KR102223149B1 - Apparatus for diluting exhaust gas - Google Patents

Abstract

An embodiment of the present invention provides an exhaust gas dilution device capable of increasing measurement accuracy. Here, the exhaust gas dilution device includes a head part, an ejector part, a nozzle part, a dilution part, and a measuring part. Exhaust gas is introduced and moved from the outside in the head. The ejector unit is coupled to the front end of the head unit, and guides the primary dilution air to be introduced and moved from the outside. The nozzle unit induces the exhaust gas flowing into the head to be ejected to the front of the ejector unit by increasing the flow velocity of the primary dilution air moving from the ejector unit. The dilution part is coupled to the front end of the ejector part, and the discharged first dilution gas is mixed with the secondary dilution air introduced from the outside after being generated by mixing the exhaust gas and the primary dilution air in the ejector part to generate the secondary dilution gas. do. The measuring part is coupled to the front end of the dilution part, and the target particle is measured in the secondary dilution gas.

Description

Exhaust gas dilution device{APPARATUS FOR DILUTING EXHAUST GAS}

The present invention relates to an exhaust gas dilution device, and more particularly, to an exhaust gas dilution device capable of increasing measurement accuracy.

When the concentration of the sampled particles exceeds the measurement range of the particle counter, the particle dilution device is installed at the front end of the particle counter, dilutes the sampled particles at a certain dilution ratio, and transfers them to the particle counter to measure even high-concentration sampling particles. It is a device that allows you to do it.

In general, a particle dilution device includes a mixing chamber in which a gas to be measured is introduced and firstly mixed with dilution air to generate a first dilution gas, and an ejector that secondly mixes the dilution air with the first dilution gas and delivers it to a particle counter. Includes.

However, in such a conventional particle dilution apparatus, a problem may occur in measurement accuracy because many particles are lost due to adhesion of the particles to be measured to the inner surface of the mixing chamber. That is, the particle counter measures the particle concentration of the diluted dilution gas and converts the concentration of the particle to be measured based on this. When loss of particles occurs in the mixing chamber, the particles included in the dilution gas supplied to the particle counter Since the number of is already small, the concentration of the particles converted based on this has a difference from the concentration of the actual particles to be measured.

In addition, since a large amount of dilution gas diluted in the mixing chamber must be sucked into the ejector, a large amount of high-pressure air is required in the ejector. Therefore, there is a problem in that a configuration of a compressor for supplying air to the ejector at high pressure must be added.

Republic of Korea Patent Publication No. 2013-0059592 (published on June 7, 2013)

In order to solve the above problems, the technical problem to be achieved by the present invention is to provide an exhaust gas dilution device capable of increasing measurement accuracy.

The technical problem to be achieved by the present invention is not limited to the technical problems mentioned above, and other technical problems that are not mentioned can be clearly understood by those of ordinary skill in the technical field to which the present invention belongs from the following description. There will be.

In order to achieve the above technical problem, an embodiment of the present invention includes a head part through which exhaust gas is introduced and moved from the outside; An ejector unit coupled to the front end of the head unit and guiding the primary dilution air to be introduced and moved from the outside; A nozzle unit for inducing the exhaust gas flowing into the head unit to be ejected to the front of the ejector unit by increasing the flow velocity of the primary dilution air moving from the ejector unit; It is coupled to the front end of the ejector unit, and the first dilution gas is generated by mixing the exhaust gas and the primary dilution air in the ejector unit, and then the discharged primary dilution gas is mixed with the secondary dilution air introduced from the outside so that the secondary dilution gas A dilution part to be generated; And it is coupled to the front end of the dilution unit, it provides an exhaust gas dilution device, characterized in that it comprises a measuring unit for measuring the target particles in the secondary dilution gas.

In an embodiment of the present invention, the measuring unit is provided on a flow path through which the secondary dilution gas moves, and a filter unit that filters the target particles included in the secondary dilution gas, and irradiates light toward the filter unit. A light source, a light receiving unit configured to receive light transmitted from the filter unit after being irradiated from the light source, and a calculating unit configured to calculate the concentration of the target particle based on the light information generated by the light receiving unit.

In an embodiment of the present invention, the filter unit is provided on the other side of the flow path, a supply roller provided on one side of the flow path, a tape filter provided to cross the flow path while being released from the supply roller, The tape filter unwound from the supply roller has a water supply roller, and the second dilution gas moves along the flow path and passes through the tape filter. The tape filter is wound around the water supply roller, and a new tape filter unwound from the supply roller may be located on the flow channel.

In an embodiment of the present invention, a separation unit provided between the dilution unit and the measurement unit and configured to separate a group of target particles to be measured in the secondary dilution gas moving from the dilution unit by cyclone to guide the flow path It may contain more.

In an embodiment of the present invention, the target particle group has a first target particle group and a second target particle group having a size smaller than that of the first target particle group, and the separation unit A first separation unit for separating a group of particles by a cyclone, a second separation unit for separating the second target particle group from the secondary dilution gas by a cyclone, and the flow channel to the first separation unit or the second separation unit. It may have a connection part that selectively connects.

