JPH0145005Y2 - - Google Patents
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- Publication number
- JPH0145005Y2 JPH0145005Y2 JP1984081454U JP8145484U JPH0145005Y2 JP H0145005 Y2 JPH0145005 Y2 JP H0145005Y2 JP 1984081454 U JP1984081454 U JP 1984081454U JP 8145484 U JP8145484 U JP 8145484U JP H0145005 Y2 JPH0145005 Y2 JP H0145005Y2
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- air conditioner
- cold
- hot water
- discharge
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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Description
【考案の詳細な説明】
[産業上の利用分野]
本考案は水式空調器の末端圧制御装置、特に空
調器の冷温水流入側末端圧を冷温水の循環流量変
動に応じて最適圧力に制御する改良された末端圧
制御装置に関する。[Detailed description of the invention] [Field of industrial application] The present invention is a terminal pressure control device for a water-type air conditioner, in particular, a device for controlling the terminal pressure of the cold and hot water inlet side of the air conditioner to the optimum pressure according to fluctuations in the circulation flow rate of the cold and hot water. The present invention relates to an improved terminal pressure control device.
[背景技術]
従来、冷水又は温水を用いた水式空調器が周知
であり、該水式空調器は、外部から供給される冷
水又は温水(以下冷温水と記す)を用い室内空気
の熱交換を行い、最適なエアコンデイシヨニング
を行つている。[Background Art] Conventionally, water-type air conditioners that use cold or hot water are well known, and these water-type air conditioners exchange heat with indoor air using cold or hot water (hereinafter referred to as cold and hot water) supplied from the outside. We are conducting optimal air conditioning system.
そして、このような水式空調器への冷温水の供
給は、蓄熱槽内にあらかじめ所定量の冷温水を蓄
えておき、冷温水供給用循環システムを用い該冷
温水を蓄熱槽と空調器との間で循環することによ
り行われる。 To supply cold and hot water to such a water-type air conditioner, a predetermined amount of cold and hot water is stored in a heat storage tank in advance, and a circulation system for supplying cold and hot water is used to distribute the cold and hot water between the heat storage tank and the air conditioner. This is done by cycling between
このため、従来の冷温水供給用循環システムに
おいては、蓄熱槽内の冷温水を吐出ポンプをもつ
て汲出し、このようにして汲出された冷温水を空
調器を介して蓄熱槽に向け循環させている。そし
て、更に冷温水の循環経路末端側に、還水圧制御
部を設け、該循環経路から蓄熱槽へ循環冷温水が
常に一定の還水圧POで還流するように制御して
いる。 For this reason, in conventional cold/hot water supply circulation systems, the cold/hot water in the heat storage tank is pumped out using a discharge pump, and the cold/hot water thus pumped out is circulated to the heat storage tank via an air conditioner. ing. Furthermore, a return water pressure control section is provided at the end of the cold and hot water circulation path, and the circulating cold and hot water is controlled so that it always flows back from the circulation path to the heat storage tank at a constant return water pressure P O.
ところで、このようにして供給される冷温水を
用いて良好なエアコンデイシヨニングを行うため
には、空調器の冷温水流入側末端圧PAを、その
下流側における圧力損、すなわち空調器内部にお
ける圧力損Pl及び還水圧POを加えた必要最小末
端圧PL以上に設定することが必要とされる。 By the way, in order to perform good air conditioning using the cold and hot water supplied in this way, it is necessary to change the terminal pressure P A of the cold and hot water inlet side of the air conditioner to the pressure loss on the downstream side, that is, It is necessary to set the required minimum terminal pressure P L, which is the sum of the pressure loss P L and the return water pressure P O , at or above the required minimum terminal pressure P L.
ここにおいて、該必要最小末端圧PLは冷温水
の循環流量Qが多くなるに従つて増大し、このよ
うな必要最小末端圧PLの変動に対応するため従
来の冷温水供給用循環システムにおいては、吐出
圧一定制御方式又は末端圧一定制御方式を採用し
ている。 Here, the required minimum end pressure P L increases as the circulation flow rate Q of cold and hot water increases, and in order to cope with such fluctuations in the required minimum end pressure P L , in the conventional cold and hot water supply circulation system. adopts a constant discharge pressure control method or a constant terminal pressure control method.
前記吐出圧一定制御方式は、吐出ポンプの吐出
圧PBを常に一定に制御するものであり、その吐
出圧PBは、定格流量時における必要最小末端圧
力PLと水路内における圧力損とを加えた値に設
定されている。このようにして、この吐出圧一定
制御方式によれば、その末端圧PAを流量Qの変
動にかかわりなく常に必要最小末端圧PL以上に
制御し空調器による良好なエアコンデイシヨニン
グを行つている。 The constant discharge pressure control method is to control the discharge pressure P B of the discharge pump to be constant at all times, and the discharge pressure P B is determined by the difference between the required minimum terminal pressure P L at the rated flow rate and the pressure loss in the water channel. is set to the value added. In this way, according to this constant discharge pressure control method, the terminal pressure P A is always controlled to be equal to or higher than the required minimum terminal pressure P L regardless of fluctuations in the flow rate Q, and good air conditioning can be achieved by the air conditioner. It's on.
