WO2015107712A1

WO2015107712A1 - Particle separation device and particle measuring device provided with same

Info

Publication number: WO2015107712A1
Application number: PCT/JP2014/071901
Authority: WO
Inventors: 友規加茂; 昌之西川; 章博矢内
Original assignee: シャープ株式会社
Priority date: 2014-01-17
Filing date: 2014-08-21
Publication date: 2015-07-23
Also published as: JP2015134325A; JP5837107B2; CN204365597U

Abstract

The purpose of the present invention is to prevent coarse particles flowing in the main flow path from reversing flow to a branch flow path side even when the size of a particle separation device is reduced. A main flow path (5b) has a flow path extension part (5d) in at least one part of a flow path from an inlet on a branched part (A) side to a terminal outlet (B). In the flow path extension part (5d), an air flow passing surface area (S) wherein an airflow passes expands gradually going from the branched part (A) side to the terminal outlet (B) side.

Description

Particle separator and particle measuring instrument equipped with the same

The present invention relates to a particle separation device and a particle measuring instrument including the particle separation device.

As a particle measuring instrument that separates fine particles floating in the atmosphere and measures the amount of the separated fine particles, for example, an apparatus disclosed in Patent Document 1 can be cited. In the particle separation method disclosed in Patent Document 1, particles suspended in a fluid are accelerated and separated by inertial force.

FIG. 11 is a schematic explanatory diagram showing the separation method disclosed in Patent Document 1. As shown in FIG. 11, in the separation method of Patent Document 1, in the branch path 13, the main flow 11 and the tributary 12 are arranged in opposite directions, and the particle-containing fluid 15 containing suspended particles is inclined to the tributary 12 side. It is introduced through the nozzle 16 through the passage 16. The main flow 11 and the tributary 12 pass through an intake passage that is sucked by a pump, a measuring instrument, or the like. By being sucked by the main flow 11 and the branch flow 12, the particle-containing fluid 15 is introduced into the system through the inflow path 16.

The particle-containing fluid 15 introduced into the system is accelerated in the nozzle portion 17, and the coarse particles 110 have a large inertial force, so that they are carried on the main flow 11 and removed from the main suction passage 112. Further, since the microparticle 18 has a small inertial force, it is reversed by the branch path 13 and is sent to the branch suction path 114 by being placed on the branch stream 12 in the reverse direction. As a result, the fine particles 18 and the coarse particles 110 contained in the particle-containing fluid 15 are separated. In the separation method of Patent Document 1, the particle classification characteristics are changed by adjusting the flow rate of the main flow 11 and the tributary 12 or adjusting the overall length of the nozzle portion 17 and its interval by moving the movable member such as the sampling pipe 116 up and down. be able to.

Japanese Patent Gazette “Japanese Unexamined Patent Publication No. 2004-89898 (published on March 25, 2004)”

However, the technique of Patent Document 1 as described above has the following problems.

That is, in the main suction path 112 and the branch suction path 114, when a portion where the air current collides with the side wall of the flow path or disturbance of the flow occurs, there arises a problem that a back flow of particles occurs. For example, the coarse particles 110 once flowing into the main suction path 112 will flow again into the support suction path 114 side.

Such a problem becomes particularly prominent when the particle measuring device is downsized and the drive source for sucking the fluid is a fan, which is susceptible to the disturbance of the air flow generated by the fan.

Moreover, in the particle | grain measuring device of patent document 1, the particle-containing fluid 15 containing a floating particle is isolate | separated into the main flow 11 and the tributary 12 in the branch path 13, and the microparticle 18 contained in one flow (branch 12) is measured. ing. In such a particle measuring instrument, when the distance between the branch path 13 and the fan is shortened, turbulence is generated in the space immediately above the fan by the rotation of the fan blades. For this reason, when the distance between the branch path 13 and the fan is shortened, the airflow in the vicinity of the branch path 13 is easily affected by the rotation of the fan. As a result, the coarse particles 110 separated in the branch path 13 flow backward due to the turbulent flow directly above the fan, and flow into an unintended flow path (for example, the branch suction path 114).

The present invention has been made in view of the above-described conventional problems, and an object thereof is to provide a particle separation device capable of preventing the coarse particles flowing in the main flow path from flowing backward to the branch flow path, and the same. It is to provide a particle measuring instrument.

In order to solve the above problems, a particle separation device according to one embodiment of the present invention branches at an introduction flow channel for introducing a gas from the outside and a branching portion at a terminal opposite to the outside in the introduction flow channel. A main flow channel and a branch flow channel, and a fluid drive unit that generates an air flow from the introduction flow channel to the terminal outlet through which the gas in each of the main flow channel and the branch flow channel is discharged to the outside through the branch portion. A particle separation device that separates particles contained in the gas introduced from the introduction flow path into the main flow path and the branch flow path by its inertial force, the main flow path from the branch side inlet At least a part of the flow path leading to the terminal outlet has a first flow path expansion portion, and in the first flow path expansion section, the airflow passage area through which the airflow passes is from the branching portion side to the terminal outlet side. Gradually toward It is characterized in that there much.

According to one aspect of the present invention, it is possible to prevent the coarse particles flowing in the main channel from flowing back to the branch channel.