In an embodiment of the present invention, a preheating unit provided at a rear end of the head unit may further include a preheating unit for preheating the exhaust gas flowing into the head unit.

In an embodiment of the present invention, the preheating unit preheats the exhaust gas to a temperature of 190°C to 210°C, and the first dilution air is 150°C to 250°C so that the first dilution gas is generated by a high-temperature dilution method. It is supplied at a temperature, and the second dilution air may be supplied at a temperature of 10°C to 30°C so that the second dilution gas is generated by a room temperature dilution method.

In an embodiment of the present invention, the head portion has a space portion through which the exhaust gas is introduced, and a through hole formed through a central axis direction and connected to the space portion, and the ejector portion is formed through the central axis direction, and the It has a first discharge hole connected to the through hole, and a first inlet for guiding the first dilution air to the first discharge hole, and the first discharge hole is formed at a rear end of the ejector part and connected to the first inlet. A suction part, an acceleration part formed at a front end of the suction part, and a diffusion part formed at a front end of the acceleration part may be provided.

In an embodiment of the present invention, the nozzle portion is formed at a front end of the connection portion, a flange portion coupled to the inner surface of the space portion, a connection portion connected to the flange portion and provided inside the through hole and the suction portion, and It may have an outer diameter corresponding to the inner diameter of the acceleration portion and have a nozzle tip portion inserted into the acceleration portion.

In an embodiment of the present invention, the nozzle tip portion may have a first discharge passage through which the primary dilution air introduced into the suction unit is discharged to the diffusion unit on an outer circumferential surface.

In an embodiment of the present invention, the acceleration unit may have a second discharge passage through which the primary dilution air introduced into the suction unit is discharged to the diffusion unit on an inner circumferential surface.

According to an embodiment of the present invention, effective decompression can be achieved in the diffusion portion by the primary dilution air moving at high speed through the first discharge passage, and thus exhaust gas can be smoothly moved through the nozzle portion, There is an advantage that compressed air for moving the exhaust gas is unnecessary.

In addition, according to an embodiment of the present invention, since the secondary dilution air flows in the direction of the center of the first flow passage through the through holes formed in the first flow passage, the number of exhaust gas particles adhered to the inner peripheral surface of the first flow passage decreases Can be. In addition, when the secondary dilution air flows into the first flow passage through the through hole, exhaust gas particles adhered to the inner circumferential surface of the first flow passage may come off. Accordingly, loss of particles can be effectively improved in the process of turning the exhaust gas into the secondary dilution gas.

In addition, according to an embodiment of the present invention, the exhaust gas is firstly diluted in the ejector unit and secondarily diluted in the dilution unit, so that the dilution rate can be increased.

In addition, according to an embodiment of the present invention, the exhaust gas preheated in the preheating unit is mixed with high-temperature primary dilution air to be diluted at high temperature, and then mixed with secondary dilution air at room temperature to be diluted at room temperature. Water droplets may be prevented from becoming droplets, and thus, measurement accuracy of particles may be improved.

In addition, according to an embodiment of the present invention, the separation unit can separate a specific target particle group by cyclone so that only the target particles included in the target particle group are collected from the filter unit in the measurement unit, and through this, only the concentration of the target particles is selected. It can also be measured individually.

In addition, according to an embodiment of the present invention, a plurality of separating units may be provided to separate different groups of target particles with a cyclone, and each separating unit may be selectively connected to a flow path by a connection unit. According to this, even if the target particle is changed, the concentration of the desired target particle can be continuously measured.

The effects of the present invention are not limited to the above effects, and should be understood to include all effects that can be deduced from the configuration of the invention described in the detailed description or claims of the present invention.

1 is a perspective view showing an exhaust gas dilution apparatus according to a first embodiment of the present invention.
2 is a cross-sectional view of an exhaust gas dilution apparatus according to a first embodiment of the present invention.
3 is an exploded cross-sectional view showing the nozzle portion of the exhaust gas dilution apparatus according to the first embodiment of the present invention.
4 is a graph for explaining the effect of the dilution temperature in the exhaust gas dilution apparatus according to the first embodiment of the present invention.
5 is a perspective view showing a nozzle part of an exhaust gas dilution apparatus according to a first embodiment of the present invention.
6 is an exploded cross-sectional view showing a nozzle portion of an exhaust gas dilution device according to a second embodiment of the present invention.
7 is an exemplary view mainly showing a measuring unit of the exhaust gas dilution device according to the first embodiment of the present invention.
8 and 9 are exemplary views mainly showing a separating part of the exhaust gas dilution device according to the first embodiment of the present invention.

Hereinafter, the present invention will be described with reference to the accompanying drawings. However, the present invention may be implemented in various different forms, and therefore is not limited to the embodiments described herein. In the drawings, parts irrelevant to the description are omitted in order to clearly describe the present invention, and similar reference numerals are attached to similar parts throughout the specification.

