WO2017043793A1 - Exhaust gas purifying apparatus - Google Patents

Exhaust gas purifying apparatus Download PDF

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Publication number
WO2017043793A1
WO2017043793A1 PCT/KR2016/009570 KR2016009570W WO2017043793A1 WO 2017043793 A1 WO2017043793 A1 WO 2017043793A1 KR 2016009570 W KR2016009570 W KR 2016009570W WO 2017043793 A1 WO2017043793 A1 WO 2017043793A1
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WIPO (PCT)
Prior art keywords
duct
exhaust gas
baffle
inlet
foreign matter
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PCT/KR2016/009570
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French (fr)
Korean (ko)
Inventor
이중의
Original Assignee
메탈젠텍 주식회사
주식회사 지스코
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Application filed by 메탈젠텍 주식회사, 주식회사 지스코 filed Critical 메탈젠텍 주식회사
Priority to CN201680047405.8A priority Critical patent/CN107921345B/en
Publication of WO2017043793A1 publication Critical patent/WO2017043793A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/04Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
    • B01D45/08Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/12Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces

Definitions

  • the present invention relates to an exhaust gas purifying apparatus, and more particularly, to an exhaust gas purifying apparatus and a baffle thereof which can be used in an installation in which it is necessary to remove foreign substances such as various ashes and suspended solids generated by the use of fossil fuels.
  • combustion facilities such as thermal power plants, incinerators and industrial boilers generate energy by burning fossil fuels such as coal, heavy oil, and natural gas.
  • fossil fuels such as coal, heavy oil, and natural gas.
  • the fossil fuel When the fossil fuel is burned, it contains a large amount of foreign matter such as ash or ash in the form of powder or solid generated after combustion, unburned fuel material, non-combustible material, nitrogen compound or carbon compound.
  • the gas containing these foreign substances is discharged to the atmosphere may cause air pollution, and in some cases may be adversely affected even in the facility that is connected to the combustion facility to process the gas generated during combustion.
  • a flue gas treatment technology that harmlessly processes harmful substances such as NOx, CO, Dioxine, etc. generated in various combustion facilities, these foreign substances get stuck in the catalyst layer, thereby improving the function and characteristics of the catalyst layer. Significantly degraded. Therefore, there is a need for a technique for separating and removing foreign matter contained in the gas generated by combustion.
  • the idea of the present invention is to guide the discharge gas containing the foreign matter toward the foreign matter accommodating portion to improve the foreign matter separation performance, and to install a first baffle and a second baffle that can induce a sudden change in the direction of the air flow and the discharge gas and It is to provide an exhaust gas purification device that facilitates the separation of foreign matter, and can accelerate the change of direction of the air flow in the discharge direction by using the air flow guide groove.
  • the exhaust gas purifying apparatus for solving the above problems is formed on the bottom surface of the first duct, the first duct to guide the exhaust gas containing foreign matter in the first direction, A foreign matter accommodating part for accommodating foreign matter contained therein, and a second duct part communicating with a purge gas outlet formed at a side surface of the first duct part and guiding the purge gas from which the foreign matter is separated in a second direction, and the inside of the first duct part.
  • a first baffle installed to protrude from the first duct part such that the air flow direction of the exhaust gas flowing into the first duct part is suddenly changed in a second direction of the second duct part direction.
  • the first inlet part installed at a position relatively close to the second duct part and the second inlet part installed adjacent to the first inlet part and installed at a position relatively far from the second duct part. It can hamhal.
  • the first baffle may have a front end protruding obliquely downward at a first downward angle with respect to the foreign substance accommodating part and a rear end fixed above the purge gas outlet.
  • the first downward angle may be 30 degrees to 50 degrees.
  • the first baffle may have a first protrusion length protruding obliquely toward the foreign substance accommodating portion at least 33 percent to 42 percent at a first orientation distance from a connection point of the purge gas outlet to a first extension point on the foreign substance accommodating portion. Can be.
  • the second duct portion may have a flow path height that is a height of a flow path through which the purge gas is discharged, and a first pass distance obtained by subtracting the first protrusion length from the first direction distance may be equal to or greater than the flow path height.
  • the first duct unit may further include a partition wall that divides the first inlet unit and the second inlet unit.
  • It may further include a second baffle installed to protrude into the first inlet, and to induce a rapid change in the air flow direction of the exhaust gas introduced into the first inlet to a second direction of the second duct part.
  • the second baffle may have a front end protruding obliquely downward at a second downward angle with respect to the foreign substance accommodating part and a rear end fixed to a lower end of the separation wall.
  • the second downward angle may be 30 degrees to 50 degrees.
  • the second baffle may have a second protrusion length protruding obliquely toward the foreign substance accommodating portion at a second direction distance from a connection point of the separation wall to a second extension point on the foreign substance accommodating portion.
  • the foreign matter receiving portion may be a funnel-shaped hopper recessed downward, and an induction plane portion having a flat surface may be formed between the first duct portion and the foreign matter receiving portion.
  • the exhaust gas purification apparatus can improve the separation performance of separating the foreign matter contained in the exhaust gas to the foreign matter receiving portion through the rapid change in the direction of the air flow of the exhaust gas.
  • FIG. 1 is a perspective view showing an exhaust gas purification apparatus according to an embodiment of the present invention.
  • FIGS. 2 to 7 are views illustrating an exhaust gas purification apparatus according to various embodiments of the present invention.
  • FIG. 8 is an operational state diagram showing the exhaust gas purification apparatus of FIG. 1.
  • FIG. 9 is a comparison table illustrating a foreign matter removal rate and a pressure difference according to the baffle angle of the exhaust gas purifying apparatus of FIG. 2.
  • FIG. 10 is a comparison table illustrating a foreign matter removal rate and a pressure difference according to the baffle length of the exhaust gas purifying apparatus of FIG. 3.
  • FIG. 1 is a perspective view showing an exhaust gas purification apparatus 100 according to an embodiment of the present invention.
  • the first duct part 10 As shown in FIG. 1, the first duct part 10, the second duct part 20, the foreign substance accommodating part 30, and the first baffle 40 may be included.
  • the first duct part 10 may be formed to guide the discharge gas G1 including the foreign matter 1 in the first direction.
  • the first duct unit 10 may be ash or ash in the form of powder or solids generated after combustion, fuel materials in an unburned state, non-burning incombustibles, nitrogen compounds, carbon bonds, or the like.
  • the first duct portion 10 is formed in a variety of ducts, such as a cylindrical or pipe, in addition to a rectangular cylindrical shape Can be.
  • the first duct part 10 is installed adjacent to the first inlet part 11 and the first inlet part 11 which are installed at a relatively close position from the second duct part 20. And a second inflow portion 12 installed at a position relatively far from the second duct portion 20. for example.
  • the first duct part 10 may further include a separation wall 50 capable of dividing the first inlet part 11 and the second inlet part 12.
  • the first duct part 10 may be formed by combining ducts connected at different positions, and may separate one duct to purify the foreign matter 1 more efficiently. It may be.
  • the dividing wall 50 may be formed by combining ducts or may be installed to separate the ducts.
  • the dividing wall 50 may be installed in a plate shape, and may be installed in a polygonal column shape that extends in the horizontal direction in order to increase the pressure into which the introduced discharge gas G1 flows.
  • an upper wall of the first inlet part 11 and the second inlet part 12 in which the separation wall 50 is horizontally laid in a pentagonal column shape and into which the exhaust gas G1 flows is introduced.
  • the inlet portion formed in the lower portion than the inlet tube formed in the narrower the pressure of the inlet gas (G1) may be higher.
  • the introduced exhaust gas G1 loses momentum due to the rapidly slowed flow rate and gravity due to the sharply lowered pressure in the wider foreign matter accommodating part 30, and thus is purified by the foreign substance accommodating part 30.
  • the first inlet 11 may be installed at a position close to the second duct 20, and the exhaust gas G1 introduced from the first inlet 11 may be faster. Although it may flow out to the second duct part 20, the direction of airflow may be changed due to the separation wall to be described later, and thus may flow out to the second duct part 20.
  • the second inflow portion 12 may be installed at a position relatively far from the first inflow portion 11 in the second duct portion 20, and in the second inflow portion 12.
  • the introduced discharge gas G1 may flow out to the second duct part 20 relatively slower than the discharge gas G1 introduced from the first inlet part, but may be purified by inertia or centrifugal force due to the separation wall to be described later. It may flow out to the two duct portion 20.
  • first inlet 11 and the second inlet 12 may be formed by combining a plurality of ducts connected at different positions.
  • the second duct part 20 communicates with a purification gas outlet H formed at a side surface of the first duct part 10, and the purification gas G2 having the foreign matter 1 separated therefrom.
  • the second duct portion 20 may be formed in various shapes such as a cylinder or a pipe in addition to the rectangular cylinder shape.
  • the second direction is a direction flowing into the processing apparatus for treating harmful components of the exhaust gas G1 before finally discharging the discharge gas G1 introduced through the first duct part 10 to the outside.
  • the treatment apparatus may be a selective catalytic reduction facility, and the exhaust gas G1 introduced into the second direction may be directed to a catalyst layer constituting the selective catalytic reduction facility.
  • the foreign matter accommodating part 30 is formed on the bottom surface of the first duct part 10, and the foreign matter 1 included in the discharge gas G1 guided in the first direction and dropped. I can accept it.
  • the foreign material accommodating part 30 may be a funnel-shaped hopper recessed downward so that the foreign materials 1 are stacked downward.
  • the first baffle 40 is installed to protrude into the first duct part 10, and the air flow direction of the discharge gas G1 introduced into the first duct part 10 is set to the first baffle 40. It can be induced to change rapidly in the second direction of the two duct portion direction.
  • the first baffle 40 may allow the exhaust gas G1 of the first duct part 10 to be diverted to the second duct part 20 via the foreign matter accommodating part 30. It may be installed to protrude into the first duct portion 10.
  • the first baffle 40 may be formed to have a rounded surface to promote the change of direction of the exhaust gas (G1), but is not necessarily limited thereto.
  • the first baffle 40 protrudes inclined at a first downward angle A1 downward with respect to a horizontal surface toward the foreign substance accommodating portion 30 and the rear end thereof is a purge gas discharge hole H. It may be fixed above.
  • the first baffle 40 sharply changes the direction of the discharge gas G1 introduced into the first direction through the first duct part 10 toward the second duct part 20. It can be induced to change. That is, the exhaust gas G1 introduced through the first duct part 10 flows in the first direction (downward in FIG. 1), and then the direction of the air flow is changed by the first duct baffle 40. 20 may be abruptly switched to the second direction. When such a sudden change of direction of the airflow occurs, the foreign matter 1 having a predetermined mass contained in the exhaust gas G1 tends to continue to move in the first direction by inertia (or centrifugal force). As it does not correspond to the change in the air flow direction is moved toward the foreign matter receiving portion 30 may be separated from the exhaust gas (G1).
