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JP6653079B2 - Water heater - Google Patents
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JP6653079B2 - Water heater - Google Patents

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JP6653079B2
JP6653079B2 JP2016013853A JP2016013853A JP6653079B2 JP 6653079 B2 JP6653079 B2 JP 6653079B2 JP 2016013853 A JP2016013853 A JP 2016013853A JP 2016013853 A JP2016013853 A JP 2016013853A JP 6653079 B2 JP6653079 B2 JP 6653079B2
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hot water
temperature
water temperature
flow rate
water supply
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JP2017133756A (en
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徳 岩崎
徳 岩崎
俊彦 ▲はま▼上
俊彦 ▲はま▼上
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Noritz Corp
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Description

本発明は、給湯温度を設定温度に保つためにフィードフォワード制御およびフィードバック制御を組み合わせて制御を行う給湯装置に関する。   The present invention relates to a hot water supply apparatus that performs control by combining feedforward control and feedback control to maintain a hot water supply temperature at a set temperature.

従来から、給湯装置において、設定温度の湯水が給湯されるように、設定温度に対する出湯温度の偏差に基づくフィードバック制御(FB制御)に加えて、設定温度と入水温度の差温に基づくフィードフォワード制御(FF制御)を組み合わせる湯温制御が行われている。   2. Description of the Related Art Conventionally, in a hot water supply apparatus, in addition to feedback control (FB control) based on a deviation of a tapping temperature from a set temperature, feedforward control based on a difference temperature between a set temperature and an incoming water temperature so that hot water at a set temperature is supplied. Hot water temperature control combined with (FF control) is performed.

例えば特許文献1には、入水温度と出湯温度の差温と流量から出力熱量を算出し、設定温度の湯水を出湯するために必要な熱量に対する出力熱量の比に基づいて演算係数を学習し、この演算係数に基づくFF制御およびFB制御を組み合わせて加熱手段の出力を調節する湯温制御を行う給湯装置が記載されている。   For example, in Patent Literature 1, an output heat amount is calculated from a difference temperature between an inlet water temperature and a tap water temperature and a flow rate, and an operation coefficient is learned based on a ratio of an output heat amount to a heat amount required for tapping hot water at a set temperature. A hot water supply apparatus that performs hot water temperature control that adjusts the output of a heating unit by combining FF control and FB control based on this calculation coefficient is described.

特開2014−137206号公報JP 2014-137206 A

しかし、入水温度が急激に変動した場合には、演算係数への入水温度の変動の反映が遅れ、給湯装置から出湯される湯水の温度が変動し、設定温度の湯水を出湯できない虞がある。例えば、入水温度が高温から低温へと急激に低下すると、給湯装置内に高温の湯水が残存しているにもかかわらず加熱手段の出力を増加させて加熱するので、高温の湯水が過度に加熱されて出湯温度が高温になる。すると給湯装置の安全動作により加熱手段が停止されるので、高温の湯水に続いて低温の湯水が出湯されることとなり、出湯温度が安定せず好ましくない。   However, when the incoming water temperature fluctuates sharply, the variation of the incoming water temperature in the operation coefficient is delayed, and the temperature of the hot water discharged from the hot water supply device fluctuates, and there is a possibility that the hot water at the set temperature cannot be discharged. For example, when the incoming water temperature suddenly drops from high temperature to low temperature, the output of the heating means is increased to heat the hot water even though the hot water remains in the water heater, so that the hot water is excessively heated. And the tapping temperature rises. Then, since the heating means is stopped by the safe operation of the hot water supply device, low-temperature hot water is discharged following high-temperature hot water, and the hot water temperature is not stable, which is not preferable.

一方、入水温度が低温から高温へと急激に上昇すると、給湯装置内に低温の湯水が残存しているにもかかわらず加熱手段の出力を減少させて加熱するので、低温の湯水の加熱量が不足し出湯温度が低温になる。すると、出湯温度の低下を補うために加熱手段の出力を増加させて加熱するので、入水した高温の湯水が過度に加熱され、給湯装置に残存していた低温の湯水に続いて高温の湯水が出湯されることとなり、出湯温度が安定せず好ましくない。   On the other hand, if the incoming water temperature rises sharply from low to high temperatures, the output of the heating means is reduced and heating is performed despite the low-temperature hot water remaining in the hot-water supply device. Insufficient and the tapping temperature becomes low. Then, since the output of the heating means is increased and the heating is performed to compensate for the drop in the hot water temperature, the incoming high-temperature hot water is excessively heated, and the high-temperature hot water remaining in the hot water supply device is followed by the high-temperature hot water. Hot water is to be discharged, and the hot water temperature is not stable, which is not preferable.

本発明の目的は、入水温度が急激に変動した場合においても、出湯温度を安定させることが可能な給湯装置を提供することである。   An object of the present invention is to provide a hot water supply device capable of stabilizing a tap water temperature even when the incoming water temperature fluctuates rapidly.