Throughout the specification, when a part is said to be “connected (connected, contacted, bonded)” with another part, it is not only “directly connected”, but also “indirectly connected” with another member in the middle. It also includes the case where it is ”. In addition, when a part "includes" a certain component, it means that other components may be further provided, rather than excluding other components unless specifically stated to the contrary.

The terms used in the present specification are only used to describe specific embodiments, and are not intended to limit the present invention. Singular expressions include plural expressions unless the context clearly indicates otherwise. In the present specification, terms such as “comprise” or “have” are intended to designate the presence of features, numbers, steps, actions, components, parts, or combinations thereof described in the specification, but one or more other features. It is to be understood that the presence or addition of elements or numbers, steps, actions, components, parts, or combinations thereof does not preclude in advance.

Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings.

1 is a perspective view showing an exhaust gas dilution apparatus according to a first embodiment of the present invention, FIG. 2 is a cross-sectional view of an exhaust gas dilution apparatus according to a first embodiment of the present invention, and FIG. 3 is a first embodiment of the present invention. It is an exploded cross-sectional view showing the nozzle part of the exhaust gas dilution device according to the example.

1 to 3, the exhaust gas dilution device may include a head unit 100, an ejector unit 200, a nozzle unit 300, a dilution unit 400, and a measurement unit 600.

In the head part 100, the exhaust gas 1 may be introduced and moved from the outside.

In addition, the ejector unit 200 may be coupled to the front end of the head unit 100, and may guide the primary dilution air 2 to be introduced and moved from the outside.

The nozzle unit 300 may increase the flow velocity of the primary dilution air 2 moving from the ejector unit 200, and through this, the exhaust gas 1 flowing into the head unit 100 is transferred to the ejector unit 200 Can be induced to erupt forward.

The dilution part 400 is coupled to the front end of the ejector part 200, and the first dilution gas discharged after being generated by mixing the exhaust gas 1 and the primary dilution air 2 in the ejector part 200 is external It is mixed with the secondary dilution air (3) introduced from the secondary dilution gas can be generated.

The measuring unit 600 is coupled to the front end of the dilution unit 400, and can measure the target particles in the secondary dilution gas.

In detail, the head part 100 may have a space part 111 into which the exhaust gas 1 is introduced, and a through hole 112 that penetrates in the central axis direction so as to be connected to the space part 111.

Hereinafter, for convenience of description, a front end/front end/front, a rear end/rear end/rear section will be described based on the flow direction of the exhaust gas. That is, when the exhaust gas is moved from the first point to the second point, the first point is referred to as the rear end/rear end/rear, and the second point is the front end/front end/front.

Accordingly, the through hole 112 may be formed at the front end of the head portion 100.

In addition, a step protrusion 120 may be formed at the front end of the head portion 100. The stepped protrusion 120 may be formed along the circumferential direction.

In addition, a cover (not shown) for sealing the space part 111 may be provided at the rear end of the head part 100, and exhaust gas may be introduced into the space part 111 through the cover.

In the present invention, the exhaust gas may be an example of the measurement object, and the measurement object is not necessarily limited to the exhaust gas. For example, when the measurement target is smoke from a chimney, a flow path through which a part of the smoke is absorbed may be provided in the chimney, and the smoke that moves through the flow path is the space part 111 of the head part 100 through the cover. ) Can be supplied.

The ejector part 200 may be coupled to the front end of the head part 100.

A first step groove 230 may be formed at the rear end of the ejector part 200, and the step protrusion 120 of the head part 100 may be inserted into the first step groove 230, through which the head The unit 100 and the ejector unit 200 may be coupled to have the same central axis with each other.

The ejector part 200 has a first discharge hole 210 formed through the center axis to be connected to the through hole 112 and connected to the first inlet 220 for guiding the supplied primary dilution air 2. I can have it.

In addition, the first discharge hole 210 may have a suction part 211, an acceleration part 212, and a diffusion part 213.

The suction part 211 may be formed at the rear end of the ejector part 200, and may be formed so that the inner diameter decreases toward the front.

The acceleration part 212 may be formed at a front end of the suction part 211 and may be connected to the suction part 211. The acceleration part 212 may be formed to have the same inner diameter.

The diffusion unit 213 may be formed at a front end of the acceleration unit 212 and may be connected to the acceleration unit 212. The diffusion part 213 may be formed such that the inner diameter increases toward the front.

In addition, the ejector unit 200 may have a first inlet 220. The first inlet 220 may be formed through in a radial direction and may be connected to the suction part 211.

The first inlet 220 may guide the primary dilution air 2 supplied from the outside to the suction unit 211. A first pipe 221 guiding the inflow of the first diluted air 2 from the outside may be coupled to the first inlet 220.

The first dilution air may be hot air, and the first dilution air may be supplied at a temperature of 150°C to 250°C.