  • the foreign matter accommodating portion 30 by the sudden change of air flow induced by the first baffle 40, and the foreign matter 1 is transferred to the second duct portion 20. Only the purged gas G2 that has been removed and purified may be discharged to the outside.
  • FIGS. 2 to 7 are views illustrating exhaust gas purifying apparatuses 200, 300, 400, 500, 600, and 700 according to various embodiments of the present disclosure.
  • the first baffle 40 of the exhaust gas purification apparatus 200 is fixed above the purification gas outlet H to face the foreign matter accommodating part 30. It may be installed to be inclined downward with respect to the horizontal plane.
  • the first baffle 40 discharges the discharge gas G1 introduced from the first duct unit 10 to the second duct unit 20 so as to discharge the discharge gas G1 from the first duct unit 10. It does not interfere with the inflow of, and may be installed so as not to interfere with the discharge of the purification gas (G2) in the second duct portion 20, inclined at a first downward angle (A1) relative to the horizontal plane to maximize the purification efficiency.
  • the first downward angle A1 may be 30 degrees to 50 degrees.
  • the first baffle 40 of the exhaust gas purification apparatus 300 may be installed to protrude a predetermined distance.
  • the length of the first baffle 40 protruding obliquely toward the foreign substance accommodating part 30 may be the first protrusion length B1.
  • the virtual extension point of the first baffle 40 located on the foreign matter receiving portion 30 may be a first extension point 41, from a connection point of the first baffle 40 and the purge gas outlet H.
  • the distance to the first extension point 41 may be a first direction distance C1.
  • the first baffle 40 may have a first protrusion length B1 of 33% to 42% or more of the first direction distance C1 to maximize the purification efficiency. For example, if the first protrusion length B1 is too long, the inlet and outlet may be narrowed, the discharge of the foreign matter 1 may be slowed down, and the purification efficiency may be lowered. If the first protrusion length B1 is too short, the foreign matter 1 may be reduced. As the rotational force is lowered, the purification efficiency may be lowered.
  • the second duct part 20 may include a flow path height E, and the discharge gas G1 introduced from the first duct part 10 is introduced to allow the first baffle 40 to flow.
  • the distance when passing through) may be greater than or equal to the channel height E.
  • the first passing distance D1 obtained by subtracting the first protrusion length B1 from the first direction distance C1 may be greater than or equal to the flow path height E.
  • the first protrusion length B1 has a flow path height E in which the first passage distance D1 through which the discharge gas G1 introduced from the first duct part 10 passes passes is formed in the second duct part 20. It can be formed so that it can be improved to the maximum purification efficiency.
  • the exhaust gas purifying apparatus 400 is installed to protrude into the first inlet 11, and discharges introduced into the first inlet 11.
  • the air flow direction of the gas G1 may further include a second baffle 60 to induce a rapid change in a second direction in the direction of the second duct part 20.
  • the second baffle 60 may be fixed to the lower portion of the separation wall 50 and be inclined downward based on a horizontal plane toward the foreign substance accommodating part 30.
  • the second baffle 60 discharges gas G1 from the first duct part 10 to discharge the discharge gas G1 introduced from the first duct part 10 to the second duct part 20.
  • the second downward angle A2 may be 30 degrees to 50 degrees.
  • the second baffle 60 of the exhaust gas purification apparatus 600 may be installed to protrude a predetermined distance.
  • the length of the second baffle 60 protruding obliquely toward the foreign substance accommodating part 30 may be the second protrusion length B2.
  • the virtual extension point of the second baffle 60 located on the foreign matter receiving portion 30 may be a second extension point 42, from the connection point of the second baffle 60 and the purge gas outlet H.
  • the distance to the second extension point 42 may be a second direction distance C2.
  • the second baffle 60 may have a second protrusion length B2 of 33% to 42% or more of the second direction distance C2 to maximize the purification efficiency. For example, if the second protrusion length B2 is too long, the inlet and outlet ports are narrowed, the discharge of the foreign matter 1 may be slowed down, and the purification efficiency may be lowered. If the second protrusion length B2 is too short, the foreign matter 1 may be As the rotational force is lowered, the purification efficiency may be lowered.
  • the foreign matter receiving portion 30 of the exhaust gas purifying apparatus 700 is a funnel-shaped hopper recessed downward, and the first duct portion 10 and the foreign matter receiving portion.
  • Induction plane portion 70 whose surface is a plane between the portions 30 may be formed.
  • the induction plane 70 is guided in a direction different from the first direction so that the airflow direction is rapidly changed, and in particular, a kind of inclined surface may be formed to more easily induce a rapid vortex.
  • the induction plane portion 70 has a significant drop in the flow rate at the foreign matter accommodating portion 30, but instead of the induction plane portion 70 and the baffles 40 and 60, a rapid vortex of rapid flow rate is generated and the foreign matter 1 is By the centrifugal force it may fall in the direction of the foreign matter receiving portion (30).
  • the induction plane portion 70 is formed in a curved surface is longer than the distance from the first baffle 40 to the induction plane portion 70 and the length of the first baffle 40 by the difference in distance It may be formed longer, and when the length of the first baffle 40 is longer, it is possible to enhance the direction change effect of the air flow by the first baffle 40.
  • FIG. 8 is an operating state diagram illustrating the exhaust gas purification apparatus 100 of FIG. 1.
  • the exhaust gas purifying apparatus 100 extracts the exhaust gas G1 from the first duct part 10 including the first inlet part 11 and the second inlet part 12. Guided in one direction, the direction of the air flow by the first baffle 40 through the first duct portion 10 can be rapidly switched to the second direction of the second duct portion 20 direction.
  • the foreign matter 1 is stacked in the foreign matter receiving portion 30, which is a funnel-shaped hopper, and the foreign matter 1 is removed by the second duct portion 20 to purify only the purified gas G2 to the outside. May be discharged.
  • the flow velocity and the pressure were changed according to the angle of the baffle, and the angle of the baffle was 30 degrees, 38 degrees, 45 degrees, 60 degrees, and 75 degrees with respect to the horizontal plane.
  • the baffle angle was 30 degrees, and Type1, 38 degrees were Type2, 45 degrees were Type3, 60 degrees were Type4, and 75 degrees were Type5.
  • Table 1 is a table showing the difference between the average pressure of the inlet and outlet for Experiment 1.
  • the first inlet is an inlet installed at a position far from the outlet
  • the second inlet is an inlet at a position close to the outlet.
  • Table 2 is a table showing the removal rate according to the size of the foreign matter for Experiment 1.
  • the first inlet is an inlet installed at a position far from the outlet
  • the second inlet is an inlet at a position close to the outlet.
  • the removal rate was tested by changing the baffle angle at 100 ⁇ m, 140 ⁇ m, and 200 ⁇ m of foreign matters. Accordingly, it was confirmed that the removal rate of foreign matter decreased as the angle of the baffle was lowered from Type 1 (30 degrees) to Type 5 (75 degrees), and on average, the overall removal rate was 70 from Type 1 (30 degrees) to Type 3 (45 degrees). You can see that it is more than a percentage.
  • FIG. 9 is a comparison table illustrating a foreign matter removal rate and a pressure difference according to the baffle angle of the exhaust gas purifying apparatus 200 of FIG. 2.
  • the flow rate and the pressure were varied according to the length of the baffle, and the ratio of the length of the baffle to the directing distance was changed.
  • the directing distance is a distance from the connection point of the baffle and the purge gas outlet to the virtual extension point of the baffle.
  • the ratio of the baffle length to the directing distance is 1: 0.54, Type6, 1: 0.49 is Type7, 1: 0.43 is Type8, 1: 0.38 is Type9, 1: 0.32 is Type10, and 1: 0.27 is Type11. .
  • Table 3 is a table showing the difference between the average pressure of the inlet and the outlet for Experiment 2.
  • the first inlet is an inlet installed at a position far from the outlet
  • the second inlet is an inlet at a position close to the outlet.
  • Table 4 is a table showing the removal rate according to the size of the foreign matter for Experiment 1.
  • the first inlet is an inlet installed at a position far from the outlet
  • the second inlet is an inlet at a position close to the outlet.
  • the removal rate was tested by changing the length of the baffle in the size of the foreign matter 100 ⁇ m, 140 ⁇ m, 200 ⁇ m. Accordingly, the removal rate of the foreign matter can be confirmed that the removal rate is the highest in Type6 (1: 0.54) when the size of the foreign matter is 100 ⁇ m.
  • FIG. 10 is a comparison table illustrating a foreign matter removal rate and a pressure difference according to the baffle length of the exhaust gas purification apparatus 300 of FIG. 3.
  • the pressure difference between the inlet and the outlet ( ⁇ P) and the size of the foreign matter are 100 ⁇ m and 140 ⁇ m. And it can be confirmed that the removal rate at 200 ⁇ m is reduced.
  • the ratio of the length of the baffle to the directing distance is determined by the inlet and the outlet. It is effective to install more than 1: 0.38 in order to maintain a high foreign material removal rate while forming a relatively low pressure difference.
  • the exhaust gas purification apparatus can improve the separation performance of separating the foreign matter contained in the exhaust gas to the foreign matter receiving portion through the rapid change in the direction of the air flow of the exhaust gas.

Abstract

The present invention relates to an exhaust gas purifying apparatus comprising: a first duct that guides an exhaust gas containing foreign substances in a first direction; a foreign-substance receiving part formed on the bottom of the first duct to receive the foreign substances contained in the exhaust gas; a second duct that communicates with a purified-gas outlet formed on a side surface of the first duct and guides a purified gas, from which the foreign substances have been removed, in a second direction; and a first baffle installed to protrude toward the inside of the first duct and guiding an exhaust gas introduced into the first duct such that the flow direction of the exhaust gas is rapidly changed into the second direction toward the second duct, wherein the first duct includes: a first inflow part installed in a position relatively close to the second duct; and a second inflow part installed adjacent to the first inflow part and installed in a position relatively far away from the second duct.

Description

배출 가스 정화 장치Exhaust gas purification device
본 발명은 배출 가스 정화 장치에 관한 것으로서, 보다 상세하게는 화석연료의 사용으로 발생되는 각종 재나 부유물과 같은 이물질의 제거가 필수적인 설비에 사용할 수 있는 배출 가스 정화 장치 및 이의 배플에 관한 것이다.The present invention relates to an exhaust gas purifying apparatus, and more particularly, to an exhaust gas purifying apparatus and a baffle thereof which can be used in an installation in which it is necessary to remove foreign substances such as various ashes and suspended solids generated by the use of fossil fuels.
