JP6025111B2 - Steam flow measurement method and heat supply system - Google Patents

Description

  The present invention relates to a steam flow rate measuring method and a heat supply system.

  In factories and the like, steam is used in a wide range of applications from heating in production processes to heating and humidification of air conditioning. For example, a system is known in which piping extending from a centrally installed boiler is laid in many places in a factory and steam is sent to a production process or the like via the piping (for example, see Patent Document 1).

JP-A-6-249450

  Conventionally, the flow rate of the steam supplied from the heat supply system to the external device (heat demand section) is generally measured using an orifice flow meter. However, since the measurement value of the orifice flowmeter changes depending on the wetness of the steam, the measurement is difficult when the wetness of the steam flowing through the pipe is unknown.

  The present invention has been made in view of the above-described problems of the prior art, and is a method capable of easily measuring the flow rate of steam regardless of the wetness of the steam, and a heat supply system excellent in steam controllability. The purpose is to provide.

The steam flow rate measuring method of the present invention is characterized in that the flow rate of wet steam flowing through a pipe is measured by an ultrasonic flow meter, and the measured value is obtained as a flow rate of only steam.
According to this method, the flow rate of only the steam can be acquired with a small error regardless of the wetness of the wet steam.

In the method for measuring the steam flow rate of the present invention, the flow rate of the wet steam flowing through the pipe is measured by an ultrasonic flowmeter, and the measured value is acquired as the total flow rate of the wet steam, and then the measured value is converted to the wetness. The correction is performed using the density of the steam, and the correction value is acquired as the total flow rate of the wet steam.
According to this method, the total flow rate of the wet steam can be acquired with a small error regardless of the wetness of the wet steam.

The heat supply system of the present invention measures the flow rate of the steam that is provided in the pipe near the inlet of the heat demand section and the steam source that supplies steam to the heat demand section through the pipe and circulates in the pipe. It has an ultrasonic flow meter and a control part which controls the output of the steam source based on the measured value of the ultrasonic flow meter.
According to this configuration, since the flow rate of the steam is measured using the ultrasonic flow meter, the steam flow rate can be acquired with a small error regardless of the wetness of the steam. And since the output of a vapor | steam source is adjusted based on this vapor | steam flow volume, the calorie | heat amount supplied with respect to a heat demand part can be controlled accurately.

The control unit obtains the measured value of the ultrasonic flowmeter as a flow rate of only steam out of the wet steam flowing through the pipe, and the heat demand unit based on the steam flow rate. A supply heat amount calculation operation for calculating the supply heat amount being supplied, and an output adjustment operation for adjusting the output of the steam source based on a comparison between the set heat amount to be supplied to the heat demand section and the supply heat amount It is good also as composition to do.
According to this configuration, the measurement value of the ultrasonic flowmeter is acquired as the flow rate of only the steam, and the supply heat amount is calculated using this, so that the steam flow rate can be easily acquired and the supply heat amount to the heat demand section is easy. Can be estimated. And by adjusting the output of the steam source based on the acquired supply heat quantity, the desired heat quantity can be accurately supplied to the heat demand section.

The control unit corrects the total flow rate using the wet steam density, and a total flow rate acquisition operation for acquiring the measurement value of the ultrasonic flowmeter as a total flow rate of the wet steam flowing through the pipe. A total flow correction operation, a supply heat amount calculation operation for calculating a supply heat amount supplied to the heat demand unit based on the corrected total flow rate, a set heat amount to be supplied to the heat demand unit, and the supply heat amount It is good also as a structure which performs the output adjustment operation | movement which adjusts the output of the said steam source based on these comparisons.
According to this configuration, the measurement value of the ultrasonic flowmeter is acquired as the total flow rate of the wet steam, and the supply heat amount is calculated using a value obtained by correcting the total flow rate using the wet steam density. Can be estimated with higher accuracy. And by adjusting the output of the steam source based on the acquired supply heat quantity, the desired heat quantity can be accurately supplied to the heat demand section.

  ADVANTAGE OF THE INVENTION According to this invention, the heat supply system excellent in the method of measuring a vapor | steam flow volume easily irrespective of the wetness of a vapor | steam, and the controllability of a vapor | steam can be provided.