しかし、この吐出圧一定制御方式は、末端圧
PAの必要最小圧力PLが流量Qとともに減少する
にもかかわらず、吐出圧を常に一定に制御し続け
るため、流量の減少とともに末端圧PAがしだい
に増加する。この結果このような吐出圧一定制御
方式によれば、流量の減少とともに必要最低圧
PLと末端圧PAとの圧力差が大きくなり、吐出ポ
ンプを運転するに際して発生するエネルギ浪費が
極めて大きくなるという欠点があつた。 However, this constant discharge pressure control method
Although the required minimum pressure P L of P A decreases with the flow rate Q, the discharge pressure is always controlled to be constant, so the terminal pressure P A gradually increases as the flow rate decreases. As a result, according to this constant discharge pressure control method, the required minimum pressure decreases as the flow rate decreases.
There was a drawback that the pressure difference between P L and the terminal pressure P A became large, and the energy waste generated when operating the discharge pump became extremely large.
また、前記末端圧一定制御方式は、吐出ポンプ
の吐出圧PBを制御し、空調器の末端圧PAを、常
に定格流量時における必要最小圧PLと等しく制
御するものである。これにより、流量Qの変動に
かかわりなく末端圧力PAを常に必要最小末端圧
PL以上に制御し空調器による良好なエアコンデ
イシヨニングを行つている。 Further, the terminal pressure constant control method controls the discharge pressure P B of the discharge pump, and controls the terminal pressure PA of the air conditioner to always be equal to the required minimum pressure PL at the time of the rated flow rate. As a result, regardless of fluctuations in the flow rate Q, the end pressure P A is always the minimum required end pressure.
Good air conditioning is performed by the air conditioner by controlling the air conditioner to a level higher than P L.
しかし、この末端圧一定制御方式も、流量の減
少にともなう必要最小圧力PLの低下に拘りなく
常にその末端圧を一定値に設定するために、循環
冷温水の流量が減少すると末端圧PAが必要最小
末端圧PLを大きく上まわる過剰な圧力となつて
しまい、吐出ポンプを運転するに際して発生する
エネルギ浪費が極めて大きくなるという欠点があ
つた。 However, even with this constant end pressure control method, the end pressure is always set to a constant value regardless of the drop in the required minimum pressure P L due to a decrease in the flow rate . This results in an excessive pressure that greatly exceeds the required minimum terminal pressure P L , resulting in an extremely large waste of energy when operating the discharge pump.
[考案の目的]
本考案は、このような従来の課題に鑑み為され
たものであり、その目的は、空調器に供給される
冷温水の流量に応じて、その末端圧を必要最小圧
に制御することにより、吐出ポンプを最小のエネ
ルギで駆動することの可能な水式空調器の末端圧
制御装置を提供することにある。[Purpose of the invention] The present invention was devised in view of these conventional problems, and its purpose is to reduce the terminal pressure to the minimum necessary pressure according to the flow rate of cold and hot water supplied to the air conditioner. An object of the present invention is to provide a terminal pressure control device for a water-type air conditioner that can drive a discharge pump with minimum energy by controlling it.
[考案の構成]
前記目的を達成するために、本考案の装置は、
蓄熱槽の冷温水を所定吐出圧で汲出し蓄熱槽と空
調器との間で循環させる吐出ポンプと、
循環冷温水の蓄熱槽への還水圧を一定に制御す
る還水圧制御部と、
を含み、冷温水を空調器に供給する水式空調器の
冷温水供給用循環システムにおいて、
循環冷温水の流量を検出する流量センサと、
検出流量から求められる空調器内圧力損と前記
還水圧との加算値に基づき空調器の冷温水流入側
における必要最小末端圧を演算し、該必要最小末
端圧と検出流量から求められる水路内圧力損とに
基づき吐出ポンプの吐出圧を演算出力する演算回
路と、
演算回路から出力される演算値に基き吐出ポン
プの吐出圧を制御する吐出圧制御回路と、
を含み、空調器の冷温水流入側末端圧を冷温水の
循環流量の変動に応じて最適な必要最小末端圧に
制御することを特徴とする。[Configuration of the invention] In order to achieve the above object, the device of the invention has the following features:
A discharge pump that pumps out cold and hot water from the heat storage tank at a predetermined discharge pressure and circulates it between the heat storage tank and the air conditioner, and a return water pressure control unit that controls the pressure of the circulating cold and hot water to the heat storage tank to be constant. , in a cold/hot water supply circulation system of a water type air conditioner that supplies cold/hot water to an air conditioner, a flow rate sensor that detects the flow rate of the circulating cold/hot water, and a pressure drop in the air conditioner determined from the detected flow rate and the return water pressure. an arithmetic circuit that calculates a required minimum end pressure on the cold and hot water inflow side of the air conditioner based on the added value, and calculates and outputs the discharge pressure of the discharge pump based on the required minimum end pressure and the pressure loss in the water channel determined from the detected flow rate; , a discharge pressure control circuit that controls the discharge pressure of the discharge pump based on the calculated value output from the calculation circuit; It is characterized by controlling the terminal pressure to the minimum necessary.