일반적으로 화력 발전소, 소각로, 산업용 보일러와 같은 연소설비에서는 석탄, 중유, 천연가스 등과 같은 화석 연료를 연소시켜서 에너지를 생성한다. 이러한 화석 연료의 연소 시에는 연소 후 발생되는 분말이나 고형물 형태의 재(Ash)나 미연소된 상태의 연료 물질이나 타지 않는 불연물질이나 질소 결합물, 탄소 결합물 등 다량의 이물질이 포함된다. 이러한 이물질을 포함하는 가스가 대기 중으로 배출되는 경우에는 대기오염을 일으킬 수 있으며, 경우에 따라 연소설비와 연결되어 연소시 발생된 가스를 처리하는 설비에도 악영향을 줄 수 있다. 예를 들어, 각종 연소설비에서 발생되는 NOx, CO, Dioxine 등과 같은 유해물질에 대해 촉매를 이용하여 무해하게 처리하는 배연기술인 선택적 촉매 환원 공정에서는 이러한 이물질들이 촉매층에 끼이게 되면서 촉매층의 기능 및 특성을 현저하게 열화시키게 된다. 따라서 연소로 인해 발생된 가스 내에 포함되는 이물질을 분리하여 제거시키는 기술이 필요하다.In general, combustion facilities such as thermal power plants, incinerators and industrial boilers generate energy by burning fossil fuels such as coal, heavy oil, and natural gas. When the fossil fuel is burned, it contains a large amount of foreign matter such as ash or ash in the form of powder or solid generated after combustion, unburned fuel material, non-combustible material, nitrogen compound or carbon compound. If the gas containing these foreign substances is discharged to the atmosphere may cause air pollution, and in some cases may be adversely affected even in the facility that is connected to the combustion facility to process the gas generated during combustion. For example, in the selective catalytic reduction process, a flue gas treatment technology that harmlessly processes harmful substances such as NOx, CO, Dioxine, etc. generated in various combustion facilities, these foreign substances get stuck in the catalyst layer, thereby improving the function and characteristics of the catalyst layer. Significantly degraded. Therefore, there is a need for a technique for separating and removing foreign matter contained in the gas generated by combustion.
본 발명의 사상은, 이물질을 포함하는 배출 가스를 이물질 수용부 방향으로 안내하여 이물질 분리 성능을 향상시키고, 급격한 기류의 방향 변화를 유도할 수 있는 제1배플 및 제2배플을 설치하여 배출 가스와 이물질의 분리를 촉진시키며, 기류 유도홈을 이용하여 기류의 배출 방향으로의 방향 변화를 가속시킬 수 있는 배출 가스 정화 장치를 제공함에 있다.The idea of the present invention is to guide the discharge gas containing the foreign matter toward the foreign matter accommodating portion to improve the foreign matter separation performance, and to install a first baffle and a second baffle that can induce a sudden change in the direction of the air flow and the discharge gas and It is to provide an exhaust gas purification device that facilitates the separation of foreign matter, and can accelerate the change of direction of the air flow in the discharge direction by using the air flow guide groove.
상기 과제를 해결하기 위한 본 발명의 사상에 따른 배출 가스 정화 장치는, 이물질이 포함된 배출 가스를 제1방향으로 유도하는 제1덕트부, 상기 제1덕트부의 저면에 형성되고, 상기 배출 가스에 포함된 이물질을 수용하는 이물질 수용부, 상기 제1덕트부의 측면에 형성되는 정화 가스 배출구와 연통되고, 이물질이 분리된 정화 가스를 제2방향으로 유도하는 제2덕트부 및 상기 제1덕트부의 내부로 돌출되게 설치되고, 상기 제1덕트부로 유입된 배출 가스의 기류 방향이 상기 제2덕트부 방향의 제2방향으로 급격하게 변화되도록 유도하는 제1배플을 포함하고, 상기 제1덕트부는, 상기 제2덕트부로부터 상대적으로 가까운 위치에 설치되는 제1유입부 및 상기 제1유입부와 이웃하여 설치되고 상기 제2덕트부로부터 상대적으로 먼 위치에 설치되는 제2유입부를 포함할 수 있다.The exhaust gas purifying apparatus according to the spirit of the present invention for solving the above problems is formed on the bottom surface of the first duct, the first duct to guide the exhaust gas containing foreign matter in the first direction, A foreign matter accommodating part for accommodating foreign matter contained therein, and a second duct part communicating with a purge gas outlet formed at a side surface of the first duct part and guiding the purge gas from which the foreign matter is separated in a second direction, and the inside of the first duct part. And a first baffle installed to protrude from the first duct part such that the air flow direction of the exhaust gas flowing into the first duct part is suddenly changed in a second direction of the second duct part direction. The first inlet part installed at a position relatively close to the second duct part and the second inlet part installed adjacent to the first inlet part and installed at a position relatively far from the second duct part. It can hamhal.
상기 제1배플은, 선단이 상기 이물질 수용부를 향하여 수평면을 기준으로 아래로 제1하향각도로 경사지게 돌출되고 후단이 상기 정화 가스 배출구의 상방에 고정되는 것일 수 있다. The first baffle may have a front end protruding obliquely downward at a first downward angle with respect to the foreign substance accommodating part and a rear end fixed above the purge gas outlet.
상기 제1하향각도는, 30도 내지 50도일 수 있다.The first downward angle may be 30 degrees to 50 degrees.
상기 제1배플은, 상기 이물질 수용부 방향으로 경사지게 돌출된 제1돌출길이가 상기 정화 가스 배출구의 연결지점에서부터 상기 이물질 수용부 상의 제1연장지점까지의 제1지향거리에 33퍼센트 내지 42퍼센트 이상일 수 있다.The first baffle may have a first protrusion length protruding obliquely toward the foreign substance accommodating portion at least 33 percent to 42 percent at a first orientation distance from a connection point of the purge gas outlet to a first extension point on the foreign substance accommodating portion. Can be.
상기 제2덕트부는, 상기 정화 가스가 배출되는 유로의 높이인 유로높이를 갖고, 상기 제1지향거리에서 상기 제1돌출길이를 차감한 제1통과거리는 상기 유로높이 이상일 수 있다.The second duct portion may have a flow path height that is a height of a flow path through which the purge gas is discharged, and a first pass distance obtained by subtracting the first protrusion length from the first direction distance may be equal to or greater than the flow path height.
상기 제1덕트부는, 상기 제1유입부와 상기 제2유입부를 분할할 수 있는 분리벽을 더 포함할 수 있다.The first duct unit may further include a partition wall that divides the first inlet unit and the second inlet unit.
상기 제1유입부의 내부로 돌출되게 설치되고, 상기 제1유입부로 유입된 배출 가스의 기류 방향이 제2덕트부 방향의 제2방향으로 급격하게 변화되도록 유도하는 제2배플을 더 포함할 수 있다.It may further include a second baffle installed to protrude into the first inlet, and to induce a rapid change in the air flow direction of the exhaust gas introduced into the first inlet to a second direction of the second duct part. .
상기 제2배플은, 선단이 상기 이물질 수용부를 향하여 수평면을 기준으로 아래로 제2하향각도로 경사지게 돌출되고 후단이 상기 분리벽의 하단부에 고정되는 것일 수 있다.The second baffle may have a front end protruding obliquely downward at a second downward angle with respect to the foreign substance accommodating part and a rear end fixed to a lower end of the separation wall.
상기 제2하향각도는, 30도 내지 50도일 수 있다.The second downward angle may be 30 degrees to 50 degrees.
상기 제2배플은, 상기 이물질 수용부 방향으로 경사지게 돌출된 제2돌출길이가 상기 분리벽의 연결지점에서부터 상기 이물질 수용부 상의 제2연장지점까지의 제2지향거리에 33퍼센트 내지 42퍼센트 이상일 수 있다.The second baffle may have a second protrusion length protruding obliquely toward the foreign substance accommodating portion at a second direction distance from a connection point of the separation wall to a second extension point on the foreign substance accommodating portion. have.
상기 이물질 수용부는, 아래로 오목한 깔때기 형상의 호퍼이고, 상기 제1덕트부와 상기 이물질 수용부 사이에 그 표면이 평면을 이루는 유도 평면부가 형성되는 것일 수 있다.The foreign matter receiving portion may be a funnel-shaped hopper recessed downward, and an induction plane portion having a flat surface may be formed between the first duct portion and the foreign matter receiving portion.
상기한 바와 같이 이루어진 본 발명의 실시예에 따르면, 배출 가스 정화 장치는 배출 가스의 급격한 기류의 방향변화를 통해 배출 가스에 포함된 이물질을 이물질 수용부로 분리시키는 분리 성능을 향상시킬 수 있다.According to the embodiment of the present invention made as described above, the exhaust gas purification apparatus can improve the separation performance of separating the foreign matter contained in the exhaust gas to the foreign matter receiving portion through the rapid change in the direction of the air flow of the exhaust gas.
또한, 여러 위치에서 흡기된 배출 가스들을 하나의 장치를 사용하여 정화할 수 있으며, 배플의 각도나 길이를 변화할 뿐 별도의 장치나 제작 방법의 변화를 주지 않고 효율을 높일 수 있어 설비 또는 제작이 용이한 효과를 가질 수 있다. 물론 이러한 효과에 의해 본 발명의 범위가 한정되는 것은 아니다.In addition, it is possible to purify the exhaust gases intake at various locations using a single device, and to change the angle or length of the baffle, and to increase the efficiency without changing a separate device or manufacturing method, so that the equipment or the production is easy. It can have an easy effect. Of course, the scope of the present invention is not limited by these effects.
도 1은 본 발명의 일 실시예에 따른 배출 가스 정화 장치를 나타내는 사시도이다.1 is a perspective view showing an exhaust gas purification apparatus according to an embodiment of the present invention.
도 2 내지 도 7은 본 발명의 여러 실시예들에 따른 배출 가스 정화 장치를 나타내는 도면들이다.2 to 7 are views illustrating an exhaust gas purification apparatus according to various embodiments of the present invention.
도 8은 도 1의 배출 가스 정화 장치를 나타내는 작동 상태도이다.8 is an operational state diagram showing the exhaust gas purification apparatus of FIG. 1.
도 9는 도 2의 배출 가스 정화 장치의 배플 각도에 따른 이물질 제거율과 압력차를 나타내는 비교표이다.FIG. 9 is a comparison table illustrating a foreign matter removal rate and a pressure difference according to the baffle angle of the exhaust gas purifying apparatus of FIG. 2.
도 10은 도 3의 배출 가스 정화 장치의 배플 길이에 따른 이물질 제거율과 압력차를 나타내는 비교표이다.FIG. 10 is a comparison table illustrating a foreign matter removal rate and a pressure difference according to the baffle length of the exhaust gas purifying apparatus of FIG. 3.
본 발명의 실시예들은 당해 기술 분야에서 통상의 지식을 가진 자에게 본 발명을 더욱 완전하게 설명하기 위하여 제공되는 것이며, 하기 실시예는 여러 가지 다른 형태로 변형될 수 있으며, 본 발명의 범위가 하기 실시예에 한정되는 것은 아니다. 오히려 이들 실시예들은 본 개시를 더욱 충실하고 완전하게 하고, 당업자에게 본 발명의 사상을 완전하게 전달하기 위하여 제공되는 것이다. 또한, 도면에서 각 층의 두께나 크기는 설명의 편의 및 명확성을 위하여 과장된 것이다.The embodiments of the present invention are provided to more fully explain the present invention to those skilled in the art, and the following examples can be modified in various other forms, and the scope of the present invention is It is not limited to an Example. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the invention to those skilled in the art. In addition, the thickness or size of each layer in the drawings is exaggerated for convenience and clarity of description.
