JP6332983B2 - Gas sampling device - Google Patents

Description

  The present invention relates to a gas sampling device that samples a gas to be detected.

  It is an extremely important issue in terms of gas leakage countermeasures to appropriately detect city gas leaked from underground gas pipes, etc. in underground construction sites or in the vicinity of gas pipe burial facilities. If a flammable gas leak occurs, the frequency of occurrence of disasters such as explosions can be reduced if the leaked part can be easily identified quickly.

  As for the city gas, those having methane as the main component or those having propane as the main component are known, but the city gas having methane as the main component is methane (CH4), which is the main component gas, It has ethane (C2H6), propane (C3H8) and butane (C4H10), which are auxiliary component gases, as combustible gases (volume ratio is usually methane: ethane: propane: butane = 88: 6: 4: 2). Therefore, detection of methane, which is the main component gas of city gas, is one of the criteria for determining the presence or absence of city gas leakage.

  In addition, since the city gas detection apparatus described above, which is a conventional technique in the present invention, is a general technique, no prior art documents such as patent documents are shown.

  When city gas leaks from a gas pipe or the like, methane is present on the ground surface. On the other hand, methane may be naturally generated from the ground, and even in this case, methane is present on the ground surface. Therefore, if the city gas leak standard is only the presence or absence of methane detection, the methane detected using the above-mentioned city gas detection device originated from the city gas leaked from the gas pipes buried in the ground or naturally occurred It is difficult to identify whether it is a thing.

  Accordingly, an object of the present invention is to provide a gas sampling device that can reliably identify city gas.

In order to achieve the above object, the gas sampling device according to the present invention is characterized in that a gas component separation unit that separates a gas to be detected for each gas component and a gas component separation unit that is disposed downstream of the gas component separation unit. A concentration measurement unit for detecting the concentration of the gas, and a gas detection unit that is disposed downstream of the concentration measurement unit and the branching unit and detects the concentration of a desired gas component. A delay unit that causes a gas flow delay in between, and the branching unit includes a path through which the desired gas component flows down the gas detection unit and a path through which the desired gas component does not flow down to the gas detection unit The branching unit switches to a path in which the desired gas component does not flow down to the gas detection unit when the concentration measuring unit detects the concentration of the desired gas component. Control There is a point, which is configured as.

  In the gas sampling device of the present invention, for example, when detecting leakage of city gas, a branching means is provided, and a gas detection unit for detecting the concentration of a desired gas component (ethane) as a different type of gas detection element, Since it has a concentration measurement unit that detects the concentration of the detection gas (methane, ethane, propane, butane, etc.), the desired gas component detection mode and the detected gas measurement mode are performed by switching the branching means. be able to. As a result, different types of gas detection elements can be assigned roles to detect the presence or absence of a gas to be detected existing in the vicinity of a gas pipe buried in the ground or a desired gas component contained in the gas to be detected.

  In particular, in this configuration, the concentration of the desired gas component (ethane) can be reliably detected by the gas detection unit by separating the desired gas component by the gas component separation unit. That is, it is possible to reliably detect and identify city gas by taking into account the presence or absence of ethane detection as a sub-component gas of city gas, for example, as a criterion for determining whether or not there is city gas leakage.

  Further, when the concentration measurement unit detects the concentration of the desired gas component in the gas component detection mode, it is not necessary to detect the concentration of the desired gas component at the gas detection unit, and the gas detection unit needlessly detects the desired gas. You may not want the ingredients to flow down. In the present invention, a delay unit can be provided upstream of the gas detection unit, and a gas flow delay can be caused by the delay unit. Therefore, it is possible to secure a sufficient time for detecting the concentration of the desired gas component in the concentration measuring unit, and to prevent the branching means from switching to the path flowing down to the gas detecting unit while detecting the gas concentration. it can. Therefore, if the concentration measuring unit detects the concentration of the desired gas component, the branching means controls the path not to flow down to the gas detecting unit. Therefore, in this configuration, it is possible to minimize the flow of a desired gas component to the gas detection unit.