It is a perspective view which shows the structure of the particle | grain measuring device which concerns on Embodiment 1 of this invention. The schematic structure of the gas flow path formed in the particle | grain measuring device which concerns on Embodiment 1 of this invention is shown, (a) is sectional drawing, (b) is a cross-sectional perspective view. It is sectional drawing which showed typically the state of the particle size in the branch part of the particle-containing fluid introduce | transduced into the system through the introduction flow path. It is an expanded sectional view which shows the structure of the main flow path in the particle | grain measuring device which concerns on Embodiment 1 of this invention. The schematic structure of the particle | grain measuring device which concerns on Embodiment 2 of this invention is shown, (a) is sectional drawing, (b) is a cross-sectional perspective view. It is a figure which shows typically the structure of the main flow path in the particle | grain measuring device which concerns on Embodiment 2 of this invention. The schematic structure of the particle | grain measuring device which concerns on Embodiment 3 of this invention is shown, (a) is sectional drawing, (b) is a cross-sectional perspective view. It is a figure which shows typically the structure of the main flow path in the particle | grain measuring device which concerns on Embodiment 3 of this invention. The schematic structure of the particle | grain measuring device which concerns on Embodiment 4 of this invention is shown, (a) is sectional drawing, (b) is a cross-sectional perspective view. It is a figure which shows typically the structure of the main flow path in the particle | grain measuring device which concerns on Embodiment 4 of this invention. It is a schematic explanatory drawing which shows the separation method disclosed by patent document 1. FIG.

Embodiment 1
Hereinafter, embodiments of the present invention will be described in detail. FIG. 1 is a perspective view showing a configuration of a particle measuring instrument 10A according to the present embodiment. The particle measuring instrument 10A according to the present embodiment sucks a gas (for example, air) from the outside and measures the amount of fine particles having a desired particle diameter contained in the gas.

As shown in FIG. 1, a particle measuring instrument 10A according to the present embodiment includes a sensor 1 (measurement unit), an intake unit 2, a sizing unit 3, and a fan 4 (fluid drive unit). Yes. The particle measuring instrument 10A introduces external air from the intake section 2 by driving the fan 4 as a single fluid drive section. The air introduced into the particle measuring instrument 10 </ b> A passes through a gas flow path formed in the apparatus and is discharged to the outside through the fan 4. The sensor 1 is provided in the middle of the gas flow path formed in the particle measuring instrument 10A, and measures the amount of fine particles contained in the passing air.

2 shows a schematic configuration of a gas flow path formed in the particle measuring instrument 10A, FIG. 2 (a) is a sectional view, and FIG. 2 (b) is a sectional perspective view. As shown in FIGS. 2A and 2B, the gas flow path formed in the particle measuring instrument 10A includes an introduction flow path 5a, a main flow path 5b, and a branch flow path 5c. .

The introduction flow path 5a is formed in the intake part 2 and is a flow path for introducing gas (air) from the outside. The main flow path 5b and the branch flow path 5c are flow paths branched at the branch portion A that is the end of the introduction flow path 5a opposite to the outside.

The particle separation device in the particle measuring instrument 10A includes a fan 4 and a gas flow path including an introduction flow path 5a, a main flow path 5b, and a branch flow path 5c. Then, using the fan 4 as a drive source, the particles contained in the gas introduced from the introduction flow path 5a are separated into the main flow path 5b and the branch flow path 5c in the branch portion A by the inertial force. The principle of separation (sizing) of particles contained in the gas introduced from the introduction channel 5a will be described later.

The sensor 1 as a measuring unit for measuring fine particles is provided in the middle of the branch flow path 5c, and measures the amount of fine particles in the gas passing through the branch flow path 5c. The sensor 1 measures the amount of fine particles in a gas by, for example, irradiating light on fine particles in a passing air stream and detecting light scattered from the fine particles (that is, a light scattering method). In addition, the sensor 1 is not limited to the light scattering method, and may measure the amount of fine particles in the gas by a gravimetric method. Moreover, the measurement part which measures a microparticle is not limited to the sensor 1, For example, it may be provided with the filter which collects a microparticle, and may measure the microparticle collected by the filter.

Only one fan 4 is provided, and generates an air flow from the introduction flow path 5a to the terminal outlets B and D through which the gas in each of the main flow path 5b and the branch flow path 5c is discharged to the outside through the branch portion A. It functions as a fluid drive unit. The fluid drive unit in the present embodiment is not limited to the fan 4 shown in FIG. 2, and the gas in each of the main channel 5 b and the branch channel 5 c is discharged to the outside from the introduction channel 5 a via the branch portion A. What is necessary is just to be able to generate the airflow toward the terminal outlets B and D. For example, the fluid drive unit may be a pump. The fan 4 may be a centrifugal fan or an axial fan.

Here, the direction perpendicular to the gas suction surface 4a of the fan 4 is defined as the Y direction. The Y direction (arrow direction) shown in FIG. 2 is the direction opposite to the gravity direction. And in the cross section perpendicular | vertical to a Y direction, let the direction of the tributary 7c which passes the sensor 1 be an X direction. A direction perpendicular to both the X direction and the Y direction is taken as a Z direction.

As shown in FIG. 2A, when the fan 4 is driven, an air fluid containing suspended particles (hereinafter referred to as a particle-containing fluid) passes through the introduction flow path 5a inclined toward the branch flow path 5c. Then, it is introduced into the particle measuring instrument 10A (air flow 7a). The introduction flow path 5a has a cross-sectional shape perpendicular to the direction of the air flow 7a, and the area that the flow path surrounds toward the branch portion A (also referred to as an area surrounded by the side walls constituting the flow path). The cross-sectional area or the airflow passage area) is reduced. Therefore, the particle-containing fluid introduced into the introduction channel 5a is accelerated along the air flow 7a toward the branch portion A. Therefore, the introduction flow path 5a is also called a fluid acceleration part.

