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JP3477317B2 - Heat storage material filling ratio measuring device, heat storage material filling ratio control device, heat storage material filling ratio measuring method, and heat storage material filling ratio control method - Google Patents
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JP3477317B2 - Heat storage material filling ratio measuring device, heat storage material filling ratio control device, heat storage material filling ratio measuring method, and heat storage material filling ratio control method - Google Patents

Heat storage material filling ratio measuring device, heat storage material filling ratio control device, heat storage material filling ratio measuring method, and heat storage material filling ratio control method

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Publication number
JP3477317B2
JP3477317B2 JP17221096A JP17221096A JP3477317B2 JP 3477317 B2 JP3477317 B2 JP 3477317B2 JP 17221096 A JP17221096 A JP 17221096A JP 17221096 A JP17221096 A JP 17221096A JP 3477317 B2 JP3477317 B2 JP 3477317B2
Authority
JP
Japan
Prior art keywords
heat storage
storage material
material filling
measuring
fluid
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 - Fee Related
Application number
JP17221096A
Other languages
Japanese (ja)
Other versions
JPH1019314A (en
Inventor
伸朗 長
正嘉 豊福
誠 藤原
正治 渡部
浩男 株根
雄一 大谷
修二 角谷
尚浩 山崎
一明 長浜
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chubu Electric Power Co Inc
Mitsubishi Heavy Industries Ltd
Original Assignee
Chubu Electric Power Co Inc
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chubu Electric Power Co Inc, Mitsubishi Heavy Industries Ltd filed Critical Chubu Electric Power Co Inc
Priority to JP17221096A priority Critical patent/JP3477317B2/en
Publication of JPH1019314A publication Critical patent/JPH1019314A/en
Application granted granted Critical
Publication of JP3477317B2 publication Critical patent/JP3477317B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、例えば地域冷暖房
等の熱輸送システムに適用される蓄熱材充填率の計測と
制御を行なう装置及び方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus and method for measuring and controlling a heat storage material filling rate applied to a heat transport system such as district cooling and heating.

【0002】[0002]

【従来の技術】ダイナミック氷蓄熱やPCM(相変化物
質)を用いた熱輸送システムにおいては、シャーベット
状の氷や相変化物質を蓄熱材として利用している。この
蓄熱材は、搬送するための水等の流体と混合された状態
で搬送されるもので、ビルディングの冷暖房装置等の負
荷側に供給される混合流体は、輸送上の条件からその混
合割合として最適な値が存在しており、該混合割合を知
ることが蓄熱状態を評価する上で重要である。
2. Description of the Related Art In a heat transport system using dynamic ice heat storage or PCM (phase change material), sherbet-like ice or phase change material is used as a heat storage material. This heat storage material is carried in a state of being mixed with a fluid such as water for carrying, and the mixed fluid supplied to the load side of a building heating / cooling device, etc. is mixed as a mixing ratio due to transportation conditions. There is an optimum value, and knowing the mixing ratio is important for evaluating the heat storage state.

【0003】この蓄熱材と流体との混合割合IPF(I
ce Packing Factor:氷充填率)を測
定するために実用化されているIPF計は現在のところ
存在せず、種々の方法が提案されているのみである。
Mixing ratio of this heat storage material and fluid IPF (I
There is currently no IPF meter put to practical use for measuring the ce packing factor (ice filling rate), and only various methods have been proposed.

【0004】その中で比較的有力な方法として、配管中
を流体が流れた時に発生するコリオリ力を利用したもの
がある。以下にコリオリ式による流量測定の原理を説明
する。
Among them, a relatively effective method is to utilize the Coriolis force generated when a fluid flows in a pipe. The principle of flow rate measurement by the Coriolis method will be described below.

【0005】すなわち、コリオリ式の質量流量センサ
は、振動するパイプ内を流れる流体に作用するコリオリ
力を検出することによって流量を求めるもので、パイプ
形状、検出方法等により多くの方式が報告されている
が、ここではU字管方式を採用したものを例として図6
にその構成を示す。
That is, the Coriolis mass flow sensor obtains the flow rate by detecting the Coriolis force acting on the fluid flowing in the vibrating pipe, and many methods have been reported depending on the pipe shape, the detection method and the like. However, here, an example of adopting the U-tube system is shown in FIG.
The configuration is shown in.