도 1은 본 발명의 일 실시예에 따른 배출 가스 정화 장치(100)를 나타내는 사시도이다.1 is a perspective view showing an exhaust gas purification apparatus 100 according to an embodiment of the present invention.
도 1에 도시된 바와 같이, 제1덕트부(10), 제2덕트부(20), 이물질 수용부(30), 제1배플(40)을 포함할 수 있다.As shown in FIG. 1, the first duct part 10, the second duct part 20, the foreign substance accommodating part 30, and the first baffle 40 may be included.
도 1에 도시된 바와 같이, 제1덕트부(10)는 이물질(1)이 포함된 배출 가스(G1)를 제1방향으로 유도할 수 있도록 형성될 수 있다. 예를 들면, 제1덕트부(10)는 연소 후 발생되는 분말이나 고형물 형태의 재(Ash)나 미연소된 상태의 연료 물질이나 타지 않는 불연물질이나 질소 결합물, 탄소 결합물 등의 이물질(1)이 포함된 배출 가스(G1)를 제1방향(도 1의 하방)으로 유도하는 것으로서, 제1덕트부(10)는 사각통 형상인 것이나 이외에도 원통, 파이프 형상 등 다양하게 덕트 형상으로 형성될 수 있다.As illustrated in FIG. 1, the first duct part 10 may be formed to guide the discharge gas G1 including the foreign matter 1 in the first direction. For example, the first duct unit 10 may be ash or ash in the form of powder or solids generated after combustion, fuel materials in an unburned state, non-burning incombustibles, nitrogen compounds, carbon bonds, or the like. Inducing the discharge gas (G1) containing the 1) in the first direction (downward in Figure 1), the first duct portion 10 is formed in a variety of ducts, such as a cylindrical or pipe, in addition to a rectangular cylindrical shape Can be.
도 1에 도시된 바와 같이, 제1덕트부(10)는 제2덕트부(20)로부터 상대적으로 가까운 위치에 설치되는 제1유입부(11) 및 제1유입부(11)와 이웃하여 설치되고 제2덕트부(20)로부터 상대적으로 먼 위치에 설치되는 제2유입부(12)를 포함할 수 있다. 예컨대. 제1덕트부(10)는 제1유입부(11)와 제2유입부(12)를 분할할 수 있는 분리벽(50)을 더 포함할 수 있다.As shown in FIG. 1, the first duct part 10 is installed adjacent to the first inlet part 11 and the first inlet part 11 which are installed at a relatively close position from the second duct part 20. And a second inflow portion 12 installed at a position relatively far from the second duct portion 20. for example. The first duct part 10 may further include a separation wall 50 capable of dividing the first inlet part 11 and the second inlet part 12.
예컨대, 도 1에 도시된 바와 같이, 제1덕트부(10)는 서로 다른 위치에서 연결된 덕트들이 결합되어 형성된 것일 수 있으며, 이물질(1)을 더욱 효율적으로 정화할 수 있도록 하나의 덕트를 분리한 것일 수도 있다.For example, as illustrated in FIG. 1, the first duct part 10 may be formed by combining ducts connected at different positions, and may separate one duct to purify the foreign matter 1 more efficiently. It may be.
도 1에 도시된 바와 같이, 분리벽(50)은 덕트들이 결합되어 형성되거나, 또는, 덕트를 분리하기 위하여 설치될 수 있다. 분리벽(50)은 판형상으로 설치될 수 있고, 유입된 배출 가스(G1)이 유입되는 압력을 높이기 위하여 가로로 길게 뻗은 다각기둥 형상으로 설치될 수 있다. 예컨대, 도 1에 도시된 바와 같이, 분리벽(50)이 가로로 누운 오각기둥 형상으로 설치되어 배출 가스(G1)가 유입되는 제1유입부(11) 및 제2유입부(12)의 상부에 형성된 유입관 보다 하부에 형성된 유입부가 더욱 좁아 유입되는 배출 가스(G1)의 압력이 더욱 높을 수 있다. 그리하여, 유입된 배출 가스(G1)는 보다 넓은 이물질 수용부(30)에서 급격하게 낮아진 압력으로 인하여 이물질(1)이 급격하게 느려진 유속과 중력에 의하여 운동량을 잃어 이물질 수용부(30)로 정화될 수 있다.As shown in FIG. 1, the dividing wall 50 may be formed by combining ducts or may be installed to separate the ducts. The dividing wall 50 may be installed in a plate shape, and may be installed in a polygonal column shape that extends in the horizontal direction in order to increase the pressure into which the introduced discharge gas G1 flows. For example, as shown in FIG. 1, an upper wall of the first inlet part 11 and the second inlet part 12 in which the separation wall 50 is horizontally laid in a pentagonal column shape and into which the exhaust gas G1 flows is introduced. The inlet portion formed in the lower portion than the inlet tube formed in the narrower the pressure of the inlet gas (G1) may be higher. Thus, the introduced exhaust gas G1 loses momentum due to the rapidly slowed flow rate and gravity due to the sharply lowered pressure in the wider foreign matter accommodating part 30, and thus is purified by the foreign substance accommodating part 30. Can be.
도 1에 도시된 바와 같이, 제1유입부(11)는 제2덕트부(20)에서 가까운 위치에 설치될 수 있고, 제1유입부(11)에서 유입된 배출 가스(G1)는 보다 빨리 제2덕트부(20)로 유출될 수 있으나 후술될 분리벽으로 인하여 기류의 방향이 바뀌어 제2덕트부(20)로 유출될 수 있다.As shown in FIG. 1, the first inlet 11 may be installed at a position close to the second duct 20, and the exhaust gas G1 introduced from the first inlet 11 may be faster. Although it may flow out to the second duct part 20, the direction of airflow may be changed due to the separation wall to be described later, and thus may flow out to the second duct part 20.
도 1에 도시된 바와 같이, 제2유입부(12)는 제2덕트부(20)에서 제1유입부(11) 보다 상대적으로 먼 위치에 설치될 수 있고, 제2유입부(12)에서 유입된 배출 가스(G1)는 제1유입부에서 유입된 배출 가스(G1) 보다 상대적으로 느리게 제2덕트부(20)로 유출될 수 있으나 후술될 분리벽으로 인하여 관성 또는 원심력에 의하여 정화되어 제2덕트부(20)로 유출될 수 있다.As shown in FIG. 1, the second inflow portion 12 may be installed at a position relatively far from the first inflow portion 11 in the second duct portion 20, and in the second inflow portion 12. The introduced discharge gas G1 may flow out to the second duct part 20 relatively slower than the discharge gas G1 introduced from the first inlet part, but may be purified by inertia or centrifugal force due to the separation wall to be described later. It may flow out to the two duct portion 20.
이외에도 도시되지 않았지만, 제1유입부(11), 제2유입부(12) 이외에도 서로 다른 위치에서 연결된 복수개의 덕트들이 결합되어 형성될 수 있다.Although not shown in addition, in addition to the first inlet 11 and the second inlet 12 may be formed by combining a plurality of ducts connected at different positions.
도 1에 도시된 바와 같이, 제2덕트부(20)는 제1덕트부(10)의 측면에 형성되는 정화 가스 배출구(H)와 연통되고, 이물질(1)이 분리된 정화 가스(G2)를 제2방향(도 1의 후방)으로 유도할 수 있다. 예컨대, 제2덕트부(20)는 사각통 형상인 것이나 이외에도 원통, 파이프 형상 등 다양하게 형성될 수 있다.As illustrated in FIG. 1, the second duct part 20 communicates with a purification gas outlet H formed at a side surface of the first duct part 10, and the purification gas G2 having the foreign matter 1 separated therefrom. Can be derived in the second direction (rear of FIG. 1). For example, the second duct portion 20 may be formed in various shapes such as a cylinder or a pipe in addition to the rectangular cylinder shape.
여기서, 상기 제2방향은 제1덕트부(10)를 통해 유입되는 배출 가스(G1)를 최종적으로 외부로 배출하기 전에 배출 가스(G1)의 유해한 성분을 처리하기 위한 처리장치로 유입되는 방향일 수 있다. 이때 상기 처리장치는 선택적 촉매 환원 설비일 수 있으며, 상기 제2방향으로 유입된 배출 가스(G1)는 선택적 촉매 환원 설비를 구성하는 촉매층으로 유도될 수 있다. Here, the second direction is a direction flowing into the processing apparatus for treating harmful components of the exhaust gas G1 before finally discharging the discharge gas G1 introduced through the first duct part 10 to the outside. Can be. In this case, the treatment apparatus may be a selective catalytic reduction facility, and the exhaust gas G1 introduced into the second direction may be directed to a catalyst layer constituting the selective catalytic reduction facility.
도 1에 도시된 바와 같이, 이물질 수용부(30)는 제1덕트부(10)의 저면에 형성되고, 상기 제1방향으로 유도되어 낙하된 배출 가스(G1)에 포함된 이물질(1)을 수용할 수 있다. 이물질 수용부(30)는, 이물질(1)들이 하방으로 적층되도록 아래로 오목한 깔때기 형상의 호퍼(hopper)일 수 있다.As illustrated in FIG. 1, the foreign matter accommodating part 30 is formed on the bottom surface of the first duct part 10, and the foreign matter 1 included in the discharge gas G1 guided in the first direction and dropped. I can accept it. The foreign material accommodating part 30 may be a funnel-shaped hopper recessed downward so that the foreign materials 1 are stacked downward.
도 1에 도시된 바와 같이, 제1배플(40)은 제1덕트부(10)의 내부로 돌출되게 설치되고, 제1덕트부(10)로 유입된 배출 가스(G1)의 기류 방향이 제2덕트부 방향의 제2방향으로 급격하게 변화되도록 유도할 수 있다.As shown in FIG. 1, the first baffle 40 is installed to protrude into the first duct part 10, and the air flow direction of the discharge gas G1 introduced into the first duct part 10 is set to the first baffle 40. It can be induced to change rapidly in the second direction of the two duct portion direction.
도 1에 도시된 바와 같이, 제1배플(40)은 제1덕트부(10)의 배출 가스(G1)가 이물질 수용부(30)를 거쳐서 제2덕트부(20)로 방향 전환 될 수 있도록 제1덕트부(10)의 내부로 돌출되게 설치될 수 있다. 또한, 제1배플(40)은 배출 가스(G1)의 방향 전환을 촉진하기 위하여 둥근 표면이 형성될 수도 있으나 반드시 이에 한정되지는 않는다.As shown in FIG. 1, the first baffle 40 may allow the exhaust gas G1 of the first duct part 10 to be diverted to the second duct part 20 via the foreign matter accommodating part 30. It may be installed to protrude into the first duct portion 10. In addition, the first baffle 40 may be formed to have a rounded surface to promote the change of direction of the exhaust gas (G1), but is not necessarily limited thereto.