第1の発明の給湯装置は、燃焼部で生じた燃焼ガスによって内部を流れる湯水を加熱するための熱交換器と、前記熱交換器に導入される入水温度を検知するための入水温度検知手段と、前記熱交換器から出湯される出湯温度を検知するための出湯温度検知手段と、前記熱交換器を通過する湯水の流量を検知するための流量検知手段と、これらの検知手段によって検知された入水温度、出湯温度、流量および給湯設定温度に基づいて所定周期ごとに前記燃焼部における必要発生熱量を制御する制御手段を備え、前記制御手段は、前記入水温度と前記出湯温度との差温と前記流量より出力熱量を算出し、前記必要発生熱量に対する前記出力熱量の比に基づいて演算係数を学習する学習手段と、前記給湯設定温度と前記入水温度との差温と前記流量と前記演算係数とに基づいて第1の必要発生熱量を算出するフィードフォワード制御手段と、前記給湯設定温度と前記出湯温度との差温と前記流量と前記演算係数とに基づいて第2の必要発生熱量を算出するフィードバック制御手段と、前記第1の必要発生熱量と前記第2の必要発生熱量とを加算して前記必要発生熱量を設定する加算手段とを有し、前記学習手段は、前記所定周期における入水温度の変化率が所定範囲外の場合には前記演算係数を初期値に戻すことを特徴としている。 A hot water supply apparatus according to a first aspect of the present invention includes a heat exchanger for heating hot water flowing inside by a combustion gas generated in a combustion section, and an input water temperature detecting means for detecting an input water temperature introduced into the heat exchanger. Hot water temperature detecting means for detecting the temperature of hot water discharged from the heat exchanger; flow rate detecting means for detecting the flow rate of hot water passing through the heat exchanger; and Control means for controlling the required amount of heat generated in the combustion unit at predetermined intervals based on the incoming water temperature, the hot water temperature, the flow rate and the hot water set temperature, and the control means includes a difference between the incoming water temperature and the hot water temperature. Learning means for calculating an output heat quantity from the temperature and the flow rate, and learning an operation coefficient based on a ratio of the output heat quantity to the required generated heat quantity, a difference temperature between the hot water supply set temperature and the incoming water temperature, and the flow rate Feedforward control means for calculating a first required heat quantity based on the calculation coefficient; and a second necessary generation based on the difference between the hot water supply set temperature and the tapping temperature, the flow rate, and the calculation coefficient. a feedback control means for calculating the amount of heat, and the first required heat generation amount and the second required amount of heat generated and adding means for setting the required amount of heat generated by adding the learning means, the predetermined When the rate of change of the incoming water temperature in a cycle is out of a predetermined range, the operation coefficient is returned to an initial value.

第2の発明の給湯装置は、第1の発明において前記給湯装置は即湯運転可能に構成されたことを特徴としている。   A hot water supply apparatus according to a second invention is characterized in that in the first invention, the hot water supply apparatus is configured to be able to operate immediately.

第1の発明の給湯装置によれば、入水温度の急激な変動により入水温度の所定周期における変化率が所定範囲外となった場合には、逐次更新される演算係数を初期値に戻して必要発生熱量を制御する湯温制御を行うことにより、出湯温度の変動を抑制して安定した温度の湯水を出湯することができる。 According to the hot water supply apparatus of the first invention, when the rate of change of the incoming water temperature in a predetermined cycle is out of the predetermined range due to a rapid change of the incoming water temperature, it is necessary to return the operation coefficient that is sequentially updated to the initial value. By performing hot water temperature control for controlling the amount of generated heat, fluctuations in the hot water temperature can be suppressed, and hot and cold water can be discharged at a stable temperature.

第2の発明の給湯装置によれば、給湯装置が即湯運転可能に構成されたので、即湯運転中に給湯栓等から給湯されて低温の上水が給湯装置に入水した場合や、即湯運転の開始により低温の湯水から加熱されて高温になった湯水が再び給湯装置に入水した場合に入水温度の変動が大きくなるが、所定周期における入水温度の変化率が所定範囲外であれば演算係数を初期値に戻して湯温制御を行うので、出湯温度の変動を抑制して安定した温度の湯水を出湯することができる。 According to the hot water supply apparatus of the second invention, since the hot water supply apparatus is configured to be capable of quick hot water operation, when hot water is supplied from a hot water tap or the like during the hot water operation and low-temperature water flows into the hot water supply apparatus, Although variations in the incoming water temperature when the hot water in which the start of the hot water operation is heated from a low temperature of hot water heated to a high temperature is drowned again water heater is increased, the rate of change of the incoming water temperature in a given period if out of the predetermined range Since the hot water temperature control is performed by returning the operation coefficient to the initial value, it is possible to control the fluctuation of the hot water temperature and to supply hot and cold water at a stable temperature.

本発明の給湯装置を有する即湯循環システムの概略構成図である。It is a schematic structure figure of an instant hot water circulation system which has a hot water supply device of the present invention. 本発明の給湯装置における湯温制御を説明するための機能ブロック図である。It is a functional block diagram for explaining hot water temperature control in the hot water supply device of the present invention. 演算係数の重み付けパラメータと流量との関係を概略的に示す図である。It is a figure which shows roughly the relationship between the weight parameter of an operation coefficient, and a flow volume. 湯温制御の処理手順を示すフローチャートである。It is a flowchart which shows the processing procedure of hot water temperature control. 本実施例に係る給湯装置の湯温制御の1例を示す図である。It is a figure showing an example of hot water temperature control of the hot water supply device concerning this example. 即湯運転開始時の湯水の昇温制御を示すフローチャートである。It is a flowchart which shows the temperature rise control of hot water at the time of the start of a hot water operation.

以下、本発明を実施するための形態について実施例に基づいて説明する。   Hereinafter, embodiments for carrying out the present invention will be described based on examples.