The nozzle part 300 is inserted into the first discharge hole 210 through the through hole 112, and as the primary dilution air 2 moves through the first discharge hole 210, the space part 111 It may have a second discharge hole 340 formed through the central axis direction so that the introduced exhaust gas 1 is sucked and discharged into the first discharge hole 210.

The nozzle part 300 may have a flange part 310, a connection part 320, and a nozzle tip part 330.

The flange portion 310 may be coupled to the inner surface of the space portion 111. The flange portion 310 may be coupled to the head portion 100 by a fastening member such as a bolt, and may be detached from the head portion 100.

The connection part 320 may be connected to the flange part 310 to extend forward. The connection part 320 may pass through the through hole 112 of the head part 100 and extend to the front of the head part 100, and may be provided inside the suction part 211. The connection part 320 may be formed to have a smaller diameter toward the front direction.

The nozzle tip part 330 may be formed at the front end of the connection part 320 and may be inserted into the acceleration part 212. The nozzle tip part 330 may have an outer diameter of a size corresponding to the inner diameter of the acceleration part 212.

In addition, the nozzle part 300 may have a second discharge hole 340, and the second discharge hole 340 may be formed through the nozzle part 300 in the direction of the central axis. A portion of the second discharge hole 340 formed in the connection portion 320 may be formed to have an inner diameter smaller toward the front, and a portion formed in the nozzle tip portion 330 may be formed with the same inner diameter.

In addition, the nozzle tip portion 330 may have a first discharge passage 331 on the outer circumferential surface. The first discharge passage 331 may be formed spirally recessed in the outer circumferential surface of the nozzle tip portion 330 (see FIG. 5A). Accordingly, when the nozzle tip part 330 is inserted into the acceleration part 212, the suction part 211 and the diffusion part 213 may be connected by the first discharge passage 331.

The primary dilution air 2 supplied through the first inlet 220 may be introduced into the suction unit 211 and may be moved to the diffusion unit 213 through the first discharge passage 331. As the primary dilution air passes through the first discharge passage 331 having a small cross-sectional area, the flow rate increases. When the primary dilution air is discharged to the diffusion unit 213, the pressure decreases. Then, a pressure difference between the diffusion part 213 and the space part 111 occurs, and the exhaust gas of the space part 111 flows into the second discharge hole 340 and is moved to be supplied to the diffusion part 213. do. Since the first dilution air moving through the first discharge passage 331 generates a vortex in the diffusion unit 213 and a centrifugal force can be induced, the pressure at the rear end of the diffusion unit 213 may be more effectively lowered.

The angle and interval of the first discharge passage 331 may be adjusted, and through this, the flow rate and pressure of the primary dilution air can be controlled.

If the central axis of the nozzle tip part 330 does not coincide with the central axis of the acceleration part 212, the cross-sectional area of the gap between the nozzle tip part 330 and the acceleration part 212 is changed according to the position and passes through it. The flow rate of the diluted air is also changed, and effective decompression may not be achieved at the rear end of the diffusion unit 213. Then, it may not be possible to stably move the exhaust gas through the second discharge hole 340.

However, in the present invention, since the outer diameter of the nozzle tip portion 330 is formed to correspond to the inner diameter of the acceleration portion 212, and the nozzle tip portion 330 is closely inserted into the acceleration portion 212, the nozzle tip portion 330 is accelerated. It may be located on the same central axis as the part 212. Therefore, the flow rate of the primary dilution air is the same at any position between the nozzle tip part 330 and the acceleration part 212, and effective decompression is performed in the diffusion part 213 and the exhaust gas through the second discharge hole 340 Can be moved stably. Further, according to this, since the movement of the exhaust gas can be smoothly performed due to the effective decompression performed in the diffusion unit 213, there is an advantage that compressed air for moving the exhaust gas is unnecessary.

The exhaust gas dilution device may further include a first adapter unit 500 and a second adapter unit 550.

The first adapter part 500 may be coupled to a front end of the ejector part 200.

The first adapter part 500 may have an extension and diffusion part 501 formed therethrough in the axial direction. The extended diffusion unit 501 may be formed to increase its inner diameter toward the front direction, and may be formed to be continuous with the diffusion unit 213 of the ejector unit 200.

The first adapter part 500 may have a second step groove 502 on an outer circumferential surface of the front end part.

In addition, the second adapter unit 550 may be coupled to a front end of the first adapter unit 500.

The second adapter part 550 may have a flow path hole 551 penetrating through the axial direction, and the flow path hole 551 may be connected to the extended diffusion part 501 of the first adapter part 500.

The first dilution gas generated by mixing the first dilution air flowing into the first inlet 220 and the exhaust gas supplied through the second discharge hole 340 in the diffusion unit 213 is an extended diffusion unit 501 and It can be moved through the flow path 551.

The second adapter part 550 may have a third step groove 552 on an outer circumferential surface of the front end part.

