JP5044494B2 - Double shell tank leak inspection device - Google Patents

Description

  The present invention relates to a leakage inspection apparatus for a double shell tank, and a leakage inspection apparatus for a double shell tank for periodically inspecting the presence or absence of leakage from a leakage detection layer formed between an inner shell and an outer shell. About.

  For example, in a refueling facility such as a gas station, an underground tank is buried in the site, and the oil liquid delivered by a tank truck is stored in the underground tank.

  In recent years, in underground tanks, pinholes due to corrosion have occurred when buried underground, causing fuel stored in the tank to leak into the ground or underground water to flow into the tank. It has become. In order to prevent such underground leakage, a double shell tank is used. The double-shell tank has a double-shell structure with an outer shell on the outside of the cylindrical inner shell, and the gap formed between the outer periphery of the inner cylinder and the inner periphery of the outer cylinder is a leak detection layer It has become. A detection cylinder is formed so as to communicate with the leakage detection layer, and a liquid level sensor is provided in the detection cylinder. The liquid level sensor detects a leak detection signal by changing the liquid level when a pinhole is generated in the outer shell and groundwater enters the leak detection layer, or when oil leaks from the inner shell enters the leak detection layer. Is configured to output.

  As this type of double shell tank, in addition to the steel double shell tank whose inner shell and outer shell are made of steel, those using reinforced plastics, that is, the inner shell is made of steel and the outer shell is strengthened. There are two types: a steel reinforced plastic tank made of plastic (SF double shell tank) and a reinforced plastic double shell tank made of reinforced plastic for both the inner and outer shells (FF double shell tank).

  Now, the law stipulates that underground tanks must be periodically inspected for leaks.

  In order to inspect whether there is a leak from the leak detection layer in such a double-shell tank made of reinforced plastic (legal check), the leak detection layer is maintained at a predetermined decompression value via the detection cylinder, and the leak is inspected. There is an urgent need for leak inspection methods.

As a conventional leakage inspection method, for example, as seen in Patent Document 1, there is a method of inspecting the presence or absence of leakage by pressurizing or depressurizing the inside of an underground tank (single cylinder type).
Japanese Patent No. 35858899

  However, what is described in the above-mentioned patent document is to inspect the presence or absence of leakage by holding the gas phase portion (space portion above the liquid level in the tank) of the single cylinder underground tank at a predetermined negative pressure. Assuming that the single cylinder underground tank described in the above-mentioned patent document is subjected to a leak test with a negative pressure for leak detection of the double shell tank leak detection layer, it is generated by a vacuum pump. The negative pressure is introduced as it is. In this way, when the negative pressure generated by the vacuum pump is introduced as it is, the space volume (space volume) composed of the leak detection layer and the detection cylinder is extremely small compared to the gas phase part in the underground tank, so that the single cylinder type The pressure of the leak detection layer is suddenly reduced compared to the case of leak inspection of the gas phase part of the underground tank. For this reason, in a leak inspection method in which the leak detection layer is rapidly depressurized, the wall made of reinforced plastic (outer shell tank) that forms the outer shell of the double shell tank is deformed, causing cracks, There may be a problem that there is a high possibility that the peripheral edge portion of the outer shell fixed to the surface of the shell (portion defining the boundary portion of the leakage detection layer) may be peeled off from the inner shell.

  In addition, as a means for preventing an excessive negative pressure from acting on the leakage detection layer, for example, a safety valve may be provided, but a safety valve having a configuration that reliably opens even a minute negative pressure can be manufactured. It is difficult, and if foreign matter adheres to the passage leading to the safety valve, this prevents the piping, that is, the safety valve from operating, and the safety valve may not operate.

  Therefore, in view of the above circumstances, an object of the present invention is to provide a double shell tank leakage inspection apparatus that solves the above-described problems.

  In order to solve the above problems, the present invention has the following means.

