JP2016080186A - Bath device - Google Patents

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JP2016080186A
JP2016080186A JP2014208177A JP2014208177A JP2016080186A JP 2016080186 A JP2016080186 A JP 2016080186A JP 2014208177 A JP2014208177 A JP 2014208177A JP 2014208177 A JP2014208177 A JP 2014208177A JP 2016080186 A JP2016080186 A JP 2016080186A
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temperature
time
heating
heat
bathtub
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幸祐 中島
Kosuke Nakajima
幸祐 中島
景介 奥備
Keisuke Oubi
景介 奥備
一久 井川
Kazuhisa Igawa
一久 井川
研 安田
Ken Yasuda
研 安田
英之 辻
Hideyuki Tsuji
英之 辻
誠人 大石
Masato Oishi
誠人 大石
大吾 伊藤
Daigo Ito
大吾 伊藤
保男 纐纈
Yasuo Koketsu
保男 纐纈
石田 宏
Hiroshi Ishida
宏 石田
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Osaka Gas Co Ltd
Tokyo Gas Co Ltd
Toho Gas Co Ltd
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Osaka Gas Co Ltd
Tokyo Gas Co Ltd
Toho Gas Co Ltd
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Priority to JP2014208177A priority Critical patent/JP2016080186A/en
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Abstract

PROBLEM TO BE SOLVED: To improve an entire energy efficiency of bath device at an indirect heating type bath device by optimizing an interval of additional heating during a heat rising operation, in particular.SOLUTION: An indirect heating type bath device comprises a heat rising operation means for keeping a temperature of bathtub water at a temperature between a set temperature and a lower limit temperature lower than the set temperature only by a hot water temperature descending limit range by transmitting an additional heating instruction to an additional heating processing means when an additional heating interval time elapses upon completion of the additional heating treatment; and an additional heating interval time changing means for calculating a descending time required for decreasing a temperature of the bathtub water to a lower limit temperature on the basis of a hot water reduction rate that is a reduction rate of temperature of the bathtub water during elapsing of the additional heating interval time from completion time of a previous time additional heating, and changing the additional heating interval time to a time in which the additional heating interval time is changed from the descending time or a time changed from the descending time only by an adjustment width.SELECTED DRAWING: Figure 1

Description

本発明は、熱媒加熱用の燃焼式加熱装置と、前記燃焼式加熱装置の燃焼により熱媒を加熱する第1熱交換器を有する熱媒循環回路と、浴槽内の浴槽水が循環される浴槽水循環回路と、前記熱媒循環回路を通流する熱媒と前記浴槽水循環回路を通流する浴槽水とを熱交換させて前記浴槽水を加熱する第2熱交換器とを備えた風呂装置に関する。   The present invention relates to a combustion-type heating device for heating a heat medium, a heat-medium circulation circuit having a first heat exchanger that heats the heat medium by combustion of the combustion-type heating device, and bathtub water in the bathtub is circulated. A bath apparatus comprising: a bathtub water circulation circuit; and a second heat exchanger that heats the bathtub water by exchanging heat between the heating medium flowing through the heating medium circulation circuit and the bathtub water flowing through the bathtub water circulation circuit. About.

特許文献1では、温水循環用の回路21,22を流れる熱媒を、バーナ4Bを用いて加熱し、当該加熱された熱媒の熱を、追焚き用熱交換器28を介して、浴槽水循環用の回路31,32を流れる浴槽水に伝えることで、浴槽水を追焚きする風呂設備が開示されている。この風呂設備では、バーナで浴槽水を直接加熱するのではなく、温水循環用の回路21,22を介して間接的に浴槽水を加熱するように構成されている   In Patent Document 1, the heat medium flowing through the circuits 21 and 22 for hot water circulation is heated using the burner 4B, and the heat of the heated heat medium is circulated through the bath heat exchanger 28 through the heat exchanger 28 for reheating. The bath equipment which retreats the bathtub water by telling the bathtub water flowing through the circuits 31 and 32 for use is disclosed. In this bath facility, bath water is not directly heated by a burner, but bath water is heated indirectly via circuits 21 and 22 for hot water circulation.

このような、いわゆる間接加熱方式の風呂装置の効率は、従来は『定格(最大)出力で連続運転した際の入力熱量にて出力熱量を除算する』形態で算出されていたが、近年、より実際の使用状態に即した効率(例えば、断続運転をも含む運転状態で算出される効率)での評価を行うことが検討されている。   The efficiency of such a so-called indirect heating system bath apparatus has been calculated in the form of “dividing the output heat amount by the input heat amount when continuously operating at the rated (maximum) output”, but in recent years, It has been studied to evaluate at an efficiency (for example, an efficiency calculated in an operation state including intermittent operation) in accordance with an actual use state.

特開2009−144935号公報JP 2009-144935 A

発明者らは、上記特許文献1に示される風呂装置にて間接加熱方式で追焚き処理を実行するときで、特に、実際の使用状態に即した効率、即ち、断続運転等をも含む状態で算出される効率での評価を行う場合、エネルギー効率に改善の余地があることを見出した。具体的には、自動的に追焚きを行って浴槽水の温度を設定温度に保つ保温運転において、追焚きを行うか否かの判定の時間間隔が固定のため、浴槽水循環ポンプを稼働して判定を行った結果追焚きが行われないことがあった。この場合、浴槽水循環ポンプ稼働分の電力を無駄に消費しており、風呂装置全体のエネルギー効率を悪化させていた。   The inventors have performed the reheating process by the indirect heating method in the bath apparatus shown in Patent Document 1 above, and in particular, the efficiency according to the actual use state, that is, including the intermittent operation and the like. When evaluating with the calculated efficiency, we found that there is room for improvement in energy efficiency. Specifically, in the heat insulation operation in which the bath water temperature is automatically maintained and the bath water temperature is kept at the set temperature, the bath water circulation pump is operated because the time interval for determining whether or not to perform the bath water is fixed. As a result of the determination, there was a case that no tracking was performed. In this case, the electric power for operating the bathtub water circulation pump was wasted, and the energy efficiency of the entire bath apparatus was deteriorated.

本発明は、上述の課題に鑑みてなされたものであり、その目的は、間接加熱方式での追焚き処理において、保温運転における追焚きの間隔を最適化することにより、風呂装置全体のエネルギー効率を改善することが可能な風呂装置を提供することである。   The present invention has been made in view of the above-described problems, and the purpose of the present invention is to optimize the energy efficiency of the bath apparatus by optimizing the reheating interval in the reheating process in the indirect heating method. It is providing the bath apparatus which can improve.

上記目的を達成するための本発明に係る風呂装置の特徴構成は、熱媒加熱用の燃焼式加熱装置と、燃焼式加熱装置の燃焼により熱媒を加熱する第1熱交換器を有する熱媒循環回路と、浴槽内の浴槽水が循環される浴槽水循環回路と、前記熱媒循環回路を通流する熱媒と前記浴槽水循環回路を通流する浴槽水とを熱交換させて前記浴槽水を加熱する第2熱交換器とを備えた風呂装置において、前記熱媒循環回路に前記熱媒を循環させる熱媒循環手段と、前記浴槽水循環回路に前記浴槽水を循環させる浴槽水循環手段と、追焚き処理指令を受けた際に、前記燃焼式加熱装置と前記熱媒循環手段と前記浴槽水循環手段とを作動させて前記浴槽水を設定温度に加熱する追焚き処理を行う追焚き処理手段と、前記追焚き処理が終了してから追焚き間隔時間が経過した時点で前記追焚き処理指令を前記追焚き処理手段に送ることにより、前記浴槽水の温度を前記設定温度と前記設定温度より湯温降下限度幅だけ低い下限温度との間に保つ保温運転手段と、前回の追焚き処理の終了時から前記追焚き間隔時間が経過する間の前記浴槽水の温度の低下率である湯温低下率に基づき、前記浴槽水の温度が前記下限温度まで低下するのに要する下降時間を算出し、前記追焚き間隔時間を前記下降時間または前記下降時間から調整時間幅だけ変更された時間へと変更する追焚き間隔時間変更手段を備えた点にある。   In order to achieve the above object, the characteristic configuration of the bath apparatus according to the present invention includes a combustion heating apparatus for heating a heating medium and a heating medium having a first heat exchanger that heats the heating medium by combustion of the combustion heating apparatus. Heat exchange is performed between the circulation circuit, the bathtub water circulation circuit in which the bathtub water in the bathtub is circulated, the heat medium that flows through the heating medium circulation circuit, and the bathtub water that flows through the bathtub water circulation circuit. In a bath apparatus including a second heat exchanger for heating, a heating medium circulating means for circulating the heating medium in the heating medium circulating circuit, a bathtub water circulating means for circulating the bathtub water in the bathtub water circulating circuit, A reheating process means for performing a reheating process for operating the combustion-type heating device, the heating medium circulation means, and the bathtub water circulation means to heat the bathtub water to a set temperature when receiving a firing treatment command; At the tracking interval after the tracking process is completed The temperature of the bath water is kept between the set temperature and a lower limit temperature lower than the set temperature by a hot water temperature drop limit width by sending the follow-up process command to the follow-up processing means when the time elapses. Based on the operating means and the hot water temperature decrease rate that is the rate of decrease in the temperature of the bath water during the elapse of the reheating interval time from the end of the previous reheating process, the temperature of the bath water is reduced to the lower limit temperature. It is provided with a tracking interval time changing means for calculating a falling time required to decrease and changing the tracking interval time from the falling time or a time changed from the falling time to an adjustment time width.

上記特徴構成によれば、風呂装置は、湯温低下率に基づいて下降時間を算出し、追焚き間隔時間を算出された下降時間へ変更するので、追焚きの間隔が、放熱による浴槽水の温度低下に応じた適切な間隔となる。従って、間隔が短すぎて湯温低下が小さいことにより追焚きが行われず浴槽水循環手段の稼働が無駄となる事態を回避できる。また、追焚きの間隔が長くなりすぎて大きな湯温低下が発生し、風呂装置の使用者に不便を強いることもない。さらに、追焚き間隔時間を下降時間から調整時間幅だけ変更された時間へ変更すると、浴室暖房や換気等で浴室の状況が変化した場合であっても、算出された下降時間よりも早いタイミングで追焚きして過大な湯温低下を抑制したり、算出された下降時間よりも遅いタイミングで追焚きしてエネルギー消費を抑制できる。すなわち、エネルギー効率と利便性・快適性を高めた風呂装置を提供することができる。   According to the above characteristic configuration, the bath device calculates the descent time based on the hot water temperature decrease rate and changes the reheating interval time to the calculated descent time. It becomes an appropriate interval according to the temperature drop. Therefore, it is possible to avoid a situation in which the operation of the bathtub water circulation means is wasted because the interval is too short and the drop in hot water temperature is small and no reheating is performed. In addition, the chasing interval becomes too long, causing a large drop in hot water temperature, which does not inconvenience the user of the bath apparatus. Furthermore, if the chasing interval time is changed from the descending time to the time changed by the adjustment time width, even if the bathroom condition changes due to bathroom heating or ventilation, etc., the timing is earlier than the calculated descending time. It is possible to suppress the excessive decrease in hot water temperature by chasing, or chasing at a timing later than the calculated descent time to suppress energy consumption. That is, it is possible to provide a bath apparatus with improved energy efficiency and convenience / comfort.

本発明に係る風呂装置の更なる特徴構成は、前記浴槽内から前記第2熱交換器に戻る浴槽水の温度である浴槽出温度を検出する検出手段を備え、前記追焚き間隔時間変更手段は、前記設定温度と、今回の追焚き処理の開始時に前記検出手段により検出された前記浴槽出温度との差から求められる湯温低下量を、前回の追焚き処理と今回の追焚き処理との時間間隔である追焚き間隔時間で除算して前記湯温低下率を求め、前記湯温降下限度幅を前記湯温低下率で除算して前記下降時間を算出する点にある。   A further characteristic configuration of the bath device according to the present invention is provided with a detecting means for detecting a bath outlet temperature that is a temperature of the bath water returning from the inside of the bathtub to the second heat exchanger, and the chasing interval time changing means includes: The amount of decrease in hot water temperature obtained from the difference between the set temperature and the bath temperature detected by the detection means at the start of the current reheating process is calculated as the previous reheating process and the current reheating process. The hot water temperature lowering rate is obtained by dividing by a chasing interval time, which is a time interval, and the lowering time is calculated by dividing the hot water temperature lowering limit width by the hot water temperature lowering rate.

上記特徴構成によれば、実際に測定された浴槽出温度に基づいて湯温低下率と下降時間を計算しているので、算出された下降時間は今回の追焚きの直前の状況を反映した値となっている。従って、より適切な追焚き間隔時間への変更を行うことができ、エネルギー効率をさらに高めることができる。   According to the above characteristic configuration, since the hot water temperature decrease rate and the descent time are calculated based on the actually measured bath temperature, the calculated descent time is a value that reflects the situation immediately before the current chasing. It has become. Therefore, a change to a more appropriate tracking interval time can be performed, and energy efficiency can be further increased.

本発明に係る風呂装置の更なる特徴構成は、前記追焚き処理手段は、前記追焚き処理指令を受けた際、前記浴槽水循環手段を作動させ、前記検出手段による前記浴槽出温度の測定が完了した後に前記燃焼式加熱装置と前記熱媒循環手段とを作動させる点にある。   A further characteristic configuration of the bath device according to the present invention is that, when the reheating processing unit receives the reheating processing command, the bath water circulation unit is operated, and the measurement of the bath temperature by the detecting unit is completed. Then, the combustion type heating device and the heat medium circulating means are operated.

上記特徴構成によれば、まず浴槽水循環手段を作動させて浴槽出温度の測定が完了した後に燃焼式加熱装置と熱媒循環手段を作動させるので、加熱された熱媒の影響を受けずに浴槽出温度の測定を確実に行うことができる。従って、下降時間の算出をより精度よく行うことができ、風呂装置のエネルギー効率をさらに高めることができる。   According to the above characteristic configuration, since the combustion heating device and the heat medium circulating means are operated after the bath water circulating means is first operated and the measurement of the bath outlet temperature is completed, the bathtub is not affected by the heated heat medium. It is possible to reliably measure the output temperature. Therefore, the fall time can be calculated more accurately, and the energy efficiency of the bath apparatus can be further enhanced.

本発明に係る風呂装置の更なる特徴構成は、前記追焚き間隔時間変更手段が前記追焚き間隔時間を前記下降時間に調整時間幅を加算した時間へと変更する点にある。   A further characteristic configuration of the bath apparatus according to the present invention is that the chasing interval time changing means changes the chasing interval time to a time obtained by adding an adjustment time width to the descending time.

