The present application is based on and claims priority to Japanese Application No. 2017-139910, filed Jul. 19, 2017, the entire contents of which are incorporated herein by reference.
The present disclosure relates to a thermal flowmeter that calculates a flow rate of a fluid on the basis of power applied to a heater, by measuring the temperature of the fluid at an upstream point and a downstream point of a pipe, and controlling the heater so as to maintain a temperature difference between the two points at a constant level.
In the known thermal flowmeters, correction has to be performed for each type of the fluid, because the thermal characteristics differ depending on the type of the fluid, as described, for example, in Japanese Unexamined Patent Application Publication No. 11-132812. With existing thermal flowmeters, the relation between an actual flow rate and a sensor output has to be acquired for each type of fluid at multiple measurement points for correction to determine a correction coefficient. Thus, the determination process of the correction coefficient is complicated.
Accordingly, the present disclosure provides a thermal flowmeter and a flow rate correction method with which the flow rate is able to be corrected through a simple process.
A thermal flowmeter according to an aspect of the present disclosure includes a pipe through which a fluid to be measured is caused to flow, a first thermal resistance element disposed on the pipe and configured to detect a first temperature of the fluid to be measured, a second thermal resistance element disposed on the pipe at a position downstream of the first thermal resistance element and configured to detect a second temperature of the fluid to be measured, a control unit configured to cause the second thermal resistance element to heat by outputting a voltage to make the second temperature higher than the first temperature by a fixed value, a power measurement unit configured to measure a power to be applied to the second thermal resistance element, a power conversion unit configured to convert the power measured by the power measurement unit to a power assumed to be required when the fluid is water, by multiplying the power measured by the power measurement unit by a constant uniquely determined depending on a type of the fluid to be measured, and a flow rate calculation unit configured to calculate a flow rate of the fluid to be measured, by converting the power converted by the power conversion unit to a value of the flow rate, using a flow rate conversion characteristic formula applicable when the fluid is water.
In the thermal flowmeter configured as above, the constant may be determined through an experiment performed beforehand, on a basis of a power obtained by backward calculation based on an inverse function of the flow rate conversion characteristic formula, from an actual flow rate of the fluid to be measured and a flow rate measured by the thermal flowmeter.
A flow rate correction method according to another aspect of the present disclosure is a method for a thermal flowmeter including a pipe through which a fluid to be measured is caused to flow, a first thermal resistance element disposed on the pipe and configured to detect a first temperature of the fluid to be measured, and a second thermal resistance element disposed on the pipe at a position downstream of the first thermal resistance element and configured to detect a second temperature of the fluid to be measured. The flow rate correction method includes causing the second thermal resistance element to heat by outputting a voltage to make the second temperature higher than the first temperature by a fixed value, measuring a power to be applied to the second thermal resistance element, converting the power measured in the measuring of the power to a power assumed to be required when the fluid is water, by multiplying the power measured in the measuring the power by a constant uniquely determined depending on a type of the fluid to be measured, and calculating a flow rate of the fluid to be measured, by converting the power converted in the converting the power to a value of the flow rate, using a flow rate conversion characteristic formula applicable when the fluid is water.
According to the aspects of the disclosure, the flow rate is corrected through a simple process of multiplying the power measured by the power measurement unit by a constant uniquely determined depending on the type of the fluid to be measured, thereby converting the power to a power assumed to be required when the fluid is water, and converting the power converted as above to a value of the flow rate, using a flow rate conversion characteristic formula applicable when the fluid is water.
Hereafter, an embodiment of the present disclosure is described, with reference to the drawings.
The thermal resistance elements 2a and 2b are each formed on a silicon wafer. The thermal resistance element 2a is fixed to the pipe 1 by bonding the silicon wafer to the pipe 1 with the face of the silicon wafer, on which the thermal resistance element 2a is formed, opposed to the outer wall of the pipe 1. The thermal resistance element 2b is also fixed in the same way as the thermal resistance element 2a. In the example illustrated in
Hereunder, an operation of the thermal flowmeter according to the embodiment is described.
The temperature acquisition units 3a and 3b respectively acquire temperature TRr, TRh of a fluid A flowing through the pipe 1 (step S100 in
The subtractor 4 subtracts the temperature TRr of the fluid A on an upstream side, from the temperature TRh on a downstream side (step S101 in
The PID control calculation unit 5 calculates the operation amount so as to make the temperature difference (TRh-TRr) calculated by the subtractor 4 a fixed value (target value of control, for example, 10° C.) (step S102 in
The control output unit 6 applies a voltage to the thermal resistance element 2b in accordance with the operation amount calculated by the PID control calculation unit 5, thereby causing the thermal resistance element 2b to heat (step S103 in
Thus, the operations of steps S100 to S103 are executed in a predetermined control cycle until the operation of the thermal flowmeter is finished (YES at step S104 in
Q=V
2/Rh (1)
The power Q required for constantly keeping the temperature TRh of the fluid A on the downstream side higher than the temperature TRr on the upstream side by the fixed value can be obtained as above.
Then the power conversion unit 8 multiplies the power Q measured by the power measurement unit 7 by a constant αA, which is uniquely determined depending on the type of the fluid A to be measured, to thereby convert the power Q to a power that would be required when the fluid is water (step S201 in
The constant αA can be obtained as follows. Here, it is assumed that a flow rate conversion characteristic formula f for obtaining a flow rate FH2O of water from a power QH2O measured by the power measurement unit 7 when the fluid is water is already known through actual measurement.