도 1에 도시된 바와 같이, 제1배플(40)은 선단이 이물질 수용부(30)를 향하여 수평면을 기준으로 아래로 제1하향각도(A1)로 경사지게 돌출되고 후단이 정화 가스 배출구(H)의 상방에 고정되는 것일 수 있다.As shown in FIG. 1, the first baffle 40 protrudes inclined at a first downward angle A1 downward with respect to a horizontal surface toward the foreign substance accommodating portion 30 and the rear end thereof is a purge gas discharge hole H. It may be fixed above.
도 1에 도시된 바와 같이, 제1배플(40)은 제1덕트부(10)를 통해 상기 제1방향으로 유입된 배출 가스(G1)의 방향을 제2덕트부(20) 방향으로 급격하게 변화되도록 유도할 수 있다. 즉, 제1덕트부(10)를 통하여 유입된 배출 가스(G1)는 상기 제1방향(도 1의 하방)으로 유입된 후 제1배플(40)에 의해 기류의 방향이 제2덕트부(20)로의 방향인 상기 제2방향으로 급격하게 전환될 수 있다. 이러한 급격한 기류의 방향 전환이 발생될 때 배출 가스(G1)에 포함되어 있는 소정의 질량을 가진 이물질(1)은 관성(혹은 원심력)에 의하여 상기 제1방향으로 계속 이동하려는 경향을 가지며, 이러한 급격한 기류방향의 전환에 대응하지 못하고 이물질 수용부(30)쪽으로 이동됨에 따라 배출 가스(G1)로부터 분리될 수 있다.As shown in FIG. 1, the first baffle 40 sharply changes the direction of the discharge gas G1 introduced into the first direction through the first duct part 10 toward the second duct part 20. It can be induced to change. That is, the exhaust gas G1 introduced through the first duct part 10 flows in the first direction (downward in FIG. 1), and then the direction of the air flow is changed by the first duct baffle 40. 20 may be abruptly switched to the second direction. When such a sudden change of direction of the airflow occurs, the foreign matter 1 having a predetermined mass contained in the exhaust gas G1 tends to continue to move in the first direction by inertia (or centrifugal force). As it does not correspond to the change in the air flow direction is moved toward the foreign matter receiving portion 30 may be separated from the exhaust gas (G1).
그러므로, 제1배플(40)에 의해 유도된 급격한 기류의 변화에 의해 대부분의 이물질(1)은 이물질 수용부(30)에 수용될 수 있고, 제2덕트부(20)로는 이물질(1)이 제거되어 정화된 정화 가스(G2)만 외부로 배출될 수 있다.Therefore, most of the foreign matter 1 can be accommodated in the foreign matter accommodating portion 30 by the sudden change of air flow induced by the first baffle 40, and the foreign matter 1 is transferred to the second duct portion 20. Only the purged gas G2 that has been removed and purified may be discharged to the outside.
도 2 내지 도 7은 본 발명의 여러 실시예들에 따른 배출 가스 정화 장치(200, 300, 400, 500, 600, 700)를 나타내는 도면들이다.2 to 7 are views illustrating exhaust gas purifying apparatuses 200, 300, 400, 500, 600, and 700 according to various embodiments of the present disclosure.
도 2에 도시된 바와 같이, 본 발명의 다른 실시예에 따른 배출 가스 정화 장치(200)의 제1배플(40)은 정화 가스 배출구(H)의 상방에 고정되어 이물질 수용부(30)를 향하여 수평면을 기준으로 아래로 경사지게 설치될 수 있다. 예컨대, 제1배플(40)은 제1덕트부(10)에서 유입된 배출 가스(G1)를 제2덕트부(20)로 배출할 수 있도록 제1덕트부(10)에서 배출 가스(G1)의 유입을 방해하지 않으며, 제2덕트부(20)에서 정화 가스(G2)의 배출을 방해하지 않도록 설치될 수 있고, 수평면을 기준으로 제1하향각도(A1)로 경사지게 설치하여 정화효율을 최대한으로 높일 수 있다. 예컨대, 제1하향각도(A1)가 일정 각도 이상이 되거나 또는 이하가 될 경우에 유입구는 넓어지고 배출구는 좁아져 유입구와 배출구의 압력차이가 너무 커지게 되며 정화 효율이 낮아질 수 있으며, 이에 따라, 제1하향각도(A1)는 30도 내지 50도일 수 있다.As shown in FIG. 2, the first baffle 40 of the exhaust gas purification apparatus 200 according to another embodiment of the present invention is fixed above the purification gas outlet H to face the foreign matter accommodating part 30. It may be installed to be inclined downward with respect to the horizontal plane. For example, the first baffle 40 discharges the discharge gas G1 introduced from the first duct unit 10 to the second duct unit 20 so as to discharge the discharge gas G1 from the first duct unit 10. It does not interfere with the inflow of, and may be installed so as not to interfere with the discharge of the purification gas (G2) in the second duct portion 20, inclined at a first downward angle (A1) relative to the horizontal plane to maximize the purification efficiency. Can be increased with For example, when the first downward angle A1 becomes greater than or equal to a certain angle or less, the inlet becomes wider and the outlet becomes narrower so that the pressure difference between the inlet and the outlet becomes too large and the purification efficiency can be lowered. The first downward angle A1 may be 30 degrees to 50 degrees.
도 3에 도시된 바와 같이, 본 발명의 다른 실시예에 따른 배출 가스 정화 장치(300)의 제1배플(40)은 소정거리 돌출되어 설치될 수 있다. 예컨대, 제1배플(40)의 이물질 수용부(30) 방향으로 경사지게 돌출된 길이는 제1돌출길이(B1)일 수 있다. 또한, 이물질 수용부(30) 상에 위치한 제1배플(40)의 가상 연장점은 제1연장지점(41)일 수 있으며, 제1배플(40)과 정화 가스 배출구(H)의 연결지점에서부터 제1연장지점(41)까지의 거리는 제1지향거리(C1)일 수 있다.As shown in FIG. 3, the first baffle 40 of the exhaust gas purification apparatus 300 according to another embodiment of the present invention may be installed to protrude a predetermined distance. For example, the length of the first baffle 40 protruding obliquely toward the foreign substance accommodating part 30 may be the first protrusion length B1. In addition, the virtual extension point of the first baffle 40 located on the foreign matter receiving portion 30 may be a first extension point 41, from a connection point of the first baffle 40 and the purge gas outlet H. The distance to the first extension point 41 may be a first direction distance C1.
도 3에 도시된 바와 같이, 제1배플(40)은 정화효율을 최대화할 수 있도록 제1돌출길이(B1)가 제1지향거리(C1)의 33퍼센트 내지 42퍼센트 이상일 수 있다. 예컨대, 제1돌출길이(B1)가 너무 길어지면 유입구와 배출구가 좁아지며 이물질(1)의 배출이 느려지고 정화효율이 낮아질 수 있으며, 제1돌출길이(B1)가 너무 짧아지면 이물질(1)의 회전력이 낮아져 정화효율이 낮아질 수 있다.As illustrated in FIG. 3, the first baffle 40 may have a first protrusion length B1 of 33% to 42% or more of the first direction distance C1 to maximize the purification efficiency. For example, if the first protrusion length B1 is too long, the inlet and outlet may be narrowed, the discharge of the foreign matter 1 may be slowed down, and the purification efficiency may be lowered. If the first protrusion length B1 is too short, the foreign matter 1 may be reduced. As the rotational force is lowered, the purification efficiency may be lowered.
도 3에 도시된 바와 같이, 제2덕트부(20)는 유로높이(E)를 포함할 수 있으며, 제1덕트부(10)에서 유입된 배출 가스(G1)가 유입되어 제1배플(40)을 통과할 때의 거리는 유로높이(E) 이상일 수 있다. 예컨대, 제1지향거리(C1)에서 제1돌출길이(B1)를 차감한 제1통과거리(D1)는 유로높이(E) 이상일 수 있다.As shown in FIG. 3, the second duct part 20 may include a flow path height E, and the discharge gas G1 introduced from the first duct part 10 is introduced to allow the first baffle 40 to flow. The distance when passing through) may be greater than or equal to the channel height E. For example, the first passing distance D1 obtained by subtracting the first protrusion length B1 from the first direction distance C1 may be greater than or equal to the flow path height E.
즉, 제1돌출길이(B1)는 제1덕트부(10)에서 유입된 배출 가스(G1)가 통과하는 제1통과거리(D1)가 제2덕트부(20)에 형성된 유로높이(E) 이상일 수 있도록 형성되어 정화효율을 최대한으로 높일 수 있다.That is, the first protrusion length B1 has a flow path height E in which the first passage distance D1 through which the discharge gas G1 introduced from the first duct part 10 passes passes is formed in the second duct part 20. It can be formed so that it can be improved to the maximum purification efficiency.
도 4에 도시된 바와 같이, 본 발명의 다른 실시예에 따른 배출 가스 정화 장치(400)는 제1유입부(11)의 내부로 돌출되게 설치되고, 제1유입부(11)로 유입된 배출 가스(G1)의 기류 방향이 제2덕트부(20) 방향의 제2방향으로 급격하게 변화되도록 유도하는 제2배플(60)을 더 포함할 수 있다. As shown in FIG. 4, the exhaust gas purifying apparatus 400 according to another embodiment of the present invention is installed to protrude into the first inlet 11, and discharges introduced into the first inlet 11. The air flow direction of the gas G1 may further include a second baffle 60 to induce a rapid change in a second direction in the direction of the second duct part 20.
도 4에 도시된 바와 같이, 제2배플(60)은 분리벽(50)의 하부에 고정되어 이물질 수용부(30)를 향하여 수평면을 기준으로 아래로 경사지게 설치될 수 있다. 예컨대, 제2배플(60)은 제1덕트부(10)에서 유입된 배출 가스(G1)를 제2덕트부(20)로 배출할 수 있도록 제1덕트부(10)에서 배출 가스(G1)의 유입을 방해하지 않으며, 제2덕트부(20)에서 정화 가스(G2)의 배출을 방해하지 않도록 설치될 수 있고, 수평면을 기준으로 제2하향각도(A2)로 경사지게 설치하여 정화효율을 최대한으로 높일 수 있다. 예컨대, 제2하향각도(A2)가 일정 각도 이상이 되거나 또는 이하가 될 경우에 유입구는 넓어지고 배출구는 좁아져 유입구와 배출구의 압력차이가 너무 커지게 되며 정화 효율이 낮아질 수 있으며, 이에 따라, 제2하향각도(A2)는 30도 내지 50도일 수 있다.As shown in FIG. 4, the second baffle 60 may be fixed to the lower portion of the separation wall 50 and be inclined downward based on a horizontal plane toward the foreign substance accommodating part 30. For example, the second baffle 60 discharges gas G1 from the first duct part 10 to discharge the discharge gas G1 introduced from the first duct part 10 to the second duct part 20. It does not interfere with the inflow of, can be installed so as not to interfere with the discharge of the purge gas (G2) in the second duct portion 20, inclined at a second downward angle (A2) relative to the horizontal plane to maximize the purification efficiency Can be increased with For example, when the second downward angle A2 becomes greater than or equal to a certain angle or less, the inlet becomes wider and the outlet becomes narrower, so that the pressure difference between the inlet and the outlet becomes too large and the purification efficiency can be lowered. The second downward angle A2 may be 30 degrees to 50 degrees.