風呂装置の運転中に、例えば浴室暖房装置が運転されて浴室内の温度が上昇する場合がある。そうすると浴槽水の温度低下が抑制され、計算された下降時間が経過しても浴槽水の温度が下限温度まで低下しない場合が考えられる。上記特徴構成によれば、追焚き間隔時間変更手段が追焚き間隔時間を、湯温低下時間に基づいて算出された下降時間に調整時間幅を加算した時間へと変更するので、より適切な時間間隔にて追焚き処理を行うことができ、風呂装置のエネルギー効率をより高めることができる。   During the operation of the bath apparatus, for example, a bathroom heating apparatus may be operated to increase the temperature in the bathroom. If it does so, the temperature fall of bathtub water will be suppressed and the case where the temperature of bathtub water does not fall to a minimum temperature even if calculated fall time passes can be considered. According to the above characteristic configuration, the chasing interval time changing means changes the chasing interval time to a time obtained by adding the adjustment time width to the descending time calculated based on the hot water temperature lowering time. The chasing process can be performed at intervals, and the energy efficiency of the bath apparatus can be further increased.

本発明に係る風呂装置の更なる特徴構成は、前記追焚き間隔時間変更手段が前記追焚き間隔時間を前記下降時間に調整時間幅を減算した時間へと変更する点にある。   A further characteristic configuration of the bath apparatus according to the present invention is that the chasing interval time changing means changes the chasing interval time to a time obtained by subtracting an adjustment time width from the descending time.

風呂装置の運転中に、例えば浴室の扉の開閉や換気扇の運転などにより浴室内の温度が下降する場合がある。そうすると浴槽水の温度低下が促進され、計算された下降時間が経過した際には浴槽水の温度が下限温度を下回る可能性がある。上記特徴構成によれば、追焚き間隔時間変更手段が追焚き間隔時間を、湯温低下時間に基づいて算出された下降時間から調整時間幅を減算した時間へと変更するので、浴槽水の温度が下限温度を下回る、すなわち浴槽水が過度に冷める事態を回避でき、風呂装置の利便性・快適性を高めることができる。   During operation of the bath apparatus, the temperature in the bathroom may drop due to, for example, opening / closing of a bathroom door or operation of a ventilation fan. If it does so, the temperature fall of bathtub water will be accelerated | stimulated and when the calculated fall time passes, the temperature of bathtub water may fall below a minimum temperature. According to the above characteristic configuration, the chasing interval time changing means changes the chasing interval time to a time obtained by subtracting the adjustment time width from the descending time calculated based on the hot water temperature lowering time. Is less than the lower limit temperature, that is, the situation where the bath water cools down excessively can be avoided, and the convenience and comfort of the bath apparatus can be enhanced.

本発明に係る風呂装置の更なる特徴構成は、前記追焚き処理手段は、所定の第1熱媒温度に前記熱媒を加熱して浴槽水を追焚きする第1追焚き処理と、前記第1追焚き処理に要する時間よりも長くかつ最長追焚き時間と同じかより短い時間で追焚き処理が完了する第2熱媒温度を決定し、前記第2熱媒温度に前記熱媒を加熱して浴槽水を追焚きする第2追焚き処理とを選択的に行う点にある。   According to a further characteristic configuration of the bath device according to the present invention, the reheating processing means heats the heat medium to a predetermined first heat medium temperature to retreat the bath water, and the first reheating process. Determining a second heat medium temperature at which the chasing process is completed in a time longer than the time required for one chasing process and equal to or shorter than the longest chasing time, and heating the heat medium to the second heat medium temperature; The second pursuit process for pursuing the bath water is selectively performed.

上記特徴構成によれば、第2追焚き処理では、第1追焚き処理に要する時間よりも長い時間で追焚き処理を完了するように第2熱媒温度を決定して追焚き処理を行うため、瞬時効率が高い状態での運転期間が第1追焚き処理に比べて長くなり、総合的な熱効率が向上する。第1特徴構成により追焚き間隔時間は最適化され、追焚き処理の開始時の浴槽水温度は下限温度付近に保たれるから、第2追焚き処理を行うことで風呂装置全体のエネルギー効率をより一層高めることができる。なお最長追焚き時間は、第2追焚き処理に要する時間の上限であって、使用者の利便性を損なわない程度の時間として予め設定された時間である。   According to the above characteristic configuration, in the second tracking process, the second heating medium temperature is determined so as to complete the tracking process in a time longer than the time required for the first tracking process. The operation period in a state where the instantaneous efficiency is high is longer than that in the first tracking process, and the overall thermal efficiency is improved. The chasing interval time is optimized by the first characteristic configuration, and the bath water temperature at the start of the chasing process is kept near the lower limit temperature, so that the energy efficiency of the entire bath apparatus is improved by performing the second chasing process. It can be further increased. The longest chasing time is an upper limit of the time required for the second chasing process, and is a time set in advance as a time that does not impair the convenience of the user.

本発明に係る風呂装置の更なる特徴構成は、前記追焚き処理手段は、前記第1追焚き処理に要する時間よりも長くかつ前記最長追焚き時間と同じかより短い時間である第2追焚き時間で追焚き処理が完了する第2熱媒温度を決定するにあたり、浴槽水を追焚き完了温度に加熱するために要する必要投入熱量を前記第2追焚き時間で除算することで求められる毎時投入熱量に基づいて前記第2熱媒温度を決定する点にある。   A further characteristic configuration of the bath device according to the present invention is that the chasing processing means has a second chasing time that is longer than the time required for the first chasing process and is equal to or shorter than the longest chasing time. When determining the second heating medium temperature at which the reheating process is completed in time, the required input heat amount required for heating the bath water to the reheating completion temperature is divided by the second reheating time to be input every hour. The second heat medium temperature is determined based on the amount of heat.

上記特徴構成によれば、浴槽水を追焚き完了温度に加熱するために要する必要投入熱量
を第2追焚き時間で除算することで求められる毎時投入熱量に基づいて第2熱媒温度を決定するので、第2追焚き時間で追焚き処理がちょうど完了する熱媒の温度を精度よく求めることができる。これにより、追焚きに要する時間を利便性が損なわれない範囲に留めつつ、その時間内で追焚き処理をできるだけ長く行うことができるので、瞬時効率が高い期間を可及的に長くでき、熱効率をより高めることができる。
According to the above characteristic configuration, the second heating medium temperature is determined based on the hourly input heat amount obtained by dividing the necessary input heat amount required for heating the bath water to the replenishment completion temperature by the second replenishment time. Therefore, it is possible to accurately obtain the temperature of the heating medium that completes the chasing process in the second chasing time. As a result, the chasing process can be performed as long as possible while keeping the time required for chasing within a range that does not impair the convenience. Can be further enhanced.

本発明に係る風呂装置の更なる特徴構成は、前記追焚き処理手段は、前記第1熱媒温度よりも低い第3熱媒温度に熱媒を加熱して浴槽水を追焚きした場合に追焚き処理に要する時間を算出し、当該時間が前記最長追焚き時間と同じかより短い場合は前記第3熱媒温度を前記第2熱媒温度に決定して前記第2追焚き処理を行い、当該時間が前記最長追焚き時間より長い場合は、前記最長追焚き時間で追焚き処理が完了する熱媒の温度を前記第2熱媒温度に決定して前記第2追焚き処理を行う点にある。   A further characteristic configuration of the bath apparatus according to the present invention is that the replenishing processing means reheats the bath water by heating the heat medium to a third heat medium temperature lower than the first heat medium temperature. Calculate the time required for the soaking process, and if the time is equal to or shorter than the longest chasing time, determine the third heating medium temperature as the second heating medium temperature and perform the second chasing process, If the time is longer than the longest tracking time, the temperature of the heat medium that completes the tracking process in the longest tracking time is determined as the second heating medium temperature and the second tracking process is performed. is there.

追焚き処理に要する時間は、浴槽に貯留された浴槽水の温度と総量により変動する。よって、第1熱媒温度よりも低い温度に予め設定された第3熱媒温度で第2追焚き処理を行う際、追焚きに要する時間が非常に長くなる場合がある。そうすると、湯張りの後に設定湯張り温度への追焚きを行う自動湯張り運転や、その後の保温運転において、設定湯張り温度に到達するのに長い時間を要することとなり、使用者の利便性を損なう恐れがある。
上記特徴構成によれば、第3熱媒温度での追焚き処理に要する時間を算出し、当該時間が最長追焚き時間と同じかより短い場合は第3熱媒温度を第2熱媒温度に決定して第2追焚き処理を行い、当該時間が最長追焚き時間より長い場合は、最長追焚き時間で追焚き処理が完了する熱媒の温度を第2熱媒温度に決定して第2追焚き処理を行うので、追焚き処理に要する時間が最長追焚き時間より長くなることがなく、使用者の利便性を損なう事態の発生を抑制できる。
The time required for the chasing process varies depending on the temperature and total amount of bathtub water stored in the bathtub. Therefore, when the second tracking process is performed at the third heating medium temperature preset to a temperature lower than the first heating medium temperature, the time required for tracking may become very long. In that case, it takes a long time to reach the set hot water temperature in the automatic hot water operation in which the hot water is refilled to the set hot water temperature after the hot water is charged, and in the subsequent heat insulation operation. There is a risk of damage.
According to the above characteristic configuration, the time required for the follow-up process at the third heat medium temperature is calculated, and when the time is equal to or shorter than the longest follow-up time, the third heat medium temperature is set to the second heat medium temperature. When the second chasing process is performed and the time is longer than the longest chasing time, the temperature of the heat medium for which the chasing process is completed in the longest chasing time is determined as the second heating medium temperature. Since the chasing process is performed, the time required for the chasing process does not become longer than the longest chasing time, and the occurrence of a situation that impairs the convenience of the user can be suppressed.

本発明の風呂装置の概略構成図Schematic configuration diagram of the bath apparatus of the present invention 本発明に係る風呂装置の制御を示す説明図Explanatory drawing which shows control of the bath apparatus which concerns on this invention 本発明に係る保温運転の状態を示す説明図Explanatory drawing which shows the state of the heat insulation driving | operation which concerns on this invention 本発明に係る風呂装置の運転状態を示す説明図(第1追焚き処理)Explanatory drawing which shows the driving | running state of the bath apparatus which concerns on this invention (1st chasing process) 本発明に係る風呂装置の運転状態を示す説明図(第2追焚き処理)Explanatory drawing which shows the driving | running state of the bath apparatus which concerns on this invention (2nd chasing process)

本発明は、所謂、間接加熱方式の風呂装置において、特に、保温運転における追焚きの間隔を最適化することにより、風呂装置全体のエネルギー効率を改善することが可能な風呂装置に関する。以下、本発明に係る風呂装置の実施形態を図面に基づいて説明する。
風呂装置100は、暖房端末HU、LUに熱を供給すると共に浴槽10および給湯栓33に温度調整した湯水を供給すべく、熱媒および湯水を加熱・供給可能な熱源機Gと、当該熱源機Gの運転を制御する運転制御部Cと、その運転制御部Cに各種運転指令を発するメインリモコンR1および浴室リモコンR2とを備えて構成されている。
ちなみに、メインリモコンR1は炊事場の近傍に設置され、浴室リモコンR2は浴槽10が設置された浴室内に設けられている。
The present invention relates to a so-called indirect heating type bath apparatus, and more particularly, to a bath apparatus capable of improving the energy efficiency of the entire bath apparatus by optimizing the reheating interval in the heat insulation operation. Hereinafter, embodiments of a bath apparatus according to the present invention will be described with reference to the drawings.
The bath apparatus 100 is configured to supply heat to the heating terminals HU and LU and supply hot water with temperature adjusted to the bathtub 10 and the hot water tap 33, and a heat source G that can heat and supply the heat medium and hot water, and the heat source An operation controller C that controls the operation of G, and a main remote controller R1 and a bathroom remote controller R2 that issue various operation commands to the operation controller C are configured.
Incidentally, the main remote controller R1 is installed in the vicinity of the kitchen, and the bathroom remote controller R2 is provided in the bathroom where the bathtub 10 is installed.

〔熱源機に係る構成〕
図1に示すように、熱源機Gは、ケーシング51により外囲されるものであり、一般家庭用の水道管に接続された給水路L2からの水をガス燃焼式の給湯用バーナg1により加熱して、加熱後の湯水を給湯栓33や浴槽10へ供給する給湯用加熱部H1と、高温暖房端末HUおよび低温暖房端末LUへ循環供給する熱媒や浴槽10の内部に貯留される浴槽水を追焚きする熱媒をガス燃焼式の熱媒加熱用バーナg2により加熱する熱媒加熱部H2とを備えて構成されている。ちなみに、高温暖房端末HUとしては浴室暖房乾燥機が、低温暖房端末LUとしては床暖房装置が設けられている。
[Configuration related to heat source equipment]
As shown in FIG. 1, the heat source machine G is surrounded by a casing 51, and heats water from a water supply path L2 connected to a general household water pipe by a gas combustion type hot water supply burner g1. Then, a hot water supply heating unit H1 that supplies hot water after heating to the hot water tap 33 and the bathtub 10, a heat medium that circulates and supplies the hot water to the high temperature heating terminal HU and the low temperature heating terminal LU, and bathtub water stored in the bathtub 10 And a heating medium heating section H2 that heats the heating medium with a gas combustion type heating medium heating burner g2. Incidentally, a bathroom heating dryer is provided as the high temperature heating terminal HU, and a floor heating device is provided as the low temperature heating terminal LU.

図1に示すように、給湯用加熱部H1に備えられる給湯用バーナg1には、一般家庭用の燃料ガス(例えば、都市ガス13A)を供給する第1ガス供給路21aが接続されており、熱媒加熱部H2に備えられる熱媒加熱用バーナg2にも、燃料ガスを供給する第2ガス供給路21bが接続されている。第1ガス供給路21aおよび第2ガス供給路21bの夫々には、燃料ガスの供給を断続する開閉弁V1、V3と、燃料ガス供給量を調整する電磁式のガス比例弁V2、V4が夫々設けられている。また、給湯用加熱部H1および熱媒加熱部H2には、給湯用バーナg1および熱媒加熱用バーナg2の夫々に、燃焼用空気を供給する燃焼用ファン12a、12bが設けられている。
なお図示は省略するが、給湯用バーナg1および熱媒加熱用バーナg2の近傍には、点火用のイグナイタおよび着火を検出するフレームロッドが設けられている。
As shown in FIG. 1, a hot water supply burner g1 provided in the hot water supply heating unit H1 is connected to a first gas supply path 21a for supplying general household fuel gas (for example, city gas 13A), A second gas supply path 21b for supplying fuel gas is also connected to the heat medium heating burner g2 provided in the heat medium heating part H2. In each of the first gas supply path 21a and the second gas supply path 21b, there are open / close valves V1 and V3 for intermittently supplying the fuel gas, and electromagnetic gas proportional valves V2 and V4 for adjusting the fuel gas supply amount, respectively. Is provided. The hot water supply heating section H1 and the heat medium heating section H2 are provided with combustion fans 12a and 12b for supplying combustion air to the hot water supply burner g1 and the heat medium heating burner g2, respectively.
Although illustration is omitted, an ignition igniter and a flame rod for detecting ignition are provided in the vicinity of the hot water supply burner g1 and the heating medium heating burner g2.

