KR100828697B1 - Air bubble type liquid-level meter - Google Patents

Abstract

The present invention provides a bubble type liquid level meter which is simple in structure, low in failure, low in consumption of compressed air, no pulsation of compressed air, no shaking of the indication value, and stable display.

A display unit for displaying the liquid level in the tank based on a detection signal from the pressure sensor, at least a lower end of which is submerged in the liquid in the tank, a compressed air supply source for supplying compressed air into the supply pipe, a pressure sensor for measuring the air pressure in the supply pipe, and a pressure sensor detection signal. And a first solenoid valve for opening and closing the compressed air supply path from the compressed air supply source to the air supply pipe, and a second solenoid valve for opening and closing the air pressure detection path from the air supply pipe to the pressure sensor. In the air supply mode in which the first solenoid valve opens the compressed air supply path, the second solenoid valve closes the air pressure detection path, and in the measurement mode in which the second solenoid valve opens the air pressure detection path, the first solenoid valve closes the compressed air supply path.

Description

Bubble type liquid level meter {Air bubble type liquid-level meter}

BRIEF DESCRIPTION OF THE DRAWINGS It is a system diagram which shows Example 1 of the bubble type liquid level meter which concerns on this invention.

FIG. 2 shows the operation of the first embodiment, (a) is a timing chart showing an operation mode, (b) is a timing chart showing a pressure change, and (c) is a conceptual diagram of an air supply pipe in liquid level lowering operation. , (d) is a conceptual diagram of the air supply pipe in bubble discharge operation.

Fig. 3 is a diagram showing the opening and closing operation of each solenoid valve of the first embodiment in each operation mode.

FIG. 4 is a graph showing the change in pressure when switching from the air supply mode to the measurement mode in Example 1. FIG.

5 is a system diagram showing Example 2 of the bubble type liquid level meter according to the present invention.

6 is a system diagram showing Example 3 of the bubble type liquid level meter according to the present invention.

FIG. 7 is a view showing the opening and closing operation in each operation mode of each solenoid valve of Embodiment 3. FIG.

8 is a system diagram showing Example 4 of the bubble-type liquid level meter according to the present invention.

Fig. 9 shows the operation of the fourth embodiment, (a) is a timing chart showing an operation mode, (b) is a timing chart showing a pressure change, and (c) is a conceptual diagram of an air supply pipe in liquid level lowering operation. , (d) is a conceptual diagram of the air supply pipe in bubble discharge operation.

FIG. 10 is a graph showing the change in pressure when switching from the air supply mode to the measurement mode in Example 4. FIG.

FIG. 11 is a system diagram showing Example 5 of the bubble-type liquid level meter according to the present invention. FIG.

Fig. 12 is a system diagram showing Example 6 of the bubble type liquid level meter according to the present invention.

13 shows a general example of a plurality of solenoid valves and a manifold combined therewith, (a) is a conceptual diagram showing an example of a plurality of solenoid valves, and (b) is a conceptual diagram showing an example of a manifold.

14 is a system diagram showing an example of a conventional bubble type liquid level meter.

Fig. 15 is a longitudinal sectional view showing the internal structure of an air purge head in the conventional bubble type liquid level meter.

Explanation of symbols on the main parts of the drawings

10 tank

12 air supply pipe

14 liquid

30 piping

34 Compressor as a Compressed Air Source

38 Control Room

52 air transducers

54 Pressure Sensor

63 Main Manifold

64 submanifolds

65 First solenoid valve

66 2nd solenoid valve

67 3 solenoid valve

The present invention relates to a bubble level gauge for measuring the level of a liquid level stored in a tank such as a ship.

Ballast tanks, oil tanks, water tanks, and the like in container ships and tankers are provided with liquid level meters for detecting the level of the stored liquid. As a measuring method of such a liquid level meter, a floating type, a bubble type, etc. have been known conventionally. Most of the conventional bubble level gauges provide a supply pipe for each tank arranged in a plurality of tanks, and deliver the compressed air made by a compressor installed in a machine room or another compartment to the supply pipe immersed in the liquid stored in the tank through a pipe.

The bubble level gauge is arranged in a vertical direction of a supply pipe composed of a pipe having a lower end at a free opening in a tank into which a liquid is placed, and is supplied through the pipe so that bubbles are discharged from the lower end of the supply pipe when liquid is contained in the tank. Supply compressed air to the engine. The internal pressure P of the air supply pipe at that time is the same as that of the head ρH multiplied by the depth H of the liquid multiplied by the density ρ of the liquid, plus the gas pressure at the top of the liquid, that is, the "voltage". Therefore, the indication of the liquid level is obtained by subtracting the gas pressure of the upper portion of the liquid from the detected voltage. Compressed air is produced by a compressor in an engine room or other compartment and supplied from the main pipe on the deck to the level detector of each tank via branch pipes or to the level detector of each tank via independent piping. have.

The pressure in the supply pipe made of pipes depends on the head of the liquid (depth of the liquid) and at the same time the head of the liquid is different for each tank. However, in the conventional bubble type liquid level gauge, since the compressed air is supplied from a single compressor, the air pressure of the compressed air needs to maintain the maximum pressure corresponding to the maximum liquid head to be measured, and the air pressure for the tank depth or the liquid head at that time. This was too high and there was a defect that the measured value was changed slightly.

Therefore, the present applicant is directed to a supply pipe submerged in a liquid in a tank, a pump capable of supplying a compressor body in a supply pipe, a check valve provided between the pump and the supply pipe, a pressure sensor for measuring the air pressure in the supply pipe, and a pressure sensor. A pneumatic liquid level meter composed of control means for controlling a pump based on the pressure data sent, and has obtained a patent for a pneumatic liquid level meter, characterized in that the air supply pipe, the pump, the check valve, and the pressure sensor are provided for each tank. See Document 1). The "pneumatic liquid level meter" referred to in Patent Document 1 is a "bubble type liquid level meter".