The air flow 7a of the particle-containing fluid is branched into a main flow 7b and a branch flow 7c at the branch portion A. The main flow 7b and the branch flow 7c pass through the main channel 5b and the branch channel 5c sucked by the fan 4, respectively. By using one fan 4 as a fluid drive source and branching into the main flow 7b and the branch flow 7c and sucking, a particle-containing fluid such as the atmosphere can be introduced into the system through the introduction flow path 5a.

In the particle measuring instrument 10A, the particle-containing fluid sucked into the system is, as shown in FIG. 3, when the air flow 7a is branched into the main flow 7b and the branch flow 7c in the branch portion A, the fine particles 8b having a desired particle diameter. And a particle-containing fluid containing coarse particles 8a other than the desired particle size. At this time, the main flow 7b includes a particle-containing fluid containing coarse particles 8a other than the desired particle diameter. On the other hand, the tributary 7c includes a particle-containing fluid including microparticles 8b having a desired particle diameter.

Here, with reference to FIG. 3, the above-described particle sizing principle will be described in detail. FIG. 3 is a cross-sectional view schematically showing the state of sizing at the branching portion A of the particle-containing fluid introduced into the system through the introduction flow path 5a.

As shown in FIG. 3, the particle-containing fluid sucked into the system by the fan 4 accelerates toward the branch portion A of the introduction flow path 5a. Whether or not the particles contained in the particle-containing fluid move along the main flow 7b along the surrounding air flow 7a depends on the density, diameter, and velocity of the particles according to the Stokes equation. As long as the particles have the same component, the particles contained in the particle-containing fluid deviate from the motion of the particle-containing fluid at a lower speed as the particle size increases. For this reason, since the coarse particles 8a having a relatively large particle size have a large inertial force, the coarse particles 8a are put on the main flow 7b and are discharged from the main flow path 5b to the outside and hardly enter the branch flow 7c. On the other hand, the microparticle 8b having a relatively small particle diameter has a small inertial force. Therefore, the movement of the microparticle 8b is governed by the viscosity of the particle-containing fluid. For this reason, the microparticles 8b are sent to the main flow path 5b and the branch flow path 5c by being put on the main flow 7b and the branch flow 7c in the opposite direction to the main flow 7b. Thus, only particles having a specific particle size or less can be guided to the tributary 7c depending on the velocity of the particles in the branch portion A.

As described above, in the particle measuring instrument 10A according to the present embodiment, the coarse particles 8a included in the particle-containing fluid sucked by the fan 4 are mainstream in the branch portion A due to the above-described flow path configuration and the arrangement of the fans 4. It does not get mixed into the branch flow path 5c extending in the direction opposite to the path 5b. On the other hand, the microparticle 8b exists in both the main channel 5b and the branch channel 5c.

As shown in FIG. 2 (a), the particle-containing fluid containing the microparticles 8b sent to the branch channel 5c rides on the branch flow 7c and passes through the sensor 1. By passing through the sensor 1 in this way, the amount of fine particles 8b contained in the particle-containing fluid is measured.

The particle-containing fluid containing the fine particles 8b flowing out from the sensor 1 flows out toward the terminal outlet D of the branch channel 5c. Here, the introduction flow path 5a, the main flow path 5b, and the fan 4 are arranged in substantially the same direction. By setting it as such a structure, the coarse particle 8a becomes easy to be discharged | emitted outside via the terminal exit D after branching to the main flow path 5b, without flowing backward to the branch flow path 5c. Therefore, the coarse particles 8a that are not the measurement target can be efficiently removed.

As described above, in the air flow of the particle-containing fluid shown in FIG. 2A, the main flow 7b of the particle-containing fluid including the coarse particles 8a is directed from the branch portion A toward the fan 4 disposed on the lower side. It passes through the main flow path 5b extending so as to be the shortest distance and is discharged from the space formed immediately above the gas suction surface 4a. On the other hand, the branch flow 7c of the particle-containing fluid containing the fine particles 8b is discharged from the terminal outlet D from the branch portion A through the branch channel 5c extending in the opposite direction to the main channel 5b and bypassing the sensor 1. . Since the coarse particles 8a and the fine particles 8b are thus sized at the branch portion A, the particle-containing fluid containing the coarse particles 8a among the particle-containing fluid sucked from the outside passes through the sensor 1. Without being discharged outside. On the other hand, the particle-containing fluid containing the fine particles 8b is discharged to the outside after the amount is measured by the sensor 1.

As described above, in the particle measuring instrument 10A according to the present embodiment, the air flow 7a of the particle-containing fluid sucked from the outside is branched into the main flow 7b and the branch flow 7c at the branching portion A, and when this branching, the coarse particles 8a and The fine particles 8b are sized. Further, the main flow 7b and the branch flow 7c are discharged to the outside through the terminal outlets B and D, respectively. Further, the branching of the main flow 7b and the branch flow 7c is realized by the fan 4 which is a single fluid drive source. Then, by providing the sensor 1 in the middle of the branch flow path 5c, the amount of fine particles 8b in the particle-containing fluid of the branch flow 7c is measured.

Therefore, it is possible to realize a particle measuring device that is small and inexpensive as compared with the technique of Patent Document 1 that uses two driving sources of a pump and a measuring device.