The dilution part 400 includes a first flow path part 410 through which the first dilution gas discharged after the exhaust gas 1 and the first dilution air 2 are mixed and generated in the first discharge hole 210 is introduced. , It may have a second passage portion 420 that is connected to the first passage portion 410 and guides the supplied secondary dilution air 3 to be mixed with the first diluting gas. In the dilution unit 400, the first dilution gas and the second dilution air 3 may be mixed to generate a second dilution gas.

Specifically, the dilution part 400 may be coupled to the front end of the second adapter part 550.

The dilution part 400 may have a first passage part 410 and a second passage part 420.

The rear end of the first passage part 410 may be coupled to the third step groove 552 of the second adapter part 550. The first passage part 410 may be formed to be continuous with the passage hole 551 of the second adapter part 550, and the primary dilution gas generated in the diffusion part 213 is transferred to the first passage part 410. Can be moved.

A plurality of through holes 411 may be formed through the first passage part 410.

The second passage part 420 may be provided to surround the first passage part 410 outside the first passage part 410. The rear end of the second passage part 420 may be coupled to the second stepped groove 502 of the first adapter part 500.

A second inlet 440 may be formed in the second passage 420, and the second inlet 440 may be formed at a front end of the outer circumferential surface of the second passage 420. The second dilution air 3 may be introduced through the second inlet 440, and a second pipe 441 for guiding the second dilution air from the outside may be connected to the second inlet 440.

In addition, the dilution part 400 may have a guide wall 430.

The guide wall 430 may be provided between the first passage part 410 and the second passage part 420.

In addition, a rear end of the guide wall 430 may be spaced apart from a front end of the first adapter unit 500. Through this, the space between the first flow passage 410 and the second flow passage 420 may be partitioned mostly by the guide wall 430, and the secondary dilution air introduced through the second inlet 440 The length of the flow can be lengthened. That is, the secondary dilution air introduced through the second inlet 440 is moved in the rear direction in the space between the second flow path 420 and the guide wall 430, and the guide wall 430 and the first adapter It may be moved to the space between the first flow path part 410 and the guide wall 430 through the space between the parts 500. Then, it is moved to the inside of the first flow path 410 through the through hole 411, and is mixed with the first dilution gas to generate a second dilution gas.

Since a plurality of through holes 411 are formed as a whole in the first passage part 410, the area of the outer circumferential surface of the first passage part 410 is reduced. Accordingly, among the exhaust gas particles of the primary dilution gas, the number of particles adhering to the inner circumferential surface of the first flow path unit 410 may be reduced, and thus the loss of exhaust gas particles may be reduced.

In addition, when the secondary dilution air flows in the center direction of the first flow path part 410 through the through hole 411, the exhaust gas particles adhered to the inner circumferential surface of the first flow path part 410 may come off. Accordingly, most of the particles in the exhaust gas moving in the first passage part 410 can be mixed with the secondary dilution air, and loss of particles in the process of turning the exhaust gas into the secondary dilution gas is also effectively reduced. Can be.

The exhaust gas dilution device may include a diffusion tube portion 570, a plug portion 580, and an exhaust pipe 590.

The diffusion tube part 570 may be coupled to the front end of the dilution part 400.

The diffusion tube part 570 may have a coupling groove 572 at its rear end. The coupling groove 572 may be formed in a circumferential direction, and the front end of the guide wall 430 may be inserted into the coupling groove 572. In addition, the rear end of the diffusion tube portion 570 may be inserted into and coupled to the inside of the second passage portion 420.

The diffusion tube portion 570 may have an additional diffusion portion 571 penetrating through the axial direction. The additional diffusion part 571 may be formed such that the inner diameter increases toward the front direction, and the secondary dilution gas generated by the dilution part 400 may be moved to the additional diffusion part 571.

The stopper 580 may be coupled to the front end of the diffusion tube part 570. The stopper 580 may seal the front end of the diffusion tube part 570.

The discharge pipe 590 may be coupled to the stopper 580. A plurality of discharge pipes 590 may be combined. A connection hole 581 may be formed through the stopper 580 so that the discharge pipe 590 is coupled, and the secondary dilution gas of the additional diffusion part 571 moves to the discharge pipe 590 through the connection hole 581 Can be. A particle counter (not shown) may be connected to the discharge pipe 590, and the secondary dilution gas may be moved to the particle counter through the discharge pipe 590.

According to the present embodiment, the exhaust gas is mixed with the first dilution air in the ejector unit 200 to be dilution first, and the dilution unit is mixed with the second dilution air in the dilution unit 400 to make the second dilution. Can be high.

As described above, the primary dilution air supplied to the ejector unit 200 may be air at a high temperature of 150° C. to 250° C., and the primary dilution gas generated by the ejector unit 200 may be generated by a high-temperature dilution method. I can.

In addition, the secondary dilution air supplied to the dilution unit 400 may be air at room temperature, and may be supplied at a temperature of 10°C to 30°C. The secondary dilution gas generated by the dilution unit 400 may be generated by a room temperature dilution method.

4 is a graph for explaining the effect of the dilution temperature in the exhaust gas dilution apparatus according to the first embodiment of the present invention.