According to the invention described in <Patent Document 1>,

1. No complicated piping is required and it can be handled simply as an electric device that operates alone.

2. It is enough to install a small capacity pump because only the compressor is needed to fill the supply pipe of the measuring part.

3. Since the compressor body is supplied from the adjacent distance of the measuring part, there is almost no influence of external temperature.

4. Simple control is sufficient because the compressor body is supplied at the adjacent distance of the measuring part. Maintenance is easy because the measuring part is housed in the detector box.

Can achieve the effect.

<Patent Document 1> Japanese Patent No. 2951954

In order to reduce costs by simplifying the liquid level gauge recently, in the explosion-proof compartments of tankers, chemical ships, or LNG ships, a bubble type liquid level meter with low failure rate and high safety compared to a low price is employed in a tank that does not require very high measurement accuracy. It is becoming.

Therefore, an example of a recent bubble level gauge will be described. In FIG. 14, FIG. 15, the liquid 10, such as oil and water, is stored in the tank 10 of a ship. The air purge head 20 is attached to the ceiling upper surface side of the tank 10 through the standpiece 16, and the air supply pipe 12 is dripped from the air purge head 20 toward the bottom of the tank 10. It is attached in the form. The pipe 30 and the pipe 32 are connected to the air purge head 20. The pipe 30 is a pipe for supplying compressed air, and the pipe 32 is a pipe for taking out a signal air.

As shown in FIG. 15, the air purge head 20 has a cup inverted shape, the inside of which is divided up and down by the partition wall 21, and the diaphragm 22 is attached to the partition wall 21. The upper space divided by the partition wall 21 communicates with the pipe 30 through a pipe. The pipe 30 also communicates with the air supply pipe 12 through the orifice 26 and the flow control valve 28. The air supply pipe 12 communicates with the pipe 32 through a flow control valve 28 and a pipe. The air supply pipe 12 is further communicated with the inner space of the diaphragm 22 through a suitable pipe. Therefore, the air pressure in the diaphragm 22 and the air pressure in the air supply pipe 12 are the same. A coil spring 24 is disposed inside the diaphragm 22 so that the diaphragm 22 is directed upward in FIG. 15 to elastically pressurize the upper space partitioned by the partition wall 21. The flow control valve 28 is integrally connected with a rod cast from the ceiling of the diaphragm 22.

The air purge head 20 operates as follows. When the compressed air is supplied from the pipe 30 while the lower end of the air supply pipe 12 is immersed in the liquid 14 in the tank 10, the air pressure in the upper space, that is, the air pressure outside the diaphragm 22 is changed to the diaphragm 22. The pressure of the internal diaphragm 22, that is, higher than the pressure in the air supply pipe 12, compresses the diaphragm 22 against the elasticity of the spring 24. By the operation of the diaphragm 22, the flow control valve 28 is pushed downward so that the valve is opened and the compressed air is supplied at a constant flow rate into the air supply pipe 12 through the orifice 26. By this compressed air, the liquid level in the air supply pipe 12 is pressed. As a result, compressed air is discharged from the lower end of the air supply pipe 12, becomes a bubble, rises up inside the liquid 14, and is released into the atmosphere. As the level of the liquid 14 in the air supply pipe 12 decreases, the air pressure in the air supply pipe 12 increases, so that the level of the gas 14 can be measured by measuring the air pressure in the air supply pipe 12. When the compressed air is supplied to the air supply pipe 12, the flow control valve 28 is greatly depressed to increase the flow rate of the compressed air, and as the liquid level in the air supply pipe 12 is pressed, the flow control valve 28 The opening amount becomes small and the flow rate becomes small. When the bubble is released and the liquid level is measured, compressed air is discharged by a predetermined amount from the lower end of the air supply pipe 12. In this manner, the air purge head 20 constitutes a predetermined flow rate mechanism.

In FIG. 14, the compressed air is supplied from the compressor 34 to the pipe 30. An inboard regulator 36 and an air supply unit 40 are interposed between the compressor 34 and the pipe 30. The inboard regulator 36 adjusts the pressure of the compressed air sent out from the compressor 34 to, for example, about 7 kg / cm 2. The air supply unit 40 is disposed in the control room 38 and includes a stop valve 42, a filter 44, a regulator 46, and a pressure gauge 48 in order from the compressor 34 side. In the control room 38, a switching valve 50, an idle converter 52, and an indicator 58 are arranged. The idle transformer 52 detects air pressure and converts the pressure into an electrical signal. The controller board 56 controls the air pressure indicating value by the indicator 58 according to the pressure sensor 54 and the output of the pressure sensor 54. ) The switching valve 50 is configured to lead the air pressure in the air supply pipe 12 to the idle converter 40 as shown, and open the air pressure applied to the idle converter in the air by rotating it 90 degrees clockwise in the illustrated state. It is possible to switch to the zero correction form.

When the switching valve 50 is in the switching mode shown in FIG. 14, the air pressure in the air supply pipe 12 is applied to the pressure sensor 54. This air pressure depends on the level of the liquid 14 stored in the tank 10 as described above. The pressure sensor 54 outputs an electric signal corresponding to the air pressure applied thereto. The signal is processed on the controller board 56 for the liquid level display by the indicator 58, and the liquid level is displayed by the indicator 58. As shown in FIG.

According to the conventional bubble-type liquid level meter described above, it has an air purge head having a diaphragm, a spring, and a flow control valve to supply compressed air to an air supply pipe at a predetermined amount. . In addition, since compressed air must always be supplied from the compressed air supply source to the supply pipe, the consumption of compressed air increases, and there is a pulsation caused by the release of compressed air, which is transmitted to the pressure sensor, which causes the display value to be shaken and thus becomes unstable.