図1に示すように、即湯循環システム1は、給湯装置2と、給湯装置2に湯水を供給する入水通路3と、給湯装置2で加熱された湯水が出湯される出湯通路4と、出湯通路4を流れる湯水を入水通路3を経由して給湯装置2に送る循環ポンプ5とを備え、給湯装置2から出湯された湯水が給湯装置2に再入水可能な循環通路6が形成されている。   As shown in FIG. 1, the hot water circulation system 1 includes a hot water supply device 2, a water supply passage 3 for supplying hot water to the hot water supply device 2, a hot water supply passage 4 from which the hot water heated by the hot water supply device 2 is supplied, A circulation pump 5 that sends hot water flowing through the passage 4 to the hot water supply device 2 via the water inlet passage 3; and a circulation passage 6 that allows hot water discharged from the hot water supply device 2 to re-enter the hot water supply device 2 is formed. .

入水通路3には、入水通路3を介して上水を給湯装置2に供給する給水通路7と、循環する湯水の熱膨張を吸収する膨張タンク8が接続され、循環する湯水に混ざったエアを分離するエアセパレータ9と逆流を防ぐ逆止弁10が備えられている。給水通路7には、入水通路3を流れる湯水が給水通路7に逆流することを防ぐ逆止弁11が設けられている。出湯通路4には、給湯栓Fが設けられている。給湯栓Fは1つでもよく複数設けられていてもよい。   The water inlet passage 3 is connected to a water supply passage 7 for supplying tap water to the hot water supply device 2 through the water inlet passage 3 and an expansion tank 8 for absorbing thermal expansion of the circulating hot water. An air separator 9 to be separated and a check valve 10 for preventing backflow are provided. The water supply passage 7 is provided with a check valve 11 for preventing hot water flowing through the water inlet passage 3 from flowing back to the water supply passage 7. A hot water tap F is provided in the hot water passage 4. One or a plurality of hot water taps F may be provided.

給湯装置2は、加熱通路12と、バーナ13と、熱交換器14と、ガス比例弁15と、出湯流量調整弁16と、制御ユニット17(制御手段に相当する)とを含む。   Hot water supply device 2 includes a heating passage 12, a burner 13, a heat exchanger 14, a gas proportional valve 15, a tap water flow control valve 16, and a control unit 17 (corresponding to control means).

加熱通路12は、上流端が入水通路3に接続され、下流端が出湯通路4に接続され、入水通路3から供給されて熱交換器14において加熱された湯水を出湯通路4に出湯する。出湯流量調整弁16は、制御ユニット17により開度を調整することによって、出湯流量を制御することができる。   The heating passage 12 has an upstream end connected to the inlet passage 3, a downstream end connected to the outlet passage 4, and supplies hot water supplied from the inlet passage 3 and heated in the heat exchanger 14 to the outlet passage 4. The tapping flow rate adjusting valve 16 can control the tapping flow rate by adjusting the opening degree by the control unit 17.

バーナ13は、図示しないガス配管から供給された燃料ガスと、図示しない燃焼ファンから供給された空気との混合気を燃焼部で燃焼させることによって、高温の燃焼ガスを発生させる。バーナ13に供給される燃料ガス供給量は、制御ユニット17によるガス比例弁15の開度の調節により制御される。燃焼ファンから供給される空気の量は、バーナ13での燃焼における空燃比が一定となるように制御される。   The burner 13 generates a high-temperature combustion gas by burning a mixture of fuel gas supplied from a gas pipe (not shown) and air supplied from a combustion fan (not shown) in a combustion section. The amount of fuel gas supplied to the burner 13 is controlled by adjusting the opening of the gas proportional valve 15 by the control unit 17. The amount of air supplied from the combustion fan is controlled so that the air-fuel ratio in combustion in the burner 13 is constant.

熱交換器14は、バーナ13での燃焼により発生した高温の燃焼ガスと加熱通路12を流れる湯水との間で熱交換させて湯水を加熱する。   The heat exchanger 14 heats hot water by exchanging heat between high-temperature combustion gas generated by combustion in the burner 13 and hot water flowing through the heating passage 12.

加熱通路12には、流量センサ18(流量検知手段に相当する)と、入水温度センサ19(入水温度検知手段に相当する)と、出湯温度センサ20(出湯温度検知手段に相当する)が設けられている。流量センサ18によって、加熱通路12の流量Qが検知される。入水温度センサ19は、熱交換器14の上流側に設けられて、入水温度Tcを検知する。出湯温度センサ20は、熱交換器14の下流側に設けられて、出湯温度Thを検知する。検知された流量Q、入水温度Tcおよび出湯温度Thは、制御ユニット17に送信される。   The heating passage 12 is provided with a flow rate sensor 18 (corresponding to flow rate detecting means), an incoming water temperature sensor 19 (corresponding to incoming water temperature detecting means), and a tapping temperature sensor 20 (corresponding to tapping temperature detecting means). ing. The flow rate Q of the heating passage 12 is detected by the flow rate sensor 18. The incoming water temperature sensor 19 is provided upstream of the heat exchanger 14 and detects the incoming water temperature Tc. Hot water temperature sensor 20 is provided downstream of heat exchanger 14, and detects hot water temperature Th. The detected flow rate Q, incoming water temperature Tc, and outgoing water temperature Th are transmitted to the control unit 17.

制御ユニット17は、操作リモコン21の操作等により設定した設定温度Trに従って出湯温度Thを制御するための湯温制御を実行する。詳しくは、制御ユニット17は、湯温制御のためにバーナ13で発生させる必要発生熱量を算出すると共に、この必要発生熱量に従ってガス比例弁15の開度を調節する。ガス比例弁15の開度の調節によりバーナ13での発生熱量が変化すると、熱交換器14を介して水温上昇に寄与する熱量が変化するので、出湯温度Thが変化する。   The control unit 17 executes hot water temperature control for controlling the hot water temperature Th according to the set temperature Tr set by operating the operation remote controller 21 or the like. More specifically, the control unit 17 calculates the required amount of heat generated by the burner 13 for controlling the hot water temperature, and adjusts the opening of the gas proportional valve 15 according to the required amount of generated heat. When the amount of heat generated in the burner 13 changes due to the adjustment of the opening of the gas proportional valve 15, the amount of heat contributing to an increase in water temperature via the heat exchanger 14 changes, so that the tapping temperature Th changes.

