Patent Application
20170184432
The present invention relates to a flow speed measurement method and a flow speed measurement system.
The present application claims priority based on Japanese patent application 2014-021298, filed on Feb. 6, 2014 and includes herein by reference the content thereof.
Conventionally, as a method for measuring the flow amount of a fluid flowing inside a pipe, in which two temperature sensors positioned upstream and downstream on the surface of the pipe detect the change in temperature of the fluid flowing inside the pipe, and the flow speed and the like of the fluid flowing inside the pipe is determined based on the time difference has been known (refer, for example, to Patent Reference 1).
If the above-noted conventional art is applied to flow speed measurement of steam, there have been cases in which measurement with good accuracy has been impossible. This is because, compared to water, the heat transfer of steam is much lower, so that the heat of the steam flowing inside the pipe does not reach the pipe surface, preventing the thermal sensors from detecting the temperature well. Given this, there has been a desire for the provision of new art enabling measurement of the flow speed of steam flowing inside the pipe from the outside of a pipe.
Japanese Patent Application Publication No. 2010-261826
One aspect of the present invention provides a flow speed measurement method and a flow speed measurement system capable of measuring the flow speed of steam flowing within a pipe with good accuracy from outside.
A flow speed measurement method of the first aspect of the present invention includes conducting a heat exchange at a prescribed part of a surface of a pipe, the flow speed measurement method further includes measuring a temperature distribution in a pipe-axis-direction on the surface of the pipe in a case that the heat exchange has been conducted at the prescribed part, and the flow speed measurement method further includes determining a flow speed of a thermal fluid flowing inside the pipe, based on the temperature distribution measured.
In the above-noted first aspect, the flow speed measurement method further includes conducting the heat exchange includes heating the prescribed part.
In the above-noted first aspect, the flow speed measurement method further includes measuring the temperature distribution that measures the temperature of the surface of the pipe at the prescribed part, at upstream from the prescribed part, and at downstream from the prescribed part.
In the above-noted first aspect, the flow speed measurement method further includes measuring the temperature distribution that measures the temperature at a plurality of locations on the pipe in a circumferential direction of the pipe.
In the above-noted first aspect, the flow speed measurement method further includes measuring the temperature distribution that measures an average value of the temperature at the plurality of locations.
In the above-noted first aspect, the flow speed measurement method further includes conducting the heat exchange that conducts the heat exchange at a prescribed part of the surface of the pipe using an annularly shaped heater.
In the above-noted first aspect, the flow speed measurement method further includes the pipe covered with a thermal insulation material at least at one of the prescribed part, upstream from the prescribed part and downstream from the prescribed part is used.
In the above-noted first aspect, the flow speed measurement method further includes determining the flow speed of the thermal fluid includes determining the flow speed of a thermal fluid that is steam.
A flow speed measurement system of the second aspect of the present invention includes a heat exchanger that conducts a heat exchange at a prescribed part on a surface of a pipe, the flow speed measurement system further includes a flow speed measurement system further includes a temperature measurer that measures a temperature distribution in a pipe-axis-direction on the surface of the pipe in a case that the heat exchange has been conducted at the prescribed part, and the flow speed measurement system further includes a flow speed determiner that determines a flow speed of a thermal fluid flowing inside the pipe, based on the temperature distribution measured.
In the above-noted second aspect, the heat exchanger may be a heating device, and further the heating device may be annularly shape heater.
In the above-noted second aspect, the flow speed measurement system further includes a temperature measurer that measures the temperature of the surface of the pipe at the prescribed part, at upstream from the prescribed part, and at downstream from the prescribed part.
In the above-noted second aspect, the flow speed measurement system further includes the temperature measurer that measures a temperature at a plurality of locations in the circumferential direction of the pipe.
In the above-noted second aspect, the flow speed measurement system further includes the flow speed determiner that determines the flow speed of the thermal fluid that is steam.
According to the flow speed measurement method and flow speed measurement system, it is possible to measure the flow speed of steam flowing inside a pipe from the outside with good accuracy.
A number of embodiments of the present invention will be described below, with references made to the drawings. A flow speed measurement system according to the present embodiment can measure the flow speed of a thermal fluid (for example, steam) flowing inside a pipe disposed between a steam producing apparatus such as a boiler and a load apparatus.