The present invention has been made to solve the problems of the conventional bubble type liquid level meter, and an object thereof is to provide a bubble type liquid level meter having a simple structure, low failure rate, and low cost.

It is another object of the present invention to provide a bubble type liquid level meter which can reduce the consumption of compressed air, can not display the pulsation of compressed air, and can stably display without shaking the indication value.

The present invention also provides a bubble type liquid level meter which can measure the switching of the detection process and the adjustment of the supply amount of the compressed air by executing an automatic control program set in consideration of a drop pattern or a landing pattern of a tank. The purpose.

The present invention also provides a bubble type liquid level meter that can be carried out in the control room, such as the execution of the automatic control program and the signal processing can be performed in the control room, the electric equipment does not exist on the deck and satisfies the conditions of intrinsically safe explosion-proof type. For the purpose of

It is another object of the present invention to provide a bubble type liquid level meter that enables the use of a manifold to reduce the number of installation steps in a bubble type liquid level meter using a plurality of solenoid valves.

According to the present invention, the air supply pipe includes at least a lower end of which is immersed in the liquid in the tank, a compressed air supply source for supplying compressed air into the air supply pipe, a pressure sensor for measuring air pressure in the air supply pipe, and a detection signal of the pressure sensor. A bubble type liquid level gauge having a display unit for displaying a liquid level in a tank, comprising: a first solenoid valve for opening and closing a compressed air supply path from a compressed air supply source to an air supply pipe; and an opening and closing air pressure detection path from a supply pipe to a pressure sensor. Having two solenoid valves is the most important feature.

The present invention is also a bubble type liquid level gauge having the first solenoid valve and the second solenoid valve as described above, having a manifold capable of mounting the first solenoid valve and the second solenoid valve, which is connected to a compressed air source. It consists of a main manifold having an air supply path, and a sub manifold integrally coupled with the main manifold, and the air inlet side of the first solenoid valve is connected to the air supply flow path of the main manifold through the sub manifold. The sub manifold may include an air passage connecting the air inlet side and the air outlet side of the plurality of solenoid valves mounted in series, an air passage communicating with the compressed air supply passage, and the air pressure detection passage. It is characterized by having an air passage.

By closing the first solenoid valve, compressed air is supplied from the compressed air supply source to the supply pipe, thereby increasing the air pressure in the supply pipe. When the liquid level in the air supply pipe is lowered to the lower end of the air supply pipe, the compressed air in the intake pipe leaks in the form of bubbles in the liquid, and the air pressure in the intake pipe becomes the air pressure corresponding to the liquid level. By closing the first solenoid valve and closing the second solenoid valve, the air pressure in the air supply pipe is detected by the pressure sensor, and the liquid level in the tank is displayed on the display unit based on the detection signal.

Hereinafter, an embodiment of a bubble type liquid level meter according to the present invention will be described with reference to the drawings. The same code | symbol is attached | subjected to the component same as the structure of the prior art example shown in FIG.

<Example 1>

In FIG. 1, a liquid 14 such as oil and water is stored in the tank 10 of the ship. The pipe 30 is connected to the ceiling upper surface side of the tank 10 via the stand piece 16 and the flange 60. Unlike the above conventional example, the air purge head is not provided. However, there are cases where a check valve is provided if necessary. The pipe 30 is, for example, a pipe on the deck of the ship, and is connected to the manifold 64 disposed in the control room 38. The pipe 30 functions as a pipe for supplying compressed air by opening and closing control of the first and second solenoid valves 65 and 66 and also serves as a pipe for taking out a signal air. From the stand piece 16, the air supply pipe 12 is attached to the bottom surface of the tank 10, and the air supply pipe 12 is immersed in the liquid 14 in the tank 10 from the lower end thereof. have.

The manifold 64 is first formed with a hole for mounting a plurality of solenoid valves and an air distribution hole connected to each other and to the external pipes. In this embodiment, three solenoid valves 65, 66, 67 are attached to the manifold 64. Each solenoid valve is controlled to be controlled by the control board 56 of the idle converter 52. Each solenoid valve moves in one direction by excitation of the drive coil to communicate with the inlet and outlet sides of the air, and when the drive coil is non-excited, it moves with elastic pressing force to block the inlet and outlet sides of the air. Will. The manifold 64 branches the air flow hole connecting each of the solenoid valves 65, 66, and 67 in series, and the air flow hole between the solenoid valves 65, 66 to connect the pipe ( 30 is provided with an air distribution hole connected to 30, and an air distribution hole branched between the solenoid valves 66 and 67 and connected to a pipe contacting the pressure sensor 54 in the idle transducer 52. Moreover, it has the air flow hole connected to the air inlet side of the solenoid valve 65 and the piping from the air supply unit 40, and the air flow hole for opening the air outlet side of the solenoid valve 67 to air | atmosphere.

Similarly to the conventional example shown in FIG. 14, a compressor 34 serving as a compressed air source is provided, and an inboard regulator 36 and an air supply unit 40 are interposed between the compressor 34 and the manifold 64. The inboard regulator 36 adjusts the pressure of the compressed air sent out from the compressor 34 to about 7 kg / cm 2, for example. The air supply unit 40 is disposed in the control room 38 and has a stop valve 42, a filter 44, a regulator 46, and a pressure gauge 48 in order from the compressor 34 side. In the control room 38, an idle converter 52 and an indicator 58 are arranged. The resonant transducer 52 detects air pressure and converts it into an electrical signal. The controller board 56 controls the pressure indication value by the indicator 58 according to the pressure sensor 54 and the output of the pressure sensor 54. Equipped with. As described above, the air flow hole between the solenoid valves 66 and 67 is branched and connected to the pressure sensor 54 through a pipe. The control board 56 has an arithmetic function which calculates the detection output of the pressure sensor 54, converts it into the liquid level in the tank 10, and displays the liquid level on the indicator 58. FIG. The control board 56 is also provided with software for controlling the opening and closing operations of the respective solenoid valves 65, 66, 67.