It is a figure which shows the outline | summary of the gas sampling apparatus of this invention. It is the schematic which shows a gas flow down path | route ((a) to-be-detected gas measurement mode, (b) gas component detection mode, (c) purge mode). It is the schematic which shows the gas flow path | route in the purge mode of another embodiment. It is the schematic which shows the gas flow path | route in the purge mode of another embodiment. It is the graph which showed the result of the output signal which generate | occur | produced as a result of carrying out gas detection by changing various separation agents with which a gas component separation part is filled. It is the graph which showed the result of having investigated the degree of removal of combustible gas (propane) by the existence of purge mode ((a) 20 ° C, (b) 40 ° C (heating)).

Hereinafter, embodiments of the present invention will be described with reference to the drawings.
The gas sampling device of the present invention samples the gas to be detected and measures the concentration of the gas to be detected. In the present embodiment, an aspect will be described in which ethane is accurately detected and it is determined whether or not city gas is included in the sampled detected gas.

As shown in FIG. 1, the gas sampling device X of the present invention is provided with a gas component separation unit 10 that separates a gas to be detected for each gas component, and downstream of the gas component separation unit 10. A concentration measuring unit 40 for detecting a concentration; and a gas detecting unit 30 disposed downstream of the concentration measuring unit 40 and the branching unit 20 to detect a concentration of a desired gas component. The concentration measuring unit 40 and the branching unit 20 includes a delay unit 60 that causes a gas flow delay.
The branching unit 20 is configured to be switchable between a path through which a desired gas component flows down the gas detection unit 30 and a path through which the desired gas component does not flow down to the gas detection unit 30. When the concentration measuring unit 40 detects the concentration of the desired gas component, the concentration measuring unit 40 is configured to control the switching so that the desired gas component does not flow down to the gas detecting unit 30.

(Gas component separation unit)
The gas component separation unit 10 may be in any form as long as the gas component separation unit 10 is configured to generate a flow delay according to the molecular weight of the combustible gas so as to be separable for each gas component. This embodiment demonstrates the case where the gas component separation part 10 is comprised with the column with which the separation agent for isolate | separating methane and ethane is filled among the gas components of city gas. Activated carbon is used as the separating agent. The separating agent is not limited to activated carbon, and in the case of separating the gas component of city gas, at least calcium oxide (CaO), silicon dioxide (SiO2), activated alumina, PEG-based member, unicarbon member, porous polymer, etc. Any one of them may be contained, and for example, a mixed powder of calcium oxide and silicon oxide may be used. Each separated gas component flows with a time lag.
It is possible to set not only one gas component separation unit 10 but also a plurality of gas component separation units. In the present embodiment, two gas component separation units 10 (first gas component separation unit 10a and second gas component separation unit 10b) are provided. The case where it is provided will be described. Thus, by providing the several gas component separation part 10, even if sampled gas is high concentration, to-be-detected gas can be reliably isolate | separated for every gas component.
The gas component separation unit 10 may perform separation while maintaining an appropriate temperature (for example, 45 ° C.) according to the separating agent.

(Branching means)
In the present embodiment, a case will be described in which five branching means 20 (first branching means 20a to fifth branching means 20e) for branching the flow path 50 are provided. For example, a three-way valve can be used as the branching unit 20, but it is not limited to such a mode.
The first branching means 20a is a gas sampling device X that samples a gas sampled from a gas inlet 1 composed of a nozzle or the like, that is, an atmospheric gas (1a) or a detected gas (1b) sampled from the ground. To switch to the inside.
The second branching unit 20b switches whether to let the gas component separation unit 10 flow down in the input gas.
The third branching unit 20c branches the gas from the first gas component separation unit 10a.
The fourth branching unit 20d and the fifth branching unit 20e branch the gas from the gas component separation unit 10.
The opening / closing of the branching means 20a to 20e may be controlled by a control means (not shown).