給湯用加熱部H1および熱媒加熱部H2には、バーナg1、g2の燃焼排ガスの顕熱を主に回収する主熱交換器EX1、EX3と、潜熱を主に回収する副熱交換器EX2、EX4とを備えて構成されている。ここで、主熱交換器EX1、EX3と副熱交換器EX2、EX4とは、給湯用バーナg1および熱媒加熱用バーナg2から排気路22へ向かう燃焼排ガスの流動方向において、副熱交換器EX2、EX4が主熱交換器EX1、EX3よりも下流側に位置する状態で配設されている。なお、本発明にあっては、熱媒加熱部H2に設けられる主熱交換器EX3と副熱交換器EX4とが第1熱交換器として機能する。
これにより、給湯用加熱部H1においては、湯水が、副熱交換器EX2にて主として給湯用バーナg1の燃焼排ガスの潜熱により加熱された後、主熱交換器EX1にて主として給湯用バーナg1の燃焼排ガスの顕熱により加熱される。また、熱媒加熱部H2においては、熱媒が、副熱交換器EX4にて主として熱媒加熱用バーナg2の燃焼排ガスの潜熱により加熱された後、主熱交換器EX3にて主として熱媒加熱用バーナg2の燃焼排ガスの顕熱により加熱される。
The hot water supply heating unit H1 and the heating medium heating unit H2 include main heat exchangers EX1 and EX3 that mainly recover sensible heat of the combustion exhaust gas of the burners g1 and g2, and auxiliary heat exchangers EX2 that mainly recover latent heat. EX4. Here, the main heat exchangers EX1 and EX3 and the auxiliary heat exchangers EX2 and EX4 are the auxiliary heat exchanger EX2 in the flow direction of the combustion exhaust gas from the hot water supply burner g1 and the heating medium heating burner g2 to the exhaust passage 22. , EX4 is disposed in a state of being located downstream of the main heat exchangers EX1, EX3. In the present invention, the main heat exchanger EX3 and the auxiliary heat exchanger EX4 provided in the heat medium heating unit H2 function as a first heat exchanger.
Thus, in the hot water supply heating section H1, hot water is heated mainly by the latent heat of the combustion exhaust gas of the hot water supply burner g1 in the auxiliary heat exchanger EX2, and then mainly in the hot water supply burner g1 in the main heat exchanger EX1. Heated by sensible heat of combustion exhaust gas. In the heat medium heating section H2, the heat medium is heated mainly by the latent heat of the combustion exhaust gas of the heat medium heating burner g2 in the sub heat exchanger EX4, and then mainly heated in the main heat exchanger EX3. It is heated by the sensible heat of the combustion exhaust gas of the burner g2.

給湯用加熱部H1の副熱交換器EX2および熱媒加熱部H2の副熱交換器EX4からは、燃焼生成水である酸性の凝縮水、即ち、ドレンが生成するが、当該ドレンはドレンパン23に集められ中和器24にて中和された後、ドレンタンク25に貯留されるように構成されている。ドレンタンク25には、ドレンの貯留量が上限貯留量以上であることを検出するドレンセンサS1が設けられおり、当該ドレンセンサS1にてドレンの貯留量が上限貯留量以上であることが検出されると、ドレン排水ポンプP3が作動し、ドレンタンク25に貯留されているドレンが、排水管L1を介して、浴室の床面に設けられた排水口13から外部に排出されるように構成されている。ちなみに、排水管L1のうち熱源機Gの外部(ケーシング51の外側)に位置する部分は、後述する浴槽戻り路L7のうち、熱源機Gの外側に配設される浴槽戻り外管L7bの内部に配設されている。   From the auxiliary heat exchanger EX2 of the hot water supply heating section H1 and the auxiliary heat exchanger EX4 of the heating medium heating section H2, acidic condensed water that is combustion generated water, that is, drain, is generated, but the drain is supplied to the drain pan 23. The collected water is neutralized by the neutralizer 24 and then stored in the drain tank 25. The drain tank 25 is provided with a drain sensor S1 for detecting that the drain storage amount is equal to or higher than the upper limit storage amount, and the drain sensor S1 detects that the drain storage amount is equal to or higher than the upper limit storage amount. Then, the drain drain pump P3 is activated, and the drain stored in the drain tank 25 is configured to be discharged to the outside through the drain pipe L1 through the drain port 13 provided on the floor surface of the bathroom. ing. Incidentally, the portion of the drain pipe L1 located outside the heat source machine G (outside of the casing 51) is the inside of the bathtub return outer pipe L7b disposed outside the heat source machine G in the bathtub return path L7 described later. It is arranged.

〔給湯に係る構成〕
給水路L2が、給湯用加熱部H1の副熱交換器EX2の入口に接続されている。一端に給湯栓33を有する給湯路L4の他端が、給湯用加熱部H1における主熱交換器EX1の出口に接続されている。これにより、給水路L2から供給される湯水は、副熱交換器EX2および主熱交換器EX1にて順に加熱された後、給湯路L4を介して給湯栓33から供給される。
[Configuration related to hot water supply]
The water supply path L2 is connected to the inlet of the auxiliary heat exchanger EX2 of the hot water supply heating unit H1. The other end of the hot water supply passage L4 having the hot water tap 33 at one end is connected to the outlet of the main heat exchanger EX1 in the hot water supply heating section H1. Thereby, the hot water supplied from the water supply path L2 is sequentially heated by the sub heat exchanger EX2 and the main heat exchanger EX1, and then supplied from the hot water tap 33 via the hot water supply path L4.

給水路L2には、給水温度を検出する給水サーミスタS7と給水流量を検出する流量センサS8とが設けられている。給水路L2における給水サーミスタS7および流量センサS8よりも下流側の箇所が、主熱交換器EX1および副熱交換器EX2を迂回する給水バイパス路L3にて、給湯路L4に接続されている。
給湯路L4には、給水バイパス路L3の接続箇所よりも上流側に、主熱交換器EX1からの湯水温度を検出する出湯サーミスタS4が設けられている。給湯路L4における給水バイパス路L3の接続箇所よりも下流側には、上流側から順に、給湯としての湯水温度を検出する給湯サーミスタS6、湯水流量を調整可能な比例弁V9、一般給湯の割り込みを検出する割り込み検出用水量センサS9が設けられている。
また、給湯路L4と給水バイパス路L3との接続箇所には、主熱交換器EX1からの湯水と給水バイパス路L3からの湯水との混合比を調整可能なミキシング弁V11が設けられている。
以上より、各サーミスタおよび流量センサの出力に基づいて、給水バイパス路L3を通流する流量が調整される形態で、給湯温度がメインリモコンR1にて設定される目標給湯温度に調整され、給湯栓33から給湯される。
The water supply path L2 is provided with a water supply thermistor S7 for detecting the water supply temperature and a flow rate sensor S8 for detecting the water supply flow rate. A location downstream of the water supply thermistor S7 and the flow rate sensor S8 in the water supply channel L2 is connected to the hot water supply channel L4 through a water supply bypass channel L3 that bypasses the main heat exchanger EX1 and the auxiliary heat exchanger EX2.
The hot water supply passage L4 is provided with a hot water thermistor S4 that detects the temperature of the hot water from the main heat exchanger EX1 upstream of the connection location of the water supply bypass passage L3. The hot water supply thermistor S6 that detects the temperature of hot water as hot water supply, the proportional valve V9 that can adjust the hot water flow rate, and the interruption of general hot water supply are provided downstream from the connection point of the water supply bypass L3 in the hot water supply line L4. An interrupt detection water amount sensor S9 for detection is provided.
In addition, a mixing valve V11 capable of adjusting the mixing ratio of the hot water from the main heat exchanger EX1 and the hot water from the water supply bypass L3 is provided at a connection point between the hot water supply path L4 and the water supply bypass L3.
As described above, the hot water temperature is adjusted to the target hot water temperature set by the main remote controller R1 in such a manner that the flow rate flowing through the feed water bypass passage L3 is adjusted based on the outputs of each thermistor and flow sensor, and the hot water tap Hot water is supplied from 33.

〔熱媒循環に係る構成〕
熱媒循環回路は、熱媒加熱部H2の主熱交換器EX3の出口から流出した熱媒を、熱媒と浴槽水とを熱交換する追焚き熱交換器EX5(第2熱交換器の一例)に通過させ熱媒加熱部H2の副熱交換器EX4の入口へ戻す追焚き回路C1と、熱媒加熱部H2の主熱交換器EX3の出口から流出した熱媒を高温暖房端末HUを通過させ熱媒加熱部H2の副熱交換器EX4の入口へ戻す高温暖房回路C2と、熱媒加熱部H2の主熱交換器EX3の出口から流出した熱媒を追焚き熱交換器EX5と高温暖房端末HUとをバイパス状態で熱媒加熱部H2の副熱交換器EX4の出口へ導く熱媒バイパス路L9と、熱媒加熱部H2の主熱交換器EX3の出口から流出した熱媒を熱媒バイパス路L9を介して低温暖房端末LUを通過させ熱媒加熱部H2の副熱交換器EX4の入口へ戻す低温暖房回路C3とを備えている。ここで、追焚き回路C1は、熱媒加熱部H2の主熱交換器EX3の出口から追焚き熱交換器EX5までに配設される追焚き往き路L11と、追焚き熱交換器EX5から熱媒加熱部H2の副熱交換器EX4の入口までに配設される追焚き戻り路L10とを備えている。
[Configuration related to heat medium circulation]
The heat medium circulation circuit is a reheating heat exchanger EX5 (an example of a second heat exchanger) that exchanges heat between the heat medium flowing out from the outlet of the main heat exchanger EX3 of the heat medium heating unit H2 and the bath water. ) And the heating medium C1 returning to the inlet of the auxiliary heat exchanger EX4 of the heating medium heating unit H2 and the heating medium flowing out from the outlet of the main heat exchanger EX3 of the heating medium heating unit H2 pass through the high temperature heating terminal HU. The high-temperature heating circuit C2 for returning to the inlet of the auxiliary heat exchanger EX4 of the heat medium heating unit H2, and the heat exchanger EX5 and the high-temperature heating for tracking the heat medium flowing out from the outlet of the main heat exchanger EX3 of the heat medium heating unit H2. The heat medium bypass path L9 that leads the terminal HU to the outlet of the auxiliary heat exchanger EX4 of the heat medium heating unit H2 in a bypass state and the heat medium that flows out from the outlet of the main heat exchanger EX3 of the heat medium heating unit H2 The auxiliary heat of the heating medium heating unit H2 through the low temperature heating terminal LU through the bypass L9 Back to the inlet of the exchanger EX4 and a low-temperature heating circuit C3. Here, the reheating circuit C1 includes a retreating path L11 disposed from the outlet of the main heat exchanger EX3 of the heat medium heating unit H2 to the reheating heat exchanger EX5, and heat from the reheating heat exchanger EX5. And a reheating return path L10 disposed up to the inlet of the auxiliary heat exchanger EX4 of the medium heating unit H2.

熱媒バイパス路L9には、熱媒のバイパス流量を調整自在なバイパス用熱動弁V12が設けられ、追焚き回路C1の追焚き往き路L11には、追焚き熱交換器EX5を通過する熱媒流量を調整可能な追焚き用熱動弁V8が設けられ、高温暖房回路C2には、高温暖房端末HUを通過する熱媒流量を調整可能な高温暖房用熱動弁V10が設けられ、低温暖房回路C3には、低温暖房端末LUを通過する熱媒流量を調整可能な低温暖房用熱動弁V13が設けられている。
また、熱媒加熱部H2の副熱交換器EX4の出口と主熱交換器EX3の入口との間には、熱媒を副熱交換器EX4から主熱交換器EX3の側へ圧送する熱媒循環ポンプP2が設けられている。
さらに、熱媒加熱部H2の主熱交換器EX3の出口には、当該出口から流出する湯水温度を検出する熱媒サーミスタS3が設けられると共に、図示は省略するが低温暖房端末LUおよび高温暖房端末HUの内部には、自身を通過した熱媒の温度を検出する高温暖房サーミスタおよび低温暖房サーミスタが夫々備えられている。
なお、熱媒加熱部H2の副熱交換器EX4への入口には、熱媒の膨張を吸収可能な膨張タンク50が設けられている。
The heat medium bypass passage L9 is provided with a bypass thermal valve V12 capable of adjusting the bypass flow rate of the heat medium, and the heat passing through the heat exchanger EX5 is provided in the heat-up path L11 of the heat-up circuit C1. A heating thermal valve V8 capable of adjusting the medium flow rate is provided, and the high temperature heating circuit C2 is provided with a high temperature heating thermal valve V10 capable of adjusting the flow rate of the heat medium passing through the high temperature heating terminal HU. The heating circuit C3 is provided with a low temperature heating thermal valve V13 capable of adjusting the flow rate of the heat medium passing through the low temperature heating terminal LU.
Further, between the outlet of the auxiliary heat exchanger EX4 and the inlet of the main heat exchanger EX3 of the heating medium heating unit H2, the heating medium that pressure-feeds the heating medium from the auxiliary heat exchanger EX4 to the main heat exchanger EX3 side. A circulation pump P2 is provided.
Further, at the outlet of the main heat exchanger EX3 of the heating medium heating unit H2, a heating medium thermistor S3 for detecting the temperature of hot water flowing out from the outlet is provided, and although not shown, the low temperature heating terminal LU and the high temperature heating terminal are omitted. Inside the HU, a high temperature heating thermistor and a low temperature heating thermistor that detect the temperature of the heat medium that has passed through the HU are provided.
An expansion tank 50 capable of absorbing the expansion of the heat medium is provided at the inlet of the heat medium heating unit H2 to the sub heat exchanger EX4.

〔追焚きに係る構成〕
追焚き熱交換器EX5の湯水出口と浴槽10の側壁部下方側に装着された循環アダプタ11とが、浴槽往き路L8にて接続され、循環アダプタ11と追焚き熱交換器EX5の湯水入口とが、浴槽戻り路L7にて接続され、その浴槽戻り路L7に、浴槽10の湯水を吸引して追焚き熱交換器EX5へ送出する浴槽水循環ポンプP1が設けられている。
説明を追加すると、浴槽往き路L8が、熱源機Gの内部に位置する浴槽往き内管L8aと、熱源機Gから外部へ延出されて循環アダプタ11の往き用接続部11aに接続される浴槽往き外管L8bとから構成されている。また、浴槽戻り路L7が、熱源機Gの内部に位置する浴槽戻り内管L7aと、熱源機Gから外部へ延出されて、循環アダプタ11の戻り用接続部11bに接続される浴槽戻り外管L7bとから構成されている。そして、浴槽戻り路L7と浴槽往き路L8とで本発明の浴槽水循環回路を構成する。
[Composition related to pursuit]
The hot water outlet of the reheating heat exchanger EX5 and the circulation adapter 11 mounted on the lower side of the side wall of the bathtub 10 are connected by a bathtub going-out path L8, and the recirculation adapter 11 and the hot water inlet of the reheating heat exchanger EX5 are connected to each other. However, the bathtub return circulation path L7 is connected, and the bathtub return circulation path L7 is provided with a bathtub water circulation pump P1 that sucks hot water from the bathtub 10 and sends it to the reheating heat exchanger EX5.
If description is added, the bathtub going out path L8 will be extended from the heat source machine G to the outside by the bathtub going inner pipe L8a located in the inside of the heat source machine G, and the bathtub connected to the outgoing connection part 11a of the circulation adapter 11 It consists of a forward outer tube L8b. Further, the bathtub return path L7 extends outside the bathtub return inner pipe L7a located inside the heat source machine G and the heat source machine G and is connected to the return connection portion 11b of the circulation adapter 11 outside the bathtub return Tube L7b. And the bathtub water circulation circuit of this invention is comprised with the bathtub return path L7 and the bathtub going-out path L8.