도 6에 도시된 바와 같이, 본 발명의 다른 실시예에 따른 배출 가스 정화 장치(600)의 제2배플(60)은 소정거리 돌출되어 설치될 수 있다. 예컨대, 제2배플(60)의 이물질 수용부(30) 방향으로 경사지게 돌출된 길이는 제2돌출길이(B2)일 수 있다. 또한, 이물질 수용부(30) 상에 위치한 제2배플(60)의 가상 연장점은 제2연장지점(42)일 수 있으며, 제2배플(60)과 정화 가스 배출구(H)의 연결지점에서부터 제2연장지점(42)까지의 거리는 제2지향거리(C2)일 수 있다.As shown in FIG. 6, the second baffle 60 of the exhaust gas purification apparatus 600 according to another embodiment of the present invention may be installed to protrude a predetermined distance. For example, the length of the second baffle 60 protruding obliquely toward the foreign substance accommodating part 30 may be the second protrusion length B2. In addition, the virtual extension point of the second baffle 60 located on the foreign matter receiving portion 30 may be a second extension point 42, from the connection point of the second baffle 60 and the purge gas outlet H. The distance to the second extension point 42 may be a second direction distance C2.
도 6에 도시된 바와 같이, 제2배플(60)은 정화효율을 최대화할 수 있도록 제2돌출길이(B2)가 제2지향거리(C2)의 33퍼센트 내지 42퍼센트 이상일 수 있다. 예컨대, 제2돌출길이(B2)가 너무 길어지면 유입구와 배출구가 좁아지며 이물질(1)의 배출이 느려지고 정화효율이 낮아질 수 있으며, 제2돌출길이(B2)가 너무 짧아지면 이물질(1)의 회전력이 낮아져 정화효율이 낮아질 수 있다.As shown in FIG. 6, the second baffle 60 may have a second protrusion length B2 of 33% to 42% or more of the second direction distance C2 to maximize the purification efficiency. For example, if the second protrusion length B2 is too long, the inlet and outlet ports are narrowed, the discharge of the foreign matter 1 may be slowed down, and the purification efficiency may be lowered. If the second protrusion length B2 is too short, the foreign matter 1 may be As the rotational force is lowered, the purification efficiency may be lowered.
도 7에 도시된 바와 같이, 본 발명의 다른 실시예에 따른 배출 가스 정화 장치(700)의 이물질 수용부(30)는 아래로 오목한 깔때기 형상의 호퍼이고, 제1덕트부(10)와 이물질 수용부(30) 사이에 그 표면이 평면을 이루는 유도 평면부(70)가 형성되는 것일 수 있다.As illustrated in FIG. 7, the foreign matter receiving portion 30 of the exhaust gas purifying apparatus 700 according to another embodiment of the present invention is a funnel-shaped hopper recessed downward, and the first duct portion 10 and the foreign matter receiving portion. Induction plane portion 70 whose surface is a plane between the portions 30 may be formed.
도 7에 도시된 바와 같이, 유도 평면부(70)는 기류 방향이 급격하게 변화되도록 상기 제1방향과 다른 방향으로 유도하는 것으로서, 특히 일종의 경사면을 형성하여 급격한 와류를 더욱 쉽게 유도할 수 있다. 유도 평면부(70)는 이물질 수용부(30)에서 유속이 현저하게 떨어지는 대신, 유도 평면부(70) 및 상기 배플(40, 60)에 의해 빠른 유속의 급격한 와류가 발생되면서 이물질(1)이 원심력에 의해 이물질 수용부(30) 방향으로 낙하될 수 있다.As shown in FIG. 7, the induction plane 70 is guided in a direction different from the first direction so that the airflow direction is rapidly changed, and in particular, a kind of inclined surface may be formed to more easily induce a rapid vortex. The induction plane portion 70 has a significant drop in the flow rate at the foreign matter accommodating portion 30, but instead of the induction plane portion 70 and the baffles 40 and 60, a rapid vortex of rapid flow rate is generated and the foreign matter 1 is By the centrifugal force it may fall in the direction of the foreign matter receiving portion (30).
반면에, 유도 평면부(70)는 곡면으로 형성되어 제1배플(40)로부터 유도 평면부(70)에 이르는 거리에 비해 더 길어지게 되고 이러한 거리의 차이만큼 제1배플(40)의 길이가 더 길게 형성될 수 있으며, 제1배플(40)의 길이가 더 길어질 경우에는 제1배플(40)에 의한 기류의 방향전환 효과를 증진시킬 수 있다.On the other hand, the induction plane portion 70 is formed in a curved surface is longer than the distance from the first baffle 40 to the induction plane portion 70 and the length of the first baffle 40 by the difference in distance It may be formed longer, and when the length of the first baffle 40 is longer, it is possible to enhance the direction change effect of the air flow by the first baffle 40.
도 8은 도 1의 배출 가스 정화 장치(100)를 나타내는 작동 상태도이다.8 is an operating state diagram illustrating the exhaust gas purification apparatus 100 of FIG. 1.
도 8에 도시된 바와 같이, 배출 가스 정화 장치(100)는 제1유입부(11) 및 제2유입부(12)를 포함하는 제1덕트부(10)에서 배출 가스(G1)를 상기 제1방향으로 유도하여, 제1덕트부(10)를 통하여 제1배플(40)에 의해 기류의 방향이 제2덕트부(20) 방향인 상기 제2방향으로 급격하게 전환될 수 있다.As illustrated in FIG. 8, the exhaust gas purifying apparatus 100 extracts the exhaust gas G1 from the first duct part 10 including the first inlet part 11 and the second inlet part 12. Guided in one direction, the direction of the air flow by the first baffle 40 through the first duct portion 10 can be rapidly switched to the second direction of the second duct portion 20 direction.
이때, 이물질(1)은 깔때기 형상의 호퍼(hopper)인 이물질 수용부(30)로 적층되고, 제2덕트부(20)로 이물질(1)이 제거되어 정화된 정화 가스(G2)만 외부로 배출될 수 있다.At this time, the foreign matter 1 is stacked in the foreign matter receiving portion 30, which is a funnel-shaped hopper, and the foreign matter 1 is removed by the second duct portion 20 to purify only the purified gas G2 to the outside. May be discharged.
이하, 본 발명의 이해를 돕기 위해서 상술한 기술적 사상을 적용한 실험예를 설명한다. 다만, 하기의 실험예는 본 발명의 이해를 돕기 위한 것일 뿐, 본 발명이 아래의 실험예에 의해서 한정되는 것은 아니다. Hereinafter, an experimental example to which the above-described technical concept is applied will be described to help understanding of the present invention. However, the following experimental examples are only for helping understanding of the present invention, and the present invention is not limited to the following experimental examples.
[실험예]Experimental Example
본 실험은 배플의 각도 변경에 따라 변화하는 이물질제거율을 확인하기 위하여 모든 해석 조건은 동일하고 배플의 각도 또는 배플의 길이의 변경에 따른 차이를 확인 하였다.In this experiment, all the analysis conditions were the same and the difference according to the change of the baffle angle or the length of the baffle was confirmed in order to confirm the removal rate of the foreign material that changes with the angle change of the baffle.
도 9는 제1실험에 대한 해석 결과이다.9 is an analysis result of the first experiment.
제1실험은 상기 배플의 각도에 따른 유속 및 압력의 변화를 실험하였으며, 상기 배플의 각도는 수평면을 기준으로 30도, 38도, 45도, 60도 및 75도 이다. 제1실험에서 배플의 각도가 30도인 실험은 Type1, 38도는 Type2, 45도는 Type3, 60도는 Type4 및 75도는 Type5이다.In the first experiment, the flow velocity and the pressure were changed according to the angle of the baffle, and the angle of the baffle was 30 degrees, 38 degrees, 45 degrees, 60 degrees, and 75 degrees with respect to the horizontal plane. In the first experiment, the baffle angle was 30 degrees, and Type1, 38 degrees were Type2, 45 degrees were Type3, 60 degrees were Type4, and 75 degrees were Type5.
[표 1]은 실험1에 대한 유입구와 배출구의 평균압력의 차이를 나타내는 표이다.[Table 1] is a table showing the difference between the average pressure of the inlet and outlet for Experiment 1.
압력(Pa)Pressure (Pa)
유입구Inlet 배출구outlet 유입구와 배출구의 압력차이Pressure difference between inlet and outlet
제1유입구Inlet 1 제2유입구2nd inlet 평균압력Average pressure
Type1(30도)Type1 (30 degrees) 28.528.5 226.5226.5 132.4132.4 -223.8-223.8 356.2356.2
Type2(38도)Type2 (38 degrees) 25.225.2 124.0124.0 7777 -225.8-225.8 302.8302.8
Type3(45도)Type3 (45 degrees) 22.222.2 71.671.6 48.148.1 -240.0-240.0 288.1288.1
Type4(60도)Type 4 (60 degrees) 22.822.8 10.210.2 16.216.2 -354.8-354.8 371.0371.0
Type5(75도)Type 5 (75 degrees) 18.718.7 0.20.2 99 -638.6-638.6 647.6647.6
상기 [표 1]에서 제1유입구는 배출구에서 먼 위치에 설치된 유입구이고, 제2유입구는 배출구에서 가까운 위치의 유입구이다.In Table 1, the first inlet is an inlet installed at a position far from the outlet, and the second inlet is an inlet at a position close to the outlet.
상기 [표 1]에 나타난 바와 같이, 유입구의 평균압력과 배출구의 압력은 Type1(30도)에서 Type5(75도)로 배플의 각도가 하향됨에 따라 감소하는 것을 확인할 수 있으나, 유입구와 배출구의 압력차이는 Type1(30도)에서 Type3(45도)까지 감소하다가 다시 증가하여 Type5(75도)에서 압력차이가 가장 큰 것으로 확인할 수 있다.As shown in [Table 1], it can be seen that the average pressure of the inlet and outlet pressure decreases as the angle of the baffle is lowered from Type 1 (30 degrees) to Type 5 (75 degrees), but the pressure of the inlet and outlet is reduced. The difference decreases from Type 1 (30 degrees) to Type 3 (45 degrees) and then increases again, indicating that the pressure difference is the largest in Type 5 (75 degrees).
이에 따라, 유입구와 배출구의 압력차이를 유지하기 위한 상기 배플의 각도가 존재하는 것을 확인할 수 있다.Accordingly, it can be seen that the angle of the baffle for maintaining the pressure difference between the inlet and outlet.
[표 2]은 실험1에 대한 이물질의 크기에 따른 제거율을 나타내는 표이다.[Table 2] is a table showing the removal rate according to the size of the foreign matter for Experiment 1.