【0006】同図で測定流体は分岐用エルボ1で分流さ
れ、ステンレス製のセンサハウジング2内に設けられた
2本のU字状のセンサチューブ3,3を均等に流れる。
センサチューブ3,3は、電磁オシレータ4によりその
固有振動数で振動しており、その内部に流体が流れる
と、流体に生じるコリオリ力Fにより図7(a)に示す
ような流量ゼロの場合とは異なり、図7(b)に示すよ
うにパイプを撓ませるトルクTが作用してセンサチュー
ブ3,3が角度θだけ撓む。この撓み角θはセンサチュ
ーブ3,3の同位置に配設された電磁位置検出センサ
5,5により検出される。
In the figure, the measurement fluid is divided by the branch elbow 1 and flows evenly through the two U-shaped sensor tubes 3 and 3 provided in the stainless steel sensor housing 2.
The sensor tubes 3 and 3 vibrate at their natural frequencies by the electromagnetic oscillator 4, and when a fluid flows inside the sensor tubes 3, 3 due to the Coriolis force F generated in the fluid, the flow rate is zero as shown in FIG. In contrast, as shown in FIG. 7B, the torque T for bending the pipe acts to bend the sensor tubes 3 and 3 by the angle θ. The bending angle θ is detected by electromagnetic position detection sensors 5 and 5 arranged at the same positions of the sensor tubes 3 and 3.

【0007】いま、センサチューブ3,3のばね定数を
Kとすると、撓み角θと質量流量Qの関係は次式で表わ
され、撓み角θを測定することにより質量流量Qを求め
ることができる。すなわち、 T=K・θ=F・S=2ω・Q・L・S …(1) (但し、ω:振動角速度、 S:センサチューブ3の幅、 L:センサチューブ3の長さ。)
Now, assuming that the spring constant of the sensor tubes 3 and 3 is K, the relationship between the deflection angle θ and the mass flow rate Q is expressed by the following equation, and the mass flow rate Q can be obtained by measuring the deflection angle θ. it can. That is, T = K · θ = F · S = 2ω · Q · L · S (1) (where ω is the vibration angular velocity, S is the width of the sensor tube 3, and L is the length of the sensor tube 3.)

【0008】[0008]

【発明が解決しようとする課題】しかしながら、上記コ
リオリの力を利用したIPF計を考えた場合、原理上か
ら装置が複雑なものとなることに加え、地域供給用等の
大容量の熱搬送システムでは実用上、装置の製作が非常
に困難である。
However, when considering the above-mentioned IPF meter utilizing the Coriolis force, the device becomes complicated in principle, and a large-capacity heat transfer system for local supply is used. In practice, it is very difficult to manufacture the device.

【0009】また、IPFを計測する他の方法として、
原理的には流体の重量を測定することにより、2成分の
混合割合を正確に規定することができるものであるが、
現状では、混合流体を一度輸送配管の系外の重量計に移
送する必要があり、混合流体の搬送が一時中断されてし
まうという不具合を有している。
As another method for measuring the IPF,
In principle, the mixing ratio of the two components can be accurately defined by measuring the weight of the fluid.
Under the current circumstances, it is necessary to transfer the mixed fluid once to a weight scale outside the system of the transportation pipe, and there is a problem that the conveyance of the mixed fluid is temporarily interrupted.

【0010】本発明は上記のような実情に鑑みてなされ
たもので、その目的とするところは、地域供給用等の大
容量の熱搬送システムにも適用可能で混合流体の搬送を
中断することなく、簡単な構造としながら正確な蓄熱材
の充填率を計測、制御することが可能な蓄熱材充填率計
測装置、蓄熱材充填率制御装置、蓄熱材充填率計測方法
及び蓄熱材充填率制御方法を提供することにある。
The present invention has been made in view of the above circumstances, and an object thereof is to be applicable to a large-capacity heat transfer system for regional supply and to interrupt the transfer of a mixed fluid. , A heat storage material filling rate measuring device capable of measuring and controlling an accurate filling rate of a heat storage material while having a simple structure, a heat storage material filling rate control device, a heat storage material filling rate measuring method and a heat storage material filling rate control method To provide.

【0011】[0011]

【課題を解決するための手段】請求項1記載の発明は、
既設熱輸送配管系統中に配設した、両端にフレキシブル
接手を有する計測用配管と、この計測用配管を支持すべ
くその下部に設けられ、該計測用配管中を流れる蓄熱材
と搬送用流体との混合流体の重量を測定する重量測定手
段と、この重量測定手段で得た測定値から混合流体中の
蓄熱材充填率を算出する算出手段とを具備したことを特
徴とする。
The invention according to claim 1 is
A measurement pipe having flexible joints at both ends, which is arranged in an existing heat transport pipe system, and a heat storage material and a transport fluid which are provided in a lower portion to support the measurement pipe and flow in the measurement pipe. And a calculating means for calculating the filling rate of the heat storage material in the mixed fluid from the measured value obtained by the weight measuring means.