(Gas detection part)
The gas detection unit 30 of the present embodiment is disposed downstream of the concentration measurement unit 40 and the fifth branching unit 20e. Moreover, the gas detection part 30 in this embodiment demonstrates the case where the semiconductor type gas detection element which can detect the gas component isolate | separated by the gas component separation part 10 is used.

The semiconductor-type gas detection element is configured to detect changes in heat conduction and electrical conductivity due to gas adsorption on the metal oxide semiconductor surface with electrodes, for example, noble metal wires such as platinum, palladium, platinum-palladium alloy, A gas sensitive part is provided which is formed by applying a metal oxide semiconductor mainly composed of a metal oxide such as indium oxide, tungsten oxide, tin oxide, zinc oxide, etc., drying and sintering.
The semiconductor type gas detection element configured as described above has a higher sensitivity as a gas component having a higher molecular weight among combustible gases.

(Concentration measurement unit)
The concentration measuring unit 40 detects the concentration of the gas to be detected. In the present embodiment, a case where a catalytic combustion type gas detection element is used as the concentration measuring unit 40 will be described.

  The catalytic combustion type gas detection element is provided with a combustion catalyst part as a gas sensitive part in which a noble metal catalyst such as platinum is supported on a sintered metal oxide such as alumina on a noble metal wire such as platinum. By causing the combustible gas to be detected to contact and burn with the noble metal catalyst, the temperature change that occurs during the combustion is detected as a change in the resistance value of the noble metal wire. The combustion heat of combustible gas is proportional to the concentration of combustible gas, and the resistance value of the noble metal wire is proportional to the combustion heat, so the combustible gas is measured by measuring the change in resistance of the noble metal wire due to the combustion of the combustible gas. Concentration can be measured.

  The concentration measurement unit 40 may be disposed either upstream or downstream of the gas component separation unit 10. The case where the concentration measuring unit 40 in the present embodiment is disposed downstream of the gas component separating unit 10 and downstream of the fourth branching unit 20d will be described.

(Delay part)
The delay unit 60 is provided between the concentration measurement unit 40 and the fifth branching unit 20e. Although the delay part 60 of this embodiment has caused the flow delay of combustible gas by forming a flow path in the shape of a coil, it is not limited to such a mode.

(Other parts)
The power source of the gas sampling device X may be a battery, but is not limited to this. By using a battery, the gas sampling device X can be reduced in size. When using a battery, it is preferable to reduce power consumption as much as possible. Therefore, it is possible to reduce the size of the pump or to achieve the same effect as when the heating is performed even if the purge mode is not heated. It is preferable to adopt (see Examples 2 and 3 described later).

  Between the first branching means 20a and the second branching means 20b, there is provided a gas storage part 2 for temporarily storing the sampled gas before putting it into the gas component separation part 10. The gas storage part 2 of this embodiment has a capacity of about 20 to 30 mL. By letting the sampled gas flow down into the gas storage unit 2 for a predetermined time (for example, about 10 seconds), the inside of the gas storage unit 2 is reliably filled with the sampled gas. If the gas inside the gas reservoir 2 is introduced into the gas component separator 10 in this state, the sampled gas can be reliably separated.

  A pump P is connected to the downstream of the gas detection unit 30 via a pipe 50. A flow rate detection unit 3 that detects the gas flow rate is disposed downstream of the pump P. By operating the pump P, the atmospheric gas and the gas to be detected are sucked and discharged from the gas exhaust port 4 through the gas component separation unit 10, the gas detection unit 30, and the like. The arrangement position of the pump P is not limited to the downstream of the gas detection unit 30 and may be upstream of the gas detection unit 30.