A flow speed measurement system 100 according to the present embodiment, as shown in
The heater 2 is for heating a prescribed part by heat exchange with the surface 10a of the pipe 10. In the present embodiment, the heater 2 is constituted by, for example, an annularly shaped heater and, as shown in
Temperature sensor groups 3A are disposed at both sides of the installation part 11 of the heater 2 on the surface 10a of the pipe 10 (upstream side and downstream side). The installation position of each temperature sensor group 3A is determined in accordance with the distance from the installation part 11. For example, taking the example of the side upstream from the installation part 11, the sensors of the temperature sensor group 3A are installed at distances of 0 mm, 6 mm, 14 mm, 24 mm, 36 mm 50 mm, 66 mm, 84 mm, 104 mm, 126 mm, 150 mm, and 176 mm from the end face of the installation part 11. In this case, a distance of 0 mm from the end face of the installation part 11 means that a temperature sensor group 3A is installed along the end face of the heater 2.
As shown in
The temperature measurement unit 3 is constituted by a plurality of (for example, 12 in the present embodiment) temperature sensor groups 3A. The temperature sensor groups 3A are disposed along the axis direction of the pipe 10 at the surface 10a of the pipe 10. Each temperature sensor group 3A includes a plurality of temperature sensors 3a, each of which measures the temperature of the surface 10a of the pipe 10. In the present embodiment, each temperature sensor group 3A is constituted by four temperature sensors 3a. The four temperature sensors 3a are disposed uniformly in the circumferential direction on the surface 10a of the pipe 10. That is, the four temperature sensors 3a are positioned 90 degrees apart in the circumferential direction of the pipe 10. Each temperature sensor group 3A outputs the average value of values measured by the four temperature sensors 3a. In this manner, by taking the average of values measured at a plurality of locations on the surface 10a of the pipe 10 as the measured value, the temperature sensor group 3A can output measurement results (temperature) with high reliability.
Based on a constitution such as this, the temperature measurement unit 3 can measure the temperature distribution of the surface 10a in the axis direction of the pipe 10 from the measurement results of the temperature sensor groups 3A. The temperature distribution measured by the temperature measurement unit 3 is sent to the control unit 4.
At least a part of the surface 10a of the pipe 10 is covered by a thermal insulation material 12. In the present embodiment, the thermal insulation material 12 is installed along the axis direction so as to cover the heater 2 and the temperature measurement unit 3 (temperature sensors 3a) provided on the surface of the pipe 10.
The CPU 62, based on measurement data and on information stored in the memory 63, can calculate the flow speed of steam flowing inside the pipe 10. The CPU 62, for example, uses the measurement results (temperature distribution of the pipe 10) of the temperature measurement unit 3 to calculate the flow speed of steam flowing inside the pipe 10 from the information stored in the memory 63, as will be described later. That is, a flow speed calculator that calculates the flow speed of steam flowing inside the pipe constitutes the control unit 4.
The flow speed measurement system 100 and the measurement method thereof focus on the point that the internal pipe heat transfer coefficient within a pipe changes in accordance with the flow speed of a fluid flowing inside the pipe, and the point that, accompanying a change in the heat transfer coefficient, the heat applied to surface of the pipe causes a temperature distribution.
First, the point of the internal pipe heat transfer coefficient changing in accordance with the flow speed of a fluid (hereinafter referred to as the piped fluid) flowing inside a pipe will be described.
In the following, Equation (1) is the Dittus-Boelter equation, Equation (2) is the equation indicating the Nusselt number, Equation (3) is the equation indicating the Prandtl number, and Equation (4) is the equation indicating the Reynolds number.
Nu=0.023×Re0.8×Pr0.4 (1)
Nu=αi×di/λ (2)
Pr=ν×ρ×Cp/λ (3)
Re=u×di/ν (4)
In the above:
di is the inner diameter of the pipe,
λ is the thermal conductivity (W/m/K),
ν is the kinematic viscosity coefficient (m2/s),
ρ is the density of the fluid (kg/m3),
Cp is the specific heat (KJ/Kg/K),
u is the flow speed of the piped fluid, and
αi is the heat transfer coefficient of the internal pipe.