【0012】このような構成とすることで、大容量の熱
搬送システムにも混合流体の搬送を中断することなく適
用でき、簡単な構造としながら正確な蓄熱材の充填率を
計測することができる。
With such a configuration, it can be applied to a large capacity heat transfer system without interrupting the transfer of the mixed fluid, and the filling rate of the heat storage material can be accurately measured while having a simple structure. .

【0013】請求項2記載の発明は、既設熱輸送配管系
統中に配設した、両端にフレキシブル接手を有する計測
用配管と、この計測用配管を支持すべくその下部に設置
され、該計測用配管中を流れる蓄熱材と搬送用流体との
混合流体の重量を測定する重量測定手段と、この重量測
定手段で得た測定値から混合流体中の蓄熱材充填率を算
出する算出手段と、この算出手段で得た蓄熱材充填率を
基に上記既設熱輸送配管系統を流れる蓄熱材及び搬送用
流体の少なくとも一方の流量を制御する制御手段とを具
備したことを特徴とする。
According to a second aspect of the present invention, there is provided a measuring pipe having flexible joints at both ends, which is arranged in an existing heat transport pipe system, and is installed at a lower portion of the measuring pipe to support the measuring pipe. Weight measuring means for measuring the weight of the mixed fluid of the heat storage material flowing in the pipe and the transporting fluid, and calculating means for calculating the heat storage material filling rate in the mixed fluid from the measurement value obtained by this weight measuring means, It is characterized by comprising a control means for controlling a flow rate of at least one of the heat storage material and the transporting fluid flowing through the existing heat transport piping system based on the heat storage material filling rate obtained by the calculation means.

【0014】このような構成とすることで、大容量の熱
搬送システムにも混合流体の搬送を中断することなく適
用でき、簡単な構造としながら正確な蓄熱材の充填率を
計測し、その計測値によりフィードバックをかけて所望
の蓄熱材充填率となるよう自動調整させることができ
る。
With such a configuration, it can be applied to a large capacity heat transfer system without interrupting the transfer of the mixed fluid, and the accurate filling rate of the heat storage material can be measured with a simple structure, and the measurement can be performed. The value can be fed back to automatically adjust the heat storage material filling rate.

【0015】請求項3記載の発明は、既設熱輸送配管系
統中に、両端にフレキシブル接手を有する計測用配管を
配設し、この計測用配管を支持して該計測用配管中を流
れる蓄熱材と搬送用流体との混合流体の重量を測定する
重量計を該計測用配管下部に設置し、上記重量計で得た
測定値から混合流体中の蓄熱材充填率を算出することを
特徴とする。
According to a third aspect of the present invention, a heat storage material having flexible joints at both ends is arranged in an existing heat transport pipe system, and the heat storage material that supports the measurement pipe and flows through the measurement pipe. A weight scale for measuring the weight of the mixed fluid of the carrier fluid and the transport fluid is installed in the lower portion of the measuring pipe, and the heat storage material filling rate in the mixed fluid is calculated from the measurement value obtained by the weight scale. .

【0016】このような方法とすることで、大容量の熱
搬送システムにも混合流体の搬送を中断することなく適
用でき、簡単な構造としながら正確な蓄熱材の充填率を
計測することができる。
By adopting such a method, it can be applied to a large capacity heat transfer system without interruption of the transfer of the mixed fluid, and the filling rate of the heat storage material can be accurately measured while having a simple structure. .

【0017】請求項4記載の発明は、既設熱輸送配管系
統中に、両端にフレキシブル接手を有する計測用配管を
配設し、この計測用配管を支持して該計測用配管中を流
れる蓄熱材と搬送用流体との混合流体の重量を測定する
重量計を該計測用配管下部に設置し、上記重量計で得た
測定値から混合流体中の蓄熱材充填率を算出し、算出さ
れた蓄熱材充填率を基に上記既設熱輸送配管系統を流れ
る蓄熱材及び搬送用流体の少なくとも一方の流量を制御
することを特徴とする。
According to a fourth aspect of the present invention, a heat storage material having flexible joints at both ends is arranged in an existing heat transport pipe system, and the heat storage material that supports the measurement pipe and flows through the measurement pipe. A weighing scale for measuring the weight of the mixed fluid of the transport fluid and the transport fluid is installed at the bottom of the measuring pipe, and the heat storage material filling rate in the mixed fluid is calculated from the measurement value obtained by the weighing scale, and the calculated heat storage It is characterized in that the flow rate of at least one of the heat storage material and the transporting fluid flowing through the existing heat transport piping system is controlled based on the material filling rate.