The present invention is a leakage inspection apparatus for a double shell tank for inspecting the presence or absence of leakage of the leakage detection layer based on a pressure change of the leakage detection layer formed in the double shell tank.
A pipe having one end connected to the leak detection layer;
A decompression pump connected to the other end of the pipe and sucking air of the leak detection layer;
An on-off valve that is provided in the middle of the pipe and opens or closes between the pressure reducing pump,
A pressure detecting means provided in the middle of the pipe between the on-off valve and the leak detection layer, for detecting the pressure of the leak detection layer;
A throttle member that is provided in the middle of the pipe near the pressure reducing pump and restricts the amount of air supplied to the suction port of the pressure reducing pump to a predetermined amount;
An air amount adjusting valve that is provided in the middle of the pipe between the throttle member and the on-off valve and finely adjusts the supply amount of air restricted by the throttle member;
By providing the above, the above-mentioned problem is solved.

  Further, the present invention solves the above problems by attaching at least the pipe, the pressure detecting means, the on-off valve, the air amount adjusting valve, and the throttle member to a mounting plate inclined at a predetermined angle with respect to a horizontal plane. To do.

  According to the present invention, when the air in the leak detection layer is sucked by starting the decompression pump, the amount of air introduced into the pipe is initially increased by the throttle member and the air amount adjustment valve, and an excessive negative pressure is applied to the leak detection layer. By further reducing the amount of air introduced into the piping and gradually increasing the negative pressure of the leak detection layer, the outer shell tank made of reinforced plastic deforms and cracks occur, It is possible to prevent the outer shell from peeling off.

  The best mode for carrying out the present invention will be described below with reference to the drawings.

  FIG. 1 is a block diagram schematically showing an embodiment of a leakage inspection apparatus for a double shell tank according to the present invention. As shown in FIG. 1, the leakage inspection apparatus 10 includes a piping path 20 having one end connected to the leakage detection layer 100 of the double shell tank 90, a decompression pump 30 connected to the other end of the piping path 20, A pressure detector (pressure detection means) 40 provided in the middle of the piping path 20, an on-off valve 50, an air amount adjusting valve 60, a throttle member 70, and a control device 80 provided in the middle of the piping path 20 are provided. In addition, a pressure gauge (pressure detection means) 42 having a pointer portion for measuring the pressure of the leak detection layer 100 and instructing the measured value is attached to the piping path 20.

  The decompression pump 30 sucks the air in the leak detection layer 100 when performing a leak test, and depressurizes the leak detection layer 100. The pressure detector 40 is disposed on the upstream side closest to the double shell tank 90 and detects the pressure of the leak detection layer 100 of the double shell tank 90. The pressure detector 40 includes a pressure transmitter, and outputs a pressure detection signal corresponding to the detected pressure value to the control device 80. As will be described later, the control device 80 monitors the pressure change rate based on the pressure detection signal, and there is a leak when a pressure change exceeding 10% is detected within a predetermined time (for example, 45 minutes). Is determined. The control device 80 is connected to a monitor 82 formed of a liquid crystal panel, and stores, for example, a control program for displaying a leakage inspection procedure guidance on the monitor 82 and displaying a leakage inspection result on the monitor 82. Yes.

  The on-off valve 50 is a manual type on-off valve, and opens or closes the piping path 20 between the pressure gauge 42 and the decompression pump 30.

  The air amount adjustment valve 60 is an adjustment valve that adjusts a manual air supply amount, and is provided in the middle of the piping path 20 to finely adjust the air supply amount supplied to the suction port 32 of the decompression pump 30. It is configured to be able to.

  The throttle member 70 is a throttle valve for restricting the manual air supply amount, and the air supply amount provided in the middle of the piping path 20 and supplied to the suction port 32 of the decompression pump 30 is stepped from a relatively large flow rate. It is configured so that it can be adjusted to.

  Further, the exhaust port 34 of the decompression pump 30 communicates with the vent pipe via an exhaust pipe 36 and a discharge jig 38.

  FIG. 2 is an enlarged front view showing the arrangement of each device of the leakage inspection apparatus 10. As shown in FIG. 2, the pipe path 20 has one end (the right end shown in FIG. 2) and an upstream joint 120 to which the leak detection pipe 110 communicated with the leak detection layer 100 of the double shell tank 90 is connected. The T-shaped joint 130 to which the pressure detector 40 is branch-connected, the T-shaped joint 140 to which the pressure gauge 42 is branch-connected, the on-off valve 50, and the T-shaped joint 150 to which the air amount adjusting valve 60 is branch-connected. The T-shaped joint 160 to which the throttle member 70 is branched and the downstream side joint 180 to which the suction hose 170 communicated with the suction port 32 of the decompression pump 30 is connected.