As shown in
According to the above-noted Equations (1) to (4), it can be seen that the thermal transfer coefficient αi inside the pipe is proportional to the 0.8th power of the flow speed u of the piped fluid.
In this case, the thermal transfer coefficient αi inside the pipe can be taken as being the ease with which heat propagates in the piped fluid from the inside to the outside in the radial direction of the pipe (hereinafter, referred to as the internal pipe heat transfer).
That is, if the flow speed of the piped fluid is high, the internal pipe heat transfer in the piped fluid becomes relatively large, and if the flow speed of the piped fluid is low, the internal pipe heat transfer in the piped fluid becomes relatively small.
In this manner, it can be verified that the internal pipe heat transfer changes in accordance with the flow speed of the piped fluid.
Continuing, the point of the occurrence of a temperature distribution in the surface of the pipe by the heat applied to the surface of pipe accompanying the changing of the internal pipe heat transfer will now be described.
In steel, which is a generally used material to constitute a pipe, compared to the internal pipe heat transfer by the fluid, thermal transfer in the pipe axis direction is sufficiently large, that being particularly prominent in the case of steam. For this reason, for example, if heat is applied to the surface of the pipe, the applied heat is transferred not internally (in the radial direction), but mainly along the surface of the pipe (in the pipe axis direction).
In contrast, a considerable amount of the heat applied to the surface of the pipe is transferred inside the pipe. The amount of thermal transfer toward the inside of the pipe is influenced by the size of the above-described internal pipe heat transfer.
That is, if the internal pipe heat transfer is relatively large (if the flow speed of the piped fluid is high), because it is easy for heat to be transferred inside the pipe, the heat applied to the surface of the pipe is transferred inside the pipe. Thus, it was learned that the temperature distribution on the surface of the pipe does not broaden in the pipe axis direction.
If the internal pipe heat transfer is relatively small (if the flow speed of the piped fluid is low), because it is difficult for heat to be transferred inside the pipe, the heat applied to the surface of the pipe transfers along the surface, rather than inside the pipe. Thus, it was learned that the temperature distribution on the surface of the pipe broadens in the pipe axis direction.
The inventors, based on the learnings described above, discovered that, when a pipe is heated from outside, it is possible to predictively compute the flow speed of the fluid flowing inside the pipe based on the temperature distribution occurring in the pipe axis direction, and completed the flow speed measurement system and flow speed measurement method of one aspect of the present invention.
Continuing, the flow speed measurement method using the flow speed measurement system 100 according to the present embodiment will now be described.
First, the control unit 4 drives the heater 2 to obtain the state in which the surface 10a of the pipe 10 is heated (first step).
Continuing, the control unit 4 starts the supply of steam from the steam producing apparatus 20 to the load apparatus 30, via the pipe 10. By the flow of steam in the pipe 10, the thermal transfer coefficient within the pipe in the radial direction changes.
The temperature measurement unit 3 measures the temperature in the axis direction of the pipe 10. Specifically, the temperature measurement unit 3 measures the temperature distribution of the surface 10a in the pipe axis direction of the pipe 10 by each of the temperature sensor groups 3A (second step).
When measuring the temperature distribution of the pipe 10, for example, the method of controlling so that the initial temperature of the heater 2 is constant and the method of making the heat entering from the heater 2 constant can be envisioned. Because the method of making the heat entering from the heater 2 constant enables the temperature difference (temperature distribution) to be made larger, it enables an improvement in the temperature sensitivity.
The control unit 4, for example, from the measurement results by the temperature measurement unit 3, acquires data in which the temperature distribution of the surface 10a of the pipe 10, as shown by the solid line in
The control unit 4 acquires data in which the temperature distribution of the surface 10a of the pipe 10, as shown by the broken line in
The measurement results (temperature distribution data) of the temperature measurement unit 3 are sent to the control unit 4. The control unit 4 uses the measurement data of temperature distribution of the pipe 10 to compute the flow speed of steam flowing inside the pipe 10 from information that had been stored in the memory 63 (refer to
The memory 63 has stored therein information regarding the steam flow speed and the temperature distribution obtained, for example, by prior experiments or simulation. The control unit 4 can read out the above-noted information stored in the memory 63 and, by comparing the measured values of the temperature distribution of the pipe 10, can compute the flow speed of steam corresponding to the actually measured temperature distribution (measurement results of the temperature measurement unit 3).