Next, the operation of the first embodiment will be described. According to the opening and closing operation of the three solenoid valves 65, 66, 67, there are three operation modes, an air supply mode, an air stop mode, and a measured pressure atmospheric release mode, as shown in FIG. The "air supply mode" is a mode for supplying compressed air from the compressed air supply source to the air supply pipe 12, that is, the "air supply mode", and the "air stop mode" is a mode for stopping the air supply of air and measuring the liquid level. Measurement mode. "Measurement pressure atmospheric discharge mode" is an operation mode for performing zero point adjustment in which the compressed air applied to the pressure sensor is released into the atmosphere to be atmospheric pressure, and the indication value of the indicator 58 at this time is zero. In FIG. 3, SV1 denotes the first solenoid valve 65, SV2 denotes the second solenoid valve 66, and SV3 denotes the third solenoid valve 67.

In the "air supply mode", the first solenoid valve 65 opens the compressed air supply path, the second solenoid valve 66 closes the air pressure detection path connected to the pressure sensor, and the compressed air is supplied to the air supply pipe 12. In the "air stop mode", the first solenoid valve 65 closes the compressed air supply path, opens only the second solenoid valve 66, opens the pressure detection path, and the air pressure in the air supply pipe 12 is reduced by To the pressure sensor 54. In the &quot; measured pressure atmospheric release mode &quot;, only the third solenoid valve 67 is opened to make the air pressure applied to the pressure sensor 54 equal to the atmospheric pressure.

The &quot; air supply mode &quot; opening only the first solenoid valve and the &quot; measurement mode &quot; opening only the second solenoid valve are intermittently switched control as shown in FIG. In Fig. 2A, "a1" represents the first air supply mode and shows the next measurement mode of this air supply mode a1 as "b1". "An" represents the nth air supply mode and "bn" represents the nth measurement mode. Until immediately before the start of the air supply mode, the liquid level in the air supply pipe 12 is at the same level as the liquid level of the liquid stored in the tank. As the air supply mode is executed, the air pressure in the air supply pipe 12 increases, and the liquid level in the air supply pipe 12 is increased. It descends as shown in this FIG.2 (c). Since the air supply mode and the measurement mode are executed alternately, the air pressure in the air supply pipe 12 rises step by step as shown on the left side of FIG.

When the air pressure in the air supply pipe 12 rises and the liquid level in the air supply pipe 12 reaches the lower end of the air supply pipe 12, as shown in FIG. It leaks out and becomes a bubble, and ascends the liquid 14 in the tank 10 and is opened to the atmosphere. Therefore, the air pressure in the air supply pipe 12 becomes the air pressure corresponding to the level (depth) of the liquid 14 in the tank 10, and the air pressure in the air supply pipe 12 does not change unless the level of the liquid 14 changes. Do not. Therefore, the level of the liquid level 14 at that time can be measured by reading the measured value at the time when the measured value is not changed in the measurement mode. The symbol "I" in FIG. 2 (b) indicates that the liquid level lowering operation in the air supply pipe 12 is in progress, and the symbol "II" indicates the bubble discharge operation from the air supply pipe 12, that is, the liquid level 14 of the liquid level 14. It shows that it is in operation which can measure a level. The symbol "an" indicates the air supply mode immediately after switching to the bubble discharge operation, and the symbol "bn" indicates the measurement mode immediately after switching to the bubble discharge operation.

It is preferable that the liquid level lowering operation (I) at the time of start of air supply be completed in a short time, and be switched to the bubble discharge operation (II) as soon as possible. Thus, as shown in a1 and b1 of FIG. 2 (a), the first and second solenoid valves 65, (so that the operation time in the air supply mode is longer than the operation time in the measurement mode performed alternately with this, ( The operation of 66 is controlled. After switching to the bubble discharge operation, compressed air may be supplied to such an extent that the air pressure in the air supply pipe 12 can be maintained. Therefore, as shown by the symbols "an" and "bn", the operation time in the measurement mode is the air supply mode. The operation of the first and second solenoid valves 65, 66 is controlled to be longer than the operating time in. When the measured value is stabilized, as shown in the right half of Figs. 2 (a) and 2 (b), the operation time in the measurement mode is longer than the operation time in the air supply mode, and the period of the air supply mode and the measurement mode is extended. It is considered that unnecessary air supply is not performed.

Now the actual depth of the liquid 14 in the tank 10 is Hm. Since the piping on the deck of the ship is long, pressure loss (ΔP) occurs in the compressed air passing through the piping. Therefore, when the pressure at the manifold 64 is considered during operation in the air supply mode, the pressure at the upstream side of the second solenoid valve 66, at the ports A1 and P2 is increased.

(H × 0.1 + ΔP) [kg / cm 2]

Becomes Therefore, when switching from the air supply mode to the measurement mode, it takes time until the pressure at the Ps port connected to the pressure sensor 54 is stabilized. In the waveform diagram shown in Fig. 2 (b), the pressure rises by ΔP every time it is switched to the measurement mode, and then slowly decreases to be stable.

Therefore, as shown in Fig. 4, the pressure at the Ps port is in the allowable accuracy range, for example, a pressure equivalent to ± 1.0% FS.

H × 0.1 + ΔP

When lowered, the pressure at the Ps port is indicated by the depth of the indicator 58. For example, when H = 3, when it descends from 3 + 0.03 = 3.03 (kg / cm <2>), it displays on the indicator 58. FIG. In other words, in the measurement mode, first, by predicting the pressure fluctuations based on the pressure loss that increases or decreases with the distance from the control room to the level detector and the factors related to the liquid level depth of the level detector, the reading is added by displaying the correction. In this case, the correct level of liquid level entering the tolerance at the time of transition to the measurement mode is indicated. After the operation of the level gauge, that is, after the ship is in service, the learning ability can be automatically corrected based on the measured value. In FIG. 4, T1 represents an operating time in the air supply mode, T2 represents a time required until the measurement is allowed at the time of transition to the measurement mode, and T3 represents a time required to reach full stability.