図2に示すように、制御ユニット17は、演算係数Rを学習する学習手段22と、フィードフォワード制御手段23(FF制御手段23)と、フィードバック制御手段24(FB制御手段24)と、加算手段25とを有し、各手段の演算により必要発生熱量Utlを設定する。一般的に給湯装置では、必要発生熱量Utlは号数を単位として演算される。号数1は、Q=1(L/min)の流量下で湯温を25℃上昇させるのに必要な熱量に相当する。従って、以下必要発生熱量を入力号数と呼ぶこともある。   As shown in FIG. 2, the control unit 17 includes a learning unit 22 for learning the operation coefficient R, a feedforward control unit 23 (FF control unit 23), a feedback control unit 24 (FB control unit 24), and an addition unit. The required heat quantity Utl is set by calculation of each means. Generally, in a hot water supply device, the required generated heat amount Utl is calculated in units of the number of units. The number 1 corresponds to the amount of heat required to raise the hot water temperature by 25 ° C. under the flow rate of Q = 1 (L / min). Therefore, the required amount of generated heat may be hereinafter referred to as the input number.

制御ユニット17は、設定温度Trに従って出湯温度Thを制御するように、入力号数Utlを設定する。設定された入力号数Utlに従って、給湯装置2のバーナ13への燃料ガスの供給量が制御され、バーナ13で発生する熱量が制御される。   The control unit 17 sets the input number Utl so as to control the tapping temperature Th according to the set temperature Tr. In accordance with the set input number Utl, the amount of fuel gas supplied to the burner 13 of the water heater 2 is controlled, and the amount of heat generated by the burner 13 is controlled.

学習手段22は、流量センサ18によって検知された流量Qと、入水温度センサ19によって検知された入水温度Tcと、出湯温度センサ20によって検知された出湯温度Thと、入力号数Utlとに基づいて、演算係数Rを学習する。   The learning means 22 is based on the flow rate Q detected by the flow rate sensor 18, the incoming water temperature Tc detected by the incoming water temperature sensor 19, the tap water temperature Th detected by the tap water temperature sensor 20, and the input number Utl. , The operation coefficient R is learned.

演算係数Rは、必要発生熱量Utlに対する、加熱された湯水の上昇温度(Th−Tc)と流量Qの積で表される出力熱量の比(出力熱量実績比)Krに相当する。Krは、下記(1)式によって定義される。   The calculation coefficient R corresponds to a ratio of the output heat amount (the output heat amount actual ratio) Kr to the required generated heat amount Utl, which is represented by the product of the temperature of the heated hot water (Th-Tc) and the flow rate Q. Kr is defined by the following equation (1).


この出力熱量実績比Krは上述した号数の定義から理想的には25である。しかし、ガス比例弁15における調節のずれや入水温度の状態等に応じて、出力熱量実績比Krは25から変動する。例えば、入水温度が高温の場合には、熱交換器14における熱交換効率が所期の熱交換効率より低下するため、出力熱量実績比Krは25より小さくなる。   The actual output heat amount ratio Kr is ideally 25 from the definition of the number described above. However, the output calorific value actual ratio Kr fluctuates from 25 in accordance with the adjustment deviation in the gas proportional valve 15, the state of the incoming water temperature, and the like. For example, when the incoming water temperature is high, the heat exchange efficiency in the heat exchanger 14 is lower than the expected heat exchange efficiency, and the actual output heat amount ratio Kr is smaller than 25.

学習手段22は、一定の制御周期Δt毎、例えば100ms毎に下記(2)式に従って演算係数Rを学習する。(2)式において、R(n)は、第n番目の制御周期での学習結果に基づいて算出された学習値であり、R(n−1)は、1周期前の第(n−1)番目の制御周期で算出された学習値である。パラメータLは、1周期前の演算係数R(n−1)と今回検知された流量Q(n)等から算出される現在の出力熱量実績比Krとに重み付けするパラメータである。   The learning means 22 learns the operation coefficient R in accordance with the following equation (2) at every fixed control period Δt, for example, at every 100 ms. In equation (2), R (n) is a learning value calculated based on the learning result in the n-th control cycle, and R (n-1) is the (n-1) -th cycle previous. ) Is the learning value calculated in the control cycle. The parameter L is a parameter that weights the operation coefficient R (n−1) one cycle before and the current output calorie actual ratio Kr calculated from the flow rate Q (n) detected this time and the like.


図3に示すように、パラメータLは、小流量時には大きい値に設定され、流量Qが大きくなるにつれて小さい値になるように設定される。流量Qが大きい場合には出力熱量の挙動が安定するので、1周期前の演算係数R(n−1)よりも現在の出力熱量実績比が演算係数R(n)に反映されるように、パラメータLにより重み付けされる。流量Qが小さい場合には出力熱量が変動し易いため、現在の出力熱量実績比よりも1周期前の演算係数R(n−1)が演算係数R(n)に反映されるようにパラメータLにより重み付けされる。パラメータLは、実機実験やシミュレーションによって、図3の特性を予め設定することができる。図3の特性に従って、流量QからパラメータLを求める関数式やテーブルを予め作成してもよい。   As shown in FIG. 3, the parameter L is set to a large value when the flow rate is small, and is set to be a small value as the flow rate Q increases. When the flow rate Q is large, the behavior of the output heat amount is stable, so that the current output heat amount actual ratio is reflected in the operation coefficient R (n) rather than the operation coefficient R (n-1) one cycle before. Weighted by the parameter L. When the flow rate Q is small, the output calorie tends to fluctuate. Therefore, the parameter L (n-1) is calculated so that the computation coefficient R (n-1) one cycle earlier than the current actual output calorie ratio is reflected in the computation coefficient R (n). Weighted by As the parameter L, the characteristics shown in FIG. 3 can be set in advance by actual machine experiments or simulations. According to the characteristics shown in FIG. 3, a function formula or a table for obtaining the parameter L from the flow rate Q may be created in advance.

