁部を有し、かつ上下両面部が加熱用気体の流出入用の開口部とされる缶体と、を備えており、
前記伝熱管は、前記複数の直状管体部が前記缶体の前後または左右の幅方向に間隔を隔てて並ぶとともに前記缶体の上下高さ方向に単段に設けられて連結用管体部を介して一連に接続された蛇行状に形成されており、
前記伝熱管の前記幅方向の両端に位置する2つの直状管体部のうち、一方は入水側管体部とされ、かつ他方は出湯側管体部とされ、前記伝熱管における湯水の流通は、前記入水側管体部から前記出湯側管体部に向けて一方向になされるように構成された、熱交換器であって、
前記複数のフィンには、これら複数のフィンどうしの間を前記加熱用気体が通過する際の抵抗となるように前記各フィンの表面の一部を突出させた加熱用気体の流れ規制部が複数設けられており、
これら複数の流れ規制部として、前記出湯側管体部とこれに対向接近する前記缶体の第2の側壁部との間またはその上方もしくは下方に位置する最出湯側の流れ規制部が設けられている一方、
前記入水側管体部とこれに対向接近する前記缶体の第1の側壁部との間およびその上下方の位置には、流れ規制部は設けられておらず、または前記最出湯側の流れ規制部よりも前記加熱用気体の流れに対する抵抗が小さい流れ規制部が設けられ、
前記入水側管体部の周辺部分よりも前記出湯側管体部の周辺部分の方が前記加熱用気体の流れに対する抵抗が大きくなるように構成されていることを特徴とする、熱交換器。
A heat transfer tube having a plurality of straight tube sections penetrating through a plurality of plate-shaped fins;
A can body having side walls surrounding the plurality of straight tubular body portions and the plurality of fins, and upper and lower both surface portions being openings for inflow and outflow of heating gas, and
In the heat transfer tube, the plurality of straight tube portions are arranged at intervals in the front-rear or left-right width direction of the can body and are provided in a single stage in the vertical height direction of the can body. Formed in a serpentine shape connected in series through the section,
Of the two straight tube portions located at both ends of the heat transfer tube in the width direction, one is a water inlet tube portion and the other is a hot water discharge tube portion, and the flow of hot water in the heat transfer tube Is a heat exchanger configured to be made in one direction from the water inlet side pipe body part toward the hot water outlet side pipe body part,
The plurality of fins are provided with a plurality of heating gas flow restricting portions in which a part of the surface of each fin is protruded so as to provide resistance when the heating gas passes between the plurality of fins. Provided,
As the plurality of flow restricting portions , there is provided a flow restricting portion on the outermost hot water side located between or above or below the hot water side pipe body portion and the second side wall portion of the can facing and approaching it. While
There is no flow restricting portion provided between the water inlet side pipe body portion and the first side wall portion of the can body facing and approaching the water inlet side, or on the upper and lower side thereof, or on the most hot water side. A flow restricting portion having a smaller resistance to the flow of the heating gas than the flow restricting portion is provided,
The heat exchanger is configured such that the resistance to the flow of the heating gas is greater in the peripheral part of the hot water side pipe part than in the peripheral part of the water inlet side pipe part. .
プレート状の複数のフィンに貫通した複数の直状管体部を有する伝熱管と、
前記複数の直状管体部および前記複数のフィンの周囲を囲む側壁部を有し、かつ上下両面部が加熱用気体の流出入用の開口部とされる缶体と、を備えており、
前記伝熱管は、前記複数の直状管体部が前記缶体の前後または左右の幅方向に間隔を隔てて並ぶとともに前記缶体の上下高さ方向に単段に設けられて連結用管体部を介して一連に接続された蛇行状に形成されており、
前記伝熱管の前記幅方向の両端に位置する2つの直状管体部のうち、一方は入水側管体部とされ、かつ他方は出湯側管体部とされ、前記伝熱管における湯水の流通は、前記入水側管体部から前記出湯側管体部に向けて一方向になされるように構成された、熱交換器であって、
前記複数のフィンには、これら複数のフィンどうしの間を前記加熱用気体が通過する際の抵抗となるように前記各フィンの表面の一部を突出させた加熱用気体の流れ規制部が複数設けられており、
これら複数の流れ規制部として、前記複数の直状管体部どうしの間に設けられた複数の流れ規制部があり、これら複数の直状管体部のうち、前記入水側管体部とこれに隣接する直状管体部との間およびその上下方の領域に設けられている流れ規制部は、他の直状管体部どうしの各間およびその上下方の領域に設けられている流れ規制部よりも前記加熱用気体の流れに対する抵抗が小さい構成とされ、
前記入水側管体部の周辺部分よりも前記出湯側管体部の周辺部分の方が前記加熱用気体の流れに対する抵抗が大きくなるように構成されていることを特徴とする、熱交換器。
A heat transfer tube having a plurality of straight tube sections penetrating through a plurality of plate-shaped fins;
A can body having side walls surrounding the plurality of straight tubular body portions and the plurality of fins, and upper and lower both surface portions being openings for inflow and outflow of heating gas, and
In the heat transfer tube, the plurality of straight tube portions are arranged at intervals in the front-rear or left-right width direction of the can body and are provided in a single stage in the vertical height direction of the can body. Formed in a serpentine shape connected in series through the section,
Of the two straight tube portions located at both ends of the heat transfer tube in the width direction, one is a water inlet tube portion and the other is a hot water discharge tube portion, and the flow of hot water in the heat transfer tube Is a heat exchanger configured to be made in one direction from the water inlet side pipe body part toward the hot water outlet side pipe body part,
The plurality of fins are provided with a plurality of heating gas flow restricting portions in which a part of the surface of each fin is protruded so as to provide resistance when the heating gas passes between the plurality of fins. Provided,
As the plurality of flow restricting portions, there are a plurality of flow restricting portions provided between the plurality of straight tubular portions, and among the plurality of straight tubular portions, the water inlet side tubular portion and The flow restricting portion provided between the adjacent straight tube portions and in the region above and below them is provided between each other straight tube portions and in the region above and below them. The resistance to the flow of the heating gas is smaller than the flow restricting portion,
The heat exchanger is configured such that the resistance to the flow of the heating gas is greater in the peripheral part of the hot water side pipe part than in the peripheral part of the water inlet side pipe part . .
請求項2または3に記載の熱交換器であって、
前記入水側管体部とこれに対向接近する前記缶体の第1の側壁部との隙間の幅は、前記出湯側管体部とこれに対向接近する前記缶体の第2の側壁部との隙間の幅よりも大きくされている、熱交換器。
The heat exchanger according to claim 2 or 3,
The width of the gap between the water inlet side pipe body part and the first side wall part of the can body facing and approaching the water inlet side pipe body part is the second side wall part of the can body facing and approaching the hot water side pipe body part. The heat exchanger is larger than the width of the gap .
請求項1ないし4のいずれかに記載の熱交換器を備えていることを特徴とする、温水装置A hot water apparatus comprising the heat exchanger according to any one of claims 1 to 4 .
JP2011238066A 2011-10-29 2011-10-29 Heat exchanger and hot water device provided with the same Active JP5835569B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2011238066A JP5835569B2 (en) 2011-10-29 2011-10-29 Heat exchanger and hot water device provided with the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2011238066A JP5835569B2 (en) 2011-10-29 2011-10-29 Heat exchanger and hot water device provided with the same