  Further, the piping path 20 is held by the mounting plate 192 of the bracket 190 at least at two places by the mounting bracket 200 formed in a U shape. Since the piping path 20, the pressure detector 40, the pressure gauge 42, the valve 50, and the air amount adjusting valves 60 and 70 are fixed to the mounting plate 192 of the bracket 190, they can be easily transported as one unit. it can.

  The on-off valve 50 is composed of, for example, a ball valve and functions as a main valve when performing a leak detection inspection. When the operation lever 52 is rotated 90 ° clockwise, the valve is closed and the operation lever 52 is counterclockwise. The valve opens when it is turned 90 °. The on-off valve 50 is provided with a rotation position detection sensor 54 that detects the rotation operation position of the operation lever 52.

  The air amount adjusting valve 60 finely adjusts the air supply amount at a relatively small flow rate, for example, by moving the needle with respect to the passage of the valve seat according to the rotation angle of the operation handle 62 formed of a needle valve. Can do. Further, an air introduction pipe 64 is communicated above the air amount adjustment valve 60, and a plurality of holes 66 for sucking air are provided on the outer periphery of the air introduction pipe 64. The air amount adjusting valve 60 is held on the mounting plate 192 by a mounting bracket 200 formed in a U shape. The air amount adjustment valve 60 is provided with a rotation position detection sensor 68 that detects the rotation operation position of the operation handle 62.

  The throttle member 70 is, for example, any one of a ball valve, a butterfly valve, a gate valve, a globe valve (ball valve), or a hole having a size that makes the flow path area 2/3. And is configured to restrict the air flow rate so as to supply a larger flow rate than the air amount adjustment valve 60 in accordance with the rotation angle of the operation lever 72. However, in the case of a fixed orifice plate, a constant opening degree (the flow path area is 2/3) is always provided. In addition, the diaphragm member 70 is configured such that the rotation angle of the operation lever 72 can be adjusted in the range from fully open to 1/3 closed. Further, an air introduction pipe 74 is communicated above the throttle member 70, and a plurality of holes 76 for sucking air are provided on the outer periphery of the air introduction pipe 74. The diaphragm member 70 is provided with a rotation position detection sensor 78 that detects the rotation operation position of the operation lever 72.

  Further, since the air amount adjusting valve 60 and the throttle member 70 are branched and connected in parallel to the piping path 20, even if the air amount adjusting valve 60 is fully closed, the air amount adjusting valve 60 and the throttle member 70 are close to the decompression pump 30. Since air is supplied from the provided throttle member 70 to the suction port 32 of the decompression pump 30 through the piping path 20, an excessive negative pressure is prevented from acting on the leakage detection layer 100 of the double shell tank 90. .

  Since the detection signals of the rotational position detection sensors 54, 68, 78 are output to the control device 80, the control device 80 recognizes the valve openings of the on-off valve 50, the air amount adjustment valve 60, and the throttle member 70. Can do.

  FIG. 3 is a side view of the leakage inspection apparatus 10. As shown in FIG. 3, the mounting plate 192 of the bracket 190 is inclined at an arbitrary angle α (α = 45 °) with respect to the bottom plate 194 (installation plate) for installation. When adjusting the valve opening degree, the angle is set so that the pointer of the pressure gauge 42 is easy to see. The inclination angle α of the mounting plate 192 can be set to an arbitrary angle in the range of 30 ° to 60 °, for example. As described above, the mounting plate 192 is inclined at a predetermined angle with respect to the bottom plate 194, thereby improving the operability of various devices and the visibility of the pressure gauge.

  Although not shown in FIGS. 2 and 3, the control device 80 is provided separately from the bracket 190.

  Here, the structure of the double shell tank 90 will be described.

  FIG. 4 is a front longitudinal sectional view of the double shell tank 90. FIG. 5 is a longitudinal sectional view of the double shell tank 90 taken along the line XX in FIG. 4 and 5, the double shell tank 90 includes an inner shell 280 made of a steel tank, and an outer shell 290 made of an FRP resin tank formed so as to cover the outer periphery of the inner shell 280. It consists of a double-structure SF double-shell tank with

  Further, on the inner peripheral surface of the inner shell 280, a corrosion-resistant layer 282 coated with a material that is not soluble in oil liquid, for example, an epoxy resin, is formed at least up to the maximum allowable liquid level height position of the inner shell 280. Yes. Thereby, the inner shell 280 can prevent corrosion from the inner peripheral surface. The corrosion-resistant layer 282 is not limited to the resin material described above, and may be a structure in which a thin sheet made of a stainless material having corrosion resistance is attached with an adhesive to at least the maximum allowable liquid level of the inner shell 280.