Here, the flow velocity of the main flow 7b of the main flow passage 5b and the flow velocity of the branch flow 7c of the branch flow passage 5c need to be adjusted very severely. For example, when the flow velocity of the main flow 7b is larger than the optimum value and the flow velocity of the branch flow 7c is smaller than the optimum value, not only the coarse particles 8a but most of the fine particles 8b flow to the main flow path 5b side. As a result, the amount of the fine particles 8b flowing toward the branch flow path 5c becomes small, and therefore, the coarse particles 8a and the fine particles 8b cannot be properly separated. On the contrary, when the flow velocity of the main flow 7b is smaller than the optimum value and the flow velocity of the branch flow 7c is larger than the optimum value, a part of the coarse particles 8a flows to the branch flow channel 5c side, and preferably, the coarse particles 8a The fine particles 8b cannot be separated. The flow velocity of the main flow 7b and the flow velocity of the branch flow 7c are determined by the flow passage resistance of the main flow passage 5b and the branch flow passage 5c and the exhaust speed of the fan 4, respectively. Among these, the channel resistance is a value determined by the shapes of the main channel 5b and the branch channel 5c, and cannot be adjusted unless the channel shape is changed. On the other hand, the exhaust speed is a value that can be adjusted only by adjusting the output of the fan 4 and is relatively easy to adjust. Therefore, as in the technique of Patent Document 1, in the configuration in which the main suction path 112 and the support suction path 114 are exhausted by individual fans, the adjustment of the flow velocity of the fluid in each of the main suction path 112 and the support suction path 114 is as follows. This can be done easily (see FIG. 11). On the other hand, in the particle measuring instrument 10A, since both the main flow path 5b and the branch flow path 5c are exhausted by the single fan 4, the exhaust velocity in each flow path (that is, the main flow 7b and the branch flow 7c is determined by the output of the fan 4). However, the problem remains that the flow rate cannot be adjusted freely.

In order to make full use of the exhaust speed of the fan 4 with respect to the flow rates of the main flow 7b and the branch flow 7c, it is desirable to make the area of the gas suction surface 4a in the fan 4 as wide as possible and use it for exhaust. . In order to take such a form, in the particle measuring instrument 10A, the end outlets B and D of the main channel 5b and the branch channel 5c are connected to the gas suction surface 4a of the fan 4. In such a configuration, when the gas suction surface 4a of the fan 4 is blocked, the resistance increases and the performance as a drive source of the fan 4 cannot be sufficiently exhibited. Therefore, in order to exhibit the performance of the fan 4 sufficiently, in the particle measuring instrument 10A, a space having the same area as the gas suction surface 4a is provided in a portion directly above the suction side of the fan 4. That is, a space is secured in the portion directly above the gas suction surface 4a. The main flow 7b and the branch flow 7c are discharged to the outside through a space formed immediately above the gas suction surface 4a.

Here, as shown in FIG. 2, in the particle measuring instrument 10A, the flow path length of the branch flow path 5c is longer than the flow path length of the main flow path 5b. For this reason, the flow path resistance is larger in the branch stream 7c than in the main stream 7b. Therefore, in the configuration in which the main flow 7b and the branch flow 7c merge, the main flow 7b has a higher flow velocity than the branch flow 7c, and thus turbulence occurs. As a result, in the space formed immediately above the gas suction surface 4a, a part of the coarse particles 8a included in the main flow 7b may flow backward to the branch flow path 5c.

Therefore, in the particle measuring instrument 10A according to the present embodiment, as shown in FIG. 2, a partition plate 6 is provided to partition the main flow 7b discharged from the main flow path 5b and the branch flow 7c discharged from the branch flow path 5c. ing. The partition plate 6 is provided at the center of the space formed immediately above the gas suction surface 4a. That is, the area of the gas suction surface 4a partitioned by the partition plate 6 is the same on the main channel 5b side and the branch channel 5c side. The partition plate 6 prevents the main flow 7b and the branch flow 7c from joining. As a result, the backflow of particles can be prevented between the main channel 5b and the branch channel 5c.

The position of the partition plate 6 is not limited to the center of the space formed immediately above the gas suction surface 4a. On the gas suction surface 4a partitioned by the partition plate 6, the area through which the main flow 7b passes and the branch flow 7c are The passing area may be different. In this way, by arranging the partition plate 6 at a position shifted from the center in the space formed immediately above the gas suction surface 4a, the particle measuring instrument 10A in which the ratio of the flow rate of the main flow 7b and the flow rate of the branch flow 7c is changed. Can be realized.

Further, the angle and thickness of the partition plate 6 may be different between the main channel 5b side and the branch channel 5c side. Moreover, in the structure shown by FIG. 2, the partition plate 6 is flat plate shape. However, the shape of the partition plate 6 is not limited to a flat plate shape as long as it prevents the merging of the main flow 7b and the branch flow 7c, and may be a shape having a curved surface. Furthermore, the partition plate 6 may have a structure that surrounds the outlet portion of the branch stream 7c.

Further, in the particle measuring instrument 10A according to the present embodiment, the main flow path 5b through which the main flow 7b of the particle-containing fluid including the coarse particles 8a passes is connected so as to be the shortest distance toward the fan 4 disposed on the lower side. ing. On the other hand, the branch flow path 5c through which the branch flow 7c of the particle-containing fluid containing the fine particles 8b passes extends in the opposite direction to the main flow path 5b from the branch portion A and is detoured via the sensor 1 and connected to the fan 4.

Thus, in the particle measuring instrument 10A according to the present embodiment, the main flow path 5b directly discharges the main flow 7b to the outside by the fan 4, so that the flow path length is relatively short. On the other hand, the branch channel 5c is provided with a sensor 1 in the middle, and the branch channel 7c is configured to pass through the sensor 1, so that the channel length is relatively long. Since the particle measuring instrument 10A includes the sensor 1 in the middle of the branch channel 5c and uses only one fan 4 as a fluid drive source, the channel length of the branch channel 5c is longer than the channel length of the main channel 5b. It becomes the composition. As described above, the flow path length of the branch flow path 5c is longer than the flow path length of the main flow path 5b, so that the flow path resistance of the branch flow 7c in the branch flow path 5c increases as a whole, and the flow of the branch flow 7c in the branch portion A increases. The flow rate can be lowered.