浴槽戻り路L7には、上流側から順に、浴槽戻り路L7の内部の湯水の圧力を検出することによって浴槽10内の水位を検出する水位センサS10、浴槽10から戻る浴槽水の温度を検出する浴槽戻りサーミスタS2、浴槽戻り路L7を開閉する電磁式の開閉弁V7、上述した浴槽水循環ポンプP1、および水流スイッチ41が設けられている。
また、浴槽往き路L8には、浴槽10に供給される湯水の温度を検出する浴槽往きサーミスタS5が設けられている。
In the bathtub return path L7, in order from the upstream side, a water level sensor S10 that detects the water level in the bathtub 10 by detecting the pressure of hot water in the bathtub return path L7, and the temperature of the bathtub water returning from the bathtub 10 are detected. The bathtub return thermistor S2, the electromagnetic on-off valve V7 for opening and closing the bathtub return path L7, the bathtub water circulation pump P1 described above, and the water flow switch 41 are provided.
Further, a bathtub going thermistor S5 for detecting the temperature of hot water supplied to the bathtub 10 is provided in the bathtub going way L8.

〔湯張りに係る構成〕
給湯路L4における比例弁V9と割り込み検出用水量センサS9との間の箇所から、給湯路L4からの湯水を浴槽10へ供給するための湯張り路L5が分岐されて、その湯張り路L5が、浴槽戻り路L7における浴槽水循環ポンプP1と水流スイッチ41との間に接続されている。当該湯張り路L5には、上流側から順に、湯張り路L5を開閉する電磁式の開閉弁V5と、湯張り路L5に連通する空気層形成用ホッパ40と、逆止弁42とが設けられている。
空気層形成用ホッパ40には、湯水を排水する排水路L6と、当該排水路L6を開閉する電磁式の排水弁V6とが設けられ、排水路L6の下流側端部が浴槽戻り路L7における開閉弁V7と浴槽水循環ポンプP1との間に接続されている。
従って、開閉弁V5を開弁すると、給湯用加熱部H1にて加熱され湯張り路L5を介して供給される湯水が、浴槽戻り路L7に供給され、浴槽戻り路L7に供給された湯水が浴槽10側と追焚き熱交換器EX5側の両側に向けて分流する形態で供給されることになる。即ち、湯張り路L5を介して供給される湯水は、浴槽往き路L8および浴槽戻り路L7の両方を介して浴槽10に供給される。
[Configuration related to hot water filling]
A hot water supply passage L5 for supplying hot water from the hot water supply passage L4 to the bathtub 10 is branched from a location between the proportional valve V9 and the interrupt detection water amount sensor S9 in the hot water supply passage L4. The bathtub water circulation pump P1 and the water flow switch 41 are connected in the bathtub return path L7. The hot water filling passage L5 is provided with an electromagnetic on-off valve V5 for opening and closing the hot water filling passage L5, an air layer forming hopper 40 communicating with the hot water filling passage L5, and a check valve 42 in order from the upstream side. It has been.
The air layer forming hopper 40 is provided with a drainage channel L6 for draining hot water and an electromagnetic drain valve V6 for opening and closing the drainage channel L6, and the downstream end of the drainage channel L6 is located in the bathtub return channel L7. It is connected between the on-off valve V7 and the bathtub water circulation pump P1.
Therefore, when the on-off valve V5 is opened, the hot water heated by the hot water supply heating unit H1 and supplied via the hot water supply passage L5 is supplied to the bathtub return passage L7, and the hot water supplied to the bathtub return passage L7 is supplied. It will be supplied in a form of diverting toward both sides of the bathtub 10 side and the follow-up heat exchanger EX5 side. That is, the hot water supplied through the hot water supply path L5 is supplied to the bathtub 10 through both the bathtub going-out path L8 and the bathtub return path L7.

〔熱源機の運転制御〕
熱源機Gは、上述した機器類を装備するものであって、上述の説明から明らかなように、加熱した湯水を給湯栓33に供給する給湯処理、加熱した湯水を浴槽10へ供給する湯張り処理、加熱した熱媒を暖房端末HU、LUへ循環供給する端末加熱処理、および浴槽10内の浴槽水を加熱する追焚き処理、並びにドレン排水処理を行うように構成されている。
[Operation control of heat source machine]
The heat source machine G is equipped with the above-described devices, and as is clear from the above description, a hot water supply process for supplying heated hot water to the hot water tap 33 and a hot water supply for supplying heated hot water to the bathtub 10. The terminal heating process which circulates the process, the heated heat medium to the heating terminals HU and LU, the reheating process for heating the bathtub water in the bathtub 10, and the drain drainage process are performed.

即ち、運転制御部Cが、後述する如く、メインリモコンR1や浴室リモコンR2からの指令情報、およびケーシング51の内部に装備したセンサ類の検出情報に基づいて、ケーシング51の内部に装備した機器類を作動させて、給湯処理による給湯運転、湯張り処理等による自動湯張り運転、自動湯張り運転に続いて行う保温運転、浴槽10に追加で湯張り給湯する足し湯運転、端末加熱処理による高温暖房運転・低温暖房運転、および追焚き処理による手動追焚き運転、並びに、ドレン排水処理によるドレン排水運転を実行するように構成されている。   In other words, as will be described later, the operation controller C installs equipment installed in the casing 51 based on command information from the main remote controller R1 and bathroom remote controller R2 and detection information of sensors installed in the casing 51. Hot water supply operation by hot water supply processing, automatic hot water filling operation by hot water filling processing, etc., heat insulation operation following the automatic hot water filling operation, additional hot water operation to add hot water to the bathtub 10 and high temperature by terminal heating treatment It is configured to execute a heating operation / low temperature heating operation, a manual reheating operation by a reheating process, and a drain draining operation by a drain draining process.

〔リモコンに係る構成〕
メインリモコンR1および浴室リモコンR2は、同様に構成されるものであり、以下、メインリモコンR1を代表にして説明する。
図1に示すように、メインリモコンR1には、運転の開始と停止を指令する運転スイッチSw1、自動湯張り運転指令を指令する風呂自動スイッチSw2、給湯温度を設定する給湯温度設定スイッチSw3、設定湯張り温度としての目標湯張り温度を設定する浴槽温度設定スイッチSw4、浴槽10の浴槽水の目標水位を設定する水位設定スイッチSw5、浴槽10に追加で湯張り給湯する足し湯スイッチSw6、手動追焚き運転を指令する追焚きスイッチSw7、設定温度等の各種情報を表示する表示部81、暖房端末HU、LUの運転の開始を指令する暖房運転スイッチSw8、および湯張りが終了したこと等を報知する報知装置82等が設けられている。メインリモコンR1は、運転制御部Cに接続され、上述の指令を運転制御部Cへ送信する。
[Configuration related to remote control]
The main remote controller R1 and the bathroom remote controller R2 are configured similarly, and will be described below with the main remote controller R1 as a representative.
As shown in FIG. 1, the main remote controller R1 has an operation switch Sw1 for instructing start and stop of operation, a bath automatic switch Sw2 for instructing an automatic hot water operation command, a hot water supply temperature setting switch Sw3 for setting a hot water supply temperature, and a setting. Bathtub temperature setting switch Sw4 for setting the target hot water temperature as the hot water temperature, water level setting switch Sw5 for setting the target water level of the bathtub water in the bathtub 10, additional hot water switch Sw6 for supplying hot water to the bathtub 10 in addition, manual addition Reminder switch Sw7 for commanding fired operation, display unit 81 for displaying various information such as set temperature, heating operation switch Sw8 for commanding start of operation of heating terminal HU, LU, and notification of completion of hot water filling, etc. A notification device 82 or the like is provided. The main remote controller R1 is connected to the operation control unit C and transmits the above-described command to the operation control unit C.

〔温度センサに係る構成〕
外気温度サーミスタS11は、熱源機Gに設けられ運転制御部Cに接続されている。外気温度サーミスタS11は、風呂装置100が設けられる住宅等の外気温度を検出して、運転制御部Cへ送信する。
浴室温度サーミスタS12は、浴室リモコンR2に設けられ運転制御部Cに接続されている。浴室温度サーミスタS12は、浴室の室温を検出して、運転制御部Cへ送信する。
[Configuration related to temperature sensor]
The outside air temperature thermistor S11 is provided in the heat source unit G and connected to the operation control unit C. The outside air temperature thermistor S11 detects the outside air temperature of a house or the like where the bath apparatus 100 is provided, and transmits it to the operation control unit C.
The bathroom temperature thermistor S12 is provided in the bathroom remote controller R2 and connected to the operation control unit C. The bathroom temperature thermistor S12 detects the room temperature of the bathroom and transmits it to the operation control unit C.

〔運転制御の詳細〕
運転制御部Cは、運転スイッチSw1が操作されると制御可能な状態になり、給湯栓33が開操作されると給湯栓33から湯水を給湯する給湯運転を実行する。
また、運転制御部Cは、風呂自動スイッチSw2がオン操作されて湯張り運転指令が指令されると、浴槽10内に湯を供給して設定湯張り温度の湯張りを完了する自動湯張り運転を実行するように構成されている。
[Details of operation control]
The operation control unit C enters a controllable state when the operation switch Sw1 is operated, and executes a hot water supply operation in which hot water is supplied from the hot water tap 33 when the hot water tap 33 is opened.
Further, when the bath automatic switch Sw2 is turned on and a hot water filling operation command is issued, the operation control unit C supplies hot water into the bathtub 10 to complete the hot water filling at the set hot water temperature. Is configured to run.

つまり運転制御部Cは、湯張り運転指令が指令されると、浴槽10の浴槽水の温度が目標湯張り温度になり且つ浴槽10の浴槽水の水位が目標水位になるように湯張り処理を行う、自動湯張り運転を実行するように構成されている。   That is, when the hot water filling operation command is instructed, the operation control unit C performs the hot water filling process so that the temperature of the bathtub water in the bathtub 10 becomes the target hot water temperature and the water level of the bathtub water in the bathtub 10 becomes the target water level. It is configured to perform automatic filling operation.

また運転制御部Cは、自動湯張り運転を終了した後、風呂自動スイッチSw2のオフにより湯張り運転指令が解除されるまでの間は、浴槽10内の浴槽水の温度が設定湯張り温度になり且つ浴槽10内の浴槽水の水位が目標水位になる湯張り状態を維持する保温運転を実行するように構成されている。   In addition, after the automatic filling operation is finished, the operation control unit C keeps the temperature of the bathtub water in the bathtub 10 at the set filling temperature until the hot water filling operation command is canceled by turning off the bath automatic switch Sw2. It is comprised so that it may become and the temperature of the bathtub water in the bathtub 10 may maintain the hot water filling state which becomes a target water level.

また運転制御部Cは、保温運転の実行中に追焚きスイッチSw7が操作されて追焚き運転指令が指令された場合や、風呂自動スイッチSw2のオフ操作により湯張り運転指令が解除され、すなわち保温運転を停止した状態において、追焚きスイッチSw7が操作されて追焚き運転指令が指令された場合には、追焚き運転を実行し、また、足し湯スイッチSw6が操作されると足し湯運転を実行するように構成されている。   Further, the operation control unit C cancels the hot water operation command when the reheating switch Sw7 is operated and the reheating operation command is instructed during the heat insulation operation or when the bath automatic switch Sw2 is turned off. In the state where the operation is stopped, when the reheating switch Sw7 is operated and a reheating operation command is instructed, the renewal operation is executed, and when the additional hot water switch Sw6 is operated, the additional hot water operation is executed. Is configured to do.

以下、自動湯張り運転、保温運転および追焚き運転について説明を加える。まず、これらの運転に先立って行われる判定処理について説明する。   In the following, explanation will be given on the automatic hot water filling operation, the heat insulation operation and the chasing operation. First, the determination process performed prior to these operations will be described.

〔判定処理〕
運転制御部Cは、自動湯張り運転、保温運転、および追焚き運転を実行する際に、次に述べる判定処理を実行して、水流スイッチ41のオンオフ情報および水位センサS10の検出水位に基づく浴槽10内の浴槽水の水位の確定や、浴槽戻りサ−ミスタS2の検出温度に基づく浴槽10内の浴槽水の温度の確定を行うように構成されている。
〔Determination process〕
The operation control unit C performs a determination process described below when executing the automatic filling operation, the heat insulation operation, and the reheating operation, and the bathtub based on the on / off information of the water flow switch 41 and the detected water level of the water level sensor S10. The water level in the bathtub 10 is determined and the temperature of the bathtub water in the bathtub 10 is determined based on the temperature detected by the bathtub return thermistor S2.

すなわち、運転制御部Cは、判定処理では、循環判定用設定時間の間、浴槽水循環ポンプP1を作動させて、その浴槽水循環ポンプP1の作動中において、水流スイッチ41や浴槽戻りサ−ミスタS2の検出情報を読み込み、水流スイッチ41が水流を検出することを条件として、浴槽水循環ポンプP1を停止させた後、待機用設定時間が経過すると、水位センサS10の検出情報を読み込むように構成されている。   That is, in the determination process, the operation control unit C operates the bathtub water circulation pump P1 during the circulation determination set time, and the water flow switch 41 and the bathtub return thermistor S2 operate during the operation of the bathtub water circulation pump P1. After the detection information is read and the water flow switch 41 detects the water flow, the detection information of the water level sensor S10 is read when the set time for standby elapses after the bathtub water circulation pump P1 is stopped. .

〔自動湯張り運転(湯張り処理、追焚き処理)〕
運転制御部Cは、風呂自動スイッチSw2がオン操作されると上述の判定処理を行い、判定処理にて確定した浴槽10の湯水の水位が目標水位よりも低いときに、自動湯張り運転を実行するように構成されている。
自動湯張り運転では、運転制御部Cは、浴槽10に湯を供給する湯張り処理と上述の判定処理を順に実行し、水位センサS10の検出水位が目標水位以上になると湯張り処理を停止して、浴槽水の温度が目標湯張り温度になるように追焚きする追焚き処理を実行した後、自動湯張り運転を終了する。
[Automatic hot water filling operation (hot water filling process, chasing process)]
When the bath automatic switch Sw2 is turned on, the operation control unit C performs the above-described determination process, and executes the automatic hot water filling operation when the hot water level in the bathtub 10 determined in the determination process is lower than the target water level. Is configured to do.
In the automatic filling operation, the operation control unit C sequentially executes the filling process for supplying hot water to the bathtub 10 and the above-described determination process, and stops the filling process when the detected water level of the water level sensor S10 is equal to or higher than the target water level. Then, after performing a reheating process for reheating so that the temperature of the bath water becomes the target hot water temperature, the automatic hot water operation is terminated.