  Between the inner shell 280 and the outer shell 290, a space securing member made of a thin resin sheet (for example, a vinylon cloth having a thickness of 0.5 mm) is interposed to form the leak detection layer 100. Since this space securing member is formed of a film-like material that is thinner than the gap between the inner shell 280 and the outer shell 290, the leak detection layer 100 having a smaller gap is formed by closely contacting the outer peripheral surface of the inner shell 280. Can be formed between the inner peripheral surface of the outer shell 290 and the inner peripheral surface of the outer shell 290. In addition to the resin sheet, the space securing member may be a thin and water-absorbent sheet such as a resin fiber layer or Japanese paper.

  A leak detection cylinder 260 is inserted into the cylindrical interior of the leak detection unit 250 to which the other end of the leak detection pipe 110 is connected. The leak detection cylinder 260 is provided so as to penetrate the inner shell 280 in the vertical direction, the lower end 262 communicates with the leak detection layer 100 at the bottom of the tank, and the upper end protrudes above the top of the double shell tank 90. The upper end 264 of the leak detection cylinder 260 is used as a negative pressure inlet for introducing a negative pressure into the leak detection layer 100, and is used as an attachment portion of a leak detection sensor that detects the liquid level after installation. . The space volume of the leak detection tube 110 and the leak detection layer 100 is a very small space compared to the internal volume of the inner shell 280.

  The double shell tank 90 is determined such that the maximum allowable liquid level height position Hmax is 90% of the total tank capacity. Accordingly, the double shell tank 90 is unloaded from the tank truck until the maximum allowable liquid level height position Hmax is reached.

  The outer shell 290 is formed not to cover the entire circumference of the inner shell 280 but to cover the outer circumference excluding the top 220 above the maximum allowable liquid level height position Hmax. Accordingly, the leakage detection layer 100 is also formed with the maximum allowable liquid level height position Hmax as the upper limit.

  Although not shown, a liquid level sensor that detects that either the outer shell 290 or the inner shell 280 is broken and water or oil stored in the tank has entered the leak detection cylinder 260. Is provided.

  Here, the procedure of the leakage inspection method for the double shell tank 90 using the leakage inspection apparatus 10 will be described.

  Procedure 1: First, as shown in FIG. 1, the worker connects one end of the leak detection pipe 110 to the leak detection layer 100 of the double shell tank 90, and connects the other end of the leak detection pipe 110 to the pipe path 20. Connect to the upstream joint 120. Further, one end of the suction hose 170 is connected to the suction port 32 of the decompression pump 30, and the other end of the suction hose 170 is connected to the downstream side joint 18 of the piping path 20.

  Then, the worker records the weather environment (temperature, humidity) and the temperature of the double shell tank 90 (each temperature in the gas phase region and the liquid phase region) before the leakage inspection.

  Procedure 2: Next, the worker rotates the on-off valve 50, the air amount adjusting valve 60, the operation lever 52, the operation handle 62, and the operation lever 72 of the throttle member 70 to open the valve. With this valve opening operation, the rotation position detection sensors 54, 68, 78 move the operation lever 52, the operation handle 62, and the operation lever 72 to the rotation position, that is, the opening / closing valve 50, the air amount adjustment valve 60, and the throttle member 70. A valve opening degree detection signal corresponding to the valve opening degree (valve opening) is output to the control device 80.

  Procedure 3: The control device 80 activates the decompression pump 30, sucks the air in the leak detection layer 100 of the double shell tank 90 through the leak detection pipe 110, the piping path 20, and the suction hose 170, and Depressurize the minute space. At this time, since the air amount adjusting valve 60 and the throttle member 70 are opened to the atmosphere, air is supplied from the air amount adjusting valve 60 and the throttle member 70 to the suction port 32 of the pressure reducing pump 30, so that the operation of the pressure reducing pump 30 is performed. Therefore, the outer shell 290 made of reinforced plastic is prevented from being deformed and cracked, and the outer shell is prevented from peeling off.