Publications (2)

Publication Number Publication Date
JP2013096609A JP2013096609A (en) 2013-05-20
JP5835569B2 true JP5835569B2 (en) 2015-12-24

Family

ID=48618733

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2011238066A Active JP5835569B2 (en) 2011-10-29 2011-10-29 Heat exchanger and hot water device provided with the same

Country Status (1)

Country Link
JP (1) JP5835569B2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6151146B2 (en) * 2013-09-25 2017-06-21 株式会社パロマ Heat exchanger in water heater, and water heater
CN103743107A (en) * 2014-01-06 2014-04-23 无锡市林志热交换器有限公司 Efficient heat absorption fin for fuel gas wall hanging stove
JP6331214B2 (en) * 2014-01-10 2018-05-30 株式会社ノーリツ Heat exchanger and hot water device provided with the same
JP6798357B2 (en) * 2017-02-28 2020-12-09 株式会社ノーリツ Heat exchanger and heat source machine
CN109416198A (en) * 2018-02-07 2019-03-01 中山市力科电器有限公司 Vehicle-mounted gas type water heater
JP7215156B2 (en) * 2018-12-26 2023-01-31 株式会社ノーリツ heat exchanger and water heater
JP7336271B2 (en) * 2019-06-17 2023-08-31 リンナイ株式会社 Combustion device

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50134168U (en) * 1974-04-19 1975-11-05
JP3834431B2 (en) * 1998-08-05 2006-10-18 株式会社ガスター Heat exchanger
JP4086455B2 (en) * 2000-07-28 2008-05-14 パロマ工業株式会社 Water heater
JP2004163059A (en) * 2002-11-15 2004-06-10 Matsushita Electric Ind Co Ltd Heat exchanger for hot water supply
JP2005180778A (en) * 2003-12-19 2005-07-07 Paloma Ind Ltd Water heating appliance
JP2009133530A (en) * 2007-11-29 2009-06-18 Hitachi Appliances Inc Heat exchanger and heat pump hot water supply machine

Also Published As

Publication number Publication date
JP2013096609A (en) 2013-05-20

Similar Documents

Publication Publication Date Title
JP5835569B2 (en) Heat exchanger and hot water device provided with the same
JP5043859B2 (en) Condenser boiler heat exchanger for heating and hot water supply
JP5818071B2 (en) Water heater
JP5790973B2 (en) Water heater
JP5180716B2 (en) Heat exchanger and hot water supply apparatus using the same
JP7357208B2 (en) Heat exchanger and water heating equipment equipped with the same
JP6610246B2 (en) Water heater
JP6256807B2 (en) Heat exchanger and hot water device provided with the same
JP4531018B2 (en) Combined heat source
JP2021134971A (en) Heat exchanger and water heater having the same
JP5234349B2 (en) Heat exchanger and water heater
JP5900731B2 (en) Water heater
JP6099003B2 (en) Heat exchanger and hot water device provided with the same
JP4160576B2 (en) Combined heat source machine
JP2000146461A (en) Heat exchanger
JP6260773B2 (en) Heat exchanger and hot water device provided with the same
JP6331214B2 (en) Heat exchanger and hot water device provided with the same
JP6256801B2 (en) Heat exchanger and hot water device provided with the same
JP5387436B2 (en) Heat exchanger
JP2024070687A (en) Heat exchanger and water heater
JP2018112323A (en) Heat exchanger
JP2016121811A (en) Heat exchanger and water heater with the same
KR101020772B1 (en) separation type heat exchanger
JP2013133955A (en) Latent heat exchanger and water heater
JP2004093064A (en) Heat exchanger

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20140926

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20150721

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20150724

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20150915

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: 20151007

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20151020

R150 Certificate of patent or registration of utility model

Ref document number: 5835569

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