FF制御手段23は、設定温度Tr(n)と入水温度Tc(n)の差温と、流量Q(n)と、学習手段22により算出された学習値R(n)とに基づいて、FF制御による入力号数Uff(n)(第1の必要発生熱量に相当する)を算出する。FF制御による入力号数Uff(n)は、給湯装置2の入水量(流量Q(n))を、入水温度Tc(n)から設定湯温Tr(n)まで変化させるために必要な号数を表す。   The FF control unit 23 determines the FF based on the difference between the set temperature Tr (n) and the incoming water temperature Tc (n), the flow rate Q (n), and the learning value R (n) calculated by the learning unit 22. The number of inputs Uff (n) (corresponding to the first necessary heat generation) by the control is calculated. The input number Uff (n) by the FF control is the number required to change the water input amount (flow rate Q (n)) of the hot water supply device 2 from the input water temperature Tc (n) to the set hot water temperature Tr (n). Represents


FB制御手段24は、下記(4)式に従って、設定温度Tr(n)と出湯温度Th(n)の差温と、流量Q(n)と、学習手段22により算出された学習値R(n)とに基づいて、FB制御による入力号数Ufb(n)(第2の必要発生熱量に相当する)を算出する。FB制御による入力号数Ufb(n)は、給湯装置2の入水量(流量Q(n))を、差温(Tr(n)−Th(n))だけ変化させるために必要な号数を表す。尚、Kpは給湯装置毎に設定される比例ゲインである。   The FB control means 24 calculates the difference between the set temperature Tr (n) and the tapping temperature Th (n), the flow rate Q (n), and the learning value R (n) calculated by the learning means 22 according to the following equation (4). ), The input number Ufb (n) (corresponding to the second necessary heat generation) by the FB control is calculated. The input number Ufb (n) by the FB control is the number required to change the water input amount (flow rate Q (n)) of the hot water supply device 2 by the difference temperature (Tr (n) -Th (n)). Represent. Kp is a proportional gain set for each water heater.


加算手段25は、下記(5)式に従って、FF制御手段23により算出されたFF制御による入力号数Uff(n)と、FB制御手段24により算出されたFB制御による入力号数Ufb(n)を加算することによって、給湯装置2の入力号数Utl(n)を設定する。
Utl(n)=Uff(n)+Ufb(n) ・・・(5)
The adding means 25 calculates the input number Uff (n) of the FF control calculated by the FF control means 23 and the input number Ufb (n) of the FB control calculated by the FB control means 24 according to the following equation (5). Are added to set the input number Utl (n) of the hot water supply apparatus 2.
Utl (n) = Uff (n) + Ufb (n) (5)

制御ユニット17による湯温制御において、入力号数Utlの設定は所定の制御周期Δt毎、例えばΔt=100ms毎に行われる。図4に示すように、第n番目の制御周期における処理では、入力号数Utl(n)の設定が行われる。尚、Sm(m=1,2・・・)は各ステップを表す。   In the hot water temperature control by the control unit 17, the input number Utl is set every predetermined control period Δt, for example, every Δt = 100 ms. As shown in FIG. 4, in the process in the n-th control cycle, the number of input signals Utl (n) is set. Sm (m = 1, 2,...) Represents each step.

まず、S1において、流量センサ18、入水温度センサ19、出湯温度センサ20により検知された今回(第n番目)の制御周期における流量Q(n)、入水温度Tc(n)、出湯温度Th(n)、設定湯温Tr(n)等の必要なデータを取得する。   First, in S1, the flow rate Q (n), the incoming water temperature Tc (n), and the outgoing water temperature Th (n) in the current (n-th) control cycle detected by the flow rate sensor 18, the incoming water temperature sensor 19, and the outgoing water temperature sensor 20 are described. ), Necessary data such as the set hot water temperature Tr (n) is acquired.

次に、S2において、入水温度Tc(n)の変化率が所定の範囲内であるか否か判定する。例えば、今回の入水温度Tc(n)と前回の入水温度Tc(n−1)の差温が所定の範囲内か否か判定する。制御周期が予め定まっているので、ここでは差温を変化率とみなすことができる。判定がYesの場合にはS3に進み、判定がNoの場合にはS4に進む。所定の範囲内とは、例えば、下記(6)式で表される範囲である。尚、(6)式で表される範囲は制御周期Δtや給湯装置2の仕様等に応じて適宜設定される。
−10℃≦(Tc(n)−Tc(n−1))≦10℃ ・・・(6)
Next, in S2, it is determined whether or not the rate of change of the incoming water temperature Tc (n) is within a predetermined range. For example, it is determined whether or not the difference between the current incoming water temperature Tc (n) and the previous incoming water temperature Tc (n-1) is within a predetermined range. Since the control cycle is predetermined, the temperature difference can be regarded as the rate of change here. When the determination is Yes, the process proceeds to S3, and when the determination is No, the process proceeds to S4. The predetermined range is, for example, a range represented by the following equation (6). The range represented by the expression (6) is appropriately set according to the control cycle Δt, the specifications of the hot water supply device 2, and the like.
−10 ° C. ≦ (Tc (n) −Tc (n−1)) ≦ 10 ° C. (6)

次に、S3において、上記(2)式に従って、学習手段22により現在の演算係数R(n)を算出し、S5に進む。尚、演算係数R(n)の初期値は、号数の定義に沿ってR(0)=25とすることができる。   Next, in S3, the current operation coefficient R (n) is calculated by the learning means 22 according to the above equation (2), and the flow proceeds to S5. The initial value of the operation coefficient R (n) can be set to R (0) = 25 according to the definition of the number.