以上の構成とすることにより、本考案によれ
ば、吐出ポンプを常に最適な必要最小動力で駆動
することができ、この結果消費エネルギの節減を
図ることが可能となる。 With the above configuration, according to the present invention, the discharge pump can always be driven with the optimum required minimum power, and as a result, it is possible to reduce energy consumption.
[実施例]
次に本考案の好適な実施例を図面に基づき説明
する。[Example] Next, a preferred example of the present invention will be described based on the drawings.
第1図には本考案に係る装置の好適な実施例が
示されており、実施例の装置は、蓄熱槽10内に
蓄えられた冷温水12を冷温水供給用循環システ
ムを用いて複数の空調器14に供給している。 FIG. 1 shows a preferred embodiment of the device according to the present invention, and the device of the embodiment uses a cold and hot water supply circulation system to supply cold and hot water 12 stored in a heat storage tank 10 to a plurality of cold and hot water supply circulation systems. It is supplied to the air conditioner 14.
実施例において、該冷温水供給用循環システム
は、その上流端部に設けられた吐出ポンプ16
と、その下流端側に設けられた還水圧制御部18
と、を含む。そして、吐出ポンプ16により蓄熱
槽10内の冷温水12を汲上げ、各空調器14に
接続された上流側配管20に向け冷温水12を所
定吐出圧PBで供給する。 In an embodiment, the cold/hot water supply circulation system includes a discharge pump 16 provided at its upstream end.
and a return water pressure control section 18 provided on the downstream end side thereof.
and, including. Then, the cold and hot water 12 in the heat storage tank 10 is pumped up by the discharge pump 16, and the cold and hot water 12 is supplied at a predetermined discharge pressure P B to the upstream piping 20 connected to each air conditioner 14.
そして、このようにして各空調器14に供給さ
れた冷温水12は、下流側配管22を介して蓄熱
槽10に向け還流する。この際、蓄熱槽10へ向
けた冷温水12の還水圧POは、配管22の下流
末端側に設けられた還水圧制御部18により常に
一定の圧力に制御される。 The cold and hot water 12 thus supplied to each air conditioner 14 flows back toward the heat storage tank 10 via the downstream piping 22. At this time, the return water pressure P O of the cold and hot water 12 directed toward the heat storage tank 10 is always controlled to a constant pressure by the return water pressure control section 18 provided at the downstream end side of the pipe 22.
実施例において、前記吐出ポンプ16は、2個
の定速ポンプ24,26及びその流量が調整可能
なインバータポンプ28を並列に接続して形成さ
れている。従つて該インバータポンプ28の流量
を調整することによりその吐出圧PBを任意に制
御することができ、該吐出圧PBは吐出ポンプ1
6の吐出口近傍に設けた吐出圧センサ30により
検出される。そして、このようにして吐出された
冷温水12は上流側の配管20内を流れ各空調器
14内に分散供給される。 In the embodiment, the discharge pump 16 is formed by connecting in parallel two constant speed pumps 24 and 26 and an inverter pump 28 whose flow rate can be adjusted. Therefore , by adjusting the flow rate of the inverter pump 28, the discharge pressure P B can be arbitrarily controlled.
The pressure is detected by a discharge pressure sensor 30 provided near the discharge port 6. The cold and hot water 12 thus discharged flows through the upstream piping 20 and is distributed and supplied to each air conditioner 14 .
このようにして冷温水12が分散供給される各
空調器14は、それぞれ任意の被空調ゾーンに設
置されており、これら各空調器14を流れる冷温
水12の流量はその下流側に設けられた流量制御
弁32により対応する被空調ゾーンの熱負荷に応
じて制御される。 Each air conditioner 14 to which cold and hot water 12 is distributed and supplied in this way is installed in an arbitrary air-conditioned zone, and the flow rate of cold and hot water 12 flowing through each of these air conditioners 14 is set on the downstream side thereof. It is controlled by the flow control valve 32 according to the heat load of the corresponding air-conditioned zone.
そして、各空調器14は、供給される冷温水1
2と周知の空気との熱交換を行い、分担する各被
空調ゾーンの最適なエアコンデイシヨニングを行
う。 Each air conditioner 14 is supplied with cold and hot water 1.
2 and the well-known air, and perform optimal air conditioning for each air-conditioned zone.
そして、このようにして各空調器14内におい
て熱交換に用いられた各冷温水12は、その下流
側において合流し配管22内を流れ還水圧制御部
18を介して蓄熱槽10内に還流される。 The cold and hot water 12 used for heat exchange in each air conditioner 14 in this way joins on the downstream side, flows through the pipe 22, and is returned to the heat storage tank 10 via the return water pressure control unit 18. Ru.