【0018】このような方法とすることで、大容量の熱
搬送システムにも混合流体の搬送を中断することなく適
用でき、簡単な構造としながら正確な蓄熱材の充填率を
計測し、その計測値によりフィードバックをかけて所望
の蓄熱材充填率となるよう自動調整させることができ
る。
By adopting such a method, it can be applied to a large capacity heat transfer system without interrupting the transfer of the mixed fluid, and an accurate filling rate of the heat storage material can be measured with a simple structure, and the measurement can be performed. The value can be fed back to automatically adjust the heat storage material filling rate.

【0019】[0019]

【発明の実施の形態】以下、本発明の実施の一形態に係
るIPF計について図面を参照して説明する。図1は既
設の熱輸送ラインに取り付けられたIPF計10の構成
を示すものである。同図で、11はIPF計測用配管で
あり、このIPF計測用配管11は既設配管12の系路
中に既設配管12と同径の配管を用いて配置される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An IPF meter according to an embodiment of the present invention will be described below with reference to the drawings. FIG. 1 shows the configuration of an IPF meter 10 attached to an existing heat transport line. In the figure, reference numeral 11 denotes a pipe for IPF measurement, and the pipe 11 for IPF measurement is arranged in the system of the existing pipe 12 by using a pipe having the same diameter as the existing pipe 12.

【0020】この場合、IPF計測用配管11の入口側
及び出口側の両端は、上下方向に剛性の小さいフレキシ
ブル接手13,13を介して既設配管12と接続される
もので、既設配管12のそれぞれフレキシブル接手1
3,13と接する端部は支点14,14で支持してい
る。
In this case, both ends of the IPF measurement pipe 11 on the inlet side and the outlet side are connected to the existing pipe 12 via flexible joints 13, 13 having small rigidity in the vertical direction. Flexible joint 1
The ends in contact with 3, 13 are supported by fulcrums 14, 14.

【0021】そして、IPF計測用配管11自体は、こ
のIPF計測用配管11下部の両端に配置された第1の
重量計15a及び第2の重量計15bで安定して支持さ
れ、その重量がそれぞれ測定される。
The IPF measurement pipe 11 itself is stably supported by the first weight scale 15a and the second weight scale 15b arranged at both ends of the lower portion of the IPF measurement pipe 11, and their weights are respectively supported. To be measured.

【0022】これら重量計15a,15bは、IPF計
測用配管11に対して垂直方向の重量のみ感知し、この
IPF計測用配管11内を流れる混合流体16の摩擦
力、運動量変化に基づく水平力には感知しない構造のも
のとし、歪みゲージを用いたもの、圧電素子を用いたも
の等で構成する。
The weight scales 15a and 15b sense only the weight in the vertical direction with respect to the IPF measuring pipe 11, and determine the frictional force of the mixed fluid 16 flowing in the IPF measuring pipe 11 and the horizontal force based on the momentum change. Is a structure that does not sense, and is composed of a strain gauge, a piezoelectric element, or the like.

【0023】次いで上記IPF計10を用いたIPFの
自動調整装置のシステム構成について図2により説明す
る。図中、21が蓄熱材としての氷を貯蔵している氷貯
槽、22がこの氷貯槽21に貯蔵されている氷に混合し
て搬送させる流体としての水を貯蔵している水貯槽であ
り、氷貯槽21に貯蔵されている氷は氷量制御弁23を
介して、水貯槽22に貯蔵されている水は水量制御弁2
4を介してそれぞれポンプ25に供給され、ここで混合
された後にこのポンプ25の吐出力により上記IPF計
10を含む既設配管12を流れてビルディングの冷暖房
装置等の負荷26に与えられるものである。
Next, the system configuration of the automatic IPF adjusting apparatus using the IPF meter 10 will be described with reference to FIG. In the figure, 21 is an ice storage tank that stores ice as a heat storage material, and 22 is a water storage tank that stores water as a fluid to be mixed with the ice stored in the ice storage tank 21 and conveyed. The ice stored in the ice storage tank 21 passes through the ice amount control valve 23, and the water stored in the water storage tank 22 passes through the water amount control valve 2
4 is supplied to each of the pumps 25 via the pump 4, and after being mixed here, the discharge force of the pumps 25 flows through the existing pipe 12 including the IPF meter 10 and is applied to the load 26 such as a cooling / heating device of the building. .