In the "measuring pressure atmospheric release mode" in which the first and second solenoid valves 65 and 66 are closed and the third solenoid valve 67 is opened, the air pressure applied to the pressure sensor 54 becomes equal to atmospheric pressure. The indication of (58) is zero. That is, the measurement pressure atmospheric emission mode is a mode for zero point adjustment.

According to the first embodiment described above, the adjustment of the flow rate of the compressed air is not only controlled by the on / off of the solenoid valve but also does not require the installation of a member that requires subtle opening / closing control such as the flow control valve, so that the configuration is simple and inexpensive. A bubble-type liquid level meter with less trouble can be obtained. Since the measurement is made by switching from the air supply mode to the measurement mode, the consumption of compressed air is low, and high-precision liquid level measurement can be performed.

The bubble level gauge according to the above embodiment is installed for each tank, and the air supply unit 40, the manifold 64, the resonant transducer 52, and the indicator 58 of each level gauge are collectively placed in the control room 38. The centralized control and centralized monitoring are performed. The automatic control program of each of the solenoid valves 65, 66, and 67 is set first by assuming a dropping pattern or a discharging pattern of the tank. The execution of the automatic control program allows the switching of the detection process and adjustment of the supply of compressed air. Is performed.

<Example 2>

Next, the second embodiment shown in FIG. 5 will be described. The second embodiment differs from the first embodiment in the compressed air supply path from the compressor 34, which is the compressed air supply source, to the first solenoid valve 65 via the inboard regulator 36 and the air supply unit 40. The orifice 72 which limits the flow rate of air is arrange | positioned. The orifice 72 is disposed in the manifold 64 at the compressed air inlet side of the first solenoid valve 65. Other configurations and control of the solenoid valves 65, 66, 67 are the same as those in the first embodiment, and description thereof is omitted.

According to the bubble type liquid level meter of Embodiment 2, since the flow rate of the compressed air which flows into the 1st solenoid valve 65 by the orifice 72 becomes small and it is a thing of the compressed air passing through the piping arrange | positioned on the deck of a ship, The pressure loss ΔP decreases. Therefore, the air pressure of the Ps port is stabilized in a short time after stopping the air supply in the air supply mode and switching to the stop mode, so that the air pressure in the air supply pipe 12 can be measured without waiting for a long time. In addition, as in the first embodiment, the readout of the measured value is improved by the calculation processing of the control unit.

<Example 3>

6 shows Example 3 of the bubble type liquid level meter according to the present invention. The third embodiment is characterized in that the fourth solenoid valve 70 is arranged in parallel with the first solenoid valve 65 of the second embodiment. More precisely, the fourth solenoid valve 70 is connected in parallel to the portion in which the orifice 72 and the first solenoid valve 65 are connected in series. If the fourth solenoid valve 70 is added to the first embodiment, the fourth solenoid valve 70 may be directly connected to the first solenoid valve 65. As shown in FIG. 7, the fourth solenoid valve 70 is controlled by the control plate 56 at the same time as the first solenoid valve 65 and in the same manner as the first solenoid valve 65. Only when the liquid level in the supply pipe 12 is lowered, the fourth solenoid valve 70 is opened and closed together with the first solenoid valve 65, and the liquid level in the supply pipe 12 is lowered so that the lower end of the supply pipe 12 is lowered. When the compressed air starts to leak from the fourth solenoid valve 70 may be controlled to be in a closed state. Since the other configurations and controls are the same as those in the first and second embodiments, the description is omitted.

According to the bubble level gauge of the third embodiment, the presence of the fourth solenoid valve 70 allows the liquid level in the air supply pipe 12 to be lowered quickly, and the level of liquid in the tank can be measured from the start of the bubble level gauge. The time until can be shortened. In addition, when the liquid 14 enters the air supply pipe 12 due to the fluctuation of the ship or the like, the liquid 14 in the air supply pipe 12 can be quickly discharged. Similarly to the first embodiment, the reading accuracy of the measured value is improved by the arithmetic processing of the controller.

<Example 4>

Fig. 8 shows Example 4 of the bubble type liquid level meter according to the present invention. This embodiment has a configuration in which piping is added to the first embodiment. That is, the compressed air outlet port A1 of the first solenoid valve 65 is connected to the air supply pipe 12 through the compressed air supply path 30, and the air inlet side port P2 of the second solenoid valve 66 is provided. ) Is connected to the air supply pipe 12 through an air pressure detection path (32). In the first embodiment, the first and second solenoid valves 65 and 66 are directly connected and the middle thereof is branched and connected to the air supply pipe 12 by a single pipe. The first and second solenoid valves 65 and 66 are divided and connected to the air supply pipe 12 through the compressed air supply path 30 and through the air pressure detection path 32, respectively. Other than that is the same as that of Example 1. Reference numeral 64 denotes a manifold.

According to the fourth embodiment, the air pressure detection path 32 is always subjected to air pressure in the air supply pipe 12 so that compressed air does not flow. Therefore, even if the pressure detection path 32 is lengthened, the pressure loss ΔP in the pressure detection path 32 does not develop, and when the pressure detection path 2 is switched from the air supply mode to the measurement mode as shown in FIG. There is no pulsating rise in pressure inside the pressure loss ΔP. As shown in FIG. 10, when the compressed air leaks from the air supply pipe during the operation in the air supply mode, that is, the "air supply mode", the air pressure in the engine is changed into a waveform. The pressure in the air supply pipe 12 and the pressure in the air pressure detection path 32 are immediately stabilized.