(湯張り処理)
運転制御部Cは、湯張り処理では、開閉弁V5を開弁し、且つ、上述の給湯処理と同様に給湯用バーナg1に点火し、浴槽温度設定スイッチSw4にて設定された目標湯張り温度、流量センサS8の検出水量、給水サ−ミスタS7の検出水温および給湯サ−ミスタS6の検出温度などに基づいて、給湯サ−ミスタS6の検出温度が目標湯張り温度になるように、ガス比例弁V2の開度およびミキシング弁V11の開度を調節する。そして湯張り処理の停止の際には、開閉弁V5を閉弁し、給湯用バーナg1の燃焼を停止するように構成されている。
(Water filling treatment)
In the hot water filling process, the operation control unit C opens the on-off valve V5, ignites the hot water supply burner g1 similarly to the hot water supply process described above, and the target hot water temperature set by the bathtub temperature setting switch Sw4. Based on the detected water amount of the flow rate sensor S8, the detected water temperature of the water supply thermistor S7, the detected temperature of the hot water thermistor S6, etc., the gas proportional so that the detected temperature of the hot water thermistor S6 becomes the target hot water filling temperature. The opening degree of the valve V2 and the opening degree of the mixing valve V11 are adjusted. When the hot water filling process is stopped, the on-off valve V5 is closed, and the combustion of the hot water supply burner g1 is stopped.

(追焚き処理)
また運転制御部Cは、追焚き処理では、追焚き用熱動弁V8を開弁した状態で浴槽水循環ポンプP1および熱媒循環ポンプP2を作動させて、浴槽10内の湯水を浴槽戻り路L7および浴槽往き路L8を通して循環させ、それに併せて、熱媒加熱部H2における燃焼用ファン12aを駆動した後、開閉弁V1を開弁してイグナイタにより熱媒加熱用バーナg2に点火し、熱媒サーミスタS3の検出温度が追焚き用設定熱媒温度(例えば80℃)になるように、ガス比例弁V4の開度を調節する。運転制御部Cにおいて、この追焚き処理を実行する機能部位を追焚き処理手段M1と記載している。
なお本実施形態では追焚き処理において、第1追焚き処理と第2追焚き処理のいずれを行うかを決定する選択処理と、第2追焚き処理を行う際の熱媒の温度を決定する熱媒温度決定処理、追焚き時間を変更・決定する追焚き時間決定処理が行われる。これらの処理については後述する。
(Remembrance process)
Further, in the reheating process, the operation control unit C operates the bathtub water circulation pump P1 and the heat medium circulation pump P2 with the reheating heat valve V8 opened, and supplies hot water in the bathtub 10 to the bathtub return path L7. In addition, after the combustion fan 12a in the heat medium heating section H2 is driven, the on-off valve V1 is opened and the heat medium heating burner g2 is ignited by the igniter. The opening degree of the gas proportional valve V4 is adjusted so that the detected temperature of the thermistor S3 becomes the reheating set heat medium temperature (for example, 80 ° C.). In the operation control unit C, a functional part that executes this chasing process is described as chasing processing means M1.
In the present embodiment, in the tracking process, a selection process that determines whether the first tracking process or the second tracking process is performed, and heat that determines the temperature of the heat medium when the second tracking process is performed. A medium temperature determination process and a tracking time determination process for changing and determining the tracking time are performed. These processes will be described later.

そして、浴槽戻りサ−ミスタS2の検出温度が目標湯張り温度以上になると、運転制御部Cは、開閉弁V3を閉弁させて熱媒加熱用バーナg2の燃焼を停止させ、燃焼用ファン12aを停止させて追焚き処理を終了する。   When the detected temperature of the bathtub return thermistor S2 becomes equal to or higher than the target hot water temperature, the operation control unit C closes the on-off valve V3 to stop the combustion of the heating medium heating burner g2, and the combustion fan 12a. Is stopped and the chasing process is terminated.

〔手動追焚き運転〕
運転制御部Cは、追焚きスイッチSw7が操作されると、上述した判定処理を行い、浴槽戻りサ−ミスタS2の検出温度を読み込む。
[Manual chasing operation]
When the tracking switch Sw7 is operated, the operation control unit C performs the above-described determination process and reads the detected temperature of the bathtub return thermistor S2.

浴槽戻りサ−ミスタS2の検出温度が目標湯張り温度よりも低い場合は、上述した追焚き処理を行う。すなわち運転制御部Cは、追焚き用熱動弁V8を開弁した状態で熱媒循環ポンプP2および浴槽水循環ポンプP1を作動させて、浴槽10内の湯水を浴槽戻り路L7および浴槽往き路L8を通して循環させ、それに併せて、熱媒加熱部H2における燃焼用ファン12aを駆動した後、開閉弁V3を開弁してイグナイタにより熱媒加熱用バーナg2を点火する。そして、熱媒サーミスタS3の検出温度が追焚き用設定熱媒温度(例えば80℃)になるように、ガス比例弁V4の開度を調節することにより、浴槽水を加熱する。   When the detection temperature of the bathtub return thermistor S2 is lower than the target hot water filling temperature, the above-described chasing process is performed. That is, the operation control unit C operates the heat medium circulation pump P2 and the bath water circulation pump P1 in a state where the reheating heat valve V8 is opened, and the hot water in the bathtub 10 is supplied to the bathtub return path L7 and the bathtub return path L8. At the same time, after the combustion fan 12a in the heat medium heating section H2 is driven, the on-off valve V3 is opened and the heat medium heating burner g2 is ignited by the igniter. Then, the bath water is heated by adjusting the opening of the gas proportional valve V4 so that the detected temperature of the heat medium thermistor S3 becomes the setting heat medium temperature for reheating (for example, 80 ° C.).

浴槽戻りサ−ミスタS2の検出温度が目標湯張り温度以上になると、開閉弁V3を閉弁させて熱媒加熱用バーナg2の燃焼を停止させ、燃焼用ファン12aを停止させて手動追焚き運転を終了する。   When the detection temperature of the bathtub return thermistor S2 is equal to or higher than the target hot water filling temperature, the on-off valve V3 is closed to stop the combustion of the heating medium heating burner g2, and the combustion fan 12a is stopped to perform manual chasing operation. Exit.

〔保温運転の詳細〕
運転制御部Cは上述の通り、自動湯張り運転を終了した後において風呂自動スイッチSw2がオン状態になっている間は、保温運転を実行する。本発明の保温運転においては、浴槽水の湯温低下率に基づいて追焚き間隔時間が変更される。また本発明の追焚き処理においては、所定の第1熱媒温度に熱媒を加熱して浴槽水を追焚きする第1追焚き処理と、第1追焚き処理に要する時間よりも長くかつ最長追焚き時間と同じかより短い時間で追焚き処理が完了する第2熱媒温度を決定し、その第2熱媒温度に熱媒を加熱して浴槽水を追焚きする第2追焚き処理とが選択的に行われる。以下、これらの処理の詳細について説明する。
まず、運転制御部Cに備えられる本発明の各特長手段M1〜M7、Mmの構成およびその働きについて、図2および図3に基づいて説明する。図2は、運転制御部Cの機能構成を示す機能構成図である。図3は、保温運転の状態を示す説明図である。
[Details of heat insulation operation]
As described above, the operation control unit C performs the heat retaining operation while the bath automatic switch Sw2 is in the on state after the automatic water filling operation is completed. In the heat insulation operation of the present invention, the chasing interval time is changed based on the hot water temperature decrease rate of the bath water. Further, in the reheating process of the present invention, the first reheating process for reheating the bath water by heating the heat medium to a predetermined first heat medium temperature and longer than the time required for the first reheating process are longest. A second heat treatment process for determining a second heat medium temperature at which the heat treatment process is completed in a time shorter than or equal to the heat time, and heating the heat medium to the second heat medium temperature to reclaim the bath water; Is selectively performed. Details of these processes will be described below.
First, configurations and functions of the respective feature means M1 to M7 and Mm of the present invention provided in the operation control unit C will be described with reference to FIGS. FIG. 2 is a functional configuration diagram illustrating a functional configuration of the operation control unit C. As illustrated in FIG. FIG. 3 is an explanatory view showing a state of the heat insulation operation.

図2に示すように、運転制御部Cには、追焚き処理において熱源機Gの各構成を制御する追焚き制御手段M2の他に、選択処理手段M3、熱媒温度決定手段M4、追焚き時間決定手段M5が備えられ、これらが追焚き処理手段M1を構成している。また運転制御部Cには、保温運転を実行する保温運転手段M6と、追焚き間隔時間を最適値に変更する追焚き間隔時間変更手段M7が備えられている。
さらに運転制御部Cには、追焚き処理手段M1で適宜使用される情報を記憶した記憶手段Mmが備えられており、この記憶手段Mmには、浴槽水の水位と浴槽10に貯留された浴槽水の量Lとの関係を示す情報Mm1、毎時投入熱量と熱媒温度との関係を示す情報Mm2、外気温度による第2追焚き時間の変更量を示す情報Mm3、浴室温度による第2追焚き時間の変更量を示す情報Mm4、浴槽の断熱性能に関する指標による第2追焚き時間の変更量を示す情報Mm5、最長追焚き時間tmaxに関する情報Mm6、最低熱媒温度Tminに関する情報Mm7、湯温降下限度幅ΔΤに関する情報Mm8、および調整時間幅Δτに関する情報Mm9が記憶情報として含まれている。
As shown in FIG. 2, the operation control unit C includes a selection processing unit M3, a heat medium temperature determining unit M4, and a chasing unit in addition to the chasing control unit M2 that controls each component of the heat source machine G in the chasing processing. A time determination means M5 is provided, and these constitute the tracking processing means M1. The operation control unit C is further provided with a heat retaining operation means M6 for performing a heat retaining operation and a chasing interval time changing means M7 for changing the chasing interval time to an optimum value.
Further, the operation control unit C is provided with a storage unit Mm that stores information that is appropriately used in the chasing processing unit M1. The storage unit Mm includes a water level of the bathtub water and a bathtub stored in the bathtub 10. Information Mm1 indicating the relationship with the amount of water L, information Mm2 indicating the relationship between the hourly input heat amount and the heat medium temperature, information Mm3 indicating the amount of change in the second reheating time due to the outside air temperature, and the second reheating due to the bathroom temperature Information Mm4 indicating the amount of change in time, information Mm5 indicating the amount of change in the second chasing time based on the index relating to the heat insulation performance of the bathtub, information Mm6 relating to the longest chasing time tmax, information Mm7 relating to the minimum heating medium temperature Tmin, hot water temperature drop Information Mm8 related to the limit width ΔΤ and information Mm9 related to the adjustment time width Δτ are included as stored information.

〔保温運転手段〕
保温運転手段M6は、図3に示す保温運転を行うよう熱源機Gの各構成を制御し、追焚きを行う旨の指令を追焚き処理手段M1に発する。以下、図3に従って保温運転手段M6および追焚き間隔時間変更手段M7の機能と動作を説明する。図3の横軸は時間を、縦軸は浴槽水の温度を表しており、図3はすなわち保温運転中の浴槽水温度の推移を表している。
[Heat insulation operation means]
The heat retaining operation means M6 controls each component of the heat source machine G so as to perform the heat retaining operation shown in FIG. 3, and issues a command to perform the reheating to the retreat processing means M1. The functions and operations of the heat retaining operation means M6 and the tracking interval time changing means M7 will be described below with reference to FIG. The horizontal axis of FIG. 3 represents time, and the vertical axis represents the temperature of the bath water, and FIG. 3 represents the transition of the bath water temperature during the heat insulation operation.

保温運転手段M6は、前回の追焚き処理が終了してから追焚き間隔時間τnが経過すると、追焚き処理手段M1に対して今回の追焚き処理を行う旨の指令を発する。追焚き処理手段M1は、先ず上述の判定処理により浴槽戻りサ−ミスタS2の検出温度に基づく浴槽10内の浴槽水の温度(浴槽出温度)Τnの確定を行い、次に浴槽10の浴槽水を設定温度Τ0へ追い焚きする追焚き処理を行う。すなわち追焚き処理手段M1は、保温運転手段M6から追焚き処理を行う旨の指令を受けた際、浴槽水循環ポンプP1を作動させ、所定時間経過後に浴槽戻りサーミスタS2による温度検出が完了した後、熱媒加熱用バーナg2と熱媒循環ポンプP2を作動させる。   When the chasing interval time τn elapses after the previous chasing process ends, the heat retaining operation means M6 issues a command to the chasing processing means M1 to perform the present chasing process. The chasing processing means M1 first determines the temperature (tubing temperature) 浴槽 n in the bathtub 10 based on the temperature detected by the bathtub return thermistor S2 by the above-described determination process, and then the bathtub water in the bathtub 10 The tracking process for tracking the temperature to the set temperature Τ0 is performed. That is, when the reheating processing means M1 receives a command to perform the reheating process from the heat retaining operation means M6, the bath water circulation pump P1 is operated, and after the predetermined time has elapsed, the temperature detection by the bath return thermistor S2 is completed. The heat medium heating burner g2 and the heat medium circulation pump P2 are operated.

今回の追焚き処理の完了後、保温運転手段M6は再度時間の計測を開始して、次に述べる追焚き間隔時間変更手段M7により変更された新しい追焚き間隔時間τn+1に基づき、当該追焚き間隔時間τn+1の経過後に追焚き処理の指令を行う。この動作により、浴槽10に貯留された浴槽水の温度は設定温度Τ0と、設定温度Τ0から湯温降下限度幅ΔΤだけ低い下限温度Τ0’との間に保たれる。   After completion of the current chasing process, the heat retaining operation means M6 starts measuring time again, and based on the new chasing interval time τn + 1 changed by the chasing interval time changing means M7 described below, the chasing interval After the elapse of time τn + 1, a chasing process command is issued. By this operation, the temperature of the bathtub water stored in the bathtub 10 is maintained between the set temperature Τ0 and the lower limit temperature Τ0 'that is lower than the set temperature Τ0 by the hot water temperature drop limit width ΔΤ.