  Procedure 4: An operator turns the operating lever 72 of the throttle member 70 by 1/3 in the closing direction to reduce the opening of the throttle member 70 to 2/3, thereby reducing the amount of air supplied to 2 Squeeze to / 3. As a result, the amount of air supplied from the throttle member 70 is reduced by 1/3, whereby the negative pressure due to the operation of the decompression pump 30 gradually increases. Here, since the throttle member 70 does not perform an operation of further reducing the opening degree, the air suction force against the leakage detection layer 100 does not increase abnormally. In this embodiment, when a valve such as a ball valve is used as the throttle member 70, the operating range of the operating lever 72 is configured to move only from a fully open range to a 1/3 closed range. Safety when 60 closes is ensured. When a fixed orifice plate is used as the throttle member, a 2/3 flow passage area is always ensured, so safety is ensured.

  Procedure 5: The worker gradually turns the operation handle 62 of the air amount adjustment valve 60 in the closing direction until the pointer of the pressure gauge 42 indicates -2 kPa. When the pointer of the pressure gauge 42 operates at a predetermined pressure reduction speed (low speed), the rotation operation of the operation handle 62 is stopped and the valve opening degree is maintained.

  Procedure 6: When the pointer of the pressure gauge 42 reaches −2 kPa, the worker rotates the operation lever 52 of the on-off valve 50 in the closing direction to close the on-off valve 50. The closed state in which the piping path 20 is blocked by closing the on-off valve 50 is continued for a predetermined time (for example, 2 minutes). Thereby, the pressure of the leak detection layer 100 is stabilized at -2 kPa.

  Procedure 7: When a predetermined time (for example, 2 minutes) elapses, the worker rotates the operation lever 52 of the opening / closing valve 50 in the opening direction to open the opening / closing valve 50. Thereby, a negative pressure due to the operation of the decompression pump 30 is introduced into the leak detection layer 100. At this time, the valve opening of the throttle member 70 is maintained at 2/3, and the air amount adjustment valve 60 also maintains the above valve opening (the valve opening at which the pointer of the pressure gauge 42 operates at a constant pressure reduction speed). To do. Since the pressure reduction speed is determined, the operation handle 62 is rotated little by little to finely adjust the valve opening degree of the air amount adjustment valve 60 so as to keep the pressure reduction speed. By maintaining the valve opening degree of the throttle member 70 at 2/3 and adjusting the air supply amount by the air amount adjustment valve 60, the leak detection pipe 110 and the leak detection layer 100 having a relatively small space volume are rapidly reduced. Therefore, it is possible to prevent the outer shell 290 made of reinforced plastic from being deformed and the outer shell 290 from being peeled off from the inner shell 280.

  Procedure 8: The procedures 5 and 6 are repeated, and the leak detection layer 100 is depressurized until the pointer of the pressure gauge 42 indicates -4 kPa.

  Step 9: When the pointer of the pressure gauge 42 reaches −4 kPa as in the above step 7, the operation lever 52 of the on-off valve 50 is turned in the closing direction to close the on-off valve 50, and a predetermined time (for example, Maintain this state for 2 minutes.

  Step 10: Further, the above steps 5 to 7 are repeated until the pointer of the pressure gauge 42 reaches −20 kPa.

  Procedure 11: After depressurizing the leak detection layer 100 to −20 kPa, a leak monitoring time of 30 minutes is set after a standing time of a predetermined time (for example, 15 minutes). The leakage monitoring time is a time set according to the capacity of the double shell tank 90. For example, in the case of a capacity exceeding 50 KL (kiloliter), 15 minutes are added for every 50 KL. It will be time.

  Procedure 12: The control device 80 checks whether the pressure change rate of the leak detection layer 100 is less than 10% or more than 10% while the leak monitoring time elapses. When the change rate of the pressure value measured by the pressure detector 40 and the pressure gauge 42 is 10% or less, it is determined that there is no leakage, and when the pressure change rate exceeds 10%, it is determined that there is leakage.