Schematic which shows the heat supply system which is one embodiment of this invention. The figure which shows an example of a structure of an ultrasonic flowmeter. The figure which shows the measuring apparatus used for the measurement accuracy verification of the ultrasonic flowmeter. The graph which shows the relationship between total flow error [%] and wetness [%]. The graph which shows the relationship between measurement error [%] and wetness [%]. The graph which shows the relationship between total flow error [%] (correction) and wetness [%]. The graph which shows the measurement error when measuring dry steam. The figure which shows an example of the structure which concerns on the modification of an ultrasonic flowmeter.

FIG. 1 is a schematic diagram showing a heat supply system according to an embodiment of the present invention.
As shown in FIG. 1, the heat supply system S <b> 1 includes a steam source 10, an ultrasonic flow meter 20, a pipe 30 that connects them, and a control unit 70. The heat supply system S <b> 1 supplies the steam generated in the steam source 10 to the heat demand unit 90 (external device) through the pipe 30 under the control of the control unit 70. The ultrasonic flow meter 20 is installed in the pipe 30 near the steam inlet of the heat demand section 90.

  The steam source 10 is, for example, a boiler, and the heat demand unit 90 is, for example, various production apparatuses or air conditioners. The pipe 30 may be heat-retained by heat retention means (not shown). As the heat retaining means, a heat insulating material that covers the outer surface of the pipe, a heating device that heats the pipe, or the like can be used.

As the ultrasonic flow meter 20, an appropriate one can be selected and used according to the temperature and pressure of the steam flowing through the pipe 30. FIG. 2 is a diagram illustrating an example of the configuration of the ultrasonic flowmeter.
An ultrasonic flow meter 20 illustrated in FIG. 2 includes a cylindrical tube body 21 and a pair of ultrasonic transmission units 22 and a reception unit 23 provided in the middle of the tube body 21. The ultrasonic flow meter 20 is installed in the pipe 30 so that the axial direction of the tube body 21 and the flow direction of the steam are substantially parallel. The ultrasonic flow meter 20 is preferably installed in the pipe 30 so that the ultrasonic transmission unit 22 and the reception unit 23 are in a horizontal state.

  The ultrasonic transmission unit 22 and the reception unit 23 are arranged in a state of being exposed in the tube body 21 through openings 24 a and 25 a of attachment portions 24 and 25 provided on the side surface of the tube body 21. In the present embodiment, as described above, since the ultrasonic transmission unit 22 and the reception unit 23 are installed in the pipe 30 so as to be in a horizontal state, the steam drainage is accumulated in the mounting units 24 and 25 so that the flow rate is increased. It is possible to prevent the occurrence of measurement failures.

  The ultrasonic flowmeter 20 transmits and receives ultrasonic waves between the ultrasonic transmission unit 22 and the reception unit 23 with respect to the vapor (measuring fluid) flowing from the vapor inlet to the vapor outlet in the tube body 21. Specifically, the ultrasonic flowmeter 20 transmits ultrasonic waves obliquely into the tube body 21, and calculates the difference in the propagation time of the ultrasonic signal between the direction along the steam flow and the direction against the steam flow. Detect and output to a flow rate converter (not shown). In the flow rate converter, the flow rate of the steam is calculated based on the difference in the propagation time of the ultrasonic signal, and the flow rate of the steam flowing through the tube body 21 is calculated by multiplying the steam flow rate by the cross-sectional area of the tube body 21. Is done. In the case of this embodiment, the flow rate value calculated by the flow rate converter is output to the control unit 70 as a measured value of the steam flow rate. In the control unit 70, the amount of heat supplied to the heat demand unit 90 is controlled based on the measurement value output from the ultrasonic flow meter 20.

  In the heat supply system of the present embodiment having the above-described configuration, the ultrasonic flowmeter 20 is used as a flow rate measuring unit for the steam supplied to the heat demand unit 90 via the pipe 30. Thereby, compared with the case where the conventional orifice flowmeter is used, it is possible to measure the flow volume of the vapor | steam which distribute | circulates the inside of the piping 30 simply and with high precision.

  Here, FIG. 3 is a diagram showing a measuring apparatus used for measuring accuracy verification of the ultrasonic flowmeter. The measuring device 100 includes a boiler 101, a superheater 102, pressure regulating valves 103 and 104, a first heat exchanger 105, a measurement pipe 106, an ultrasonic flow meter 20, a back pressure valve 107, a second pressure valve 107, and a second pressure valve 107. The heat exchanger 108 and the Coriolis flow meter 109 are connected in a ring shape via a steam pipe 150 and a condensed water pipe 151.