【0024】しかるに、上記IPF計10で得られたI
PF測定値27は制御器28へ送出される。制御器28
では、IPF測定値27から混合流体16のIPFを算
出し、その算出結果から予め設定されているIPFとの
誤差値を算出して、上記氷量制御弁23、水量制御弁2
4へそれぞれフィードバック信号29a,29bとして
帰還させ、各流入量を加減制御させる。
However, I obtained by the above IPF meter 10
The PF measurement value 27 is sent to the controller 28. Controller 28
Then, the IPF of the mixed fluid 16 is calculated from the IPF measurement value 27, and an error value with respect to the preset IPF is calculated from the calculation result, and the ice amount control valve 23 and the water amount control valve 2 are calculated.
4 as feedback signals 29a and 29b, respectively, to control each inflow amount.

【0025】上記のような構成にあって、次のその動作
について説明する。まずその動作原理を図3を用いて述
べる。いま、図中に示す如く、IPF計10全体の体積
V、IPF計10内の氷の体積VICE 、IPF計10内
の水の体積VW 、第1の重量計15aと第2の重量計1
5bの各測定値WA ,WB の和WA+WB とし、水の比
重γW (=1000kg/m3 )、氷の比重γICE (=
920kg/m3 )、IPF計10内に水のみがある場
合の重量WW 、IPF計10内に水と氷が混在する場合
の重量W、IPF計10内に氷のみがある場合の重量W
ICE とすると、次式によりIPFを導き出すことができ
る。すなわち、
The operation of the above arrangement will be described below. First, the operating principle will be described with reference to FIG. Now, as shown in the figure, the volume V of the entire IPF meter 10, the volume V ICE of ice in the IPF meter 10, the volume V W of water in the IPF meter 10, the first weighing scale 15a and the second weighing scale. 1
Each measurement W A of 5b, and the sum W A + W B of W B, water specific gravity γ W (= 1000kg / m 3 ), ice density gamma ICE (=
920 kg / m 3 ), the weight W W when there is only water in the IPF meter 10, the weight W when water and ice are mixed in the IPF meter 10, and the weight W when there is only ice in the IPF meter 10
With ICE , the IPF can be derived by the following equation. That is,

【0026】[0026]

【数1】 となるもので、得られたIPFと(W/WW )との関係
を図4に示す。ここで、WW は一定値であるから、(W
/WW )はWのみに比例することとなる。
[Equation 1] The relationship between the obtained IPF and (W / WW ) is shown in FIG. Here, since W W is a constant value, (W
/ W W) becomes to be proportional only to the W.

【0027】上記のような原理の下に、上記図2に示し
た如く熱輸送ライン中にIPF計10を配設し、IPF
測定値27を制御器28に送出して、設定したIPF値
となるようなフィードバック信号29a,29bを作成
させて氷量制御弁23、水量制御弁24へ帰還させるこ
とで、自動的なIPFの調整を行なうことができる。
Under the above principle, the IPF meter 10 is arranged in the heat transport line as shown in FIG.
The measured value 27 is sent to the controller 28, and the feedback signals 29a and 29b that produce the set IPF value are generated and fed back to the ice amount control valve 23 and the water amount control valve 24, thereby automatically adjusting the IPF. Adjustments can be made.

【0028】図5は上記フィードバックループにおける
一定時間ごとに行なわれる一連の処理手順を例示するも
のであり、その当初にIPF計10からの測定値27で
ある値W/WW を得る(ステップS1)。
[0028] Figure 5 is intended to illustrate a series of processing procedures performed at fixed time intervals in the feedback loop to obtain a measure 27 is the value W / W W from IPF meter 10 to its original (step S1 ).

【0029】次いで、上記式(3),(4)を用いて上
記制御器28で測定値IPFM を算出する(ステップS
2)。その後、制御器28で予め与えられている設定値
IPFS を入力し(ステップS3)、測定値IPFM
設定値IPFS との誤差ΔIPFを計算「IPFM −I
PFS 」により算出する(ステップS4)。
Next, the controller 28 calculates the measured value IPF M using the equations (3) and (4) (step S).
2). Then, the preset value IPF S given in advance by the controller 28 is input (step S3), and the error ΔIPF between the measured value IPF M and the set value IPF S is calculated “IPF M −I
PF S ”(step S4).

【0030】こうして得た誤差ΔIPFの符号が負であ
るか否かを判断することによりフィードバック制御すべ
き方向を判断するもので(ステップS5)、例えば誤差
ΔIPFの符号が負であれば、上記フィードバック信号
29aにより氷量制御弁23を一定量開けて、混合流体
16における氷供給量を増加させる(ステップS6)。
The direction in which the feedback control should be performed is judged by judging whether the sign of the error ΔIPF obtained in this way is negative (step S5). For example, if the sign of the error ΔIPF is negative, the above feedback is performed. The signal 29a opens the ice amount control valve 23 by a certain amount to increase the ice supply amount in the mixed fluid 16 (step S6).