According to the bubble-type liquid level meter according to the fourth embodiment, there is a disadvantage in that one pipe between the manifold 64 and the air supply pipe 12 is increased, and as soon as the air supply mode 12 is switched from the air supply mode to the measurement mode, Since the pressure can be detected by the pressure sensor 54 and the level of the liquid can be displayed on the display 58, there is no waiting time, so that a quick measurement is possible. Moreover, as soon as the pressure in the air supply pipe 12 is stabilized as soon as it is switched to the "measurement mode", high-precision liquid level measurement is attained.

In the embodiment of the bubble level gauge described above, a plurality of solenoid valves are connected to each other using a manifold. However, if the manifold is not used, the number of processes increases in the construction pipe. 1, 5, and 6, the outlet port A1 of the first solenoid valve 65 and the inlet port P2 of the second solenoid valve 66 are shown in FIGS. 5, 6 and 8, the outlet port A2 of the second solenoid valve 66 and the inlet side port P3 of the third solenoid valve 67 must be connected to each other by piping. There is a problem of increasing the number of processes.

Therefore, each embodiment of the present invention uses a manifold. The inventors of the present invention came up with the idea of using a manifold 642 as shown in Fig. 13B and mounting a solenoid valve as shown in Fig. 13A. The manifold 642 shown in FIG. 13 is a manifold having a generally conceivable configuration, and has an air inlet port P, an air outlet port R, and an air passage passing through these ports, respectively. . The manifold 642 has portions for mounting the first, second, and third solenoid valves 65, 66, and 67. When the solenoid valves are mounted at a predetermined position, the inlet port of each solenoid valve ( P1), P2, and P3 communicate with the inlet port P of the manifold 642, and the outlet ports A1, A2, and A3 of each solenoid valve are manifold 642. It is comprised so that it may communicate with the exit port R of (). In other words, the manifold 642 connects a plurality of solenoid valves in parallel.

Since the manifold usually conceived as shown in Fig. 13 does not connect a plurality of solenoid valves in series and does not branch the air passages connecting the solenoid valves, the "air supply mode", It is not possible to switch to the "measurement mode" and to switch to the "measurement pressure atmospheric release" mode.

Therefore, in the present invention, a unique configuration for applying to a bubble level gauge using a plurality of solenoid valves by adding the invention to the configuration of a manifold that can be usually conceived, enables the manifold to be used and at the same time reduces the number of installation steps. Promoted. The bubble type liquid level meter which concerns on Example 5 and Example 6 is demonstrated below.

<Example 5>

In FIG. 11, the tank 10, the air supply pipe 12, the piping 30, the compressor 34, the inboard regulator 36, the control room 38, the air supply unit 40, the first and the second ship of FIG. The components consisting of the third solenoid valves 65, 66, 67, the resonant transducer 52, the pressure sensor 54, and the like are the same as those of the embodiment shown in FIG. The description of the same components will be simplified and the configuration of the manifold which is a component unique to the present embodiment will be mainly described.

The manifold is composed of a main manifold 63 and a sub manifold 64, and an air passage for mounting a plurality of solenoid valves in advance, and an air passage connected to each other and to an external pipe, are installed. have. The main manifold 63 and the sub manifold 64 are integrally coupled. The main manifold 63 is used as a common manifold, the sub manifold 64 is installed at an appropriate position of the main manifold 63, and a pair of solenoid valves is mounted thereon to the air supply pipe 12. The pipe is connected to the pressure sensor 54 of the idle transducer 52. In other words, even when a bubble level gauge is installed for each of a plurality of tanks in a ship, the main manifold 63 is installed as a common one, and the sub manifold 64 is installed at an appropriate position of the main manifold 63, where a pair of Provide necessary piping by installing solenoid valve. By doing in this way, the conventional complicated piping which surrounds the compressed air supply piping for each of a plurality of bubble-type level gauges can be simplified.

In this embodiment, three solenoid valves 65, 66, 67 are attached to the submanifold 64. Each solenoid valve is controlled to be controlled by the control board 56 of the idle converter 52. Each solenoid valve moves in one direction by the excitation of the drive coil to communicate with the inlet and outlet sides of the air, and when the drive coil is non-excited, it moves with elastic pressing force to block the inlet and outlet sides of the air. Will. The sub manifold 64 branches the air passage between the solenoid valves 65, 66 and 67 in series, and the air passage between the solenoid valves 65 and 66 so as to branch off the piping 30. ) And an air passage connected to a pipe branching the air passage between the solenoid valves 66 and 67 and reaching the pressure sensor 54 in the idle transducer 52. The main manifold 63 has an air supply passage 68, one end of which is connected to the compressed air supply path from the air supply unit 40, and an air opening passage 69, one end of which is open to the atmosphere. . The other ends of the air passages 68 and 69 are closed.

When the first solenoid valve 65 is mounted on the sub manifold 64, the air inlet port P1 of the solenoid valve 65 passes the air of the main manifold 63 through the air passage of the sub manifold 64. The air outlet side port A1 of the solenoid valve 65 is connected to the supply flow path 68 and is connected to the air inlet side port P2 of the second solenoid valve 66 through the air passage of the submanifold 64. It is configured to be connected. When the second solenoid valve 65 is mounted on the sub manifold 64, the air outlet side port A2 passes through the air inlet side port of the third solenoid valve 67 through the air passage of the sub manifold 64. It is configured to connect to P3). When the third solenoid valve 67 is mounted on the sub manifold 64, the air outlet side port A3 passes through the air passage of the sub manifold 64 to the atmospheric opening passage 69 of the main manifold 63. It is configured to connect to.