  In addition, the measuring device 100 is provided with a cooling device 110 that uses water as a cooling medium and a control unit 170 that controls the measuring device 100. The cooling device 110 includes a cooling water storage unit 111, a cooling tower 112, a first cooling unit 113, and a second cooling unit 114, which are annularly connected via a cooling water pipe 115. Has been. The control unit 170 comprehensively controls the entire measurement apparatus 100 including the cooling device 110.

  In the measuring apparatus 100, the steam generated in the boiler 101 is converted into superheated steam in the superheater 102, and then adjusted to a predetermined pressure by the pressure control valves 103 and 104 and supplied to the first heat exchanger 105. In the first heat exchanger 105, the steam in the steam pipe 150 is cooled to a predetermined temperature by heat exchange between the steam pipe 150 and the first cooling unit 113 of the cooling device 110. As a result, the steam flowing through the steam pipe 150 becomes wet steam containing condensed water and is introduced into the measurement pipe 106.

  The wetness of the wet steam generated in the first heat exchanger 105 includes the temperature and pressure of the steam supplied to the first cooling unit 113 (measured by the thermometer 120 and the pressure gauge 123), and the first cooling. The temperature and flow rate of the cooling water supplied to the unit 113 (measured by the thermometer 121 and the cooling water flow meter 127) can be adjusted.

  The wet steam introduced into the measurement pipe 106 is subjected to flow measurement by the ultrasonic flowmeter 20 installed in the middle of the measurement pipe 106. Further, the pressure and temperature of the wet steam are measured by a pressure gauge 124 and a thermometer 125 provided on the downstream side of the ultrasonic flowmeter 20. The wet steam after the measurement is supplied to the second heat exchanger 108 while being adjusted to a constant pressure by the back pressure valve 107.

  In the second heat exchanger 108, the steam in the steam pipe 150 is cooled to a predetermined temperature by heat exchange between the second cooling unit 114 of the cooling device 110 and the steam pipe 150, and almost all of the steam is converted into condensed water. It returns to the boiler 101 through the water pipe 151. Since the cooling water after being used for cooling the steam in the second cooling unit 114 has a relatively high temperature, it is cooled by the cooling tower 112 and then returned to the cooling water storage unit 111 such as an underground water tank. .

  The condensed water discharged from the second heat exchanger 108 is measured for flow rate by a Coriolis flow meter 109. Thereby, the total flow rate of the wet steam measured by the ultrasonic flow meter 20 can be acquired. The condensed water after being measured by the Coriolis flow meter 109 is supplied to the boiler 101 and reused.

  According to the measuring apparatus 100 described above, the wet steam controlled in the first heat exchanger 105 is generated and measured by the ultrasonic flow meter 20, and then the Coriolis flow meter 109 is used. The total flow rate of wet steam used for the measurement (total flow rate of steam and condensed water) can be measured. Thereby, the measured value of the ultrasonic flowmeter 20 about the vapor | steam of arbitrary wetness can be verified by the comparison with the measured value by the Coriolis flowmeter 109. FIG.

  Table 1 below shows sample conditions for an accuracy verification test of an ultrasonic flowmeter using the measuring apparatus 100. Note that the pressure and flow conditions shown in Table 1 are obtained when dry steam is supplied to the measurement pipe 106 without operating the first heat exchanger 105 and the dry steam is measured by the ultrasonic flowmeter 20. Pressure and flow rate.

  Here, FIG. 7 is a graph showing a measurement error of the ultrasonic flow meter 20 with respect to the Coriolis flow meter 109 when dry steam is measured by the measurement apparatus 100. When the measurement target is dry steam, the measurement value of the ultrasonic flow meter 20 and the measurement value of the Coriolis flow meter 109 are in good agreement, and the difference between them is about ± 1% in a wide flow range. In the measurement of wet steam whose conditions are shown in Table 1, the pressure and flow conditions where the error was within ± 1% in the measurement of dry steam were selected, and measurement was performed by generating wet steam under each condition. .

  In Table 1, a plurality of numerical values described in the column of wetness indicate that the measurement was performed by changing the wetness conditions in a state where the pressure and the flow rate were fixed. Specifically, the condition shown in the first row of Table 1 is that the wetness is 6.1 by adjusting the cooling conditions in the first heat exchanger 105 for dry steam having a pressure of 0.2 MPaA and a flow rate of 200 kg / h. It shows that three kinds of wet steam of%, 7.8%, and 15.1% were generated, and the measurement by the ultrasonic flowmeter 20 and the Coriolis flowmeter 109 was performed for each. Overall, measurements were made for 36 conditions.