  Here, the control process executed by the control device 80 will be described with reference to the flowchart shown in FIG. As shown in FIG. 6, the control device 80 displays an operation procedure such as “open the on-off valve 50, the air amount adjustment valve 60, and the throttle member 70” on the monitor 82 in S <b> 11. As a result, the worker rotates all of the on-off valve 50, the air amount adjusting valve 60, the operation lever 52, the operation handle 62, and the operation lever 72 of the throttle member 70 to open them all.

  In the next S12, the valve corresponding to the rotation operation position of the operation lever 52, the operation handle 62, and the operation lever 72 from the rotation position detection sensors 54, 68, 78 of the opening / closing valve 50, the air amount adjustment valve 60, the throttle member 70. The opening degree detection signal is read, and it is checked whether the on-off valve 50, the air amount adjustment 60, and the throttle member 70 are all fully opened. When any one of the on-off valve 50, the air amount adjusting valve 60, and the throttle member 70 is closed (in the case of NO), the process returns to S11.

  Further, when it is detected that the on-off valve 50, the air amount adjusting valve 60, and the throttle member 70 are all opened (in the case of YES), the process proceeds to S13, and the decompression pump 30 is activated. At this time, since air is introduced by opening the air amount adjusting valve 60 and the throttle member 70, the air in the leak detection layer 100 of the double shell tank 90 has not been sucked yet.

  In the next S14, an operation instruction such as “adjust the valve openings of the air amount adjusting valve 60 and the throttle member 70 to a predetermined valve opening (see steps 4 and 5)” is displayed on the monitor 82. As a result, the worker performs the operations in steps 4 and 5 above. That is, the worker rotates the operation lever 72 of the throttle member 70 in the closing direction to reduce the opening degree of the throttle member 70 to 2/3. Further, the worker gradually turns the operation handle 62 of the air amount adjustment valve 60 in the closing direction until the pointer of the pressure gauge 42 points to −2 kPa, and when the pointer of the pressure gauge 42 operates at a constant decompression speed, The rotation operation of the operation handle 62 is stopped, and the valve opening degree is maintained. As a result, the amount of air supplied to the pipe path 20 by the air amount adjusting valve 60 and the throttle member 70 is throttled, and the air suction amount of the leak detection layer 100 is gradually increased accordingly, and the leak detection layer 100 is gradually depressurized. The

  In the next S15, the valve position detection signals are read from the rotation position detection sensors 68 and 78, and it is checked whether or not the adjustment operation of the air amount adjustment valve 60 and the throttle member 70 has been completed. In S15, when it is detected that the adjustment operation of the air amount adjustment valve 60 and the opening degree of the throttle member 70 is completed (in the case of YES), the process proceeds to S16, and the pressure detection signal detected by the pressure detector 40 is displayed. Read and check if pressure is reduced to -2 kPa.

  In S16, when it is detected that the pressure detected by the pressure detector 40 has reached -2 kPa (in the case of YES), the process proceeds to S17, and whether or not a first predetermined time (for example, 2 minutes) has elapsed. To check. Further, when the adjustment operation of the air amount adjusting valve 60 and the opening of the throttle member 70 is not completed in S15 (in the case of NO), or the pressure detected by the pressure detector 40 in S16 has not reached −2 kPa. In the case (in the case of NO), the processes of S15 and S16 are repeated.

  In S17, when a first predetermined time (for example, 2 minutes) has elapsed (in the case of YES), the process proceeds to S18, and an operation instruction such as “close the on-off valve 50” is displayed on the monitor 82. Subsequently, the process proceeds to S18a, in which a valve opening degree detection signal corresponding to the rotational operation position of the operation lever 52 is read from the rotational position detection sensor 54 of the on-off valve 50 to check whether the on-off valve 50 is closed. . In S18a, when it is detected that the on-off valve 50 is closed, the process proceeds to S19.

  In the next S19, it is checked whether or not the processes in S16 to S18 have been repeated a predetermined number of times (for example, n = 10 times). In the present embodiment, the pressure of the leak detection layer 100 is reduced to -2 kPa at a time. Therefore, in order to reduce the pressure to -20 kPa, the processes of S16 to S18 are repeated 10 times. As described above, by repeating the processes of S16 to S18 a plurality of times (in this embodiment, 10 times), the leak detection tube 110 and the leak detection layer 100 having a relatively small space volume are gradually decompressed stepwise. As a result, it is possible to prevent the pressure from being suddenly reduced and to prevent the outer shell 290 made of reinforced plastic from being deformed and the outer shell 290 from being peeled off from the inner shell 280.