4, the exhaust gas discharged from the nozzle unit 300 is in a high-temperature state (P0). If the primary dilution air mixed with the high-temperature exhaust gas is air at room temperature, that is, the high temperature When the exhaust gas is diluted at room temperature, all of the moisture in the exhaust gas may be converted into droplets. Accordingly, the primary dilution gas in the first state P1 generated by the diffusion unit 213 may contain a large amount of droplets. And, when the primary dilution gas containing a large amount of droplets is mixed with the secondary dilution air at room temperature in the dilution unit 400 to generate the secondary dilution gas in the second state (P2), a large amount of the secondary dilution gas The droplets of will continue to be included. Since such droplets can be treated as particles during measurement in a particle counter (not shown), it may cause a decrease in measurement accuracy.

However, according to the present invention, the primary dilution gas generated in the diffusion unit 213 by mixing the high-temperature exhaust gas P0 with the high-temperature primary dilution air, that is, the high-temperature dilution of the high-temperature exhaust gas, is A third state (P3) may be established, and moisture in the exhaust gas may be prevented from becoming droplets. In addition, since the dilution part 400 is mixed with the secondary dilution air at room temperature to form the secondary dilution gas in the second state (P2), no droplets are included in the secondary dilution gas, or the content of the droplets can be minimized. , Through this, the measurement accuracy of the particles can be improved.

5 is a perspective view showing a nozzle part of an exhaust gas dilution apparatus according to a first embodiment of the present invention.

FIG. 5A shows that the first discharge passage 331 formed on the outer circumferential surface of the nozzle tip portion 330 is formed in a spiral shape, and since this has been described above, a description thereof will be omitted.

Meanwhile, as shown in FIGS. 5B and 5C, the first discharge passage 331a may be formed in the axial direction of the nozzle tip portion 330a, and the first discharge passage 331a is It may be formed in plural at predetermined intervals along the circumferential direction of the nozzle tip portion 330a.

Here, the flange part 310a, the connection part 320a, and the second discharge hole 340 of the nozzle part 300a are the flange part 310, the connection part 320, and the second discharge shown in FIG. 5A. It may be the same as the hole 340.

6 is an exploded cross-sectional view showing a nozzle portion of an exhaust gas dilution device according to a second embodiment of the present invention. In this embodiment, the first discharge passage formed on the outer circumferential surface of the nozzle tip may be formed on the inner circumferential surface of the accelerator 212, and other configurations are the same as those of the first embodiment described above, so the repeated contents are omitted as much as possible.

First, as shown in (a) of FIG. 6, the acceleration unit 1212 may have a second discharge passage 1215 on an inner circumferential surface. Here, the second discharge passage 1215 may be formed spirally recessed in the inner circumferential surface of the acceleration unit 1212.

In addition, the nozzle part 1300 may have a flange part 1310, a connection part 1320, and a nozzle tip part 1330, and a second discharge hole 1340 may be formed through the nozzle part 1300 in the axial direction. have. The nozzle tip portion 1330 may be formed such that an outer diameter corresponds to an inner diameter of the acceleration portion 1212.

When the nozzle tip part 1330 is inserted into the acceleration part 1212, the first dilution air flowing into the first inlet 1220 is flown from the suction part 1211 of the first discharge hole 1210 to the second discharge passage 1215. It may be moved to the diffusion unit 1213 through.

Meanwhile, as shown in FIGS. 6B and 6C, the second discharge passage 1215a may be formed in the axial direction on the inner circumferential surface of the acceleration part 1212a, and the second discharge passage 1215a ) May be formed in plural at predetermined intervals along the circumferential direction of the acceleration part 1212a.

When the nozzle tip part 1330 is inserted into the acceleration part 1212a, the primary dilution air flowing into the first inlet 1220 is from the suction part 1211 of the first discharge hole 1210a to the second discharge passage 1215a. It can be moved to the diffusion unit 1213 through.

7 is an exemplary view mainly showing a measuring unit of the exhaust gas dilution device according to the first embodiment of the present invention.

As shown in FIG. 7, the measurement unit 600 may include a filter unit 610, a light source 620, a light receiving unit 630, and a calculation unit 640.

The filter unit 610 is connected to the discharge pipe 590 and may be provided on the flow passage 591 through which the secondary dilution gas moves from the discharge pipe 590, and may filter target particles included in the secondary dilution gas. .

The filter unit 610 may have a supply roller 611, a tape filter 612 and a supply roller 613.

The supply roller 611 may be provided on one side of the flow passage 591.

The tape filter 612 may be provided by being wound around the supply roller 611. The tape filter 612 may be provided to cross the flow passage 591 while being unwound from the supply roller 611.

The supply roller 613 may be provided on the other side of the flow passage 591, and the tape filter 612 unwound from the supply roller 611 may be wound around the supply roller 613.