Further, in the particle measuring instrument 10A according to the present embodiment, the position of the inlet of the branch flow path 5c at the branch portion A is arranged below the position of the sensor 1 in the gravity direction. In this case, the direction of the branch flow 7c branched at the branching portion A is the direction opposite to the direction of gravity.

Sensor 1 has microparticles 8b such as PM2.5 as a measurement target. The air flow 7a of the particle-containing fluid flowing from the introduction flow path 5a includes coarse particles 8a such as dust in addition to the fine particles 8b. The coarse particles 8a move straight by inertia and are discharged to the outside. Here, since the coarse particles 8a such as dust are greatly affected by the natural sedimentation due to their own weight, the position of the inlet of the branch channel 5c in the branch portion A is arranged below the position of the sensor 1 in the gravity direction. Thus, it is possible to reliably prevent the coarse particles 8a from being mixed into the sensor 1 with certainty.

Here, in the particle measuring instrument 10A of the present embodiment, the main flow path 5b is a part of the flow path extending from the inlet on the branching section A side to the terminal outlet B, and the flow path expanding section 5d (the first flow path 5d shown in FIG. 4). A flow path expansion section). FIG. 4 is an enlarged cross-sectional view showing the configuration of the main flow path 5b of the particle measuring instrument 10A.

As shown in Fig. 4, in the flow path expanding portion 5d, the airflow passage area S through which the airflow passes gradually increases from the branching portion A side toward the terminal outlet B side. It can be said that this airflow passage area S is an area (flow channel cross-sectional area) surrounded by the side walls constituting the flow channel. Moreover, it can be said that the shape of the flow path expansion part 5d is what is called a taper shape.

The two opposite side walls that constitute the flow path expanding portion 5d are configured to become wider from the branching portion A side toward the terminal outlet B side. In addition, of the two side walls facing each other that constitute the flow path expanding portion 5d, one side wall is provided with a surface parallel to the direction of the main flow 7b, and the other side wall is in the direction of the main flow 7b. An inclined surface that is continuously inclined is provided.

Since the air flow passage area S gradually increases from the branching part A side toward the terminal outlet B side, the flow path expanding part 5d has a shape in which the flow path is narrowed at the end part on the branching part A side. It has become. Therefore, the flow velocity of the main flow 7b passing through the flow path expanding portion 5d is highest at the end portion on the branching portion A side, and becomes smaller toward the terminal outlet B.

Therefore, even if the coarse particles included in the turbulent flow due to the rotation of the blades in the fan 4 or the coarse particles colliding with the wall surface of the main flow path 5b flow back toward the branch portion A, the main flow at the end portion on the branch portion A side. Since the flow rate of 7b is the largest, coarse particles are not mixed into the branch channel 5c from the branch part A. Therefore, even when the distance between the branch part A and the fan 4 is reduced and the size of the particle measuring device 10A is reduced, the coarse particles flowing in the main flow path 5b are prevented from flowing back to the branch flow path 5c side. Can do.

Further, as shown in FIG. 4, the main flow path 5b has the smallest airflow passage area Sa at the inlet on the branching part A side in the flow path from the inlet on the branching part A side to the terminal outlet B. . Therefore, the flow velocity of the main flow 7b passing through the main flow channel 5b is the largest at the inlet on the branching portion A side. Therefore, it is possible to reliably prevent the coarse particles flowing through the main flow path 5b from flowing backward to the branch flow path 5c.

Further, the main flow path 5b has the largest airflow passage area Sb at the terminal outlet B in the flow path from the inlet on the branching section A side to the terminal outlet B. Thus, since the airflow passage area Sb at the terminal outlet B is the largest, the intake area of the fan 4 can be secured sufficiently wide. For this reason, the intake efficiency of the main flow 7b by the fan 4 can be improved.

Further, in the particle measuring instrument 10A according to the present embodiment, the branch flow path 5c has a second flow path expanding portion in at least a part of the flow path from the gas outlet C to the terminal outlet D in the sensor 1. In the second flow path expanding portion, the airflow passage area through which the airflow passes gradually increases from the gas outlet C side to the terminal outlet D side in the sensor 1.

Specifically, as shown in FIG. 2, the branch flow path 5 c has an inclined wall surface 5 e in the flow path from the gas outlet C to the terminal outlet D in the sensor 1. The inclined wall surface 5e is inclined such that the distance in the Z direction between the inclined wall surface 5e and the opposite wall surface gradually increases from the outlet C side toward the terminal outlet D side. On the other hand, the distance between the two wall surfaces standing on the inclined wall surface 5e is constant in the flow path from the outlet C side to the terminal outlet D side. For this reason, in the branch flow path 5c, the flow path including the inclined wall surface 5e is the second flow path expansion portion because the airflow passage area increases from the outlet C side toward the terminal outlet D side.

Here, the particle measuring instrument 10A is configured to generate two fluids such as a main flow 7b and a tributary 7c using one fan 4 as a fluid drive unit. Therefore, the coarse particles discharged from the terminal outlet B of the main flow path 5b may flow backward from the terminal outlet D of the branch flow path 5c to the sensor 1 due to the rotation of the blades of the fan 4.

According to the particle measuring instrument 10A according to the present embodiment, since at least a part of the flow path from the gas outlet C to the terminal outlet D in the sensor 1 has the above-described second flow path extension, The flow velocity of the tributary 7c passing through the flow path expanding portion is largest at the end portion on the outlet C side, and becomes smaller toward the terminal outlet D. Therefore, even if the coarse particles discharged from the terminal outlet B of the main flow path 5b flow backward from the terminal outlet D of the branch flow path 5c to the sensor 1 due to the rotation of the fan 4, the main flow at the end on the outlet C side. Since the flow rate of 7b is the largest, coarse particles are not mixed into the sensor 1.