【0031】また、反対に誤差ΔIPFの符号が負では
ない場合には、上記フィードバック信号29aにより氷
量制御弁23を一定量閉めて、混合流体16における氷
供給量を減少させる(ステップS7)。
On the contrary, when the sign of the error ΔIPF is not negative, the feedback control signal 29a closes the ice amount control valve 23 by a certain amount to decrease the ice supply amount in the mixed fluid 16 (step S7).

【0032】なお、上記図5の処理ではフィードバック
信号29aに基づいて氷量制御弁23のみを開閉制御
し、混合流体16における氷供給量を増減させるものと
したが、これに限らず、フィードバック信号29aに代
えてフィードバック信号29bに基づいて水量制御弁2
4のみを開閉制御し、混合流体16における水供給量を
増減させるものとしてもよく、さらにはこれらフィード
バック信号29a,29bを共に用いて既設配管12及
びIPF計測用配管11を流れる混合流体16全体の流
量を変えることなくIPFを制御させるようにしてもよ
い。
In the processing shown in FIG. 5, only the ice amount control valve 23 is opened / closed based on the feedback signal 29a to increase / decrease the ice supply amount in the mixed fluid 16. However, the present invention is not limited to this. Water quantity control valve 2 based on feedback signal 29b instead of 29a
4 may be controlled to be opened / closed to increase / decrease the amount of water supply in the mixed fluid 16, and further, the feedback signal 29a, 29b may be used together to control the entire mixed fluid 16 flowing through the existing pipe 12 and the IPF measurement pipe 11. The IPF may be controlled without changing the flow rate.

【0033】また、上記実施の形態では蓄熱材として氷
を、流体として水を使用した例を示したが、例えば蓄熱
材として相変化物質(PCM)を用いるなど、他のもの
を用いても差し支えない。その他、本発明は上記実施の
形態に限定されるものではなく、その要旨を逸脱しない
範囲内で種々変形可能であるものとする。
Further, in the above-described embodiment, an example in which ice is used as the heat storage material and water is used as the fluid is shown. However, other materials such as a phase change material (PCM) may be used as the heat storage material. Absent. Besides, the present invention is not limited to the above-described embodiment, and various modifications can be made without departing from the gist thereof.

【0034】[0034]

【発明の効果】以上に述べた如く本発明によれば、地域
供給用等の大容量の熱搬送システムにも適用可能で混合
流体の搬送を中断することなく、簡単な構造としながら
正確な蓄熱材の充填率を計測、制御することが可能な蓄
熱材充填率計測装置、蓄熱材充填率制御装置、蓄熱材充
填率計測方法及び蓄熱材充填率制御方法を提供すること
ができる。
As described above, according to the present invention, it can be applied to a large-capacity heat transfer system for local supply, etc., and can accurately transfer heat without interrupting the transfer of the mixed fluid. It is possible to provide a heat storage material filling rate measuring device, a heat storage material filling rate control device, a heat storage material filling rate measuring method, and a heat storage material filling rate control method capable of measuring and controlling the material filling rate.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の実施の一形態に係るIPF計の構成を
示す図。
FIG. 1 is a diagram showing a configuration of an IPF meter according to an embodiment of the present invention.

【図2】同実施の形態に係るIPFの自動調整装置のシ
ステム構成を示す図。
FIG. 2 is a diagram showing a system configuration of an IPF automatic adjustment apparatus according to the embodiment.

【図3】同実施の形態に係るIPF計の動作原理を説明
する図。
FIG. 3 is a view for explaining the operation principle of the IPF meter according to the same embodiment.

【図4】同実施の形態に係るIPF計の測定値とIPF
値との関係を示す図。
FIG. 4 shows measured values and IPF of the IPF meter according to the same embodiment.
The figure which shows the relationship with a value.

【図5】同実施の形態に係る処理手順を示すフローチャ
ート。
FIG. 5 is a flowchart showing a processing procedure according to the embodiment.

【図6】コリオリ式質量流量センサの構成を示す図。FIG. 6 is a diagram showing a configuration of a Coriolis mass flow sensor.

【図7】コリオリ式質量流量センサの動作原理を説明す
る図。
FIG. 7 is a diagram illustrating the operating principle of a Coriolis mass flow sensor.