The secondary dilution gas coming out of the discharge pipe 590 moves along the flow passage 591 and passes through the tape filter 612 provided to cross the flow passage 591. The tape filter 612 may filter target particles included in the passing secondary dilution gas. The secondary dilution gas may pass through the tape filter 612 for a preset passage time.

The light source 620 may irradiate light 621 toward the filter unit 610. Specifically, the light source 620 may irradiate the light 621 to the tape filter 612 on the flow path 591.

The light receiving unit 630 may receive light 621 that passes through the tape filter 612 after being irradiated from the light source 620.

The calculation unit 640 may calculate the concentration of the target particle based on light information generated based on the light 621 received by the light receiving unit 630.

Here, as an example, a beta ray (β-ray) may be used as the light 621, and the measurement unit 600 may be implemented in the form of a beta ray absorbing device using a beta ray absorption method. In this case, the light source 620 may be a beta ray source, and particles collected by measuring the relative intensity of the beta ray absorbed when the beta ray irradiated from the beta ray source passes through the particles (dust) collected on the tape filter 612 The mass concentration of can be measured. The particle concentration calculation through the beta ray absorption method can be measured by calculating the difference between the beta ray absorbed and extinguished when the beta ray irradiated from the light source emitting the beta ray passes through the particles collected on the paper filter.

Alternatively, as another example, the measurement unit 600 may be implemented in a tapered element oscillating microbalance (TEOM) method in which the aerosol floating in the secondary dilution gas is sampled and the specimen is vibrated to measure the frequency. In the TEOM method, sampling particles are collected in a tapered sample, vibrated, and then the frequency is measured, and the frequency before and after the sampling is compared to measure the weight of the particles.

When the passage time for the secondary dilution gas to move along the flow channel 591 and pass through the tape filter 612 elapses, the tape filter through which the secondary dilution gas has passed is wound around the receiving roller 613, and the flow channel 591 A new tape filter 612 that is unwound from the supply roller 611 may be located on ).

8 and 9 are exemplary views mainly showing a separating part of the exhaust gas dilution device according to the first embodiment of the present invention.

First, as shown in FIG. 8, the exhaust gas dilution device may further include a separation unit 700.

The separation unit 700 may be provided between the dilution unit 400 and the measurement unit 600. More specifically, the separation unit 700 may be provided between the discharge pipe 590 and the measurement unit 600.

The separating unit 700 may cyclone-separate a group of target particles to be measured from the secondary dilution gas moving from the dilution unit 400 and guide them to the flow passage 591. The target particle group is PM10 (Particulate Matter with a diameter less than 10㎛), usually referred to as fine dust with a particle size of 10㎛ or less, or PM2, which is usually referred to as ultrafine dust with a particle size of 2.5㎛ or less. Can be 5.

When the separation unit 700 separates a specific target particle group by cyclone, the measurement unit 600 can collect only the target particles included in the target particle group from the filter unit 610, through which only the concentration of the target particles is selected. It can also be measured individually.

Meanwhile, as shown in FIG. 9, the separation unit 700 may include a first separation unit 710, a second separation unit 720, and a connection unit 730.

The target particle group may have a first target particle group and a second target particle group having a size smaller than that of the first target particle group.

The first separating unit 710 may cyclone-separate the first target particle group from the secondary dilution gas. In addition, the second separating unit 720 may cyclone-separate the second target particle group from the secondary dilution gas.

The connection part 730 may be connected to the first separation unit 710, the second separation unit 720, and the flow channel 591, and the flow channel 591 is connected to the first separation unit 710 or the second separation unit ( 720) can be selectively connected.

For example, assuming that the first target particle group is PM10 and the second target particle group is PM2.5, when the target particle group is PM10, the connection unit 730 is the first separation unit 710 It can be connected to the flow path 591. In addition, when the target particle group is to be PM2.5, the connection unit 730 may allow the second separation unit 720 to be connected to the flow channel 591. According to this, even if the target particles are changed, the concentration of different target particles can be continuously measured by continuously using the exhaust gas dilution device.

In addition, the exhaust gas dilution device may further include a preheating unit 800.

Referring back to FIGS. 1 and 2, the preheating unit 800 may be provided at a rear end of the head unit 100. The preheating unit 800 may pre-heat the exhaust gas 1 flowing into the head unit 100.

The preheating unit 800 may preheat the exhaust gas 1 to a temperature of 190°C to 210°C. When the exhaust gas 1 is preheated and moved to the ejector unit 200, it is mixed with the above-described primary dilution air, so that it can be diluted at a higher temperature more effectively.

A guide passage 810 for guiding the moving exhaust gas 1 to be moved to the preheating unit 800 may be further provided at the rear end of the preheating unit 800.

The above description of the present invention is for illustrative purposes only, and those of ordinary skill in the art to which the present invention pertains will be able to understand that other specific forms can be easily modified without changing the technical spirit or essential features of the present invention. will be. Therefore, it should be understood that the embodiments described above are illustrative and non-limiting in all respects. For example, each component described as a single type may be implemented in a distributed manner, and similarly, components described as being distributed may also be implemented in a combined form.