제거율 (%)Removal rate (%)
100100 140140 200200 평균 제거율Average removal rate
제1유입구Inlet 1 제2유입구2nd inlet 제거율 Removal rate 제1유입구Inlet 1 제2유입구2nd inlet 제거율 Removal rate 제1유입구Inlet 1 제2유입구2nd inlet 제거율Removal rate
Type1(30도)Type1 (30 degrees) 85.585.5 78.978.9 82.182.1 91.691.6 89.989.9 90.790.7 93.593.5 95.395.3 94.494.4 90.290.2
Type2(38도)Type2 (38 degrees) 82.582.5 48.848.8 65.165.1 92.292.2 90.490.4 91.391.3 93.593.5 93.393.3 93.493.4 86.686.6
Type3(45도)Type3 (45 degrees) 82.182.1 14.514.5 47.247.2 92.392.3 88.988.9 90.590.5 93.793.7 92.792.7 93.293.2 82.582.5
Type4(60도)Type 4 (60 degrees) 79.779.7 0.20.2 38.638.6 91.491.4 22.222.2 55.655.6 98.998.9 98.998.9 98.998.9 66.766.7
Type5(75도)Type 5 (75 degrees) 72.272.2 0.00.0 34.934.9 94.094.0 0.70.7 45.845.8 99.199.1 37.637.6 67.467.4 50.950.9
상기 [표 2]에서 제1유입구는 배출구에서 먼 위치에 설치된 유입구이고, 제2유입구는 배출구에서 가까운 위치의 유입구이다.In Table 2, the first inlet is an inlet installed at a position far from the outlet, and the second inlet is an inlet at a position close to the outlet.
상기 [표 2]에 나타난 바와 같이, 이물질의 크기가 100㎛, 140㎛, 200㎛에서의 상기 배플 각도를 변화하여 제거율을 실험하였다. 이에 따라, 이물질 제거율은 Type1(30도)에서 Type5(75도)로 배플의 각도가 하향됨에 따라 감소하는 것을 확인할 수 있었으며, 평균적으로 Type1(30도)에서 Type3(45도)에서 전체 제거율이 70퍼센트 이상인 것을 확인할 수 있다.As shown in [Table 2], the removal rate was tested by changing the baffle angle at 100 μm, 140 μm, and 200 μm of foreign matters. Accordingly, it was confirmed that the removal rate of foreign matter decreased as the angle of the baffle was lowered from Type 1 (30 degrees) to Type 5 (75 degrees), and on average, the overall removal rate was 70 from Type 1 (30 degrees) to Type 3 (45 degrees). You can see that it is more than a percentage.
도 9는 도 2의 배출 가스 정화 장치(200)의 배플 각도에 따른 이물질 제거율과 압력차를 나타내는 비교표이다.FIG. 9 is a comparison table illustrating a foreign matter removal rate and a pressure difference according to the baffle angle of the exhaust gas purifying apparatus 200 of FIG. 2.
도 9에 도시된 바와 같이, 상기 배플의 각도가 Type1(30도)에서 Type5(75도)로 하향됨에 따라 유입구와 배출구의 압력차이(△P)는 증가하는 것을 확인할 수 있으며, 이물질의 크기가 100㎛, 140㎛ 및 200㎛에서의 제거율이 감소하는 것을 확인할 수 있다. 따라서, 상기 배플의 각도에 따른 유입구와 배출구의 압력의 차이가 낮게 나타고 이물질 제거율이 높은 상기 배플의 설치각도는 30도 내지 50도일 때 효과적이다.As shown in FIG. 9, as the angle of the baffle is lowered from Type 1 (30 degrees) to Type 5 (75 degrees), the pressure difference (ΔP) between the inlet and the outlet increases, and the size of the foreign matter is increased. It can be seen that the removal rates at 100 μm, 140 μm and 200 μm decrease. Therefore, the difference in pressure between the inlet and the outlet according to the angle of the baffle is low and the installation angle of the baffle having a high foreign matter removal rate is effective when the angle of 30 to 50 degrees.
도 10은 제2실험에 대한 해석 결과이다.10 is an analysis result of the second experiment.
제2실험은 상기 배플의 길이에 따른 유속 및 압력의 변화를 실험하였으며, 지향거리에 대한 상기 배플의 길이의 비율을 변화하여 실험하였다. 여기서, 상기 지향거리는 상기 배플과 정화 가스 배출구의 연결지점에서부터 상기 배플의 가상 연장지점까지의 거리이다. 상기 지향거리에 대한 상기 배플의 길이의 비율이 1:0.54인 실험은 Type6, 1:0.49는 Type7, 1:0.43은 Type8, 1:0.38은 Type9, 1:0.32는 Type10 및 1:0.27은 Type11이다.In the second experiment, the flow rate and the pressure were varied according to the length of the baffle, and the ratio of the length of the baffle to the directing distance was changed. Here, the directing distance is a distance from the connection point of the baffle and the purge gas outlet to the virtual extension point of the baffle. In the experiment where the ratio of the baffle length to the directing distance is 1: 0.54, Type6, 1: 0.49 is Type7, 1: 0.43 is Type8, 1: 0.38 is Type9, 1: 0.32 is Type10, and 1: 0.27 is Type11. .
[표 3]은 실험2에 대한 유입구와 배출구의 평균압력의 차이를 나타내는 표이다.[Table 3] is a table showing the difference between the average pressure of the inlet and the outlet for Experiment 2.
압력(Pa)Pressure (Pa)
유입구Inlet 배출구outlet 유입구와 배출구의 압력차이Pressure difference between inlet and outlet
제1유입구Inlet 1 제2유입구2nd inlet 평균압력Average pressure
Type6(1:0.54)Type 6 (1: 0.54) 28.528.5 226.5226.5 132.4132.4 -223.8-223.8 356.2356.2
Type7(1:0.49)Type7 (1: 0.49) 19.519.5 197.9197.9 113.1113.1 -191.7-191.7 304.8304.8
Type8(1:0.43)Type8 (1: 0.43) 14.914.9 152.4152.4 8787 -169.7-169.7 256.1256.1
Type9(1:0.38)Type9 (1: 0.38) 18.118.1 110.4110.4 66.566.5 -146-146 212.5212.5
Type10(1:0.32)Type10 (1: 0.32) 16.116.1 60.660.6 39.439.4 -130.7-130.7 170.1170.1
Type11(1:0.27)Type11 (1: 0.27) 16.916.9 22.522.5 19.919.9 -115.9-115.9 135.8135.8
상기 [표 3]에서 제1유입구는 배출구에서 먼 위치에 설치된 유입구이고, 제2유입구는 배출구에서 가까운 위치의 유입구이다.In Table 3, the first inlet is an inlet installed at a position far from the outlet, and the second inlet is an inlet at a position close to the outlet.
상기 [표 3]에 나타난 바와 같이, 유입구의 평균압력과 배출구의 압력은 Type6(1:0.54)에서 Type11(1:0.27)로 배플의 길이가 짧아짐에 따라 감소하는 것을 확인할 수 있으며, 유입구와 배출구의 압력차이도 Type6(1:0.54)에서 Type11(1:0.27)로 배플의 길이가 짧아짐에 따라 압력차이도 낮아지는 것을 확인할 수 있다.As shown in [Table 3], the average pressure of the inlet and the outlet pressure decrease as the length of the baffle is shortened from Type 6 (1: 0.54) to Type 11 (1: 0.27). It can be seen that the pressure difference is lowered as the baffle length becomes shorter from Type6 (1: 0.54) to Type11 (1: 0.27).
[표 4]은 실험1에 대한 이물질의 크기에 따른 제거율을 나타내는 표이다.[Table 4] is a table showing the removal rate according to the size of the foreign matter for Experiment 1.
제거율 (%)Removal rate (%)
100100 140140 200200
제1유입구 Inlet 1 제2유입구2nd inlet 제거1율1st removal rate 제1유입구Inlet 1 제2유입구2nd inlet 제거율 Removal rate 제1유입구Inlet 1 제2유입구2nd inlet 제거율Removal rate
Type6(1:0.54)Type 6 (1: 0.54) 85.585.5 78.978.9 82.182.1 91.691.6 89.989.9 90.790.7 93.593.5 95.395.3 94.494.4
Type7(1:0.49)Type7 (1: 0.49) 76.876.8 35.835.8 55.655.6 97.297.2 90.790.7 93.893.8 98.198.1 97.797.7 97.997.9
Type8(1:0.43)Type8 (1: 0.43) 56.856.8 0.00.0 27.527.5 93.893.8 55.755.7 74.174.1 97.897.8 96.996.9 97.397.3
Type9(1:0.38)Type9 (1: 0.38) 51.951.9 0.00.0 25.125.1 93.993.9 0.00.0 45.445.4 100.0100.0 85.885.8 92.792.7
Type10(1:0.32)Type10 (1: 0.32) 50.950.9 0.00.0 24.624.6 93.793.7 0.00.0 45.345.3 100.0100.0 8.78.7 52.952.9
Type11(1:0.27)Type11 (1: 0.27) 51.951.9 0.00.0 25.125.1 92.892.8 0.00.0 44.944.9 100.0100.0 0.00.0 48.448.4
상기 [표 4]에서 제1유입구는 배출구에서 먼 위치에 설치된 유입구이고, 제2유입구는 배출구에서 가까운 위치의 유입구이다.In Table 4, the first inlet is an inlet installed at a position far from the outlet, and the second inlet is an inlet at a position close to the outlet.
상기 [표 2]에 나타난 바와 같이, 이물질의 크기가 100㎛, 140㎛, 200㎛에서의 상기 배플의 길이를 변화하여 제거율을 실험하였다. 이에 따라, 이물질 제거율은 이물질의 크기가 100㎛일 때 Type6(1:0.54)에서 제거율이 가장 높은 것을 확인할 수 있다.As shown in [Table 2], the removal rate was tested by changing the length of the baffle in the size of the foreign matter 100㎛, 140㎛, 200㎛. Accordingly, the removal rate of the foreign matter can be confirmed that the removal rate is the highest in Type6 (1: 0.54) when the size of the foreign matter is 100㎛.
또한, 이물질의 크기가 200㎛일 때는 Type6(1:0.54), Type7(1:0.49), Type8(1:0.43) 및 Type9(1:0.38)에서 높은 제거율을 보였으며 상기 배플의 길이가 더 짧은 Type10(1:0.32) 및 Type11(1:0.27)에서는 비교적 낮은 제거율을 확인할 수 있다.In addition, when the size of the foreign matter was 200 μm, the removal rate was high in Type 6 (1: 0.54), Type 7 (1: 0.49), Type 8 (1: 0.43), and Type 9 (1: 0.38), and the length of the baffle was shorter. In Type 10 (1: 0.32) and Type 11 (1: 0.27), relatively low removal rates can be seen.
도 10은 도 3의 배출 가스 정화 장치(300)의 배플 길이에 따른 이물질 제거율과 압력차를 나타내는 비교표이다.FIG. 10 is a comparison table illustrating a foreign matter removal rate and a pressure difference according to the baffle length of the exhaust gas purification apparatus 300 of FIG. 3.