For example, an example of the determination of the information (relationship between the steam flow speed and the temperature distribution) stored in the memory 63 is determined by a computed simulation will be described.
The conditions for the computed simulation are a pipe inner diameter of 100 mm, a pipe outer diameter of 110 mm, saturated steam at 0.8 MPa flowing at a flow speed of 10 m/s inside the pipe, and the material constituting the pipe being steel with thermal conductivity of 50 W/m/K. The mesh size was made 5 mm in the pipe axis direction and the pipe thickness direction. Asymptotic calculation was done so that amount of heat entering the mesh is the same as the amount of heat leaving the mesh.
Specifically, in this computation, the amount of heat entering the mesh in the initial mesh is the heat conducted from the heater 2, and in the next mesh is the heat entering by thermal conduction is from the steel of the neighboring mesh. The amount of heat leaving the mesh is, for all meshes, the heat leaving by heat transfer to the steam flow within the pipe.
The temperature distribution is determined by performing an asymptotic calculation of the thermal balance of each mesh, with the heat entering from the heater 2 as the heat leaving and propagating to the steam.
The conditions for computing the temperature distribution are an initial temperature of 50° C. at steam flow speeds of both 10 m/s and 5 m/s. In this case, the entering heat at the steam flow speed of 10 m/s is 118.9 W per unit cell and the entering heat at the steam flow speed of 5 m/s is 88.4 W per unit cell.
By such a computed simulation, for example, it is possible to acquire the data shown in the graph of
The control unit 4 compares the results of measurement (temperature distribution) by the temperature measurement unit 3 such as shown in
As described above, according to the present embodiment, it is possible to determine the flow speed of the steam based on the temperature distribution occurring in the surface 10a of the pipe 10, without using the temperature of the steam, which is the internal fluid, the temperature of which cannot be directly measured. Therefore, the flow speed of the steam can be determined from outside the pipe 10, both simply and with good accuracy.
Although an embodiment of the present invention has been described above, there is no restriction to the above-noted embodiment, and appropriate changes can be made within the scope of spirit of the invention. For example, although in the above-noted embodiment the heater 2 and the temperature measurement unit 3 (each of the temperature sensors 3a) have been described as the example of being constituted so as to be covered by the thermal insulation material 12, this is not a restriction. For example, if the control unit 4 is in a form that, taking into consideration radiation of heat from the surface 10a of the pipe 10, corrects the measurement data (temperature distribution) sent from the temperature measurement unit 3, there is no need to cover the surface 10a of the pipe 10 with the thermal insulation material 12. Alternatively, the constitution may be such that only a part of the surface 10a (the part at which the temperature measurement unit 3 is installed) is covered with the thermal insulation material 12.
Although the above-noted embodiment takes the example of the case of measuring the flow speed of steam as the thermal fluid flowing inside a pipe, this does not restrict the present invention, which can be applied to the case of measuring the flow speed of heated water flowing inside a pipe. Additionally, the fluid flowing inside a pipe may be Freon, ammonia, LNG (liquefied natural gas), or the like, and the present invention may also be applied to the measurement of the flow speed of these fluids.
Also, although in the above-noted embodiment, the heater 2 has been shown as an example of a heat exchanger that conducts heat exchange with the pipe 10, this does not restrict the present invention. For example, a cooler that cools the surface 10a of the pipe 10 may be used as the heat exchanger, and the flow speed of the steam flowing inside the pipe 10 may be measured based on the temperature distribution occurring in the pipe axis direction of the pipe 10 by cooling. In this case, if the steam is saturated steam or superheated steam that is close to being saturated steam, because there is a possibility of condensation occurring, it is necessary to consider that when computing the heat transfer coefficient.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2014-021298 | Feb 2014 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2015/053069 | 2/4/2015 | WO | 00 |