  The output signal generated as a result of detection is calculated by the calculation unit (not shown) in the city gas component (ethane) contained in the gas to be detected, and the calculation result is displayed in the display unit (not shown) as necessary. indicate. Further, when it is determined that the calculation result includes city gas having a concentration equal to or higher than a predetermined value, the alarm unit (not shown) can notify the user by means of an alarm or the like.

(About gas flow path)
The gas sampling device X described above includes a plurality of branching means 20 and can change the path through which the gas flows according to the operation mode. In the present embodiment, three modes, i.e., (i) gas detection mode, (ii) gas component detection mode, and (iii) purge mode will be described.

(I) Detected gas measurement mode In the detected gas measurement mode, the concentration of the detected gas contained in the vicinity of the gas pipe buried in the ground is detected. For example, the city gas 13A includes methane, ethane, propane, and butane as combustible gases. In the detected gas measurement mode, the concentration of all these combustible gases is detected. Therefore, in this mode, the branching units 20a to 20e are controlled so that the concentration measuring unit 40 flows down without flowing down the gas component separating unit 10 that separates the gas components (FIG. 2A).

(Ii) Gas component detection mode In the gas component detection mode, the concentration of a desired gas component (such as ethane) contained in the gas to be detected is detected. Therefore, in this mode, first, the gas to be detected flows down and is stored in the gas storage unit 2 (the flow path is the same as the flow in FIG. 2A), and then the gas components are separated by switching the flow path. The branching means 20a to 20e are controlled so that the desired gas component that has flowed through the gas component separation unit 10 and separated from other gases flows down the gas detection unit 30 (FIG. 2B). )). The order of flowing the gas to be detected is the order of the first gas component separation unit 10a and the second gas component separation unit 10b.

(Iii) Purge mode In the purge mode, the branching means 20a to 20e are controlled so that the combustible gas remaining inside the gas component separation unit 10 is pushed out by clean air (atmosphere gas) (FIG. 2C )). That is, in the purge mode, the flammable gas remaining inside the gas component separation unit 10 is removed by flowing air in a direction opposite to the direction of the gas flowing down the gas component separation unit 10 in the detected gas detection mode. To do. When purging both gas component separation units 10a and 10b by flowing air in series to the first gas component separation unit 10a and the second gas component separation unit 10b, the order of flowing the air is the second gas component separation unit. 10b and the first gas component separator 10a. This purge mode is preferably performed after the end of detection of city gas leakage.

When detecting a leak of city gas, for example, the sampled detected gas is allowed to flow down inside the gas reservoir 2 and (i) the detected gas contained in the vicinity of the gas pipe buried in the ground in the detected gas measurement mode. The concentration measuring unit 40 detects the gas concentration. At this time, for example, when methane is included in the gas to be detected, methane derived from city gas leaked from a gas pipe or the like buried in the ground or naturally generated methane is detected as combustible gas. Therefore, after a predetermined time (about 10 seconds) has elapsed, (ii) the gas detection mode is switched to the gas component detection mode and the presence or absence of a desired gas component (ethane) contained in the detected gas is detected by the gas detection unit 30. At this time, if ethane is detected by the gas detection unit 30, it can be reliably determined that the leakage of the city gas has been detected. On the other hand, if (ethane) ethane is not detected in the gas component detection mode, it can be determined that (i) the combustible gas detected in the detected gas measurement mode is not city gas but naturally generated methane.

As described above, in the gas sampling device X of the present invention, when the city gas leakage is detected, the branching means 20 is provided, and different types of gas detection elements, that is, the gas detection unit 30 that detects the concentration of a desired gas component, Further, since the concentration measuring unit 40 for detecting the concentration of the gas to be detected is provided, (i) the gas detection mode and (ii) the gas component detection mode can be performed by switching the branching unit 20. Thereby, it is possible to detect the presence or absence of a gas to be detected existing in the vicinity of a gas pipe buried in the ground or a desired gas component contained in the gas to be detected.
In particular, in this configuration, the gas component separation unit 10 separates the gas component, so that the concentration of the desired gas component (ethane) can be reliably detected. That is, it is possible to reliably detect and identify city gas by taking into account the presence or absence of ethane detection, which is a sub-component gas of city gas, as a criterion for determining the presence or absence of city gas leakage.