도 10에 도시된 바와 같이, 상기 배플의 길이가 Type6(1:0.54)에서 Type11(1:0.27)로 짧아짐에 따라 유입구와 배출구의 압력차이(△P)와 이물질의 크기가 100㎛, 140㎛ 및 200㎛에서의 제거율이 감소하는 것을 확인할 수 있다. As shown in FIG. 10, as the length of the baffle is shortened from Type 6 (1: 0.54) to Type 11 (1: 0.27), the pressure difference between the inlet and the outlet (ΔP) and the size of the foreign matter are 100 μm and 140 μm. And it can be confirmed that the removal rate at 200 μm is reduced.
이에 따라, 상기 배플의 길이가 짧아지면 상기 유입구와 상기 유출구의 압력차이는 감소하지만 제거율을 낮아지는 것을 확인할 수 있으며, 따라서, 상기 지향거리에 대한 상기 배플의 길이의 비율은 상기 유입구와 상기 유출구의 압력차이가 비교적 낮게 형성되면서 높은 이물질 제거율을 유지하도록 하기 위하여 1:0.38 이상으로 설치하여야 효과적이다.Accordingly, when the length of the baffle is shortened, it can be seen that the pressure difference between the inlet and the outlet decreases but the removal rate is lowered. Thus, the ratio of the length of the baffle to the directing distance is determined by the inlet and the outlet. It is effective to install more than 1: 0.38 in order to maintain a high foreign material removal rate while forming a relatively low pressure difference.
본 발명은 도면에 도시된 실시예를 참고로 설명되었으나 이는 예시적인 것에 불과하며, 당해 기술분야에서 통상의 지식을 가진 자라면 이로부터 다양한 변형 및 균등한 다른 실시예가 가능하다는 점을 이해할 것이다. 따라서 본 발명의 진정한 기술적 보호 범위는 첨부된 특허청구범위의 기술적 사상에 의하여 정해져야 할 것이다.Although the present invention has been described with reference to the embodiments shown in the drawings, this is merely exemplary, and those skilled in the art will understand that various modifications and equivalent other embodiments are possible. Therefore, the true technical protection scope of the present invention will be defined by the technical spirit of the appended claims.
상기한 바와 같이 이루어진 본 발명의 실시예에 따르면, 배출 가스 정화 장치는 배출 가스의 급격한 기류의 방향변화를 통해 배출 가스에 포함된 이물질을 이물질 수용부로 분리시키는 분리 성능을 향상시킬 수 있다.According to the embodiment of the present invention made as described above, the exhaust gas purification apparatus can improve the separation performance of separating the foreign matter contained in the exhaust gas to the foreign matter receiving portion through the rapid change in the direction of the air flow of the exhaust gas.
또한, 여러 위치에서 흡기된 배출 가스들을 하나의 장치를 사용하여 정화할 수 있으며, 배플의 각도나 길이를 변화할 뿐 별도의 장치나 제작 방법의 변화를 주지 않고 효율을 높일 수 있어 설비 또는 제작이 용이한 효과를 가지어 배출 가스 정화 장치의 제작 단가를 낮출 수 있다.In addition, it is possible to purify the exhaust gases intake at various locations using a single device, and to change the angle or length of the baffle, and to increase the efficiency without changing a separate device or manufacturing method, so that the equipment or the production is easy. It is possible to reduce the manufacturing cost of the exhaust gas purification device with an easy effect.

Claims (11)

  1. 이물질이 포함된 배출 가스를 제1방향으로 유도하는 제1덕트부;A first duct unit guiding a discharge gas containing foreign matter in a first direction;
    상기 제1덕트부의 저면에 형성되고, 상기 배출 가스에 포함된 이물질을 수용하는 이물질 수용부;A foreign material accommodating part formed on a bottom surface of the first duct part and accommodating foreign matter contained in the exhaust gas;
    상기 제1덕트부의 측면에 형성되는 정화 가스 배출구와 연통되고, 이물질이 분리된 정화 가스를 제2방향으로 유도하는 제2덕트부; 및A second duct portion communicating with a purge gas discharge port formed at a side surface of the first duct portion and guiding the purge gas from which foreign substances are separated in a second direction; And
    상기 제1덕트부의 내부로 돌출되게 설치되고, 상기 제1덕트부로 유입된 배출 가스의 기류 방향이 상기 제2덕트부 방향의 제2방향으로 급격하게 변화되도록 유도하는 제1배플;A first baffle installed to protrude into the first duct part and causing the air flow direction of the exhaust gas introduced into the first duct part to change rapidly in a second direction of the second duct part;
    을 포함하고,Including,
    상기 제1덕트부는,The first duct portion,
    상기 제2덕트부로부터 상대적으로 가까운 위치에 설치되는 제1유입부; 및A first inflow part installed at a position relatively close to the second duct part; And
    상기 제1유입부와 이웃하여 설치되고 상기 제2덕트부로부터 상대적으로 먼 위치에 설치되는 제2유입부;A second inlet part installed adjacent to the first inlet part and installed at a position relatively far from the second duct part;
    를 포함하는, 배출 가스 정화 장치.Comprising, exhaust gas purification device.
  2. 제1항에 있어서,The method of claim 1,
    상기 제1배플은,The first baffle,
    선단이 상기 이물질 수용부를 향하여 수평면을 기준으로 아래로 제1하향각도로 경사지게 돌출되고 후단이 상기 정화 가스 배출구의 상방에 고정되는 것인, 배출 가스 정화 장치.The front end protrudes inclined downward with respect to the foreign substance accommodating part at a first downward angle with respect to a horizontal plane, and the rear end is fixed above the purge gas outlet, exhaust gas purification apparatus.
  3. 제2항에 있어서,The method of claim 2,
    상기 제1하향각도는, 30도 내지 50도인, 배출 가스 정화 장치.The first downward angle is 30 to 50 degrees, exhaust gas purification device.
  4. 제2항에 있어서,The method of claim 2,
    상기 제1배플은,The first baffle,
    상기 이물질 수용부 방향으로 경사지게 돌출된 제1돌출길이가 상기 정화 가스 배출구의 연결지점에서부터 상기 이물질 수용부 상의 제1연장지점까지의 제1지향거리에 33퍼센트 내지 42퍼센트 이상인, 배출 가스 정화 장치.And a first projection length projecting obliquely toward the foreign substance accommodating portion is 33% to 42 percent or more at a first direction distance from a connection point of the purge gas outlet to a first extension point on the foreign substance accommodating portion.
  5. 제4항에 있어서,The method of claim 4, wherein
    상기 제2덕트부는,The second duct portion,
    상기 정화 가스가 배출되는 유로의 높이인 유로높이를 갖고,Has a flow path height which is a height of a flow path through which the purge gas is discharged,
    상기 제1지향거리에서 상기 제1돌출길이를 차감한 제1통과거리는 상기 유로높이 이상인, 배출 가스 정화 장치.And a first passage distance obtained by subtracting the first protrusion length from the first direction distance is greater than or equal to the flow path height.
  6. 제1항에 있어서,The method of claim 1,
    상기 제1덕트부는,The first duct portion,
    상기 제1유입부와 상기 제2유입부를 분할할 수 있는 분리벽;A partition wall capable of dividing the first inflow portion and the second inflow portion;
    을 더 포함하는, 배출 가스 정화 장치.Further comprising, exhaust gas purification device.
  7. 제6항에 있어서,The method of claim 6,
    상기 제1유입부의 내부로 돌출되게 설치되고, 상기 제1유입부로 유입된 배출 가스의 기류 방향이 제2덕트부 방향의 제2방향으로 급격하게 변화되도록 유도하는 제2배플;A second baffle installed to protrude into the first inlet, and causing the airflow direction of the exhaust gas introduced into the first inlet to be rapidly changed in a second direction of the second duct part;
    을 더 포함하는, 배출 가스 정화 장치.Further comprising, exhaust gas purification device.
  8. 제7항에 있어서,The method of claim 7, wherein
    상기 제2배플은,The second baffle,
    선단이 상기 이물질 수용부를 향하여 수평면을 기준으로 아래로 제2하향각도로 경사지게 돌출되고 후단이 상기 분리벽의 하단부에 고정되는 것인, 배출 가스 정화 장치.The front end is projected inclined downward with a second downward angle toward the foreign matter receiving portion relative to the horizontal plane, and the rear end is fixed to the lower end of the separation wall, exhaust gas purification apparatus.
  9. 제8항에 있어서,The method of claim 8,
    상기 제2하향각도는, 30도 내지 50도인, 배출 가스 정화 장치.The second downward angle is 30 to 50 degrees, exhaust gas purification device.
  10. 제8항에 있어서,The method of claim 8,
    상기 제2배플은,The second baffle,
    상기 이물질 수용부 방향으로 경사지게 돌출된 제2돌출길이가 상기 분리벽의 연결지점에서부터 상기 이물질 수용부 상의 제2연장지점까지의 제2지향거리에 33퍼센트 내지 42퍼센트 이상인, 배출 가스 정화 장치.And a second projection length protruding obliquely toward the foreign substance accommodating portion is 33% to 42 percent or more at a second direction distance from a connection point of the separation wall to a second extension point on the foreign substance accommodating portion.
  11. 제1항에 있어서,The method of claim 1,
    상기 이물질 수용부는,The foreign matter receiving portion,
    아래로 오목한 깔때기 형상의 호퍼이고, 상기 제1덕트부와 상기 이물질 수용부 사이에 그 표면이 평면을 이루는 유도 평면부가 형성되는 것인, 배출 가스 정화 장치.A funnel-shaped hopper concave down, wherein an induction plane portion whose surface is planar is formed between the first duct portion and the foreign matter accommodating portion.
PCT/KR2016/009570 2015-09-10 2016-08-29 Exhaust gas purifying apparatus WO2017043793A1 (en)

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KR20020061621A (en) * 1999-12-23 2002-07-24 두르 인더스트리즈 인 코포레이티드 Baffle System for Separating Liquid from A Gas Stream
JP2003265378A (en) * 2002-03-17 2003-09-24 Masaaki Kimura Dust separator for separating dust by applying physical force such as inertial force, centrifugal force, gravity or the like to be used for vacuum cleaner or dust collector
KR20060042688A (en) * 2004-11-10 2006-05-15 엘지전자 주식회사 Baffle filter
JP2007054371A (en) * 2005-08-25 2007-03-08 Masaaki Kimura Vacuum cleaner which separates dust by physical force such as inertia force, centrifugal force, gravity
KR101218403B1 (en) * 2012-07-16 2013-01-03 강릉원주대학교산학협력단 Cleaning apparatus of exhaust gas and its baffle

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JP2003265378A (en) * 2002-03-17 2003-09-24 Masaaki Kimura Dust separator for separating dust by applying physical force such as inertial force, centrifugal force, gravity or the like to be used for vacuum cleaner or dust collector
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