〔追焚き間隔時間変更手段〕
追焚き間隔時間変更手段M7は、判定処理により浴槽水の温度(浴槽出温度)が確定されると、以下に述べる手順にて追焚き間隔時間を変更・決定する。
(1)目標湯張り温度(設定温度)Τ0と浴槽出温度Τnの差を、今回の追焚き間隔時間τn(前回の追焚きから今回の追焚きまでの時間)で除算することにより、以下のように湯温低下率αnを算出する。
湯温低下率αn=(設定温度Τ0−浴槽出温度Τn)/今回の追焚き間隔時間τn
(2)次に、湯温降下限度幅ΔΤを(1)で求めた湯温低下率αnで除算することにより、下降時間Xを算出する。
下降時間X=湯温降下限度幅ΔΤ/湯温低下率αn=τn×ΔΤ/(Τ0−Τn)
(3)次回の追焚き間隔時間τn+1を算出された下降時間Xに決定する。
時間間隔τn+1 = 下降時間X
[Measuring interval time change means]
The chasing interval time changing means M7 changes and determines the chasing interval time according to the procedure described below when the temperature of the bath water (tubing temperature) is determined by the determination process.
(1) By dividing the difference between the target hot water filling temperature (set temperature) Τ0 and the bath temperature Τn by the current reheating interval time τn (the time from the previous reheating to the current reheating), Thus, the hot water temperature decrease rate αn is calculated.
Hot water temperature decrease rate αn = (set temperature Τ0−bath temperature Τn) / current renewal interval time τn
(2) Next, the descent time X is calculated by dividing the hot water temperature drop limit width ΔΤ by the hot water temperature decrease rate αn obtained in (1).
Falling time X = Water temperature drop limit width ΔΤ / Water temperature drop rate αn = τn × ΔΤ / (Τ0−Τn)
(3) The next pursuit interval time τn + 1 is determined as the calculated fall time X.
Time interval τn + 1 = Fall time X

前項の(3)に換えて、次回の追焚き間隔時間τn+1を、算出された下降時間Xに調整時間幅Δτを加算した値に決定するように構成してもよい。
時間間隔τn+1 = 下降時間X+調整時間幅Δτ
この場合の調整時間幅Δτは次のように決定する。高温暖房端末HU(浴室暖房乾燥機)が運転している場合には、その運転状態(設定風量、運転時間、設定温度など)に対応する調整時間幅Δτの値を、記憶手段Mmに記憶された情報Mm9から読み出して決定する。また、浴室温度サーミスタS12により取得される浴室温度を監視しておき、所定の量を超える温度上昇(あるいは所定の変化率を超える温度上昇)があった場合には、その温度上昇に対応する調整時間幅Δτの値を、記憶手段Mmに記憶された情報Mm9から読み出して決定する。
なお、高温暖房端末HUの運転による調整時間幅Δτと浴室温度の上昇による調整時間幅Δτの両方を下降時間Xに加算してもよい。
すなわち、次回の追焚き間隔時間τn+1を、算出された下降時間Xから調整時間幅Δτだけ変更された値に決定するように構成してもよい。
Instead of (3) in the previous section, the next pursuit interval time τn + 1 may be determined to be a value obtained by adding the adjustment time width Δτ to the calculated fall time X.
Time interval τn + 1 = fall time X + adjustment time width Δτ
The adjustment time width Δτ in this case is determined as follows. When the high-temperature heating terminal HU (bathroom heating dryer) is operating, the value of the adjustment time width Δτ corresponding to the operation state (set air volume, operation time, set temperature, etc.) is stored in the storage means Mm. It is determined by reading from the information Mm9. Further, the bathroom temperature acquired by the bathroom temperature thermistor S12 is monitored, and if there is a temperature rise exceeding a predetermined amount (or a temperature rise exceeding a predetermined change rate), an adjustment corresponding to the temperature rise is performed. The value of the time width Δτ is determined by reading from the information Mm9 stored in the storage means Mm.
Note that both the adjustment time width Δτ due to the operation of the high-temperature heating terminal HU and the adjustment time width Δτ due to the rise in bathroom temperature may be added to the fall time X.
That is, the next pursuit interval time τn + 1 may be determined to be a value changed from the calculated falling time X by the adjustment time width Δτ.

前々項の(3)に換えて、次回の追焚き間隔時間τn+1を、算出された下降時間Xから調整時間幅Δτを減算した値に決定するように構成してもよい。
時間間隔τn+1 = 下降時間X−調整時間幅Δτ
この場合の調整時間幅Δτは次のように決定する。浴室に備えられた換気扇が稼働している場合には、その稼働状況(設定風量、運転時間など)に対応する調整時間幅Δτの値を、記憶手段Mmに記憶された情報Mm9から読み出して決定する。また、浴室温度サーミスタS12により取得される浴室温度を監視しておき、所定の量を超える温度下降(あるいは所定の変化率を超える温度下降)があった場合には、その温度下降に対応する調整時間幅Δτの値を、記憶手段Mmに記憶された情報Mm9から読み出して決定する。
なお、換気扇の稼働による調整時間幅Δτと浴室温度の下降による調整時間幅Δτの両方を下降時間Xから減算してもよい。
また、高温暖房端末HUの運転による調整時間幅Δτの加算、浴室温度の上昇による調整時間幅Δτの加算、換気扇の稼働による調整時間幅Δτの減算、浴室温度の下降による調整時間幅Δτの減算のうち、いくつかを組み合わせて下降時間Xに加算・減算してもよいし、全てを下降時間Xに加算・減算してもよい。
Instead of (3) in the preceding paragraph, the next pursuit interval time τn + 1 may be determined to be a value obtained by subtracting the adjustment time width Δτ from the calculated fall time X.
Time interval τn + 1 = fall time X−adjustment time width Δτ
The adjustment time width Δτ in this case is determined as follows. When the ventilation fan provided in the bathroom is in operation, the value of the adjustment time width Δτ corresponding to the operation status (set air volume, operation time, etc.) is read from the information Mm9 stored in the storage means Mm and determined. To do. Further, the bathroom temperature acquired by the bathroom temperature thermistor S12 is monitored, and if there is a temperature drop exceeding a predetermined amount (or a temperature drop exceeding a predetermined change rate), an adjustment corresponding to the temperature drop is performed. The value of the time width Δτ is determined by reading from the information Mm9 stored in the storage means Mm.
Note that both the adjustment time width Δτ due to the operation of the ventilation fan and the adjustment time width Δτ due to the decrease in the bathroom temperature may be subtracted from the fall time X.
Also, addition of adjustment time width Δτ due to operation of high temperature heating terminal HU, addition of adjustment time width Δτ due to increase in bathroom temperature, subtraction of adjustment time width Δτ due to operation of ventilation fan, subtraction of adjustment time width Δτ due to decrease in bathroom temperature Of these, some may be combined and added to or subtracted from the falling time X, or all may be added to or subtracted from the falling time X.

以上述べた通り、保温運転手段M6により追焚き処理が繰り返し行われ、その度に追焚き間隔時間変更手段M7により追焚き間隔時間の最適化が行われる。
続いて、追焚き処理手段M1により行われる第1追焚き運転と第2追焚き運転について説明する。
As described above, the chasing process is repeatedly performed by the heat retaining operation means M6, and the chasing interval time changing means M7 optimizes the chasing interval time each time.
Next, the first chasing operation and the second chasing operation performed by the chasing processing means M1 will be described.

〔追焚き制御手段〕
追焚き制御手段M2は、追焚き処理を行う旨の指令を受け付けると、追焚き用熱動弁V8を開弁した状態で熱媒循環ポンプP2を作動させることにより、主熱交換器EX3および副熱交換器EX4にて加熱された熱媒を追焚き熱交換器EX5に循環供給する。そしてその状態において、浴槽水循環ポンプP1を作動させることにより、浴槽10に貯留された浴槽水を浴槽戻り路L7および浴槽往き路L8を通して追焚き熱交換器EX5に循環供給して、追焚き熱交換器EX5にて加熱する。
[Turning control means]
Upon receipt of a command to perform the tracking process, the tracking control means M2 operates the heat medium circulation pump P2 with the tracking thermal valve V8 opened, thereby causing the main heat exchanger EX3 and the auxiliary heat exchanger M2 to operate. The heating medium heated by the heat exchanger EX4 is tracked and circulated and supplied to the heat exchanger EX5. In that state, by operating the bathtub water circulation pump P1, the bathtub water stored in the bathtub 10 is circulated and supplied to the reheating heat exchanger EX5 through the bathtub return path L7 and the bathtub return path L8, and reheating heat exchange is performed. Heat in vessel EX5.

これに併せて追焚き制御手段M2は、熱媒加熱部H2における燃焼用ファン12aを駆動した後、開閉弁V1を開弁してイグナイタにより熱媒加熱用バーナg2に点火し、熱媒サーミスタS3の検出温度に基づいてガス比例弁V4の開度を調節することにより、熱媒の温度を追焚き用設定熱媒温度になるように制御する。追焚き用設定熱媒温度は、第1追焚き処理が行われる場合は、あらかじめ記憶手段に記憶された第1熱媒温度(例えば、80℃)へと設定され、第2追焚き処理が行われる場合は、後述する熱媒温度決定手段M4により決定された第2熱媒温度へと設定される。   At the same time, the follow-up control means M2 drives the combustion fan 12a in the heat medium heating section H2, then opens the on-off valve V1, ignites the heat medium heating burner g2 by the igniter, and the heat medium thermistor S3. By adjusting the opening of the gas proportional valve V4 based on the detected temperature, the temperature of the heat medium is controlled so as to become the set heat medium temperature for tracking. The heating medium setting heat medium temperature is set to the first heating medium temperature (for example, 80 ° C.) stored in the storage unit in advance when the first heating process is performed, and the second heating process is performed. In the case where it is determined, the temperature is set to the second heat medium temperature determined by the heat medium temperature determining means M4 described later.

〔選択処理手段〕
選択処理手段M3は、風呂装置100の動作状態およびリモコンへの操作に基づいて、追焚き処理において第1追焚き処理と第2追焚き処理のいずれを行うかを以下の通り決定する。
(1)高温暖房運転が行われている間に追焚き処理を行う旨の指令があった場合、第1追焚き処理を行うよう決定する。
(2)メインリモコンR1または浴室リモコンR2から手動追焚き運転を行う旨の指令があった場合、第1追焚き処理を行うよう決定する。
(3)上記以外の状況で追焚き処理を行う旨の指令があった場合、第2追焚き処理を行うよう決定する。
第1追焚き処理を行うよう決定された場合、選択処理手段M3は追焚き制御手段M2に対してその旨を指令する。第2追焚き処理を行うよう決定された場合、選択処理手段M3は熱媒温度決定手段M4に対して熱媒温度の決定を行うよう指令する。
[Selection processing means]
The selection processing means M3 determines whether to perform the first chasing process or the second chasing process in the chasing process based on the operation state of the bath apparatus 100 and the operation on the remote controller.
(1) When there is a command to perform the tracking process while the high-temperature heating operation is being performed, it is determined to perform the first tracking process.
(2) When there is a command to perform a manual chasing operation from the main remote controller R1 or the bathroom remote controller R2, it is determined to perform the first chasing process.
(3) When there is a command to perform the tracking process in a situation other than the above, it is determined to perform the second tracking process.
When it is determined to perform the first chasing process, the selection processing means M3 instructs the chasing control means M2. When it is determined to perform the second tracking process, the selection processing unit M3 instructs the heat medium temperature determining unit M4 to determine the heat medium temperature.

〔熱媒温度決定手段〕
熱媒温度決定手段M4は、第2追焚き処理を行う場合に第2熱媒温度を決定する。第2熱媒温度は、第1追焚き処理に要する時間よりも長くかつ最長追焚き時間tmaxと同じかより短い時間で追焚き処理が完了する第2熱媒温度を、浴槽水を追焚き完了温度(目標湯張り温度)に加熱するために要する必要投入熱量を第2追焚き時間で除算することで求められる毎時投入熱量に基づいて決定する。
以下、第2熱媒温度を決定する処理について説明する。
[Heat medium temperature determination means]
The heat medium temperature determining means M4 determines the second heat medium temperature when performing the second tracking process. The second heat transfer medium temperature is longer than the time required for the first reheating process, and the reheating process is completed in a time equal to or shorter than the longest renewal time tmax. It is determined on the basis of the hourly input heat amount obtained by dividing the necessary input heat amount required for heating to the temperature (target hot water filling temperature) by the second reheating time.
Hereinafter, the process which determines 2nd heat-medium temperature is demonstrated.

(1)必要投入熱量の算出
必要投入熱量は、浴槽水を目標湯張り温度に加熱するために要する熱量であって、判定処理によって決定される浴槽水の温度と目標湯張り温度との差ΔTと、浴槽10に貯留されている浴槽水の量Lにより算出される。浴槽水の量Lは、判定処理によって決定される浴槽水の水位に基づいて、情報Mm1(浴槽水の水位と浴槽10に貯留された浴槽水の量Lとの関係を示す情報)を参照して求められる。すなわち、
必要投入熱量 = 浴槽水の量L × ΔT × 比熱
として、必要投入熱量が算出される。
(1) Calculation of required input heat amount The required input heat amount is the amount of heat required to heat the bath water to the target hot water temperature, and the difference ΔT between the temperature of the bath water determined by the determination process and the target hot water temperature And the amount L of bathtub water stored in the bathtub 10 is calculated. The amount L of bathtub water refers to information Mm1 (information indicating the relationship between the water level of bathtub water and the amount L of bathtub water stored in the bathtub 10) based on the water level of the bathtub water determined by the determination process. Is required. That is,
Necessary input heat amount = amount of bath water L × ΔT × specific heat The required input heat amount is calculated.

(2)毎時投入熱量
必要投入熱量を第2追焚き時間で除算することにより、毎時投入熱量が算出される。毎時投入熱量は、第2追焚き時間により追焚き処理を完了するために浴槽へ投入するべき単位時間当たりの熱量である。第2追焚き時間は、第1追焚き処理に要する時間よりも長くかつ最長追焚き時間tmaxと同じかより短い時間として、本実施形態では予め設定され記憶手段Mmに記憶されている。すなわち、
毎時投入熱量 = 必要投入熱量 / 第2追焚き時間
として、毎時投入熱量が算出される。
(2) Hourly input heat amount By dividing the required input heat amount by the second tracking time, the hourly input heat amount is calculated. The amount of heat input per hour is the amount of heat per unit time that should be input to the bathtub in order to complete the tracking process with the second tracking time. The second pursuit time is set in advance and stored in the storage unit Mm as a time longer than the time required for the first pursuit process and equal to or shorter than the longest pursuit time tmax. That is,
Hourly input heat amount = Necessary input heat amount / second heating time The hourly input heat amount is calculated.

(3)第2熱媒温度の決定
第2熱媒温度は、毎時投入熱量に基づいて、情報Mm2(毎時投入熱量と熱媒温度との関係を示す情報)を参照して決定される。毎時投入熱量は浴槽10へ投入される単位時間当たりの熱量であり、追焚き熱交換器EX5を通流する熱媒の温度により変化する。従って、毎時投入熱量を熱媒の温度の関数として情報Mm2に格納しておくことにより、毎時投入熱量に基づいて第2熱媒温度を決定することができる。情報Mm2は関数の他、マップやテーブルの形態であってもよいし、熱媒流量の影響を考慮した情報であってもよい。
(3) Determination of second heat medium temperature The second heat medium temperature is determined with reference to information Mm2 (information indicating the relationship between the hourly input heat amount and the heat medium temperature) based on the hourly input heat amount. The amount of heat input per hour is the amount of heat per unit time input to the bathtub 10, and varies depending on the temperature of the heat medium flowing through the additional heat exchanger EX5. Therefore, the second heat medium temperature can be determined based on the hourly input heat amount by storing the hourly input heat amount in the information Mm2 as a function of the temperature of the heat medium. The information Mm2 may be in the form of a map or table in addition to the function, or may be information in consideration of the influence of the heat medium flow rate.

最後に、情報Mm7(最低熱媒温度Tminに関する情報)を参照して、決定された第2熱媒温度が最低熱媒温度Tminを下回っている場合には、第2熱媒温度を最低熱媒温度Tminに決定する。熱媒の温度が低すぎた場合、追焚き回路C1等の熱媒循環回路において配管の低温腐食が発生する可能性があるが、上述の処理により第2追焚き処理の際の熱媒の温度が低すぎる事態を回避することができる。なお、必要投入熱量が大きいことによって第2熱媒温度が第1熱媒温度 よりも大きくなってしまう場合には、第1熱媒温度にて追焚き処理を行う。   Finally, referring to the information Mm7 (information on the minimum heating medium temperature Tmin), when the determined second heating medium temperature is lower than the minimum heating medium temperature Tmin, the second heating medium temperature is set to the minimum heating medium temperature. The temperature is determined as Tmin. If the temperature of the heating medium is too low, there is a possibility that low-temperature corrosion of the piping may occur in the heating medium circulation circuit such as the heating circuit C1, but the temperature of the heating medium during the second heating process by the above-described processing. Can be avoided too low. If the second heat medium temperature becomes higher than the first heat medium temperature due to the large amount of required heat input, the chasing process is performed at the first heat medium temperature.