実施例において、前記還水圧制御部18は、配
管22の末端側に設けられその還水圧POを検出
する還水圧センサ34と、該センサ34の下流側
においてその還水圧POを制御する一対の還水圧
制御弁36と、を含む。そして制御部38によ
り、還水圧センサ34で検出される還水圧POが
常に一定の圧力となるように還水圧制御弁36を
制御している。これにより、配管22内を流れて
くる冷温水12は、常に一定の還水圧POをもつ
て蓄熱槽10内に還流されることになる。 In the embodiment, the return water pressure control unit 18 includes a return water pressure sensor 34 provided at the end side of the pipe 22 to detect the return water pressure P O , and a pair of return water pressure sensors 34 located downstream of the sensor 34 to control the return water pressure P O. and a return water pressure control valve 36. The control unit 38 controls the return water pressure control valve 36 so that the return water pressure P O detected by the return water pressure sensor 34 is always a constant pressure. As a result, the cold and hot water 12 flowing through the pipe 22 is always returned to the heat storage tank 10 with a constant return water pressure PO .
以上のように、実施例の装置によれば、被空調
エリアにそれぞれ設けられた各空調器14に対
し、流量が必要熱負荷に対応して制御される冷温
水が循環供給されることになり、これにより各空
調器14か分担する各被空調エリアのエアコンデ
イシヨニングを行うことになる。 As described above, according to the device of the embodiment, cold and hot water whose flow rate is controlled according to the required heat load is circulated and supplied to each air conditioner 14 provided in each air-conditioned area. As a result, each air conditioner 14 performs air conditioning for each area to be air conditioned.
ここにおいて、空調器14内における圧力損Pl
とすると、各空調器14内において良好なエアコ
ンデイシヨニングを行うためには、前述のよう
に、該空調器14の冷温水流入口側末端圧PAを
次式で表わされる必要最小末端圧PL以上の圧力
に制御することが必要となる。 Here, the pressure loss Pl in the air conditioner 14 is
Then, in order to perform good air conditioning in each air conditioner 14, as mentioned above, the end pressure P A on the cold/hot water inlet side of the air conditioner 14 is set to the necessary minimum end pressure P A expressed by the following equation. It is necessary to control the pressure to over L.
PL=Pl+PO
ここにおいて、
空調器14内の圧力損Plは冷温水12の流量Q
の変化に応じて変動し、従つて必要最小末端圧
PLも冷温水12の流量Qに応じて変動すること
になる。 P L = Pl + P OHere , the pressure loss Pl in the air conditioner 14 is the flow rate Q of the hot and cold water 12
and therefore the required minimum end pressure
P L also changes according to the flow rate Q of the cold and hot water 12.
第2図には、循環冷温水12の流量Qと空調器
14内の圧力損Pl1、すなわち空調器14内に設
けられたコイル部を冷温水12が通過する際発生
する損失Plとの関係が示されており、空調器14
内の損失Plは流量Qに基づき次式に従つて求めら
れる。 FIG. 2 shows the relationship between the flow rate Q of the circulating cold and hot water 12 and the pressure loss Pl 1 in the air conditioner 14, that is, the loss Pl that occurs when the cold and hot water 12 passes through the coil section provided in the air conditioner 14. is shown, and the air conditioner 14
The loss Pl within is calculated based on the flow rate Q according to the following formula.
Pl=cQm
ここにおいて、c,mはそれぞれ空調器14内
のコイル部によつて定まる定数であり、実施例に
おいては前式m=2で近似し次式に基づき表わし
ている。 Pl=cQ m Here, c and m are constants each determined by the coil section in the air conditioner 14, and in the embodiment, they are approximated by the previous equation m=2 and expressed based on the following equation.
Pl=cQ2
従つて、還水圧POをPO=bとすれば、流量Q
に対応する空調器14の必要最小末端圧PLは、
次式をもつて表わされる。 Pl=cQ 2 Therefore, if the return water pressure P O is P O = b, then the flow rate Q
The required minimum terminal pressure P L of the air conditioner 14 corresponding to
It is expressed by the following formula.
PL=Pl+PO=cQ2+b …(1)
尚、ここで本実施例において、第1図に示され
る空調器内の圧力損Plは、例えば大型の1台の空
調器でも、また2台以上の複数台設けた空調器で
も同じ流量Qであれば、その合計加算圧力損は、
同一となる。 P L = Pl + P O = cQ 2 + b...(1) In this example, the pressure loss Pl in the air conditioner shown in FIG. If the air conditioners installed above have the same flow rate Q, the total added pressure loss is:
be the same.
これは、すなわち、空調器内部における圧力損
Plは、複数台(n台)の空調器の場合には、
Pl1=o
〓i=1
CiQi2
=C1Q1 2+C2Q2 2+…
+CnQn2
となり、
ここでC1〜Coは定数であり、本実施例ではす
べて同一の空調器のため同一とし、Q1〜Qoは空
調器内の流量とする。 This means that the pressure loss inside the air conditioner is
In the case of multiple (n) air conditioners, Pl becomes Pl 1 = o 〓 i=1 CiQi 2 = C 1 Q 1 2 + C 2 Q 2 2 +... +CnQn 2 , where C 1 ~ C o is a constant, and in this example, it is the same since all the air conditioners are the same, and Q 1 to Q o are the flow rates in the air conditioner.
従つて、 Pl1=C1o 〓i=1 Qi2 …(1) となる。 Therefore, Pl 1 = C 1o 〓 i=1 Qi 2 …(1).