一方、S2の判定がNoの場合にはS4において、演算係数R(n)を初期値25に設定し、S5に進む。   On the other hand, if the determination in S2 is No, in S4, the operation coefficient R (n) is set to the initial value 25, and the process proceeds to S5.

次に、S5において、上記(3)式に従って、S3またはS4で設定された演算係数R(n)を反映したFF制御を実行し、FF制御による入力号数Uff(n)を算出してS6に進む。   Next, in S5, FF control reflecting the operation coefficient R (n) set in S3 or S4 is executed in accordance with the above equation (3), and the number of input signals Uff (n) by FF control is calculated. Proceed to.

次に、S6において、上記(4)式に従って、S3またはS4で設定された演算係数R(n)を反映したFB制御を実行し、FB制御による入力号数Ufb(n)を算出してS7に進む。   Next, in S6, FB control reflecting the operation coefficient R (n) set in S3 or S4 is executed according to the above equation (4), and the number of input signals Ufb (n) by FB control is calculated. Proceed to.

次に、S7において、上記(5)式に従って、今回(第n番目)の制御周期における給湯装置2の入力号数Utl(n)を設定する。   Next, in S7, the input number Utl (n) of the water heater 2 in the current (n-th) control cycle is set according to the above equation (5).

次に、本発明の給湯装置2の作用および効果について説明する。
図5に示すように、設定温度Tr=75℃の湯水を給湯可能なように循環流量Q=8L/minで即湯運転を実行している即湯循環システム1において、例えば経過時間t=110sでは、入水温度Tc=72℃程度、出湯温度Th=83℃程度で安定し、演算係数R(n)=20程度である。尚、実線は本発明の給湯装置2による値を表し、破線および1点鎖線は特許文献1に記載の従来の給湯装置による値を表す。従来の給湯装置は、上述の湯温制御以外は本発明の給湯装置と同等の構成を有する。
Next, the operation and effect of the hot water supply device 2 of the present invention will be described.
As shown in FIG. 5, in the instant hot water circulation system 1 in which the hot water operation is executed at the circulation flow rate Q = 8 L / min so that hot water at the set temperature Tr = 75 ° C. can be supplied, for example, the elapsed time t = 110 s Is stable at the inlet water temperature Tc = about 72 ° C. and the tap water temperature Th = about 83 ° C., and the calculation coefficient R (n) = about 20. Note that a solid line represents a value obtained by the hot water supply device 2 of the present invention, and a broken line and a dashed line represent values obtained by the conventional hot water supply device described in Patent Document 1. The conventional hot water supply device has the same configuration as the hot water supply device of the present invention except for the above-described hot water temperature control.

経過時間t=127s付近で給湯栓F等から給湯されて約15℃の上水が給湯装置2に入水すると、入水温度Tcが低下する。この入水温度Tcの変化率が所定範囲外の場合、例えば−10℃/100msより急激に入水温度Tcが低下した場合には、演算係数R(n)を初期値に戻す。ここでは入水温度Tcの変化率は−11℃/100ms程度で所定範囲外なので、演算係数R(n)を25に設定する。   When hot water of about 15 ° C. is supplied from the hot-water tap F or the like to the hot water supply device 2 around the elapsed time t = 127 s, the incoming water temperature Tc decreases. When the rate of change of the incoming water temperature Tc is out of the predetermined range, for example, when the incoming water temperature Tc drops sharply from −10 ° C./100 ms, the operation coefficient R (n) is returned to the initial value. Here, the change rate of the incoming water temperature Tc is about −11 ° C./100 ms, which is out of the predetermined range, so that the calculation coefficient R (n) is set to 25.

入力号数Utl(n)は上記(2)〜(5)式に基づいて設定されるので、演算係数R(n)を初期値に戻したことにより所期の熱交換効率が反映された入力号数Utl(n)が設定される。従って、入水温度が急激に低下した場合でも、湯温制御による入力号数Utl(n)が必要以上に大きくなることがないので、経過時間t=127s以降において出湯温度Thが高くなって安全動作によりバーナ13を停止させることがなく、出湯温度Thの過度の降温が発生することがない。即ち、本発明の給湯装置2によれば、安定した温度で出湯が可能である。   Since the input number Utl (n) is set based on the above equations (2) to (5), the input reflecting the desired heat exchange efficiency by returning the operation coefficient R (n) to the initial value. The number Utl (n) is set. Therefore, even if the incoming water temperature drops rapidly, the input signal number Utl (n) by the hot water temperature control does not become unnecessarily large, so that the outgoing water temperature Th becomes high after the elapsed time t = 127 s and the safe operation is performed. As a result, the burner 13 is not stopped, and an excessive temperature drop of the tapping temperature Th does not occur. That is, according to the hot water supply device 2 of the present invention, hot water can be discharged at a stable temperature.