Further, the branch flow path 5c has the smallest airflow passage area at the outlet C in the flow path from the gas outlet C to the terminal outlet D in the sensor 1. Therefore, the flow velocity of the branch flow 7c passing through the branch flow channel 5c is highest at the gas outlet C in the sensor 1. Therefore, the backflow of coarse particles to the sensor 1 can be reliably prevented.

Further, the branch channel 5c has the largest airflow passage area at the terminal outlet D among the channels from the inlet on the branching section A side to the terminal outlet D. Thus, since the airflow passage area at the terminal outlet D is the largest, the intake area of the fan 4 can be secured sufficiently wide. For this reason, the intake efficiency of the branch 7c by the fan 4 can be improved.

[Embodiment 2]
The following will describe another embodiment of the present invention with reference to FIGS. FIG. 5 shows a schematic configuration of the particle measuring instrument 10B according to the present embodiment. FIG. 5 (a) is a sectional view, and FIG. 5 (b) is a sectional perspective view. FIG. 6 is a diagram schematically showing the configuration of the main channel in the particle measuring instrument 10B according to the present embodiment. For convenience of explanation, members having the same functions as those described in the embodiment are given the same reference numerals, and descriptions thereof are omitted. In FIG. 5, the fan 4 is omitted for the sake of simplicity.

In the particle measuring instrument 10A according to the first embodiment, the main flow path 5b includes a flow path expansion section 5d (first flow path expansion section) in a part of the flow path from the inlet on the branching section A side to the terminal outlet B. Had.

However, as shown in FIGS. 5 and 6, in the particle measuring instrument 10 </ b> B according to the present embodiment, the main flow path 5 b has a flow path extending portion in the entire flow path from the inlet on the branching section A side to the terminal outlet B. The point having 5d is different from the particle measuring instrument 10A according to the first embodiment. That is, in the main flow path 5b of the particle measuring instrument 10B, the airflow passage area through which the airflow passes gradually increases from the inlet on the branching portion A side toward the terminal outlet B.

According to the particle measuring instrument 10B according to the present embodiment, the airflow passage area Sa in the main channel 5b has the smallest airflow passage area Sa at the entrance on the branching portion A side. And it gradually increases from the inlet on the branching part A side toward the terminal outlet B, and the airflow passage area Sb at the terminal outlet B is maximized. Therefore, even when the distance between the branch portion A and the fan 4 is reduced, it is possible to prevent the coarse particles flowing in the main flow path 5b from flowing back to the branch flow path 5c.

[Embodiment 3]
The following will describe still another embodiment of the present invention with reference to FIGS. FIG. 7 shows a schematic configuration of a particle measuring instrument 10C according to the present embodiment. FIG. 7A is a cross-sectional view, and FIG. 7B is a cross-sectional perspective view. FIG. 8 is a diagram schematically showing the configuration of the main flow path in the particle measuring instrument 10C according to the present embodiment. For convenience of explanation, members having the same functions as those described in the embodiment are given the same reference numerals, and descriptions thereof are omitted. In FIG. 7, the fan 4 is omitted for the sake of brevity.

As shown in FIGS. 7 and 8, in the particle measuring instrument 10C according to the present embodiment, the airflow passage area Sa ′ at the end portion on the branching portion A side in the flow path expanding portion 5d is the inlet at the branching portion A side. The point which is the same as airflow passage area Sa differs from the said Embodiment 1 and 2.

According to the particle measuring instrument 10C according to the present embodiment, the air flow passage area in the main flow path 5b is the same in the flow path from the inlet on the branching section A side to the branching section A side end in the flow path expanding section 5d. Airflow passage area Sa · Sa ′. And it gradually increases from the inlet on the branching part A side toward the terminal outlet B, and the airflow passage area Sb at the terminal outlet B is maximized. Therefore, even when the distance between the branch portion A and the fan 4 is reduced, it is possible to prevent the coarse particles flowing in the main flow path 5b from flowing back to the branch flow path 5c.

[Embodiment 4]
The following will describe still another embodiment of the present invention with reference to FIGS. FIG. 9 shows a schematic configuration of a particle measuring instrument 10D according to the present embodiment. FIG. 9A is a sectional view, and FIG. 9B is a sectional perspective view. FIG. 10 is a diagram schematically showing the configuration of the main channel in the particle measuring instrument 10D according to the present embodiment. For convenience of explanation, members having the same functions as those described in the embodiment are given the same reference numerals, and descriptions thereof are omitted. In FIG. 9, the fan 4 is omitted for the sake of brevity.

In the particle measuring instrument 10A according to the first embodiment, the two opposing side walls constituting the flow path expanding portion 5d are configured to become wider from the branching portion A side toward the terminal outlet B side. In addition, of the two side walls facing each other that constitute the flow path expanding portion 5d, one side wall is provided with a surface parallel to the direction of the main flow 7b, and the other side wall is in the direction of the main flow 7b. An inclined surface that is continuously inclined is provided.

However, in the particle measuring instrument 10D according to the present embodiment, one of the two opposing side walls constituting the flow path expanding portion 5d is provided with a surface parallel to the direction of the main flow 7b. The other side wall is different from the first embodiment in that an inclined surface that is discontinuously inclined with respect to the direction of the main flow 7b is provided.