一方、大型の空調器1台の場合には、 Pl2=CQ2 …(2) となる。 On the other hand, in the case of one large air conditioner, Pl 2 = CQ 2 (2).
これは、大型の空調器は複数台(n台)の空調
器を単純に合体したものと見なされるため、式(1)
と(2)とにより、
Pl1=Pl2
となる。 This is because a large air conditioner is considered to be a simple combination of multiple (n) air conditioners, so Equation (1)
and (2), Pl 1 = Pl 2 .
以上のことから、空調器内圧力損Plは、各空調
器の流量制御弁32の開閉状態によつても同じ流
量でも同一であることが理解される。 From the above, it is understood that the pressure loss Pl within the air conditioner is the same depending on the open/closed state of the flow rate control valve 32 of each air conditioner and even when the flow rate is the same.
本考案の特徴的事項は、空調器14の冷温水流
入側末端圧PAを、空調器14の循環流量Qの変
動に応じて常に必要最小末端圧PLとなるよう制
御し、吐出ポンプ16を最小エネルギで駆動可能
とすることにある。 The characteristic feature of the present invention is that the terminal pressure P A on the cold/hot water inflow side of the air conditioner 14 is always controlled to the required minimum terminal pressure P L according to the fluctuation of the circulation flow rate Q of the air conditioner 14, and the discharge pump 16 The objective is to make it possible to drive with minimum energy.
このため、本考案の装置においては、循環冷温
水12の流量を検出する流量センサ40が設けら
れており、実施例において、この流量センサ40
は、下流側配管22内を流れる循環冷温水12の
流量を検出し、その検出信号を変換器42を介し
て演算回路44に供給している。 For this reason, the apparatus of the present invention is provided with a flow rate sensor 40 that detects the flow rate of the circulating cold and hot water 12, and in the embodiment, this flow rate sensor 40 is
detects the flow rate of the circulating cold/hot water 12 flowing within the downstream piping 22 and supplies the detection signal to the arithmetic circuit 44 via the converter 42 .
本考案の演算回路44は、このようにして検出
される循環流量Qに基づき空調器14内において
発生する圧力損Plを演算し、該圧力損Plとあらか
じめ定められた還水圧POとを前記第1式に基づ
き加算し必要最小末端圧PLを求める。そして、
空調器14の冷温水流入側末端圧PAを、前述の
ようにして求めた必要最小末端圧PLに制御する
ために、検出流量Qから水路内において発生する
圧損Pmを求め、該水路内圧損Pmと必要最小末
端圧PLとを加算し吐出ポンプ16の吐出圧PBを
演算出力する。 The calculation circuit 44 of the present invention calculates the pressure loss Pl generated in the air conditioner 14 based on the circulating flow rate Q detected in this way, and calculates the pressure loss Pl and the predetermined return water pressure P O as described above. Add based on the first equation to find the required minimum terminal pressure P L. and,
In order to control the end pressure P A on the cold and hot water inlet side of the air conditioner 14 to the required minimum end pressure P L obtained as described above, the pressure drop Pm generated in the water channel is determined from the detected flow rate Q, and The pressure drop Pm and the required minimum terminal pressure P L are added to calculate and output the discharge pressure P B of the discharge pump 16.
第3図には、本実施例の装置に用いられる演算
回路44の具体的な構成が示されており、第4図
には該装置によつて演算出力される吐出ポンプ1
6の吐出圧PBと流量Qとの関係が示されている。 FIG. 3 shows a specific configuration of the arithmetic circuit 44 used in the device of this embodiment, and FIG.
6 shows the relationship between the discharge pressure P B and the flow rate Q.
第4図からも明らかなように空調器14の冷温
水流入側末端圧PAを必要最小末端圧PLに制御す
るためには、吐出ポンプ16の吐出圧PBを前記
必要最小末端圧PLに循環水路内における圧力損
Pmを加えた値に設定してやることが必要であ
る。 As is clear from FIG. 4, in order to control the end pressure P A on the cold/hot water inflow side of the air conditioner 14 to the required minimum end pressure P L , the discharge pressure P B of the discharge pump 16 must be adjusted to the required minimum end pressure P L is the pressure loss in the circulation channel.
It is necessary to set it to a value that includes Pm.
この循環水路内における圧力損は、
Pm=aQnをもつて表され、a,nは循環水路
系に応じた所定の定数として与えられる。実施例
においては、該水路系における圧力損をn=2を
もつて近似し、次式に基づき定めている。 The pressure loss in this circulation waterway is expressed as Pm=aQ n , where a and n are given as predetermined constants depending on the circulation waterway system. In the embodiment, the pressure loss in the waterway system is approximated by n=2 and determined based on the following equation.
Pm=aQ2
従つて、本実施例においては、空調器14の冷
温水流入側末端圧PAを必要最小末端圧PLに制御
するために必要な吐出圧PBを次式に基づき演算
出力している。 Pm=aQ 2 Therefore, in this embodiment, the discharge pressure P B required to control the end pressure P A on the cold/hot water inflow side of the air conditioner 14 to the required minimum end pressure P L is calculated and output based on the following formula. are doing.