In the same manner as in the above example, the compressor 34 is a compressed air supply source, and an inboard regulator 36 and an air supply unit 40 are interposed between the compressor 34 and the manifold 64. The inboard regulator 36 adjusts the pressure of the compressed air sent out from the compressor 34 to, for example, about 7 kg / cm 2. The air supply unit 40 is disposed in the control room 38 and includes a stop valve 42, a filter 44, a regulator 46, and a pressure gauge 48 in order from the compressor 34 side. In the control room 38, an idle converter 52 and an indicator 58 are arranged. The idle transformer 52 detects air pressure and converts it into an electrical signal. The controller board 56 controls the air pressure indicating value by the indicator 58 according to the pressure sensor 54 and the output of the pressure sensor 54. Is done. As described above, the air passage of the sub manifold 64 interposed between the solenoid valves 66 and 67 is branched and connected to the pressure sensor 54 through the pipe 61. The control board 56 has an arithmetic function which calculates the detection output of the pressure sensor 54, converts it into the liquid level in the tank 10, and displays the liquid level on the indicator 58. FIG. The control board 56 is also provided with software for controlling the opening and closing operations of the respective solenoid valves 65, 66, 67.

Since the operation of the fifth embodiment is the same as that of the first embodiment shown in Fig. 1, the description of the operation is omitted.

According to the fifth embodiment described above, even when a bubble level gauge is provided for each of the plurality of tanks, there is no need to pipe from the compressor 34 which is the compressed air supply source to the individual bubble level meters, and the main manifold 63 is used as a common manifold. Simplify the piping because it is enough to install the sub manifold 64 at a position adjacent to the main manifold 63 and mount a pair of solenoid valves to the air supply pipe 12 and the pressure sensor 54. can do. The main manifold 63 having an air supply passage 68 connected to the compressed air supply pipe, and the sub manifold 64 integrally with the main manifold 63 are coupled to the sub manifold 64. Since the solenoid valve is mounted, it is possible to switch to the "air supply mode", the "measurement mode" and the like even though the manifold is used. The main manifold 63 is fixed as a simple form having an air supply passage 68, and the sub manifold 64 is designed to be adapted to a combination of a pair of solenoid valves and piping to the outside of the bubble type liquid level gauge. It can respond flexibly by the structure corresponding to a structure.

<Example 6>

Next, Example 6 shown in FIG. 12 will be described. The sixth embodiment has a configuration in which piping is added to the fifth embodiment. That is, the compressed air outlet port A1 of the first solenoid valve 65 is connected to the air supply pipe 12 through the air passage of the submanifold 641 and the compressed air supply path 30, and the second solenoid valve. The air inlet side port P2 of 66 is connected to the air supply pipe 12 through the air passage of the submanifold 641 and the air detection path 32. In the fifth embodiment, the first and second solenoid valves 65 and 66 are connected through the air passage of the sub manifold 64, and the middle thereof is branched so that the air supply pipe 12 is connected by one pipe 30. In the sixth embodiment, the first and second solenoid valves 65 and 66 are divided as described above, and the compressed air supply path 30 and the air pressure detection path 32 are separated. It is connected to the air supply pipe 12 through. In order to realize the above configuration, the sub manifold 641 includes an air passage passing through a pipe 30 for connecting the air outlet side port A1 of the first solenoid valve 65 to the air supply pipe 12; The air inlet side port P2 of the two solenoid valve 66 has an air passage through the pipe 32 for connecting to the air supply pipe 12. There is no air passage in the submanifold 641 that directly connects the air outlet side port A1 of the first solenoid valve 65 and the air inlet side port P2 of the second solenoid valve 66. Other than that is the same as that of Example 5.

According to the sixth embodiment, the air pressure detection path 32 always has air pressure in the air supply pipe 12 so that compressed air does not flow. Therefore, even if the air pressure detection path 32 is long, the pressure loss ΔP in the air pressure detection path 32 does not occur, and when the pressure in the air pressure detection path 32 is switched to the measurement mode, the pressure loss ΔP There is no significant pulsating rise. Therefore, there is a disadvantage in that one pipe between the submanifold 641 and the air supply pipe 12 is increased. As soon as the air supply mode 12 is switched from the air supply mode to the measurement mode, the pressure in the air supply pipe 12 is detected by the pressure sensor 54. Therefore, the liquid level can be displayed on the indicator 58, so that quick measurement is possible without waiting time. In addition, as soon as the pressure in the air supply pipe 12 is stabilized as soon as it is switched to the "measurement mode", high-precision liquid level measurement is attained. Also in the second embodiment, by having the main manifold 63 and the sub manifold 641, the same effect as in the first embodiment can be obtained.

The bubble level gauge according to the present invention can be applied as a liquid level measurement of a tank, such as a cargo storage tank, a ballast tank, a purified water tank, a drinking tank, a tanker, a LNG tanker, a cargo vessel, or a water gauge. It can be applied to tanks of various uses installed on the ground.

In addition, although the gas supplied to an air supply pipe was described as air in each Example, it may be gas other than air depending on the kind of dripping.

According to the bubble level gauge according to the present invention, by using the solenoid valve in place of the flow control valve used in the conventional bubble type level gauge, the overall configuration is simplified, and a bubble type level gauge with little trouble and low cost can be obtained.

The solenoid valve can control its operation with an automatic control program, and manual operation is unnecessary. In addition, the control by the automatic control program can be carried out in the control room, and since it is not necessary to install the electric equipment on the deck, it can satisfy the condition of intrinsically safe explosion-proof type. In addition, adjustment of the supply amount of compressed air can be measured by first executing the automatic control program set assuming the dripping pattern or the landing pattern of the tank.

The consumption of compressed air can be reduced and there is no pulsation of compressed air, so stable display can be performed without shaking the displayed value.