FH2O=f(QH2O) (2)
It is also assumed that an actual flow rate Fa of the fluid A to be measured and a measured flow rate Fm obtained by the thermal flowmeter according to this embodiment are already known through experiments. However, to obtain the measured flow rate Fm for the calculation of the constant αA, the power Q measured by the power measurement unit 7 may be directly substituted into the flow rate conversion characteristic formula f, to thereby obtain the measured flow rate Fm from f (Q) instead of executing the power conversion of step S201.
A power Qa corresponding to a flow rate Fa when the fluid is water can be obtained from the equation (3) given below.
Q
a
=f
−1(Fa) (3)
Here, f−1 is the inners function of the flow rate conversion characteristic formula f.
In addition, the power Qm corresponding to the flow rate Fm when the fluid is other than water can be obtained from the equation (4) given below.
Q
m
=f
−1(Fm) (4)
As above, the power Qa, Qm can be calculated backward using the inverse function f−1 of the flow rate conversion characteristic formula f. An approximation formula can be established as below with respect to the power Qa, Qm, and therefore the constant αA can be determined in advance by obtaining, through experiments, the flow rate Fa, Fm, of the fluid A to be measured.
Qa≈αAQm (5)
By determining, as above, in advance the constant an αA with respect to the fluid A to be measured, the power Q measured by the power measurement unit 7 can be converted to the power required when the fluid is water, by multiplying the power Q by the constant αA.
The flow rate calculation unit 9 converts a power αAQ converted by the power conversion unit 8 to the value of the flow rate, using the flow rate conversion characteristic formula f, to thereby calculate a flow rate F of the fluid A to be measured (step S202 in
F=f(αAQ) (6)
Thus, the operations of steps S200 to S202 are executed at predetermined time intervals until the operation of the thermal flowmeter is finished (YES at step S203 in
Since the relation between the actual flow rate and the flow rate measured by the thermal flowmeter according to this embodiment is non-linear, it is difficult to directly correct the measured flow rate. In this embodiment, accordingly, the power Q measured by the power measurement unit 7 is corrected so as to indirectly correct the flow rate. As a result, with the method according to this embodiment, the actual flow rate can be approximately obtained through a simple process.
Here, a supplementary description is given about the basis for the effectiveness of the present disclosure. The power Q in the thermal flowmeter configured as
Q=kFα (7)
k denotes a coefficient indicating the characteristics of the fluid (thermal conductivity, Reynolds number, density, and so forth), F denotes the flow velocity of the fluid, and α denotes an exponential coefficient for the flow velocity (coefficient based on a physical structure of a flow path and a sensor system, approximately ½). The inverse function f−1 of the flow rate conversion characteristic formula f can be expressed as follows.
F=f
−1( )=(Q/k)−α (8)
When the fluid is other than water, the physical structure of the flow path is the same, but the characteristics of the fluid are different (an impact of thermal conductivity of the fluid is important in the first approximation), and therefore it may be assumed that the coefficient α is the same as that of water, and the coefficient k is different from that of water. The coefficient k of the fluid other than water will hereinafter be expressed as km. The flow velocity Fm of the fluid other than water can be expressed as follows.
F
m=(Qm/km)−α (9)
Then the power required to allow water and the fluid other than water to flow at the same velocity is measured. In other words, Q and Qm corresponding to the case of F=Fm is measured. In this case, the following equation can be established from the equation (8)/and the equation (9).
F/F
m=1((Q/k)−α)/((Qm/km)−α) (10)
From the equation (10) above, the following equation can be obtained.
Q/k=Q
m
/k
m (11)
Since the power Q required for water, the coefficient k representing the characteristics of water, and the power Qm required for the fluid other than water are available from actual measurement, the coefficient km representing the characteristics of the fluid other than water can be obtained.
From the equation (11) above, the following equation (12) can be obtained.
Q=(Qm/km)×k (12)
Accordingly, the flow velocity F calculated from the power Q obtained by multiplying the power Qm for the fluid other than water by (k/km) can be construed as an approximate value of the flow velocity of the fluid other than water. The value (k/km) corresponds to the constant αA. Therefore, the actual flow rate can be approximately obtained through a simple process.
Although the constant αA is a fixed value in this embodiment, the constant αA may be variable, depending on the power Q measured by the power measurement unit 7. For example, the constant αA in the equation (6) may be substituted with a constant αA(Q), as expressed by the following equation (13).
αA(Q)=αA(1−exp(−βQ)) (13)
Here, the coefficient β is a value obtained from experimental values.
Out of the components of the thermal flowmeter according to this embodiment, at least the subtractor 4, the PID control calculation unit 5, the power conversion unit 8, and the flow rate calculation unit 9 can be realized by a computer including a CPU or other processing circuitry, a storage device, and an interface with outside, and a program for controlling the mentioned hardware resources. The flow rate correction method performed by the thermal flowmeter can be realized, when the CPU executes the operations according to the foregoing embodiment, in accordance with the program stored in the storage device.
The present disclosure is applicable to a thermal flowmeter.
Number | Date | Country | Kind |
---|---|---|---|
2017-139910 | Jul 2017 | JP | national |