PB=aQ2+cQ2+b …(2)
このような演算を行うため、実施例の演算回路
44は、変換器42からI/V変換器48を介し
て入力された検出流量Qを増幅器50,52及び
乗算器54,59にそれぞれ供給する。乗算器5
0は、このようにして供給された検出量Qに基づ
きaQを出力し、他の増幅器52はCQを出力す
る。そして、乗算器54は増幅器50から出力さ
れるaQとI/V変換器48から出力されるQを
乗算し、aQ2を出力する。 P B =aQ 2 +cQ 2 +b (2) In order to perform such calculation, the calculation circuit 44 of the embodiment converts the detected flow rate Q input from the converter 42 via the I/V converter 48 into the amplifier 50. , 52 and multipliers 54 and 59, respectively. Multiplier 5
0 outputs aQ based on the detected quantity Q thus supplied, and the other amplifiers 52 output CQ. Then, the multiplier 54 multiplies aQ output from the amplifier 50 and Q output from the I/V converter 48, and outputs aQ 2 .
また、乗算器59は、増幅器52から出力され
るcQとI/V変換器48から出力されるQを乗
算し、cQ2を出力する。加算器56は、このよう
にして乗算器54及び59からの出力aQ2,cQ2
及び可変抵抗器58から出力される還水圧bを前
記第2式に基づき加算し吐出PBを求め、該演算
値PBを吐出圧制御回路46に供給する。 Furthermore, multiplier 59 multiplies cQ output from amplifier 52 and Q output from I/V converter 48, and outputs cQ 2 . Adder 56 thus outputs aQ 2 , cQ 2 from multipliers 54 and 59
and the return water pressure b output from the variable resistor 58 are added based on the second equation to obtain the discharge P B , and the calculated value P B is supplied to the discharge pressure control circuit 46.
そして、吐出圧制御回路46は、このようにし
て演算出力された値PBに基づき、吐出ポンプ1
6の吐出圧を制御する。実施例において、この吐
出圧制御回路46は、演算回路44が出力する演
算値PBと、吐出圧センサ30にて検出される吐
出圧とを照合し、両者が一致するようインバータ
ポンプ28をPID制御する。 Then, the discharge pressure control circuit 46 controls the discharge pump 1 based on the value P B calculated and output in this way.
Control the discharge pressure of 6. In the embodiment, the discharge pressure control circuit 46 compares the calculated value P B output by the calculation circuit 44 with the discharge pressure detected by the discharge pressure sensor 30, and controls the inverter pump 28 by PID so that the two match. Control.
このように、本考案の装置によれば、流量セン
サ40により循環冷温水12の流量変化を検出
し、空調器14の冷温水流量側末端圧PAを検出
流量Qに応じた必要最小末端圧PLとするよう吐
出ポンプ30の吐出圧PBを制御するため、吐出
ポンプ16を冷温水12の循環流量Qに応じて常
に必要最小吐出圧で運転することができ消費エネ
ルギの節約を図ることが可能となる。 As described above, according to the device of the present invention, the flow rate sensor 40 detects the change in the flow rate of the circulating cold/hot water 12, and the terminal pressure P A on the cold/hot water flow side of the air conditioner 14 is determined as the required minimum terminal pressure according to the detected flow rate Q. Since the discharge pressure P B of the discharge pump 30 is controlled to be P L , the discharge pump 16 can always be operated at the required minimum discharge pressure according to the circulation flow rate Q of the cold and hot water 12, thereby saving energy consumption. becomes possible.
特に、本考案の装置によれば、空調器14の冷
温水流入側末端圧PAは、常に流量センサ40の
検出流量Qに基づきフイードバツク制御されるた
め、該末端圧PAを高い信頼性をもつて制御する
ことが可能となる。 In particular, according to the device of the present invention, the terminal pressure P A on the cold/hot water inflow side of the air conditioner 14 is always feedback-controlled based on the flow rate Q detected by the flow sensor 40, so that the terminal pressure P A can be controlled with high reliability. It becomes possible to control the
第5図には、本考案の装置を用いて行う末端圧
可変制御と、従来の吐出圧一定制御、末端圧一定
制御との関係が示されており、図中100a,1
00bは本考案の末端圧可変制御による末端圧
PAと吐出圧PBとを示し、図中200a,200
bは従来の末端圧一定制御による末端圧PAと吐
出圧PBとを示し、図中300a,300bは従
来の吐出圧一定制御による末端圧PA及び吐出圧
PBを示している。 FIG. 5 shows the relationship between variable end pressure control performed using the device of the present invention, conventional constant discharge pressure control, and constant end pressure control.
00b is the end pressure due to the end pressure variable control of the present invention.
P A and discharge pressure P B are shown at 200a and 200a in the figure.
b indicates the terminal pressure P A and discharge pressure P B obtained by conventional constant terminal pressure control, and 300a and 300b in the figure indicate terminal pressure P A and discharge pressure obtained by conventional constant discharge pressure control.
It shows P B.