〔追焚き時間決定手段〕
追焚き時間決定手段M5は、熱源機Gの外気温度、浴室の浴室温度、あるいは浴槽10の断熱性能に応じて、第2追焚き処理に要する時間である第2追焚き時間を変更し決定する。なお、追焚き時間決定手段M5による第2追焚き時間の変更・決定は、上述の毎時投入熱量の算出に先立って行われる。
(1)施設の外気温度による変更
追焚き時間決定手段M5は、外気温度サーミスタS11により取得された外気温度に基づいて、情報Mm3(外気温度による第2追焚き時間の変更量を示す情報)を参照して、第2追焚き時間を変更し決定する。例えば外気温度が10℃未満の場合は、第2追焚き時間からΔt1を減じた時間を新たな第2追焚き時間として決定する。外気温度が30℃を超える場合は、第2追焚き時間にΔt2を加えた時間を新たな第2追焚き時間として決定する。そして熱媒温度決定手段M4は、変更された新たな第2追焚き時間に基づいて第2熱媒温度を決定する。外気温度が低いほど、第2追焚き時間を短くするよう構成するのが好ましい。
[Measuring time determination means]
The chasing time determining means M5 changes and determines the second chasing time, which is the time required for the second chasing process, according to the outside air temperature of the heat source machine G, the bathroom temperature of the bathroom, or the heat insulating performance of the bathtub 10. . Note that the change / determination of the second chasing time by the chasing time determining means M5 is performed prior to the calculation of the hourly input heat amount.
(1) Change according to the outside air temperature of the facility The tracking time determination means M5 provides information Mm3 (information indicating the amount of change in the second tracking time due to the outside air temperature) based on the outside air temperature acquired by the outside air temperature thermistor S11. Referring to and changing the second tracking time. For example, when the outside air temperature is less than 10 ° C., a time obtained by subtracting Δt1 from the second pursuit time is determined as a new second pursuit time. When the outside air temperature exceeds 30 ° C., a time obtained by adding Δt2 to the second pursuit time is determined as a new second pursuit time. Then, the heat medium temperature determining means M4 determines the second heat medium temperature based on the changed new second tracking time. It is preferable that the second pursuit time is shortened as the outside air temperature is lower.

(2)浴室温度による変更
追焚き時間決定手段M5は、浴室温度サーミスタS12により取得された浴室温度に基づいて、情報Mm4(浴室温度による第2追焚き時間の変更量を示す情報)を参照して、第2追焚き時間を変更し決定する。例えば浴室温度が30℃を超える場合は、第2追焚き時間にΔt4を加えた時間を新たな第2追焚き時間として決定する。浴室温度が20℃未満の場合は、第2追焚き時間からΔt3を減じた時間を新たな第2追焚き時間として決定する。そして熱媒温度決定手段M4は、変更された新たな第2追焚き時間に基づいて第2熱媒温度を決定する。浴室温度が低いほど、第2追焚き時間を短くするよう構成するのが好ましい。
(2) Change by bathroom temperature The reheating time determination means M5 refers to the information Mm4 (information indicating the amount of change in the second reheating time by the bathroom temperature) based on the bathroom temperature acquired by the bathroom temperature thermistor S12. Then, the second tracking time is changed and determined. For example, when the bathroom temperature exceeds 30 ° C., a time obtained by adding Δt4 to the second pursuit time is determined as a new second pursuit time. When the bathroom temperature is lower than 20 ° C., a time obtained by subtracting Δt3 from the second pursuit time is determined as a new second pursuit time. Then, the heat medium temperature determining means M4 determines the second heat medium temperature based on the changed new second tracking time. It is preferable that the second chasing time is shortened as the bath temperature is lower.

(3)浴槽の断熱性能による変更
追焚き時間決定手段M5は、浴槽の断熱性能に関する指標に基づいて、情報Mm5(浴槽の断熱性能に関する指標による第2追焚き時間の変更量を示す情報)を参照して、第2追焚き時間を変更し決定する。浴槽の断熱性能に関する指標は、風呂装置100を設置した際に用いた浴槽10の断熱性能に応じて記憶手段Mmに記憶され、住宅リフォーム等により浴槽10が交換された場合には、新しい浴槽10の断熱性能に応じて変更され記憶される。例えば指標が「低断熱」の場合には、第2追焚き時間からΔt6を減じた時間を新たな第2追焚き時間として決定する。指標が「非断熱」の場合には、第2追焚き時間からΔt5を減じた時間を新たな第2追焚き時間として決定する。そして熱媒温度決定手段M4は、変更された新たな第2追焚き時間に基づいて第2熱媒温度を決定する。断熱性能が低いほど、第2追焚き時間を短くするよう構成するのが好ましい。
(3) Change due to thermal insulation performance of bathtub The chasing time determination means M5 provides information Mm5 (information indicating the change amount of the second chasing time based on the index related to the thermal insulation performance of the bathtub) based on the index related to the thermal insulation performance of the bathtub. Referring to and changing the second tracking time. The index regarding the thermal insulation performance of the bathtub is stored in the storage means Mm according to the thermal insulation performance of the bathtub 10 used when the bath apparatus 100 is installed, and when the bathtub 10 is replaced by housing reform or the like, the new bathtub 10 It is changed and stored according to the heat insulation performance. For example, when the index is “low insulation”, a time obtained by subtracting Δt6 from the second pursuit time is determined as a new second pursuit time. When the index is “non-adiabatic”, a time obtained by subtracting Δt5 from the second pursuit time is determined as a new second pursuit time. Then, the heat medium temperature determining means M4 determines the second heat medium temperature based on the changed new second tracking time. The lower the heat insulation performance, the shorter the second chasing time is preferable.

なお本実施形態において第2追焚き時間は、第1追焚き処理に要する時間よりも長くかつ最長追焚き時間tmaxと同じかより短い時間として予め設定され記憶手段Mmに記憶されているが、第1追焚き処理に要する時間に所定時間(例えば、1.5分)を加えた時間としてもよい。すなわち、判定処理によって決定された浴槽水の温度・水位と第1熱媒温度に基づいて、必要投入熱量と毎時投入熱量から第1追焚き処理に要する時間を算出し、当該時間に所定時間を加えた時間としてもよい。   In the present embodiment, the second tracking time is preset and stored in the storage means Mm as a time longer than the time required for the first tracking process and equal to or shorter than the longest tracking time tmax. It may be a time obtained by adding a predetermined time (for example, 1.5 minutes) to the time required for one tracking process. That is, based on the temperature / water level of the bathtub water determined by the determination process and the first heat medium temperature, the time required for the first reheating process is calculated from the required input heat amount and the input heat amount per hour, and the predetermined time is set to the time. It may be added time.

〔第2実施形態〕
上述の第1実施形態においては、必要投入熱量を第2追焚き時間で除算することで求められる毎時投入熱量に基づいて第2熱媒温度を決定したが、あらかじめ設定された第3熱媒温度にて追焚きした場合に追焚き処理に要する時間(第3追焚き時間)を算出し、当該時間が最長追焚き時間tmaxと同じかより短い場合は第3熱媒温度を第2熱媒温度に決定して第2追焚き処理を行い、当該時間が最長追焚き時間tmaxより長い場合は、最長追焚き時間tmaxで追焚き処理が完了する熱媒の温度を第2熱媒温度に決定して第2追焚き処理を行う構成としてもよい。
[Second Embodiment]
In the first embodiment described above, the second heat medium temperature is determined based on the hourly input heat quantity obtained by dividing the required input heat quantity by the second tracking time. However, the preset third heat medium temperature is determined. The time required for the chasing process (third chasing time) is calculated when the chasing process is performed at the time, and when the time is equal to or shorter than the longest chasing time tmax, the third heating medium temperature is set to the second heating medium temperature. When the second tracking process is performed and the time is longer than the longest tracking time tmax, the temperature of the heat medium that completes the tracking process at the longest tracking time tmax is determined as the second heating medium temperature. The second tracking process may be performed.

〔第3追焚き時間の算出〕
第3追焚き時間は、追焚き処理手段M1において次のように算出される。あらかじめ設定され記憶手段Mmに記憶されている第3熱媒温度に基づいて、情報Mm2(毎時投入熱量と熱媒温度との関係を示す情報)を参照し、毎時投入熱量を求める。この毎時投入熱量は、第3熱媒温度に熱媒を加熱して追焚き処理を行った場合に、浴槽10に投入される単位時間当たりの熱量である。
次に、浴槽水を目標湯張り温度に加熱するために要する熱量である必要投入熱量を、第1実施形態と同様に、
必要投入熱量 = 浴槽水の量L × ΔT × 比熱
として算出する。浴槽水の量Lは、判定処理によって決定される浴槽水の水位に基づいて、情報Mm1(浴槽水の水位と浴槽10に貯留された浴槽水の量Lとの関係を示す情報)を参照して求められる。Δtは、判定処理によって決定される浴槽水の温度と目標湯張り温度との差である。
そして、以下の関係に基づいて第3追焚き時間を算出する。
第3追焚き時間 = 必要投入熱量 / 毎時投入熱量
[Calculation of third tracking time]
The third pursuit time is calculated in the pursuit processing means M1 as follows. Based on the third heat medium temperature set in advance and stored in the storage means Mm, information Mm2 (information indicating the relationship between the hourly input heat amount and the heat medium temperature) is referred to obtain the hourly input heat amount. The amount of heat input per hour is the amount of heat per unit time input to the bathtub 10 when the reheating process is performed by heating the heat medium to the third heat medium temperature.
Next, as in the first embodiment, the required input heat amount, which is the amount of heat required to heat the bath water to the target hot water temperature,
Necessary input heat amount = amount of bath water L × ΔT × specific heat The amount L of bathtub water refers to information Mm1 (information indicating the relationship between the water level of bathtub water and the amount L of bathtub water stored in the bathtub 10) based on the water level of the bathtub water determined by the determination process. Is required. Δt is a difference between the temperature of the bath water determined by the determination process and the target hot water temperature.
Then, the third pursuit time is calculated based on the following relationship.
3rd tracking time = required heat input / hourly heat input

〔第2熱媒温度の決定〕
次に、算出された第3追焚き時間と最長追焚き時間tmaxとを比較することにより、第2熱媒温度を決定する。
第3追焚き時間が最長追焚き時間tmaxと同じかより短い場合、第3熱媒温度を第2熱媒温度に決定する。
第3追焚き時間が最長追焚き時間tmaxより長い場合は、以下に述べる処理により、最長追焚き時間tmaxで追焚き処理が完了する熱媒の温度(最長追焚き温度)を求め、第2熱媒温度に決定する。
[Determination of the second heating medium temperature]
Next, the second heating medium temperature is determined by comparing the calculated third tracking time with the longest tracking time tmax.
When the third tracking time is equal to or shorter than the longest tracking time tmax, the third heating medium temperature is determined as the second heating medium temperature.
When the third chasing time is longer than the longest chasing time tmax, the temperature of the heat medium (the longest chasing temperature) at which the chasing process is completed at the longest chasing time tmax is obtained by the process described below, and the second heat Determine the medium temperature.

最長追焚き温度は次のようにして求める。上述の第3追焚き時間の算出において、必要投入熱量は既に求められているので、以下の関係式に基づいて、最長追焚き時間で追焚き処理が完了する毎時投入熱量を算出する。
毎時投入熱量 = 必要投入熱量 / 最長追焚き時間
そして情報Mm2(毎時投入熱量と熱媒温度との関係を示す情報)を参照し、算出された毎時投入熱量を実現する温度として、最長追焚き温度が求まり、これを第2熱媒温度に決定する。
The longest chasing temperature is obtained as follows. In the calculation of the above-described third pursuit time, since the required input heat amount has already been obtained, the hourly input heat amount is calculated based on the following relational expression so that the pursuit processing is completed in the longest pursuit time.
Heat input per hour = Necessary heat input / longest reheating time And referring to information Mm2 (information indicating the relationship between hourly heat input and heat medium temperature), the longest reheating temperature as the temperature that realizes the calculated heat input per hour Is determined, and this is determined as the second heat medium temperature.

〔追焚き処理に係る風呂装置の運転状態〕
図4により、第1追焚き処理に係る風呂装置の運転状態を説明する。5秒経過時点で熱媒流量12L/minで熱媒循環ポンプP2が作動し、併せて浴槽水循環ポンプP1が流量8L/minで作動する。15秒経過時点で熱媒加熱用バーナg2が点火され、熱媒サーミスタS3の検出温度が第1熱媒温度(例えば80℃)になるように、ガス比例弁V4の開度が調整される。図中「ガス入力」は、熱媒加熱用バーナg2で使用される燃焼ガスの量を熱量(kW)で表したものである。熱源機Gから出力される熱量である熱源機出力(kW)の増加に伴って、瞬時効率(ガス入力に対する熱源機出力の割合)が増加する。
[Operating condition of the bath equipment related to the reheating process]
With reference to FIG. 4, the operation state of the bath apparatus according to the first chasing process will be described. When 5 seconds have elapsed, the heat medium circulation pump P2 operates at a heat medium flow rate of 12 L / min, and the bathtub water circulation pump P1 operates at a flow rate of 8 L / min. When 15 seconds have elapsed, the heating medium heating burner g2 is ignited, and the opening of the gas proportional valve V4 is adjusted so that the detected temperature of the heating medium thermistor S3 becomes the first heating medium temperature (for example, 80 ° C.). “Gas input” in the figure represents the amount of combustion gas used in the heating medium heating burner g2 in terms of heat (kW). As the heat source machine output (kW), which is the amount of heat output from the heat source machine G, increases, the instantaneous efficiency (the ratio of the heat source machine output to the gas input) increases.

1分30秒経過時点(燃焼開始から1分15秒)の付近で、瞬時効率は平均的に60%を超えるようになる。1分45秒経過時点(燃焼開始から1分30秒)で浴槽戻りサ−ミスタS2の検出温度が目標湯張り温度を超え、熱媒加熱用バーナg2が消火される。その後順次、熱媒循環ポンプP2が2分強経過時点で停止し、浴槽水循環ポンプP1が2分45秒経過時点で停止し、追焚き処理が終了する。追焚き処理に要した時間(熱媒加熱用バーナg2の燃焼時間)は1分15秒であり、瞬時効率が60%を超えていた期間は約15秒間である。   Near 1 minute 30 seconds (1 minute 15 seconds from the start of combustion), the instantaneous efficiency averages over 60%. When 1 minute and 45 seconds have elapsed (1 minute and 30 seconds from the start of combustion), the temperature detected by the bathtub return thermistor S2 exceeds the target hot water filling temperature, and the heating medium heating burner g2 is extinguished. Thereafter, the heat medium circulation pump P2 is stopped at the time when a little over 2 minutes have elapsed, and the bathtub water circulation pump P1 is stopped at the time when 2 minutes and 45 seconds have elapsed, and the chasing process ends. The time required for the chasing process (burning time of the heating medium heating burner g2) is 1 minute 15 seconds, and the period during which the instantaneous efficiency exceeds 60% is about 15 seconds.