FIG. 4 shows the difference (total flow error [%]) between the measured value of the ultrasonic flow meter 20 and the measured value of the Coriolis flow meter 109 for each condition shown in Table 1, and the wetness [%] on the horizontal axis. Is a graph plotted as The total flow error ε _t was calculated by the following equation (1).

  As shown in FIG. 4, the greater the wetness, the greater the total flow rate error on the minus side. That is, as the wetness degree increases, the ultrasonic flowmeter 20 outputs a smaller measurement value to the Coriolis flowmeter 109.

On the other hand, FIG. 5 shows the difference (measurement error [%]) between the measured value of the ultrasonic flow meter 20 and the value obtained by subtracting the flow rate corresponding to the condensed water from the measured value of the Coriolis flow meter 109, and the horizontal axis is wet. It is the graph plotted as degree [%]. The measurement error ε _r can be calculated by the above equation (2). The coefficient x in the equation (2) is a ratio of the steam contained in the wet steam. The coefficient x can be expressed as x = 1−β when the wetness of the wet steam is β (0 <β <1).

As shown in FIG. 5, the measurement error ε _r is suppressed within ± 3%, and no dependency on the wetness is observed. From this result, if the measurement value of the ultrasonic flowmeter 20 is acquired not as a total flow rate of steam and condensed water but as a flow rate of only steam, the steam flow rate is measured with practical accuracy regardless of the wetness. be able to.

It is to be noted that the orifice flow meter conventionally used as a steam flow meter does not have a tendency that the measurement error ε _r tends to be substantially constant with respect to the wetness as shown in FIG. It has become clear. Specifically, in the case of an orifice flow meter, the tendency that the total flow error ε _t becomes larger on the minus side as the wetness increases is the same as in the case of the ultrasonic flow meter, but the measurement error ε _r The greater the degree, the greater the positive side. As described above, since the total flow error ε _t and the measurement error ε _r both depend on the wetness, it is difficult to accurately measure the flow of wet steam whose wetness is unknown in the case of an orifice flow meter. It is.

On the other hand, as shown in FIG. 4, since the total flow error ε _t is a parameter that depends on the wetness, it can be corrected by using another state quantity that depends on the wetness.
Therefore, looking at the calculation formula of the ultrasonic flow rate shown in the following formula (3), ρ is the saturated vapor density, K is the K factor, A is the cross-sectional area of the tube body 21, and u _uls is the vapor flow velocity. Among these, the K factor is a constant, and u _uls is the output value of the ultrasonic flowmeter 20, so that the fluctuation factor of the ultrasonic flow rate Q _uls is substantially a term of the saturated vapor density ρ.

In correcting the term of the saturated vapor density ρ, the present inventors define a wet vapor density ρ _wet assuming a homogeneous flow as shown in the equation (4), and an ultrasonic flow rate as shown in the equation (5). Tried to correct. That is, by the wet steam density ρ _wet obtained by proportionally dividing the steam-only density ρ _str and the density of condensed water ρ _wat according to the coefficient x (= 1−β) related to the wetness, the formula (5 ), The saturated vapor density ρ was corrected.

FIG. 6 shows the difference (total flow error [%]) between the correction value obtained by correcting the measurement value of the ultrasonic flow meter 20 by the equation (5) and the measurement value of the Coriolis flow meter 109, and the wetness [ %] Is a graph plotted.
The total flow error shown in FIG. 6 is in the range of ± 3% or less under all conditions. Thus, it is understood that a good agreement with the measured value of the Coriolis flow meter 109 can be obtained by correcting the measured value of the ultrasonic flow meter 20 with the wet steam density ρ _wet .

As described in detail above, by using the ultrasonic flowmeter 20 for measuring the wet steam flow rate, the steam flow rate can be measured with practical accuracy regardless of the wetness of the wet steam. According to the verification test of the present inventors, as shown in FIG. 5, even when the measurement value of the ultrasonic flowmeter 20 is acquired as the flow rate of only the steam, the flow rate is measured with a measurement error within ± 3%. Can be measured. Furthermore, if the measurement value of the ultrasonic flowmeter 20 is corrected using the _wet steam density ρ _wet , the total flow rate can be measured with a measurement error within ± 3%.