ここにおいて、従来の末端圧一定制御法によれ
ば、その末端圧PAを200aで示すように定格
流量時における必要最小末端圧PLmaxとなるよ
う制御している。従つて、その吐出圧PBは該末
端圧PLmaxに、水路系における圧力損aQ2を加え
合せた値として、図中200bをもつて示される
曲線に沿つて制御されることになる。これに対
し、本考案に係る装置によれば、その末端圧PA
を流量Qの変化に応じて図中100aに示す曲線
に沿つて制御するため、ポンプ16の吐出圧PB
を、図中100bで示すごとく、末端圧一定制御
法の吐出圧200bに比し低く設定することがで
き、この差分だけ、エネルギを節約して吐出ポン
プを運転することが可能となる。 Here, according to the conventional terminal pressure constant control method, the terminal pressure P A is controlled to be the required minimum terminal pressure P L max at the rated flow rate, as shown by 200a. Therefore, the discharge pressure P B is controlled as the sum of the end pressure P L max and the pressure loss aQ 2 in the waterway system along the curve indicated by 200b in the figure. On the other hand, according to the device according to the present invention, the terminal pressure P A
The discharge pressure P B of the pump 16 is controlled according to the change in the flow rate Q along the curve shown at 100a in the figure.
As shown by 100b in the figure, can be set lower than the discharge pressure 200b of the constant terminal pressure control method, and it is possible to operate the discharge pump while saving energy by this difference.
また、従来の吐出圧一定制御法は、冷温水12
の定格流量水においてその末端圧PAが必要最小
末端圧PLmaxと等しくなるよう、図中300b
で示すごとく吐出圧PBを一定値PBmaxに制御す
るものである。従つてこの吐出圧一定制御法によ
れば流量が減少し空調器14内における圧力損失
が減少しても、吐出圧PBは常にPBmaxに制御さ
れ続けるため、その末端圧PAは流量Qが減少す
るに従い図中の曲線300aに沿つて増大し、必
要最小末端圧PLを示す直線100aとの圧力差
が増大することとなる。 In addition, the conventional discharge pressure constant control method
300b in the figure so that the terminal pressure P A is equal to the required minimum terminal pressure P L max at the rated flow rate of water.
As shown, the discharge pressure P B is controlled to a constant value P B max. Therefore, according to this constant discharge pressure control method, even if the flow rate decreases and the pressure loss in the air conditioner 14 decreases, the discharge pressure P B will always continue to be controlled to P B max, so the terminal pressure P A will be equal to the flow rate. As Q decreases, it increases along the curve 300a in the figure, and the pressure difference with the straight line 100a indicating the required minimum terminal pressure P L increases.
これに対し、本願考案に係る装置は、その末端
圧PAを図中100aに示す必要最小末端圧
PL=cQ2+bに沿つて制御するため、これら両
曲線300aと100aとの差圧分だけ吐出ポン
プ16の吐出圧PBを低く設定して運転すること
が可能となり、この結果、従来の吐出圧一定制御
法に比し吐出ポンプ16の運転に要するエネルギ
を大幅に節減することが可能となる。 On the other hand, the device according to the present invention controls its end pressure P A along the necessary minimum end pressure P L =cQ 2 +b shown at 100a in the figure, so the pressure difference between these two curves 300a and 100a As a result, the energy required to operate the discharge pump 16 can be significantly reduced compared to the conventional constant discharge pressure control method. becomes.
尚、本実施例においては、空調器14の冷温水
流量側末端圧PAを、その必要最小末端圧PLに沿
つて正確に制御する場合を例に取り説明したが、
本考案はこれに限らず、末端圧PAを必要最小末
端圧PLに近い値に沿つて制御すれば十分であり、
例えば第4図において1点鎖線に示すごとく、該
必要最小末端圧を直線をもつて近似し、該近似直
線に沿つて空調器14の冷温水流入側末端圧PA
を制御することも可能である。 In this embodiment, the case where the end pressure P A on the cold/hot water flow rate side of the air conditioner 14 is accurately controlled in accordance with the required minimum end pressure P L has been described as an example.
The present invention is not limited to this, but it is sufficient to control the end pressure P A to a value close to the required minimum end pressure P L ,
For example, as shown by the dashed line in FIG. 4, the necessary minimum terminal pressure is approximated by a straight line, and the terminal pressure P A on the cold and hot water inflow side of the air conditioner 14 is calculated along the approximate straight line
It is also possible to control
[考案の効果]
以上説明したように、本考案によれば、空調器
の冷温水流入側末端圧をその流量に応じて常に最
適な必要最小末端圧に制御するため、空調器へ冷
温水を供給するために駆動される吐出ポンプを常
に最小の吐出圧をもつて運転することができ、こ
の結果、吐出ポンプの運転に要するエネルギを大
幅に節減することが可能となる。[Effects of the invention] As explained above, according to the invention, in order to always control the terminal pressure on the cold/hot water inflow side of the air conditioner to the optimal required minimum terminal pressure according to the flow rate, the cold/hot water is supplied to the air conditioner. The discharge pump that is driven for supply can always be operated with a minimum discharge pressure, and as a result, the energy required for operating the discharge pump can be significantly reduced.