In the above inclined surface, “discontinuously inclined” means that the surfaces constituting the inclined surface are not flush with each other. Examples of the “discontinuously inclined surfaces” include stepped inclined surfaces shown in FIGS. 9 and 10.

[Summary]
The particle separation device according to the first aspect of the present invention includes an introduction channel 5a for introducing a gas from the outside, a main channel 5b and a tributary branching at a branch part A at the end opposite to the outside of the introduction channel 5a. Fluid drive for generating an air flow from the channel 5c and the introduction channel 5a to the terminal outlets B and D through which the gas in each of the main channel 5b and the branch channel 5c is discharged to the outside through the branch portion A Part (fan 4), and a particle separation device that separates particles contained in the gas (airflow 7a) introduced from the introduction flow path 5a into the main flow path 5b and the branch flow path 5c by its inertial force. The main flow path 5b includes a first flow path expansion section (flow path expansion section 5d) in at least a part of the flow path from the inlet on the branching section A side to the terminal outlet B. 1st channel expansion part (channel expansion part In d), the air flow passage area S airflow passes is in progressively increasing toward the branch portion A side to the distal outlet B side. Here, the category of “gradual increase” includes configurations that are continuously increasing and configurations that are discontinuously increasing. As a configuration that increases discontinuously, for example, the distance between one wall surface constituting the first flow channel expansion portion (flow channel expansion portion 5d) and the opposite wall surface is from the branching portion A side to the end outlet B side. A configuration that is inclined stepwise so that it becomes wider as it goes to is mentioned.

According to said structure, since the 1st flow path expansion part (flow path expansion part 5d) is gradually increasing as the airflow passage area S goes to the terminal exit B side from the branch part A side, it branches The channel is narrowed at the end on the part A side. Therefore, the flow velocity of the airflow (main flow 7b) passing through the flow path expanding portion 5d is the largest at the end portion on the branching portion A side and becomes smaller toward the terminal outlet B.

Therefore, even if the coarse particles included in the turbulent flow due to the rotation of the blades in the fluid drive unit (fan 4) or the coarse particles colliding with the wall surface of the main flow path 5b flow back toward the branch portion A, Since the flow velocity of the main flow 7b at the end is the highest, coarse particles are not mixed into the branch channel 5c from the branch portion A. Therefore, according to said structure, even if it is a case where the distance of the branch part A and the fan 4 is made small, the particle separation apparatus which can prevent the coarse particle which flows through the main flow path 5b from flowing backward to the branch flow path 5c side is provided. Can be provided.

The particle separation device according to aspect 2 of the present invention is the particle separation apparatus according to aspect 1, in which the main flow path 5b passes through the air flow at the inlet on the branching part A side in the flow path from the inlet on the branching part A side to the terminal outlet B. It is preferable that the area Sa is the smallest.

According to the above configuration, the flow velocity of the air flow (main flow 7b) passing through the main flow path 5b is the largest at the entrance on the branching section A side. Therefore, according to said structure, it can prevent reliably that the coarse particle which flows through the main flow path 5b flows backward to the branch flow path 5c side.

The particle separation apparatus according to Aspect 3 of the present invention is the particle separation apparatus according to Aspect 1 or 2, wherein the main flow path 5b is an airflow passage area at the terminal outlet B in the flow path from the inlet on the branching section A side to the terminal outlet B. It is preferable that Sb be the largest.

According to the above configuration, since the airflow passage area Sb at the end outlet B is the largest, the intake area of the fluid drive unit (fan 4) can be secured sufficiently wide. For this reason, according to said structure, the intake efficiency of the airflow (main flow 7b) by a fluid drive part (fan 4) can be improved.

The particle separation device according to aspect 4 of the present invention is the particle separation apparatus according to aspects 1 to 3, wherein the first flow path expansion section (flow path expansion section 5d) is connected from the inlet on the branching section A side to the end outlet of the main flow path 5b. You may be provided in the whole flow path to B.

Thereby, even when the distance between the branch part A and the fluid drive part (fan 4) is reduced, it is possible to prevent the coarse particles flowing in the main flow path 5b from flowing back to the branch flow path 5c.

A particle measuring instrument 10A according to Aspect 5 of the present invention is provided with a particle separation apparatus according to any one of Aspects 1 to 4 and a measuring unit (sensor 1) that is provided in the middle of the branch flow path 5c and measures fine particles in a gas. And.

According to said structure, even if it is a case where the distance of the branch part A and the fan 4 is made small, the particle measuring device 10A which can prevent the coarse particle which flows through the main flow path 5b from flowing backward to the branch flow path 5c side is provided. can do.

A particle measuring instrument 10A according to Aspect 6 of the present invention includes an introduction channel 5a for introducing a gas from the outside, a main channel 5b branched at a branch part A at the end opposite to the outside in the introduction channel 5a, and Fluid that generates airflow from the branch channel 5c and the introduction channel 5a to the terminal outlets B and D through which the gas in each of the main channel 5b and the branch channel 5c is discharged to the outside through the branch portion A A driving unit (fan 4) and a measuring unit (sensor 1) that is provided in the middle of the branch channel 5c and measures fine particles in the gas are provided, and the branch channel 5c is provided in the measuring unit (sensor 1). At least a part of the flow path from the gas outlet C to the terminal outlet D has a second flow path expansion portion (a flow path including the inclined wall surface 5e), and the second flow path expansion portion (the inclined wall surface 5e). Air flow) That the air flow passage area is in progressively increasing toward the distal outlet D side from the outlet C side of the gas in the measuring unit (sensor 1).