  In S19, when the processes of S16 to S18 are repeated n times (for example, n = 10 times) (in the case of YES), the process proceeds to S20, and whether or not a second predetermined time (for example, 45 minutes) has elapsed. To check. In S20, when it is detected that the second predetermined time (for example, 45 minutes) has elapsed (in the case of YES), the process proceeds to S21, in which the pressure detection signal detected by the pressure detector 40 is read, The pressure fluctuation rate with respect to the reduced pressure value (−20 kPa) is obtained.

  In next S22, it is checked whether or not the pressure fluctuation rate exceeds a preset allowable value (10%). In S22, when the pressure fluctuation rate exceeds the allowable value (10%) (in the case of YES), the process proceeds to S23, it is determined that there is leakage in the leakage detection layer 100, and the determination result is displayed on the monitor 82. In S22, when the pressure fluctuation rate is equal to or less than the allowable value (10%) (in the case of NO), the flow proceeds to S24, where the leakage detection layer 100 determines that there is no leakage, and the determination result is displayed on the monitor 82. This completes the leakage inspection of the double shell tank 90 by the leakage detection device 10.

  Further, the allowable value of the pressure fluctuation rate is not limited to 10%, but it is needless to say that a value of 10% or less may be set.

  Moreover, although the case where the first and second predetermined times are set to 2 minutes and 45 minutes has been described as an example, any other time can be set.

  In the description of the above embodiment, the underground tank buried in the fuel supply station has been described as an example. However, the present invention is not limited to this, and liquids other than oil (for example, chemicals, water, milk, liquor, etc.) Of course, the present invention can be applied to a tank for storing a liquid or the like or a tank installed on the ground.

It is a block diagram which shows typically one Example of the leakage inspection apparatus of the double shell tank by this invention. It is a front view which expands and shows arrangement | positioning of each apparatus of the leak test | inspection apparatus. 1 is a side view of a leak inspection apparatus 10. FIG. 2 is a front longitudinal sectional view of a double shell tank 90. FIG. It is a longitudinal cross-sectional view of the double shell tank 90 which follows the XX line in FIG. 5 is a flowchart for explaining control processing executed by a control device 80.

Explanation of symbols

DESCRIPTION OF SYMBOLS 10 Leakage inspection apparatus 20 Piping path 30 Pressure reduction pump 40 Pressure detector 42 Pressure gauge 50 On-off valve 52,72 Operation lever 54,68,78 Rotation position detection sensor 60 Air quantity adjustment valve 62 Operation handle 64 Air introduction pipe 70 Restriction member 74 Air introduction pipe 80 Control device 82 Monitor 90 Double shell tank 100 Leakage detection layer 110 Leakage detection pipe 120 Upstream side joint 170 Suction hose 180 Downstream side joint 190 Bracket 192 Mounting plate 200 Mounting bracket 220 Top 260 Leakage detection cylinder 280 Inner shell 290 outer shell

Claims (2)

In the leakage inspection device for a double shell tank that inspects the presence or absence of leakage of the leakage detection layer based on the pressure change of the leakage detection layer formed in the double shell tank,
A pipe having one end connected to the leak detection layer;
A decompression pump connected to the other end of the pipe and sucking air of the leak detection layer;
An on-off valve that is provided in the middle of the pipe and opens or closes between the leak detection layer and the pressure reducing pump;
A pressure detecting means provided in the middle of the pipe between the on-off valve and the leak detection layer, for detecting the pressure of the leak detection layer;
A throttle member that is provided in the middle of the pipe near the pressure reducing pump and restricts the amount of air supplied to the suction port of the pressure reducing pump to a predetermined amount;
An air amount adjusting valve that is provided in the middle of the pipe between the throttle member and the on-off valve and finely adjusts the supply amount of air restricted by the throttle member;
A leakage inspection device for a double-shell tank characterized by comprising:   The at least the pipe, the pressure detecting means, the on-off valve, the air amount adjusting valve, and the throttle member are attached to a mounting plate inclined at a predetermined angle with respect to an installation plate for installation. 1. The double shell tank leakage inspection apparatus according to 1.

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