一方、従来の給湯装置では入水温度Tcの急激な低下が演算係数R(n)にすぐに反映されず、経過時間t=140s付近まで急激に上昇している。この演算係数R(n)には低下した熱交換効率が反映されているので、演算係数R(n)に基づいて低温の湯水を加熱するための入力号数Utl(n)が設定されると入力号数Utl(n)が必要以上に大きくなる。そのため、経過時間t=140s付近で出湯温度Thが過度に上昇して安全動作によりバーナ13の燃焼が停止し、経過時間t=145s以降で燃焼停止による出湯温度Thの過度の低下が発生している。   On the other hand, in the conventional hot water supply apparatus, a sudden decrease in the incoming water temperature Tc is not immediately reflected in the calculation coefficient R (n), but rises rapidly to around the elapsed time t = 140 s. Since the reduced heat exchange efficiency is reflected in the calculation coefficient R (n), if the input number Utl (n) for heating the low-temperature hot and cold water is set based on the calculation coefficient R (n). The input number Utl (n) becomes larger than necessary. Therefore, the tapping temperature Th rises excessively around the elapsed time t = 140 s, and the combustion of the burner 13 is stopped by the safe operation. After the elapsed time t = 145 s, the tapping temperature Th is excessively decreased due to the stop of the combustion. I have.

次に、給湯システム1の循環通路6が低温の湯水で満たされた状態で即湯運転を開始した場合について説明する。   Next, a case will be described in which the hot water operation is started in a state where the circulation passage 6 of the hot water supply system 1 is filled with low-temperature hot water.

図6に示すように、即湯運転が開始され、S11において、初期燃焼期間か否か判定される。詳しくは、特許文献1に記載されているので省略するが、設定温度Trと出湯温度Thの差温が所定温度α℃(例えばα=3)以下か否か判定される。判定がYesの場合はS13に進んで、速やかな昇温を行うために流量Qに基づく初期昇温制御が実行され、判定がNoの場合はS12に進んで、上述の湯温制御を行う。   As shown in FIG. 6, the instant hot water operation is started, and in S11, it is determined whether or not it is the initial combustion period. Although not described in detail because it is described in Patent Document 1, it is determined whether or not the difference between the set temperature Tr and the tapping temperature Th is equal to or lower than a predetermined temperature α ° C. (eg, α = 3). When the determination is Yes, the process proceeds to S13, and the initial temperature increase control based on the flow rate Q is performed to perform the temperature increase quickly. When the determination is No, the process proceeds to S12 to perform the above-described hot water temperature control.

即湯運転開始後すぐに、出湯温度Thが設定温度Trに近づき、上記S11において初期燃焼期間でない(No)と判定された場合、加熱された湯水が循環通路6を通って再び給湯装置2に入水されるまでは低温の湯水が入水する。このとき、学習により演算係数R(n)は25より大きくなる場合がある。   Immediately after the start of the hot water operation, the hot water temperature Th approaches the set temperature Tr, and if it is determined in the above S11 that it is not the initial combustion period (No), the heated hot water passes through the circulation passage 6 and returns to the hot water supply device 2 again. Until water is supplied, low-temperature hot water is supplied. At this time, the operation coefficient R (n) may become larger than 25 due to learning.

加熱された湯水が再び給湯装置2に入水すると入水温度Tcの上昇が検知される。この入水温度の変化率が所定範囲外の場合、例えば入水温度が10℃/100msより急激に上昇した場合には、演算係数R(n)を初期値に戻す。   When the heated hot water enters the hot water supply device 2 again, an increase in the incoming water temperature Tc is detected. When the rate of change of the incoming water temperature is outside the predetermined range, for example, when the incoming water temperature rises sharply from 10 ° C./100 ms, the operation coefficient R (n) is returned to the initial value.

入力号数Uff(n)は上記(2)〜(5)式に従って演算係数R(n)の初期値を反映して算出されるので、入水温度Tcが急激に上昇した場合でも、湯温制御による入力号数Utl(n)は必要以上に小さくなることがない。従って、給湯装置2からの出湯温度Thが過度に低下することがない。即ち、本発明の給湯装置2によれば、温度が安定した出湯が可能である。   Since the input signal number Uff (n) is calculated by reflecting the initial value of the operation coefficient R (n) according to the above equations (2) to (5), even if the incoming water temperature Tc rises sharply, the hot water temperature control is performed. The number of input numbers Utl (n) cannot be reduced unnecessarily. Therefore, the hot water temperature Th from the hot water supply device 2 does not excessively decrease. That is, according to the hot water supply apparatus 2 of the present invention, hot water can be stably discharged.

以上説明したように、本発明の給湯装置2は、湯温制御において、入水温度の変化率が所定の範囲外であれば演算係数R(n)を初期値に設定し、この初期値がFF制御およびFB制御の両方に反映されている。従って、入水温度の急激な変化に対応して演算係数R(n)の学習による更新を止めて初期値に戻すので、演算係数R(n)の更新の遅れが生じず、入水温度Tcの急激な変化に対応したFF制御およびFB制御を行って給湯装置2の湯温制御の精度を向上することが可能である。   As described above, hot water supply apparatus 2 of the present invention sets operation coefficient R (n) to an initial value in hot water temperature control if the rate of change of incoming water temperature is outside a predetermined range, and this initial value is FF. This is reflected in both control and FB control. Therefore, the update of the operation coefficient R (n) by learning is stopped and returned to the initial value in response to the rapid change of the incoming water temperature, so that the update of the operation coefficient R (n) does not delay, and the abrupt increase of the incoming water temperature Tc occurs. It is possible to improve the accuracy of hot water temperature control of hot water supply device 2 by performing FF control and FB control corresponding to various changes.