【符号の説明】[Explanation of symbols]

1…流体分岐用エルボ 2…センサハウジング 3…センサチューブ(U字状管) 4…電磁オシレータ 5…電磁位置検出センサ 10…IPF計 11…IPF計測用配管 12…既設配管 13…フレキシブル接手 14…支点 15a…第1の重量計 15b…第2の重量計 16…混合流体 21…氷貯槽 22…水貯槽 23…氷量制御弁 24…水量制御弁 25…ポンプ 26…負荷 27…IPF測定値 28…制御器 29a,29b…フィードバック信号 1 ... Elbow for fluid branch 2 ... Sensor housing 3 ... Sensor tube (U-shaped tube) 4 ... Electromagnetic oscillator 5 ... Electromagnetic position detection sensor 10 ... IPF meter 11 ... IPF measurement piping 12 ... Existing piping 13 ... Flexible joint 14 ... fulcrum 15a ... first weighing scale 15b ... second weighing scale 16 ... Mixed fluid 21 ... Ice storage tank 22 ... Water storage tank 23 ... Ice quantity control valve 24 ... Water control valve 25 ... Pump 26 ... Load 27 ... IPF measurement value 28 ... Controller 29a, 29b ... Feedback signal

───────────────────────────────────────────────────── フロントページの続き (72)発明者 藤原 誠 兵庫県高砂市荒井町新浜2丁目1番1号 三菱重工業株式会社高砂製作所内 (72)発明者 渡部 正治 兵庫県高砂市荒井町新浜2丁目1番1号 三菱重工業株式会社高砂研究所内 (72)発明者 株根 浩男 兵庫県高砂市荒井町新浜2丁目1番1号 三菱重工業株式会社高砂研究所内 (72)発明者 大谷 雄一 兵庫県高砂市荒井町新浜2丁目1番1号 三菱重工業株式会社高砂研究所内 (72)発明者 角谷 修二 兵庫県高砂市荒井町新浜2丁目1番1号 三菱重工業株式会社高砂製作所内 (72)発明者 山崎 尚浩 兵庫県高砂市荒井町新浜2丁目8番19号 高菱エンジニアリング株式会社内 (72)発明者 長浜 一明 広島県広島市西区横川新町9丁目12番 中外テクノス株式会社内 (56)参考文献 特開 平6−265184(JP,A) 特開 昭59−57833(JP,A) 特開 平7−190421(JP,A) 実開 平1−110329(JP,U) (58)調査した分野(Int.Cl.7,DB名) F24F 5/00 102 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Makoto Fujiwara 2-1-1 Shinhama, Arai-cho, Takasago-shi, Hyogo Mitsubishi Heavy Industries, Ltd. Takasago Plant (72) Inventor Shoji Watanabe 2-chome, Niihama, Arai-cho, Takasago-shi, Hyogo No. 1 Mitsubishi Heavy Industries, Ltd. Takasago Laboratory (72) Inventor Hiroo Sone 2-1-1, Niihama, Arai-cho, Takasago-shi, Hyogo Prefecture Mitsubishi Heavy Industries Ltd. Takasago Laboratory (72) Inventor Yuichi Otani 2 Niihama, Arai-cho, Takasago-shi, Hyogo Prefecture 1-1-1 Mitsubishi Heavy Industries, Ltd. Takasago Research Institute (72) Inventor Shuji Sumiya 2-11-1, Niihama, Arai-cho, Takasago-shi, Hyogo Prefecture Mitsubishi Heavy Industries Takasago Works (72) Inventor Naohiro Yamazaki Arai-cho, Takasago-shi, Hyogo Prefecture 2-8-19 Niihama Takahishi Engineering Co., Ltd. (72) Inventor Kazuaki Nagahama Hiroshima, Hiroshima 9-12 Yokomachi Shinmachi, Nishi-ku, Chugai Technos Co., Ltd. (56) Reference JP-A-6-265184 (JP, A) JP-A-59-57833 (JP, A) JP-A-7-190421 (JP, A) Jitsukaihei 1-110329 (JP, U) (58) Fields surveyed (Int.Cl. 7 , DB name) F24F 5/00 102