Here, the particle measuring instrument 10A is configured to generate two air streams such as a main flow 7b and a tributary 7c by using one fluid driving unit (fan 4) as a driving source. Therefore, the coarse particles discharged from the terminal outlet B of the main flow path 5b may flow backward from the terminal outlet D of the branch flow path 5c to the measuring section (sensor 1) due to the rotation of the blades of the fluid drive section (fan 4). is there.

According to the above configuration, since at least a part of the flow path from the gas outlet C to the terminal outlet D in the measurement section (sensor 1) has the second flow path expansion section, the second flow path expansion is performed. The flow velocity of the airflow passing through the section (branch stream 7 c) is greatest at the end portion on the outlet C side and decreases toward the terminal outlet D. Therefore, even if the coarse particles discharged from the terminal outlet B of the main flow path 5b flow backward from the terminal outlet D of the branch flow path 5c to the sensor 1, the flow velocity of the main flow 7b at the end on the outlet C side is the largest. Coarse particles are not mixed into the sensor 1.

The particle measuring instrument 10A according to aspect 7 of the present invention is the particle measuring apparatus 10A according to aspect 6, in which the branch flow path 5c is measured in the flow path from the gas outlet C to the terminal outlet D in the measurement unit (sensor 1). It is preferable that the airflow passage area of the gas outlet C in the part (sensor 1) is the smallest.

According to the above configuration, the flow velocity of the airflow (branch flow 7c) passing through the branch flow path 5c is greatest at the gas outlet C in the measurement unit (sensor 1). Therefore, the backflow of coarse particles to the measurement unit (sensor 1) can be reliably prevented.

The particle measuring instrument 10A according to Aspect 8 of the present invention is the particle detector 10A according to Aspect 6 or 7, wherein the branch flow path 5c is an air flow at the end outlet D in the flow path from the inlet on the branching section A side to the end outlet D. It is preferable that the passage area is the largest.

According to the above configuration, since the airflow passage area at the end outlet D of the branch flow path 5c is the largest, it is possible to ensure a sufficiently large intake area of the fluid drive unit (fan 4). For this reason, the intake efficiency of the airflow (branch 7c) by the fluid drive unit (fan 4) can be improved.

In the particle separation device according to aspect 9 of the present invention, in the above aspects 1 to 4, the airflow passage area Sa ′ at the end portion on the branching portion A side in the flow path expanding portion 5d is airflow passage at the inlet on the branching portion A side. The configuration may be the same as the area Sa.

In the particle separator according to the tenth aspect of the present invention, in the first to fourth and ninth aspects, it is preferable that one fluid driving unit (fan 4) is provided. Thereby, the particle separator can be further reduced in size.

The present invention is not limited to the above-described embodiments, and various modifications are possible within the scope shown in the claims, and embodiments obtained by appropriately combining technical means disclosed in different embodiments. Is also included in the technical scope of the present invention. Furthermore, a new technical feature can be formed by combining the technical means disclosed in each embodiment.

The present invention can be used for a fine particle measuring apparatus and a fine particle sensor for separating fine particles floating in the atmosphere and measuring the amount of the separated fine particles.

1 Sensor (measurement unit)
2 Intake section 3 Sizing section 4 Fan (fluid drive section)

5a Introduction channel

5b Main channel 5c Branch channel 5d Channel expansion part (first channel expansion part)
5e Inclined wall surface (part of the wall surface constituting the second flow path extension)
6, Partition plate 7a Air flow 7b Main flow 7c Branch flow

8a Coarse particle

8b Fine particle

10A, 10B, 10C, 10D Fine particle measuring device A Branch part B Terminal outlet C Outlet D Terminal outlet S, Sa, Sb Air flow passage area

Claims

An introduction channel for introducing gas from the outside;
A main channel and a branch channel branched at a branching portion on the opposite end to the outside in the introduction channel;
A fluid drive unit that generates an air flow from the introduction channel to the terminal outlet through which the gas in each of the main channel and the branch channel is discharged to the outside through the branch portion, and from the introduction channel A particle separation device for separating particles contained in a gas to be introduced into the main channel and the branch channel by inertial force thereof,
The main channel has a first channel expansion part in at least a part of the channel from the inlet on the branching part side to the terminal outlet, and an airflow through which an airflow passes in the first channel expansion part. The particle separation device, wherein the passage area gradually increases from the branching portion side toward the terminal outlet side.
The particle separation device according to claim 1, wherein the main channel has the smallest airflow passage area at the branch side inlet among the channels from the branch side inlet to the terminal outlet.
The particle separation apparatus according to claim 1 or 2, wherein the main channel has the largest airflow passage area at the end outlet among the channels from the branch side inlet to the terminal outlet.
The first flow path extension section is provided in the entire flow path from the branch side inlet to the terminal outlet of the main flow path. Particle separator.
The particle separator according to any one of claims 1 to 4,
A particle measuring instrument, comprising: a measuring unit that is provided in the middle of the branch channel and measures fine particles in a gas.
An introduction channel for introducing gas from the outside;
A main channel and a branch channel branched at a branching portion on the opposite end to the outside in the introduction channel;
A fluid drive unit that generates an air flow from the introduction channel to the terminal outlet through which the gas in each of the main channel and the branch channel is discharged to the outside through the branch unit;
Provided in the middle of the branch flow path, and a measuring unit for measuring fine particles in the gas,
The branch channel has a second channel expansion part in at least a part of the channel from the gas outlet to the terminal outlet in the measurement unit, and the airflow passes through the second channel expansion unit. The air flow passage area gradually increases from the gas outlet side toward the terminal outlet side in the measurement unit.
The particle measurement according to claim 6, wherein the branch channel has the smallest airflow passage area at the gas outlet in the measurement unit among the channels from the gas outlet to the terminal outlet in the measurement unit. vessel.