図5により、第2追焚き処理に係る風呂装置の運転状態を説明する。8秒経過時点で熱媒流量12L/minで熱媒循環ポンプP2が作動し、併せて浴槽水循環ポンプP1が流量8L/minで作動する。20秒経過時点で熱媒加熱用バーナg2が点火され、熱媒サーミスタS3の検出温度が第2熱媒温度(例えば60℃)になるように、ガス比例弁V4の開度が調整される。   With reference to FIG. 5, the operation state of the bath apparatus according to the second chasing process will be described. When 8 seconds have elapsed, the heat medium circulation pump P2 operates at a heat medium flow rate of 12 L / min, and the bathtub water circulation pump P1 operates at a flow rate of 8 L / min. When 20 seconds have elapsed, the heating medium heating burner g2 is ignited, and the opening of the gas proportional valve V4 is adjusted so that the temperature detected by the heating medium thermistor S3 becomes the second heating medium temperature (for example, 60 ° C.).

1分45秒経過時点(燃焼開始から1分25秒)の付近で、瞬時効率は平均的に60%を超えるようになる。2分40秒経過時点(燃焼開始から2分20秒)で浴槽戻りサ−ミスタS2の検出温度が目標湯張り温度を超え、熱媒加熱用バーナg2が消火される。その後順次、熱媒循環ポンプP2が2分50秒経過時点で停止し、浴槽水循環ポンプP1が3分30秒経過時点で停止し、追焚き処理が終了する。追焚き処理に要した時間(熱媒加熱用バーナg2の燃焼時間)は2分30秒であり、第1追焚き処理に比べ約2倍の時間を要している。また、瞬時効率が60%を超えていた期間は約55秒間であり、第1追焚き処理に比べ大幅に長くなっており、追焚き処理全体の熱効率も約1%向上している。   Near 1 minute 45 seconds (1 minute 25 seconds from the start of combustion), the instantaneous efficiency averages over 60%. When 2 minutes and 40 seconds have elapsed (2 minutes and 20 seconds from the start of combustion), the temperature detected by the bathtub return thermistor S2 exceeds the target hot water filling temperature, and the heating medium heating burner g2 is extinguished. Thereafter, the heat medium circulation pump P2 is stopped when 2 minutes and 50 seconds have elapsed, and the bathtub water circulation pump P1 is stopped when 3 minutes and 30 seconds have elapsed, and the chasing process is completed. The time required for the follow-up process (combustion time of the heating medium heating burner g2) is 2 minutes 30 seconds, which is about twice as long as the first follow-up process. Moreover, the period when the instantaneous efficiency exceeded 60% is about 55 seconds, which is significantly longer than that of the first chasing process, and the thermal efficiency of the chasing process as a whole is improved by approximately 1%.

第1実施形態および第2実施形態では、水位センサS10の検出情報に基づいて、判定処理により浴槽水の水位を決定し、浴槽水の量Lを算出したが、水位センサS10を設けない構成としてもよい。例えば、浴槽水循環ポンプP1を作動させて水流スイッチ41が水流を検出した場合に、自動湯張り運転においてそれまでに浴槽10に供給した湯の合計量をもとめ、当該合計量が現在の浴槽水の量Lであると推定してもよい。   In 1st Embodiment and 2nd Embodiment, based on the detection information of water level sensor S10, the water level of the bathtub water was determined by the determination process, and the amount L of bathtub water was calculated, However As a structure which does not provide the water level sensor S10 Also good. For example, when the bathtub water circulation pump P1 is activated and the water flow switch 41 detects a water flow, the total amount of hot water that has been supplied to the bathtub 10 in the automatic hot water operation is obtained, and the total amount is the current bath water. The quantity L may be estimated.

なお、上記実施形態(別実施形態を含む、以下同じ)で開示される構成は、矛盾が生じない限り、他の実施形態で開示される構成と組み合わせて適用することが可能であり、また、本明細書において開示された実施形態は例示であって、本発明の実施形態はこれに限定されず、本発明の目的を逸脱しない範囲内で適宜改変することが可能である。   Note that the configurations disclosed in the above-described embodiments (including other embodiments, the same applies hereinafter) can be applied in combination with the configurations disclosed in the other embodiments as long as no contradiction arises. The embodiment disclosed in this specification is an exemplification, and the embodiment of the present invention is not limited to this. The embodiment can be appropriately modified without departing from the object of the present invention.

以上説明したように、保温運転における追焚き間隔時間を最適化できるので、エネルギー効率の高い風呂装置として有効に利用することができる。   As described above, since the chasing interval time in the heat retaining operation can be optimized, it can be effectively used as a bath device with high energy efficiency.

10 :浴槽
100 :風呂装置
C :運転制御部
C1 :追焚き回路(熱媒循環回路)
EX3 :主熱交換器(第1熱交換器)
EX4 :副熱交換器(第1熱交換器)
EX5 :追焚き熱交換器(第2熱交換器)
g2 :熱媒加熱用バーナ(燃焼式加熱装置)
L7 :浴槽戻り路(浴槽水循環回路)
L8 :浴槽往き路(浴槽水循環回路)
M1 :追焚き処理手段
M6 :保温運転手段
M7 :追焚き間隔時間変更手段
P1 :浴槽水循環ポンプ(浴槽水循環手段)
P2 :熱媒循環ポンプ(熱媒循環手段)
S2 :浴槽戻りサーミスタ(検出手段)
10: Bathtub 100: Bath apparatus C: Operation control unit C1: Reheating circuit (heat medium circulation circuit)
EX3: Main heat exchanger (first heat exchanger)
EX4: Sub heat exchanger (first heat exchanger)
EX5: Reheating heat exchanger (second heat exchanger)
g2: Heating medium heating burner (combustion heating device)
L7: Bathtub return path (tub water circulation circuit)
L8: Bathtub going way (tub water circulation circuit)
M1: reheating processing means M6: heat insulation operation means M7: reheating interval time changing means P1: bathtub water circulation pump (tub water circulation means)
P2: Heat medium circulation pump (heat medium circulation means)
S2: Bathtub return thermistor (detection means)

Claims (8)

熱媒加熱用の燃焼式加熱装置と、前記燃焼式加熱装置の燃焼により熱媒を加熱する第1熱交換器を有する熱媒循環回路と、浴槽内の浴槽水が循環される浴槽水循環回路と、前記熱媒循環回路を通流する熱媒と前記浴槽水循環回路を通流する浴槽水とを熱交換させて前記浴槽水を加熱する第2熱交換器とを備えた風呂装置において、
前記熱媒循環回路に前記熱媒を循環させる熱媒循環手段と、
前記浴槽水循環回路に前記浴槽水を循環させる浴槽水循環手段と、
追焚き処理指令を受けた際に、前記燃焼式加熱装置と前記熱媒循環手段と前記浴槽水循環手段とを作動させて前記浴槽水を設定温度に加熱する追焚き処理を行う追焚き処理手段と、
前記追焚き処理が終了してから追焚き間隔時間が経過した時点で前記追焚き処理指令を前記追焚き処理手段に送ることにより、前記浴槽水の温度を前記設定温度と前記設定温度より湯温降下限度幅だけ低い下限温度との間に保つ保温運転手段と、
前回の追焚き処理の終了時から前記追焚き間隔時間が経過する間の前記浴槽水の温度の低下率である湯温低下率に基づき、前記浴槽水の温度が前記下限温度まで低下するのに要する下降時間を算出し、前記追焚き間隔時間を前記下降時間または前記下降時間から調整時間幅だけ変更された時間へと変更する追焚き間隔時間変更手段を備えた風呂装置。
Combustion type heating device for heating medium heating, a heat medium circulation circuit having a first heat exchanger that heats the heat medium by combustion of the combustion type heating device, a bathtub water circulation circuit in which bathtub water in the bathtub is circulated, and In the bath apparatus comprising a second heat exchanger that heats the bathtub water by exchanging heat between the heating medium flowing through the heating medium circulation circuit and the bathtub water flowing through the bathtub water circulation circuit,
A heating medium circulating means for circulating the heating medium in the heating medium circulation circuit;
Bathtub water circulation means for circulating the bathtub water to the bathtub water circulation circuit;
When a reheating process command is received, reheating process means for performing a reheating process for operating the combustion heating device, the heat medium circulating means, and the bathtub water circulating means to heat the bathtub water to a set temperature; ,
By sending the follow-up process command to the follow-up processing means when the follow-up interval time has elapsed since the end of the follow-up process, the temperature of the bath water is set to the hot water temperature from the set temperature and the set temperature. Thermal insulation operation means to keep between the lower limit temperature that is lower by the lowering limit width;
Although the temperature of the bath water is reduced to the lower limit temperature based on the hot water temperature decrease rate, which is the rate of decrease in the temperature of the bath water during the elapse of the reheating interval time from the end of the previous reheating process. A bath apparatus provided with a chasing interval time changing means for calculating a descending time required and changing the chasing interval time from the descending time or the descending time to a time changed by an adjustment time width.
前記浴槽内から前記第2熱交換器に戻る浴槽水の温度である浴槽出温度を検出する検出手段を備え、前記追焚き間隔時間変更手段は、前記設定温度と、今回の追焚き処理の開始時に前記検出手段により検出された前記浴槽出温度との差から求められる湯温低下量を、前回の追焚き処理と今回の追焚き処理との時間間隔である追焚き間隔時間で除算して前記湯温低下率を求め、前記湯温降下限度幅を前記湯温低下率で除算して前記下降時間を算出する請求項1に記載の風呂装置。   It has a detecting means for detecting a bath outlet temperature which is a temperature of the bath water returning from the inside of the bathtub to the second heat exchanger, and the reheating interval time changing means is configured to start the reheating process at the set temperature and the current reheating process. The amount of decrease in hot water temperature obtained from the difference from the bath temperature detected by the detection means is sometimes divided by the reheating interval time, which is the time interval between the previous reheating process and the current reheating process. The bath apparatus according to claim 1, wherein a hot water temperature decrease rate is obtained, and the descending time is calculated by dividing the hot water temperature decrease limit width by the hot water temperature decrease rate. 前記追焚き処理手段は、前記追焚き処理指令を受けた際、前記浴槽水循環手段を作動させ、前記検出手段による前記浴槽出温度の測定が完了した後に前記燃焼式加熱装置と前記熱媒循環手段とを作動させる請求項2に記載の風呂装置。   The reheating processing means operates the bath water circulation means when receiving the reheating processing command, and after the measurement of the bath outlet temperature by the detection means is completed, the combustion heating device and the heating medium circulation means The bath apparatus according to claim 2 which operates. 前記追焚き間隔時間変更手段が前記追焚き間隔時間を前記下降時間に調整時間幅を加算した時間へと変更する請求項1〜3のいずれか一項に記載の風呂装置。   The bath apparatus according to any one of claims 1 to 3, wherein the chasing interval time changing unit changes the chasing interval time to a time obtained by adding an adjustment time width to the descending time. 前記追焚き間隔時間変更手段が前記追焚き間隔時間を前記下降時間から調整時間幅を減算した時間へと変更する請求項1〜3のいずれか一項に記載の風呂装置。   The bath apparatus according to any one of claims 1 to 3, wherein the chasing interval time changing unit changes the chasing interval time to a time obtained by subtracting an adjustment time width from the descending time. 前記追焚き処理手段は、所定の第1熱媒温度に前記熱媒を加熱して浴槽水を追焚きする第1追焚き処理と、前記第1追焚き処理に要する時間よりも長くかつ最長追焚き時間と同じかより短い時間で追焚き処理が完了する第2熱媒温度を決定し、前記第2熱媒温度に前記熱媒を加熱して浴槽水を追焚きする第2追焚き処理とを選択的に行う、請求項1〜5のいずれか一項に記載の風呂装置。   The reheating processing means includes a first reheating process that heats the heat medium to a predetermined first heat medium temperature to retreat the bath water, and a longest additional time that is longer than the time required for the first reheating process. A second heating process for determining a second heating medium temperature at which the heating process is completed in a time shorter than or equal to the burning time, and heating the heating medium to the second heating medium temperature to track the bath water; The bath apparatus according to any one of claims 1 to 5, which is selectively performed. 前記追焚き処理手段は、前記第1追焚き処理に要する時間よりも長くかつ前記最長追焚き時間と同じかより短い時間である第2追焚き時間で追焚き処理が完了する第2熱媒温度を決定するにあたり、浴槽水を追焚き完了温度に加熱するために要する必要投入熱量を前記第2追焚き時間で除算することで求められる毎時投入熱量に基づいて前記第2熱媒温度を決定する、請求項6に記載の風呂装置。   The second heating medium temperature at which the tracking process is completed in a second tracking time that is longer than the time required for the first tracking process and equal to or shorter than the longest tracking time. The second heating medium temperature is determined based on the hourly input heat amount obtained by dividing the required input heat amount required for heating the bath water to the completion temperature by dividing by the second additional time. The bath apparatus according to claim 6. 前記追焚き処理手段は、前記第1熱媒温度よりも低い第3熱媒温度に熱媒を加熱して浴槽水を追焚きした場合に追焚き処理に要する時間を算出し、当該時間が前記最長追焚き時間と同じかより短い場合は前記第3熱媒温度を前記第2熱媒温度に決定して前記第2追焚き処理を行い、当該時間が前記最長追焚き時間より長い場合は、前記最長追焚き時間で追焚き処理が完了する熱媒の温度を前記第2熱媒温度に決定して前記第2追焚き処理を行う、請求項6に記載の風呂装置。   The reheating processing means calculates a time required for the reheating process when the heat medium is heated to a third heat medium temperature lower than the first heat medium temperature and the bath water is reheated, and the time is When it is the same as or shorter than the longest chasing time, the third heat medium temperature is determined as the second heat medium temperature and the second chasing process is performed, and when the time is longer than the longest chasing time, The bath apparatus according to claim 6, wherein the temperature of the heat medium that completes the chasing process in the longest chasing time is determined as the second heating medium temperature, and the second chasing process is performed.
JP2014208177A 2014-10-09 2014-10-09 Bath device Pending JP2016080186A (en)

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JP2010054127A (en) * 2008-08-28 2010-03-11 Osaka Gas Co Ltd Heat utilization equipment and heat source machine
JP2010210227A (en) * 2009-07-14 2010-09-24 Panasonic Corp Water heater
JP2013210176A (en) * 2012-03-30 2013-10-10 Osaka Gas Co Ltd Heat supply system

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009097730A (en) * 2007-10-12 2009-05-07 Kyuhen Co Ltd Automatic reheating device using hot water storage type water heater
JP2010054127A (en) * 2008-08-28 2010-03-11 Osaka Gas Co Ltd Heat utilization equipment and heat source machine
JP2010210227A (en) * 2009-07-14 2010-09-24 Panasonic Corp Water heater
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