  Further, (ii) when the concentration measurement unit 40 detects the concentration of the desired gas component in the gas component detection mode, the gas detection unit 30 does not need to detect the concentration of the desired gas component, and the gas detection unit 30 There is a case where it is not desired to flow down a desired gas component unnecessarily. In the present invention, a delay unit 60 is provided between the concentration measuring unit 40 and the fifth branching unit 20e. That is, the delay unit 60 can be provided upstream of the gas detection unit 30, and the gas flow delay can be caused by the delay unit 60. Therefore, it is possible to secure a sufficient time for the concentration measuring unit 60 to detect the concentration of the desired gas component, and while the concentration of the gas is being detected, the fifth branching unit 20e switches to a path that flows down to the gas detecting unit 30. Can be prevented. Therefore, if the concentration measuring unit 40 detects the concentration of a desired gas component, the fifth branching unit 20e controls the path not to flow down to the gas detecting unit. Therefore, with this configuration, it is possible to minimize the flow of a desired gas component to the gas detection unit 30.

[Another embodiment 1]
A purge mode different from the purge mode in the above-described embodiment will be described (FIGS. 3 and 4). In the present embodiment, two gas component separation units 10a and 10b are provided, the concentration measurement unit 40 is arranged in series with the gas detection unit 30, and the branching units 20a to 20h are controlled.

  In the present embodiment, in the first gas component separation unit 10a and the second gas component separation unit 10b, by flowing air in a direction opposite to the direction of the gas flowing down these gas component separation units 10 in the detected gas detection mode. The purging for removing the combustible gas remaining in the gas component separation unit 10 is performed.

  In FIG. 3A, the order of flowing air is the order of the second gas component separator 10b and the first gas component separator 10a. In FIG. 3B, air flows only in the first gas component separator 10a, in FIG. 4C, air flows only in the second gas component separator 10b, and in FIG. 4D, the first gas component separator 10a. The purging is performed by flowing air simultaneously in 10a and the second gas component separation unit 10b, that is, in parallel.

It is also possible to combine the above purge modes so that purging is performed in two stages. For example, first, only the second gas component separation unit 10b is purged (FIG. 4C), and it is confirmed by the gas detection unit 30 or the concentration measurement unit 40 that there is no residue in the second gas component separation unit 10b. Then, control is performed so that purging is performed in the first gas component separation unit 10a and the second gas component separation unit 10b (FIG. 3A). By being able to purge in this way, the residue can be efficiently removed even when the residual amount of the residue is different in the gas component separation units 10a and 10b.
In addition, since various purges can be performed as described above, optimal residue removal can be performed depending on the usage state of the gas component separation unit 10 and the degree of adhesion of the residue.

[Another embodiment 2]
In the embodiment described above, the case where the concentration measurement unit 40 is disposed downstream of the gas component separation unit 10 has been described. However, the present invention is not limited to this mode, and the concentration measuring unit 40 may be disposed upstream of the gas component separating unit 10, for example, between the first branching unit 20a and the second branching unit 20b (not shown).

[Example 1]
Various separation agents filled in the gas component separation unit were changed, and the state of separation of methane and ethane was investigated.

As the separating agent, activated carbon, Polapack N, and activated alumina were used (manufactured by GL Sciences Inc.). The column conditions were 3.0 cm for activated carbon, 70 cm for Polapack N, and 70 cm for activated alumina (common conditions: column id: 3 mm, packing particle size 80/100 mesh). The experimental conditions were a temperature of 40 ° C., and the flow rates were 100 mL / min for activated carbon, 20 mL / min for Polapack N, and 20 mL / min for activated alumina.
The concentration of the sample gas was 440 ppm of methane and 30 ppm of ethane, and the gas injection amount was 5 mL / min.