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 既設熱輸送配管系統中に配設した、両端
にフレキシブル接手を有する計測用配管と、 この計測用配管を支持すべくその下部に設けられ、該計
測用配管中を流れる蓄熱材と搬送用流体との混合流体の
重量を測定する重量測定手段と、 この重量測定手段で得た測定値から混合流体中の蓄熱材
充填率を算出する算出手段とを具備したことを特徴とす
る蓄熱材充填率計測装置。
1. A measuring pipe having flexible joints at both ends, which is arranged in an existing heat transport piping system, and a heat storage material which is provided at a lower portion to support the measuring pipe and flows through the measuring pipe. A weight measuring means for measuring the weight of the mixed fluid of the carrier fluid and the transport fluid, and a calculating means for calculating the heat storage material filling rate in the mixed fluid from the measurement value obtained by the weight measuring means. Heat storage material filling rate measuring device.
【請求項2】 既設熱輸送配管系統中に配設した、両端
にフレキシブル接手を有する計測用配管と、 この計測用配管を支持すべくその下部に設置され、該計
測用配管中を流れる蓄熱材と搬送用流体との混合流体の
重量を測定する重量測定手段と、 この重量測定手段で得た測定値から混合流体中の蓄熱材
充填率を算出する算出手段と、 この算出手段で得た蓄熱材充填率を基に上記既設熱輸送
配管系統を流れる蓄熱材及び搬送用流体の少なくとも一
方の流量を制御する制御手段とを具備したことを特徴と
する蓄熱材充填率制御装置。
2. A measuring pipe having flexible joints at both ends, which is arranged in an existing heat transport piping system, and a heat storage material which is installed at a lower portion to support the measuring pipe and flows through the measuring pipe. A weight measuring means for measuring the weight of the mixed fluid of the carrier fluid and the transport fluid, a calculating means for calculating the heat storage material filling rate in the mixed fluid from the measurement value obtained by the weight measuring means, and a heat storage obtained by the calculating means. A heat storage material filling rate control device comprising: a control means for controlling the flow rate of at least one of the heat storage material and the transport fluid flowing through the existing heat transport piping system based on the material filling rate.
【請求項3】 既設熱輸送配管系統中に、両端にフレキ
シブル接手を有する計測用配管を配設し、 この計測用配管を支持して該計測用配管中を流れる蓄熱
材と搬送用流体との混合流体の重量を測定する重量計を
該計測用配管下部に設置し、 上記重量計で得た測定値から混合流体中の蓄熱材充填率
を算出することを特徴とする蓄熱材充填率計測方法。
3. An existing heat-transporting piping system is provided with a measuring pipe having flexible joints at both ends, and the measuring pipe is supported to support a heat storage material and a conveying fluid. A heat storage material filling rate measuring method, characterized in that a weight scale for measuring the weight of the mixed fluid is installed at a lower portion of the measuring pipe, and the heat storage material filling rate in the mixed fluid is calculated from the measurement value obtained by the weight scale. .
【請求項4】 既設熱輸送配管系統中に、両端にフレキ
シブル接手を有する計測用配管を配設し、 この計測用配管を支持して該計測用配管中を流れる蓄熱
材と搬送用流体との混合流体の重量を測定する重量計を
該計測用配管下部に設置し、 上記重量計で得た測定値から混合流体中の蓄熱材充填率
を算出し、 算出された蓄熱材充填率を基に上記既設熱輸送配管系統
を流れる蓄熱材及び搬送用流体の少なくとも一方の流量
を制御することを特徴とする蓄熱材充填率制御方法。
4. An existing heat-transporting piping system is provided with a measuring pipe having flexible joints at both ends, and the measuring pipe is supported to connect the heat storage material and the transporting fluid. A weighing scale for measuring the weight of the mixed fluid is installed at the lower part of the pipe for measurement, the heat storage material filling rate in the mixed fluid is calculated from the measurement value obtained by the above weighing scale, and based on the calculated heat storage material filling rate. A heat storage material filling rate control method, characterized in that the flow rate of at least one of the heat storage material and the transport fluid flowing through the existing heat transport piping system is controlled.
JP17221096A 1996-07-02 1996-07-02 Heat storage material filling ratio measuring device, heat storage material filling ratio control device, heat storage material filling ratio measuring method, and heat storage material filling ratio control method Expired - Fee Related JP3477317B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17221096A JP3477317B2 (en) 1996-07-02 1996-07-02 Heat storage material filling ratio measuring device, heat storage material filling ratio control device, heat storage material filling ratio measuring method, and heat storage material filling ratio control method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17221096A JP3477317B2 (en) 1996-07-02 1996-07-02 Heat storage material filling ratio measuring device, heat storage material filling ratio control device, heat storage material filling ratio measuring method, and heat storage material filling ratio control method

Publications (2)

Publication Number Publication Date
JPH1019314A JPH1019314A (en) 1998-01-23
JP3477317B2 true JP3477317B2 (en) 2003-12-10

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Country Status (1)

Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018127712A1 (en) * 2017-01-09 2018-07-12 Robert Long Thermal management systems and methods

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018127712A1 (en) * 2017-01-09 2018-07-12 Robert Long Thermal management systems and methods
US11506405B2 (en) 2017-01-09 2022-11-22 Organic Heat Exchangers Limited Thermal management systems and methods

Also Published As

Publication number Publication date
JPH1019314A (en) 1998-01-23

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