  In the above description, the case where the ultrasonic transmitter 22 and the receiver 23 are installed in the pipe 30 so as to be in a horizontal state has been described as an example, but the present invention is not limited to this. Absent. For example, as shown in FIG. 8, the ultrasonic flow meter 20 may be installed in the pipe 30 so that the mounting portions 24 and 25 are arranged in the vertical direction (vertical direction). In this configuration, the valve 26 may be provided in the connection portion 25 arranged on the lower side in the vertical direction. According to this, for example, when the flow rate is not measured, by opening the valve 26, the drain accumulated in the connecting portion 25 can be discharged. Therefore, it is not necessary to separately provide a drain discharge mechanism, and it is possible to provide a heat supply system S1 with high added value.

Next, supply heat amount control in the heat supply system S1 will be described.
As described above, by using the ultrasonic flowmeter 20, it is possible to accurately measure the flow rate of only the steam in the wet steam, and it is possible to accurately measure the total flow rate by further correcting the vapor density. Therefore, in the heat supply system S1 of the present embodiment, (control 1) the supply heat amount control can be executed using the measurement value of the ultrasonic flow meter 20 as it is, and (control 2) the measurement of the ultrasonic flow meter 20 is performed. It is also possible to correct the value using the wet steam density and execute the supply heat amount control using the obtained correction value.

  In the case of the above (Control 1), the control unit 70 acquires the measured value of the ultrasonic flowmeter 20 as a flow rate of only steam among the wet steam supplied from the steam source 10 to the heat demand unit 90. Then, the supply heat amount calculation operation for calculating the amount of heat (supply heat amount) supplied to the heat demand unit 90 from the steam flow rate, the supply heat amount, and the set heat amount (heat demand from the steam source 10) set in the control unit 70 Output adjustment operation for adjusting the output of the steam source 10 based on the comparison with the amount of heat set to be supplied to the unit 90.

In the steam flow rate acquisition operation, the ultrasonic flow meter 20 installed in the pipe 30 is operated, and the flow rate of the wet steam flowing through the pipe 30 is measured. In the operation in this example, based on the result shown in FIG. 5, the measurement value of the ultrasonic flowmeter 20 is acquired as the flow rate of only steam.
In the supply heat amount calculation operation, the supply heat amount supplied to the heat demand unit 90 is calculated from the steam flow rate and the latent heat of the steam. Thereby, the supply heat quantity currently supplied to the heat demand part 90 can be estimated accurately.
In the output adjustment operation, the output of the steam source 10 is adjusted so that the supply heat amount calculated from the steam flow rate matches the set heat amount. In other words, if the supply heat quantity is insufficient with respect to the set heat quantity, control is performed to increase the steam flow rate (supply heat quantity) by increasing the output of the steam source 10. On the other hand, if the supply heat quantity is excessive with respect to the set heat quantity, control is performed to reduce the steam flow rate (supply heat quantity) by reducing the output of the steam source 10.
By continuously executing the steam flow rate acquisition operation, the supply heat amount calculation operation, and the output adjustment operation, a desired heat amount (set heat amount) can be continuously supplied to the heat demand unit 90.

  On the other hand, in the case of (Control 2), the control unit 70 takes the total flow rate acquisition operation for acquiring the measurement value of the ultrasonic flow meter 20 as the total flow rate of the wet steam supplied from the steam source 10 to the heat demand unit 90, and A total flow correction operation for correcting the total flow rate using the wet steam density, a supply heat amount calculation operation for calculating the amount of heat (supplied heat amount) supplied to the heat demand unit 90 from the corrected total flow rate, and the supply heat amount And an output adjustment operation for adjusting the output of the steam source 10 based on a comparison with the set heat amount set in the control unit 70 (the heat amount set to be supplied from the steam source 10 to the heat demand unit 90). .

The total flow rate acquisition operation is the same as (Control 1) in which the flow rate is measured using the ultrasonic flow meter 20, but the measurement value of the ultrasonic flow meter 20 is acquired as the total flow rate of wet steam. Different.
In the total flow rate correcting operation, the total flow rate is corrected using the _wet steam density ρ _wet . As a result, the corrected total flow rate is a value that agrees well with the measured value of the Coriolis flow meter 109 regardless of the wetness.
In the supply heat amount calculation operation, the supply heat amount supplied to the heat demand unit 90 is calculated from the corrected total flow rate, the latent heat of the steam, and the sensible heat of the condensed water. Thereby, the supply heat quantity currently supplied to the heat demand part 90 can be estimated accurately.
In the output adjustment operation, similarly to (Control 1), the output adjustment of the steam source 10 is executed based on the comparison with the set heat amount, and the amount of heat supplied to the heat demand section 90 is controlled.
By continuously executing the above total flow acquisition operation, total flow correction operation, supply heat amount calculation operation, and output adjustment operation, a desired amount of heat (set heat amount) is continuously supplied to the heat demand unit 90. be able to.