The scope of the present invention is indicated by the claims to be described later, and all changes or modified forms derived from the meaning and scope of the claims and the concept of equivalents thereof should be construed as being included in the scope of the present invention.

1: Exhaust gas 2: Primary dilution air
3: second dilution air 100: head
200: ejector part 210: first discharge hole
211: suction unit 212, 1212, 1212a: acceleration unit
213: diffusion unit 220: first inlet
300, 300a, 1300: nozzle portion 330, 330a, 1330: nozzle tip portion
331, 331a: first discharge passage 400: dilution part
410: first euro part 411: tonggong
420: second passage part 430: guide wall
500: first adapter unit 550: second adapter unit
570: diffusion tube portion 580: plug portion
590: discharge pipe 591: flow passage
600: measuring unit 610: filter unit
620: light source 630: light receiving unit
640: calculation unit 700: separation unit
710: first separation unit 720: second separation unit
730: connection part 800: preheating part
1215, 1215a: 2nd discharge passage

Claims (11)

A head portion through which exhaust gas is introduced and moved from the outside;
An ejector unit coupled to the front end of the head unit and guiding the primary dilution air to be introduced and moved from the outside;
A nozzle unit for inducing the exhaust gas flowing into the head unit to be ejected to the front of the ejector unit by increasing the flow velocity of the primary dilution air moving from the ejector unit;
It is coupled to the front end of the ejector unit, and the first dilution gas is generated by mixing the exhaust gas and the primary dilution air in the ejector unit, and then the discharged primary dilution gas is mixed with the secondary dilution air introduced from the outside, so that the secondary dilution gas is A dilution part to be generated;
A separating unit for separating a group of target particles to be measured from the secondary dilution gas discharged from the dilution unit by cyclone and guiding the secondary dilution gas to a flow path; And
An exhaust gas dilution apparatus comprising a measuring unit provided at a front end of the separating unit and measuring target particles included in the target particle group moving in the flow passage. The method of claim 1,
The measuring unit
A filter unit provided on the flow passage through which the secondary dilution gas moves to filter the target particles,
A light source for irradiating light toward the filter unit,
A light receiving unit configured to receive light transmitted through the filter unit after being irradiated from the light source,
And a calculation unit for calculating the concentration of the target particles based on the light information generated by the light receiving unit. The method of claim 2,
The filter unit
A supply roller provided on one side of the flow passage,
A tape filter provided to cross the flow path while being released from the supply roller,
It is provided on the other side of the flow channel, and has a supply roller to which the tape filter unwound from the supply roller is wound,
When the passage time for the secondary dilution gas to move along the flow channel and pass through the tape filter elapses, the tape filter through which the secondary dilution gas has passed is wound around the receiving roller, and the supply roller on the flow channel Exhaust gas dilution device, characterized in that the new tape filter unwound in the position. delete The method of claim 1,
The target particle group has a first target particle group and a second target particle group having a size smaller than that of the first target particle group,
The separating part
A first separating unit for cyclone separating the first target particle group from the secondary dilution gas,
A second separating unit for cyclone separating the second target particle group from the secondary dilution gas,
And a connection portion selectively connecting the flow passage to the first separation unit or the second separation unit. The method of claim 1,
An exhaust gas dilution device, further comprising a preheating unit provided at a rear end of the head unit and preheating the exhaust gas flowing into the head unit. The method of claim 6,
The preheating unit preheats the exhaust gas to a temperature of 190°C to 210°C, and the first dilution air is supplied at a temperature of 150°C to 250°C so that the first dilution gas is generated by a high-temperature dilution method, and the secondary The exhaust gas dilution device, characterized in that the secondary dilution air is supplied at a temperature of 10 ℃ to 30 ℃ so that the dilution gas is generated by the room temperature dilution method. The method of claim 1,
The head portion has a space portion through which the exhaust gas is introduced, and a through hole formed through the central axis and connected to the space portion,
The ejector part has a first discharge hole formed through the central axis direction and connected to the through hole, and a first inlet for guiding the primary dilution air to the first discharge hole,
The first discharge hole has a suction part formed at a rear end of the ejector part and connected to the first inlet, an acceleration part formed at a front end of the suction part, and a diffusion part formed at a front end of the acceleration part. Gas dilution device. The method of claim 8,
The nozzle portion has a flange portion coupled to the inner surface of the space portion, a connection portion connected to the flange portion and provided inside the through hole and the suction portion, and an outer diameter formed at a front end of the connection portion and corresponding to the inner diameter of the acceleration portion And a nozzle tip portion inserted into the accelerator portion. The method of claim 9,
The exhaust gas dilution device, characterized in that the nozzle tip portion has a first discharge passage through which the primary dilution air introduced into the suction unit is discharged to the diffusion unit on an outer circumferential surface. The method of claim 9,
And a second discharge passage through which the primary dilution air introduced into the suction unit is discharged to the diffusion unit on an inner circumferential surface of the accelerator.

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