  FIG. 5 shows the result of the output signal generated as a result of separation and detection by the gas component separation unit. As a result, it was recognized that the separation of methane and ethane of the activated carbon was excellent even when the amount of the separating agent was small, and that the separation of ethane was particularly excellent.

[Example 2]
In order to function as the gas sampling device X, it is necessary to ensure a predetermined flow rate. For the gas sampling device X of the present invention, it is preferable to use a pump with a reduced size in order to realize a reduction in size. From the viewpoint of power consumption, it is preferable to use a miniaturized pump. However, if a miniaturized pump is used, the capacity of the pump is limited. Therefore, for example, the pressure required to achieve a gas flow rate of 100 mL / min was evaluated.

  Columns with various lengths between 1 and 10 cm are used, the pressure measurement point is downstream of the gas component separation unit 10 and upstream of the fourth branching means 20d, and the pressure is measured using a manometer at the pressure measurement point. did. The results are shown in Table 1.

  Thus, in order to maintain a predetermined flow rate and to reduce the load on the pump to a predetermined value or less (for example, −15 kPa or less), it cannot be achieved if the column length is long. It was recognized that it was decided to be a short range.

Example 3
In the purge mode (reverse purge) described above, the degree of removal of the combustible gas (propane) was compared with that in the case of the forward purge (flowing forward). In this comparison, the temperature of the air to be flowed down was 20 ° C. and 40 ° C. (heating).

  The column conditions were a column length of 3 cm, a column id: 3 mm, a filler particle size of 80/100 mesh, and a flow rate of 580 mL / min for both reverse purge and forward purge. The results are shown in FIG. 6 ((a) 20 ° C., (b) 40 ° C.).

  As a result, at 20 ° C., when the reverse purge is performed, the output of propane decreases to near zero after 250 seconds, whereas when the forward purge is performed, 400 ΔmV after 250 seconds. A degree of output was obtained. In the case of 40 ° C. (heating), when the reverse purge is performed, the time when the propane output is reduced to near zero is about 150 seconds. When the forward purge is performed, the output is about 400 ΔmV after 150 seconds. was gotten.

Therefore, at 20 ° C. and 40 ° C. (heating), when reverse purging was performed, it was recognized that the same tendency was shown although the time when the output of propane decreased to near zero was different. From this, the combustible gas of the gas component separation part 10 can be reliably removed by performing the reverse purge, and this effect was recognized to be the same when the heating is not performed and when the heating is performed. .
From Examples 1 to 3, by using activated carbon as a separating agent, it is possible to perform sufficient gas component separation even if the column length is short (the packing amount is small). It can be seen that sufficient gas components can be separated even when used.
It can also be seen that sufficient residue can be removed without heating by shortening the column length and using activated carbon as the separating agent.
Therefore, it can be seen that sufficient gas component separation and residue removal can be realized even when the battery is used as a power source.

  The present invention can be used in a gas sampling device that samples a gas to be detected.

X gas sampling device 10 gas component separation unit 20 branching means 30 gas detection unit 40 concentration measurement unit 60 delay unit

Claims (1)

A gas component separation unit for separating the gas to be detected for each gas component;
A concentration measuring unit disposed downstream of the gas component separating unit to detect the concentration of the gas to be detected;
A gas detection unit disposed downstream of the concentration measurement unit and the branching unit and detecting a concentration of a desired gas component;
Between the concentration measuring unit and the branching unit, provided with a delay unit that causes a gas flow delay ,
The branching unit is configured to be switchable between a path through which the desired gas component flows down the gas detection unit and a path through which the desired gas component does not flow down to the gas detection unit,
The gas sampling device configured to control the branching unit to switch to a path in which the desired gas component does not flow down to the gas detection unit when the concentration measurement unit detects the concentration of the desired gas component. .

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