  Thus, in any case of (Control 1) and (Control 2), the amount of heat supplied to the heat demand section 90 can be accurately estimated based on the measurement value of the ultrasonic flowmeter 20, and the heat demand By adjusting the output of the steam source 10 based on the comparison with the set heat amount to be supplied to the unit 90, the desired heat amount can be reliably supplied to the heat demand unit 90.

  In the operation of (Control 1), since the output of the steam source 10 is adjusted using the flow rate of only the steam obtained from the measurement value of the ultrasonic flowmeter 20, it is necessary to correct the measurement value as in (Control 2). In addition, since it is easy to calculate the amount of heat supplied, it is possible to simply control the amount of heat supplied. In addition, since the supply heat amount is calculated from the flow rate of only steam in (Control 1), it becomes a value different from the actual supply heat amount, but the heat amount of the wet steam is mostly the latent heat of the steam, There is no big difference between the two.

On the other hand, in the operation of (Control 2), since the total flow rate corrected by the ultrasonic flowmeter 20 using the wet steam density ρ _wet is used, the error of the total flow value itself is smaller than that in the case of (Control 1). Get smaller.
Further, since the supply heat amount is calculated from the total flow rate of the wet steam, a value closer to the actual supply heat amount can be obtained. From these, in (Control 2), it is possible to control the amount of heat supplied to the heat demand section 90 with higher accuracy than in (Control 1).

DESCRIPTION OF SYMBOLS 10 ... Steam source, 20 ... Ultrasonic flowmeter, 30, 150 ... Steam piping, 151 ... Condensate water piping, 70, 170 ... Control part, 90 ... Heat demand part, S1 ... Heat supply system

Claims (5)

Steam that measures the flow rate of wet steam flowing in a pipe with an ultrasonic flowmeter without dividing the wet steam into water and dry steam, and obtains the measured value as the flow rate of the dry steam only How to measure the flow rate. The flow rate of the wet steam flowing through the pipe is measured by an ultrasonic flowmeter, the measured value is corrected using the density of the wet steam, and the corrected value is acquired as the total flow rate of the wet steam. To measure the flow rate of steam.   The said ultrasonic flowmeter is installed in the said piping so that an ultrasonic transmission part and a receiving part may become a horizontal state, The measuring method of the steam flow rate of Claim 1 or 2 characterized by the above-mentioned. A steam source for supplying wet steam to the heat demand section via piping;
An ultrasonic flowmeter that is provided in the pipe near the entrance of the heat demand section and measures the flow rate of the wet steam flowing through the pipe;
A control unit for controlling the output of the steam source based on the measurement value of the ultrasonic flowmeter;
Have
The controller is
A steam flow rate acquisition operation for acquiring the measurement value of the ultrasonic flowmeter as a flow rate of only dry steam out of wet steam flowing through the pipe;
Supply heat amount calculation operation for calculating the supply heat amount supplied to the heat demand unit based on the steam flow rate;
An output adjustment operation for adjusting the output of the steam source based on a comparison between the set heat amount to be supplied to the heat demand section and the supplied heat amount;
Heat supply system that is characterized in that the run. A steam source for supplying wet steam to the heat demand section via piping;
An ultrasonic flowmeter that is provided in the pipe near the entrance of the heat demand section and measures the flow rate of the wet steam flowing through the pipe;
A control unit for controlling the output of the steam source based on the measurement value of the ultrasonic flowmeter;
Have
The controller is
Wherein the measurement of the ultrasonic flowmeter, corrected using the density before Symbol wet steam, and the total flow rate correction operation for obtaining the correction value as a total flow rate of the wet steam,
Supply heat amount calculation operation for calculating the supply heat amount supplied to the heat demand unit based on the corrected total flow rate,
An output adjustment operation for adjusting the output of the steam source based on a comparison between the set heat amount to be supplied to the heat demand section and the supplied heat amount;
Heat supply system that is characterized in that the run.

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