第1図は本考案に係る水式空調器の末端圧制御
装置の好適な実施例を示すブロツク図、第2図は
第1図に示す装置の空調器14内における圧力損
の特性図、第3図は第1図に示す装置の演算回路
の詳細なブロツク図、第4図は本考案に係る装置
によつて制御される吐出圧の説明図、第5図は本
考案に係る装置と従来装置との関係を示す特性比
較図である。
10……蓄熱槽、12……冷温水、14……空
調器、16……吐出ポンプ、18……還水制御
部、40……流量センサ、44……演算回路、4
6……吐出圧制御回路。
FIG. 1 is a block diagram showing a preferred embodiment of the terminal pressure control device for a water-type air conditioner according to the present invention, and FIG. 2 is a characteristic diagram of pressure loss in the air conditioner 14 of the device shown in FIG. 3 is a detailed block diagram of the arithmetic circuit of the device shown in FIG. 1, FIG. 4 is an explanatory diagram of the discharge pressure controlled by the device according to the present invention, and FIG. 5 is a diagram showing the device according to the present invention and the conventional one. It is a characteristic comparison diagram showing the relationship with the device. 10... Heat storage tank, 12... Cold/hot water, 14... Air conditioner, 16... Discharge pump, 18... Return water control unit, 40... Flow rate sensor, 44... Arithmetic circuit, 4
6...Discharge pressure control circuit.
Claims (1)
と空調器との間で循環させる吐出ポンプと、 循環冷温水の蓄熱槽への還水圧を一定に制御
する還水圧制御部と、 を含み、冷温水を空調器に供給する水式空調器
の冷温水供給用循環システムにおいて、 循環冷温水の流量を検出する流量センサと、 検出流量から求められる空調器内圧力損と前
記還水圧との加算値に基づき空調器の冷温水流
入側における必要最小末端圧を演算し、該必要
最小末端圧と検出流量から求められる水路内圧
力損とに基づき吐出ポンプの吐出圧を演算出力
する演算回路と、 演算回路から出力される演算値に基き吐出ポ
ンプの吐出圧を制御する吐出圧制御回路と、 を含み、空調器の冷温水流入側末端圧を冷温水
の循環流量の変動に応じて最適な必要最小末端
圧に制御することを特徴とする水式空調器の末
端圧制御装置。 (2) 実用新案登録請求の範囲(1)記載の装置におい
て、吐出圧制御回路は、演算回路からの出力に
基づき吐出ポンプをPID制御することを特徴と
する水式空調器の末端圧制御装置。[Scope of claim for utility model registration] (1) A discharge pump that pumps out cold and hot water from the heat storage tank at a predetermined discharge pressure and circulates it between the heat storage tank and the air conditioner, and a system that maintains a constant pressure of the circulating cold and hot water to the heat storage tank. In a cold/hot water supply circulation system for a water-type air conditioner that supplies cold/hot water to the air conditioner, the system includes: a return water pressure control unit that controls the flow rate of the circulating cold/hot water; Calculate the required minimum end pressure on the cold/hot water inflow side of the air conditioner based on the added value of the pressure loss inside the air conditioner and the return water pressure, and discharge based on the required minimum end pressure and the pressure loss in the waterway determined from the detected flow rate. A calculation circuit that calculates and outputs the discharge pressure of the pump; and a discharge pressure control circuit that controls the discharge pressure of the discharge pump based on the calculation value output from the calculation circuit, and adjusts the end pressure of the cold and hot water inlet side of the air conditioner to the cold temperature. A terminal pressure control device for a water-type air conditioner, which is characterized by controlling the terminal pressure to the optimum required minimum terminal pressure according to fluctuations in the circulating flow rate of water. (2) A terminal pressure control device for a water-type air conditioner, wherein the device according to claim (1) is characterized in that the discharge pressure control circuit performs PID control of the discharge pump based on the output from the arithmetic circuit. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8145484U JPS60194234U (en) | 1984-06-01 | 1984-06-01 | Terminal pressure control device for water type air conditioner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8145484U JPS60194234U (en) | 1984-06-01 | 1984-06-01 | Terminal pressure control device for water type air conditioner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60194234U JPS60194234U (en) | 1985-12-24 |
| JPH0145005Y2 true JPH0145005Y2 (en) | 1989-12-26 |
Family
ID=30628249
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8145484U Granted JPS60194234U (en) | 1984-06-01 | 1984-06-01 | Terminal pressure control device for water type air conditioner |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60194234U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016044832A (en) * | 2014-08-20 | 2016-04-04 | 株式会社Nttファシリティーズ | Heat medium circulation system |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4602816B2 (en) * | 2005-03-25 | 2010-12-22 | 株式会社東芝 | Heat source pump control method and air conditioning heat source system |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5758031A (en) * | 1980-09-25 | 1982-04-07 | Takasago Thermal Eng Co Lts | Water circulating device for air conditioning facility |
-
1984
- 1984-06-01 JP JP8145484U patent/JPS60194234U/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016044832A (en) * | 2014-08-20 | 2016-04-04 | 株式会社Nttファシリティーズ | Heat medium circulation system |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60194234U (en) | 1985-12-24 |
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