According to the invention in which the solenoid valve is mounted on the manifold, even when a bubble level gauge is installed in each tank, the main manifold is used as a common manifold because there is no need to pipe from the compressed air supply source to the individual bubble level gauge. Since it is enough to install the sub manifold at the proper position of the main manifold and install a solenoid valve to the air supply pipe, the piping can be simplified. In addition, since the main manifold having an air supply passage connected to the compressed air supply source, the sub manifold are integrally integrated with the main manifold, and a plurality of solenoid valves of the sub manifold are mounted, the "air supply mode" and the "measurement mode" ", Etc. can be used.

Although the present invention has been described with reference to the embodiments shown in the drawings, this is merely exemplary, and it will be understood by those skilled in the art that various modifications and equivalent other embodiments are possible. will be. Therefore, the true technical protection scope of the present invention will be defined by the matter described in the appended claims.

Claims (18)

A liquid level in the tank based on a supply signal having at least a lower end submerged in liquid in the tank, a compressed air supply source for supplying compressed air into the supply pipe, a pressure sensor for measuring the air pressure in the supply pipe, and a detection signal of the pressure sensor A bubble type liquid level meter having a display portion displaying A first valve for opening and closing the compressed air supply path from the compressed air supply source to the supply pipe; A second valve for opening and closing an air pressure detection path from the air supply pipe to the pressure sensor, And a control unit for controlling the first valve and the second valve to stop the supply of the compressed air to the air supply pipe during the measurement. The bubble level gauge according to claim 1, further comprising a third valve capable of opening a pressure detection path from the air supply pipe to the pressure sensor. The bubble level gauge according to claim 1 or 2, wherein the opening and closing operation of each valve is controlled by software. delete The bubble level gauge according to claim 1, wherein the controller controls the first valve and the second valve so that the air supply mode and the measurement mode are alternately performed. The air conditioner according to claim 5, wherein the control unit controls the air supply mode time to be longer than the measurement mode time at the time of supplying compressed air to the air supply pipe, and shortens the time of the air supply mode to the time of the measurement mode after the measured value is stabilized. Bubble level meter to say. 7. The bubble level gauge according to claim 6, wherein in the measurement mode, the pressure sensor measures after a predetermined time elapses until the measured value becomes stable at the time of transition to the measurement mode. The bubble level gauge according to claim 1, wherein an orifice for restricting the flow rate of the compressed air is disposed in the compressed air supply path from the compressed air source to the first valve. According to claim 1, wherein the fourth valve is arranged in parallel with the first valve, the fourth valve and the first valve is opened and closed at the same time at the time of supply of compressed air until the measurement mode is operating normally, the measurement mode is normally A bubble level gauge in which the fourth valve is closed and the first and second valves are controlled to open and close alternately when in operation. The bubble level gauge according to claim 1, wherein the first valve and the second valve are connected in series, and the middle of the first valve and the second valve are branched and piped to the air supply pipe. The bubble level gauge according to claim 1, wherein the compressed air outlet side of the first valve is connected to the air supply pipe through a compressed air supply path, and the air inlet side of the second valve is connected to the air supply pipe through an air pressure detection path. A liquid level in the tank based on a supply signal having at least a lower end submerged in liquid in the tank, a compressed air supply source for supplying compressed air into the supply pipe, a pressure sensor for measuring the air pressure in the supply pipe, and a detection signal of the pressure sensor A bubble type liquid level gauge having a display unit for displaying a pressure gauge, a first valve for opening and closing a compressed air supply path from a compressed air supply source to an air supply pipe, and a second valve for opening and closing a pressure detection path from the air supply pipe to a pressure sensor, It has a manifold to mount the first valve and the second valve, The manifold includes a main manifold having an air supply path connected to a compressed air source, and a sub manifold integrally coupled with the main manifold, The air inlet side of the first valve is connected to the air supply flow path of the main manifold through the sub manifold, The sub manifold includes an air passage connecting the air inlet side and the air outlet side of the plurality of valves mounted in series, an air passage communicating with the compressed air supply passage, and an air passage communicating with the air pressure detection passage. A bubble type liquid level meter comprising: 13. The submanifold of claim 12, wherein the submanifold may be equipped with a third valve for opening an air pressure detection path from the air supply pipe to the pressure sensor, and the main manifold is connected to the air outlet side of the third valve through the submanifold. Bubble level gauge with open air path in communication. The bubble level gauge according to claim 12 or 13, wherein the opening and closing operation of each valve is controlled by software. 13. The method of claim 12, wherein in the air supply mode in which the first valve opens the compressed air supply path, the second valve closes the air pressure detection path, and in the measurement mode in which the second valve opens the air pressure detection path, the first valve opens the compressed air supply path. Closed bubble level gauge. 13. The bubble level gauge according to claim 12, wherein the first valve and the second valve are controlled such that the air supply mode and the measurement mode are alternately performed. 13. The bubble level gauge according to claim 12, wherein the first valve and the second valve are connected in series through a submanifold, and the submanifold branched between the first valve and the second valve and piped to the supply pipe. A liquid level in the tank based on a supply signal having at least a lower end submerged in liquid in the tank, a compressed air supply source for supplying compressed air into the supply pipe, a pressure sensor for measuring the air pressure in the supply pipe, and a detection signal of the pressure sensor A bubble type liquid level gauge having a display unit for displaying a pressure gauge, a first valve for opening and closing a compressed air supply path from a compressed air supply source to an air supply pipe, and a second valve for opening and closing a pressure detection path from the air supply pipe to a pressure sensor, It has a manifold to mount the first valve and the second valve, The manifold has a main manifold having an air supply path connected to a compressed air source, and a sub manifold integrally coupled with the main manifold, The air inlet side of the first valve is connected to the air supply flow path of the main manifold through the sub manifold, The air outlet side of the first valve is connected to the supply pipe through the sub manifold and the compressed air supply path. The air inlet side of the second valve is a bubble level gauge connected to the air supply pipe through the sub manifold and the air detection path.

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