また、入水温度の変化率が所定の範囲内であれば演算係数R(n)を学習し、この学習値がFF制御およびFB制御の両方に反映されている。実際の演算係数R(n)を学習してFF制御およびFB制御に反映するため、給湯装置2の湯温制御の精度の向上が可能である。   If the change rate of the incoming water temperature is within a predetermined range, the operation coefficient R (n) is learned, and this learned value is reflected in both the FF control and the FB control. Since the actual operation coefficient R (n) is learned and reflected in the FF control and the FB control, the accuracy of the hot water temperature control of the hot water supply device 2 can be improved.

本実施例の給湯装置2では、燃料ガスを燃焼させるバーナ13により湯水を加熱するための熱量を発生させる例を示したが、制御ユニット17によって設定される必要発生熱量に応じて発生熱量を制御可能に構成されるものであれば、石油を燃焼する石油バーナ等、任意の熱源装置を採用することができる。   In the hot water supply apparatus 2 of the present embodiment, an example has been described in which the calorie for heating hot water is generated by the burner 13 that burns the fuel gas. However, the amount of generated heat is controlled in accordance with the required generated heat quantity set by the control unit 17. Any heat source device, such as a petroleum burner that burns petroleum, can be used as long as it is configured as possible.

その他、当業者であれば、本発明の趣旨を逸脱することなく、前記実施例に種々の変更を付加した形態で実施可能であり、本発明はそのような変更形態を包含するものである。   In addition, those skilled in the art can implement various modifications to the above-described embodiment without departing from the spirit of the present invention, and the present invention includes such modifications.

1 即湯循環システム
2 給湯装置
6 循環通路
12 加熱通路
13 バーナ
14 熱交換器
15 ガス比例弁
16 出湯流量調整弁
17 制御ユニット(制御手段)
18 流量センサ(流量検知手段)
19 入水温度センサ(入水温度検知手段)
20 出湯温度センサ(出湯温度検知手段)
22 学習手段
23 フィードフォワード制御手段(FF制御手段)
24 フィードバック制御手段(FB制御手段)
25 加算手段
DESCRIPTION OF SYMBOLS 1 Hot water circulation system 2 Hot water supply apparatus 6 Circulation passage 12 Heating passage 13 Burner 14 Heat exchanger 15 Gas proportional valve 16 Hot water flow control valve 17 Control unit (control means)
18 Flow rate sensor (flow rate detection means)
19 Incoming water temperature sensor (incoming water temperature detecting means)
20 Hot water temperature sensor (hot water temperature detecting means)
22 learning means 23 feed forward control means (FF control means)
24 Feedback control means (FB control means)
25 Addition means

Claims (2)

燃焼部で生じた燃焼ガスによって内部を流れる湯水を加熱するための熱交換器と、
前記熱交換器に導入される入水温度を検知するための入水温度検知手段と、
前記熱交換器から出湯される出湯温度を検知するための出湯温度検知手段と、
前記熱交換器を通過する湯水の流量を検知するための流量検知手段と、
これらの検知手段によって検知された入水温度、出湯温度、流量および給湯設定温度に基づいて所定周期ごとに前記燃焼部における必要発生熱量を制御する制御手段を備え、
前記制御手段は、
前記入水温度と前記出湯温度との差温と前記流量より出力熱量を算出し、前記必要発生熱量に対する前記出力熱量の比に基づいて演算係数を学習する学習手段と、
前記給湯設定温度と前記入水温度との差温と前記流量と前記演算係数とに基づいて第1の必要発生熱量を算出するフィードフォワード制御手段と、
前記給湯設定温度と前記出湯温度との差温と前記流量と前記演算係数とに基づいて第2の必要発生熱量を算出するフィードバック制御手段と、
前記第1の必要発生熱量と前記第2の必要発生熱量とを加算して前記必要発生熱量を設定する加算手段とを有し、
前記学習手段は、前記所定周期における入水温度の変化率が所定範囲外の場合には前記演算係数を初期値に戻すことを特徴とする給湯装置。
A heat exchanger for heating the hot water flowing inside by the combustion gas generated in the combustion section,
Incoming water temperature detecting means for detecting the incoming water temperature introduced into the heat exchanger,
Tapping temperature detection means for detecting tapping temperature of tapping water from the heat exchanger,
Flow rate detection means for detecting the flow rate of hot and cold water passing through the heat exchanger,
Control means for controlling the required amount of heat generated in the combustion section at predetermined intervals based on the incoming water temperature, the outlet water temperature, the flow rate and the hot water supply set temperature detected by these detection means,
The control means includes:
Learning means for calculating an output heat amount from the difference between the inlet water temperature and the tap water temperature and the flow rate, and learning an operation coefficient based on a ratio of the output heat amount to the required generated heat amount,
Feedforward control means for calculating a first necessary generated heat amount based on the difference between the hot water supply set temperature and the incoming water temperature, the flow rate, and the calculation coefficient;
Feedback control means for calculating a second required generated heat amount based on the difference between the hot water supply set temperature and the tapping temperature, the flow rate, and the calculation coefficient;
Adding means for adding the first necessary heat quantity and the second necessary heat quantity to set the required heat quantity,
The water heater, wherein the learning means returns the operation coefficient to an initial value when a change rate of the incoming water temperature in the predetermined cycle is out of a predetermined range.
前記給湯装置は即湯運転可能に構成されたことを特徴とする請求項1に記載の給湯装置。   The hot water supply device according to claim 1, wherein the hot water supply device is configured to be able to operate immediately.
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