KR20010060712A - Method and apparatus for remove dust in filtering machine - Google Patents

Method and apparatus for remove dust in filtering machine Download PDF

Info

Publication number
KR20010060712A
KR20010060712A KR1019990063121A KR19990063121A KR20010060712A KR 20010060712 A KR20010060712 A KR 20010060712A KR 1019990063121 A KR1019990063121 A KR 1019990063121A KR 19990063121 A KR19990063121 A KR 19990063121A KR 20010060712 A KR20010060712 A KR 20010060712A
Authority
KR
South Korea
Prior art keywords
dust
fan
dust collecting
backwashing
collecting chamber
Prior art date
Application number
KR1019990063121A
Other languages
Korean (ko)
Other versions
KR100460666B1 (en
Inventor
배기진
길일섭
이상윤
Original Assignee
이구택
포항종합제철 주식회사
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 이구택, 포항종합제철 주식회사 filed Critical 이구택
Priority to KR10-1999-0063121A priority Critical patent/KR100460666B1/en
Publication of KR20010060712A publication Critical patent/KR20010060712A/en
Application granted granted Critical
Publication of KR100460666B1 publication Critical patent/KR100460666B1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/66Regeneration of the filtering material or filter elements inside the filter
    • B01D46/70Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter
    • B01D46/72Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter with backwash arms, shoes or nozzles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/08Filter cloth, i.e. woven, knitted or interlaced material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/02Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
    • B01D46/023Pockets filters, i.e. multiple bag filters mounted on a common frame
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/02Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
    • B01D46/04Cleaning filters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/42Auxiliary equipment or operation thereof
    • B01D46/44Auxiliary equipment or operation thereof controlling filtration
    • B01D46/446Auxiliary equipment or operation thereof controlling filtration by pressure measuring
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/66Regeneration of the filtering material or filter elements inside the filter
    • B01D46/70Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter
    • B01D46/71Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter with pressurised gas, e.g. pulsed air
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2239/00Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/06Filter cloth, e.g. knitted, woven non-woven; self-supported material
    • B01D2239/0604Arrangement of the fibres in the filtering material
    • B01D2239/0618Non-woven

Abstract

PURPOSE: Provided are a method and an apparatus for cleaning a dust collector by collecting dust on the outside of a filter bag and dusting off the filter bag using backwash air, to increase a filtering speed and to reduce operating costs. CONSTITUTION: The method comprises the steps of: collecting dust and discharging cleaned gas to a stack(34); measuring the loss of pressure by a manometer(29), stopping the operation of an inhaling fan(21) according to the measured value and backwashing outside air into a dust-collecting room(11) by operating a backwashing fan(25); and cleaning dust attached on the outside of the filter bag(12). The apparatus includes the inhaling fan(21), the backwashing fan(25) and a controller(30) to control dampers(23,27) of backwashing lines(22,26), a dust-collecting hood(19), dampers(18a,19a) of a backwashing line(18), the inhaling fan(21) and the backwashing fan(25).

Description

집진기의 탈진방법 및 장치{METHOD AND APPARATUS FOR REMOVE DUST IN FILTERING MACHINE}Dust collection method and apparatus of dust collector {METHOD AND APPARATUS FOR REMOVE DUST IN FILTERING MACHINE}

본 발명은 부직포로 이루어진 여과백의 외면에 분진을 집진하고, 역기류방식으로 역세되는 외부공기로서 여과백에 부착된 분진을 탈진함으로서 여과속도가 크고 운영비용을 줄일수 있는 집진기의 탈진 방법 및 장치에 관한 것이다.The present invention provides a dust collecting method and apparatus for collecting dust on the outer surface of a filter bag made of a nonwoven fabric, and dust collecting dust attached to the filter bag as an external air backwashed by a backflow method to reduce the operating cost and increase the filtration speed. It is about.

일반적으로 여과집진기술은 배가스중에 함유된 분진을 여과포를 이용하여 포집하는 방법으로 전기집진기술, 세정집진기술등과 더불어 산업체에서 널리 이용되고 있다.In general, the filter dust collecting technology is a method of collecting the dust contained in the exhaust gas by using a filter cloth, and is widely used in the industry along with the electrostatic dust collecting technology, cleaning dust collecting technology.

여과집진기술은 산업체의 분진발생공정에 대부분 이용될 수 있으며 대표적인 산업공정으로는 철강공정, 소각공정, 시멘트공정, 연소공정, 제지공정 및 코크스공정등에 이용될수 있다.Filtration and dust collection technology can be used in most industrial dust generation process, and representative industrial processes can be used in steel process, incineration process, cement process, combustion process, papermaking process and coke process.

통상 여과집진기는 여과포의 종류, 집진기내의 여과포 설치방법, 여과포표면에 표집된 분진을 탈진하는 방법등에 따라 달라질 수 있으며, 탈진방법에 따라 진동탈진(shake cleaning), 역기류탈진(reverse air cleaning), 충격기류탈진(pulse-jet cleaning)방식등이 알려져 있는데 이중에 역기류탈진방식과 충격기류탈진방식이 산업체에 널리 이용되고 있으며, 이들 방식의 적용시에는 각각의 특징을 가지고 있다.In general, the bag filter may vary depending on the type of filter cloth, the method of installing the filter cloth in the bag, the method of dedusting the dust collected on the surface of the bag, and depending on the method of dust removal, the vibration cleaning (shake cleaning), reverse air cleaning, Shock-jet cleaning methods are known, among which counter-air and dust-free dust removal methods are widely used in the industry, and these methods have their characteristics.

즉, 역기류탈진방식은 도 1(a)(b)에 도시한 바와같이, 단위 집진실(31)내로 함진가스를 집진팬(33)의 흡입력으로 유입하여 여과포(32)에 분진을 부착하고, 일정시간 경과한 후에 상기 집진실(31)에 함진가스의 유입을 중단시킨 후 함진가스의 유입방향과 반대방향으로 외부공기를 불어넣어 상기 여과포(32)의 표면에 부착된 분진을 탈진시키는 것으로서, 이러한 방식의 특징은 여과포(32)의 내면에 분진이포집되는 내면여과 방식이며, 상기 여과포는 직포(woven filter)를 사용한다는 것이다.That is, in the reverse airflow dedusting method, as shown in Fig. 1 (a) and (b), the dust containing gas is introduced into the unit dust collection chamber 31 by the suction force of the dust collecting fan 33 to attach dust to the filter cloth 32. After stopping for a certain time, the inflow of the impregnated gas into the dust collecting chamber 31 is stopped, and blows external air in a direction opposite to the inflow direction of the impregnated gas to dedust dust adhered to the surface of the filter cloth 32. The characteristic of this method is an internal filtration method in which dust is collected on the inner surface of the filter cloth 32, and the filter cloth uses a woven filter.

미설명부호 34는 분진이 제거된 가스가 배출되는 스택(stack)이고, 39는 로타리밸브이다.Reference numeral 34 denotes a stack from which dust-free gas is discharged, and 39 denotes a rotary valve.

그리고, 상기 집진실(31)내의 여과포(32)는 도 1(c)에 도시한 바와같이 상부와 하부를 빔(35a)(35b)으로서 동시에 고정되며, 상부는 스프링고리(36)를 연결하여 텐션을 조정하여 집진실(31)상부에 부착시킨다. 이때 상기 여과포(32)의 하부는 열려 있고, 상부는 막혀있다.In addition, the filter cloth 32 in the dust collecting chamber 31 is fixed at the same time as the upper and lower beams 35a, 35b, as shown in Fig. 1 (c), the upper portion is connected to the spring ring 36 The tension is adjusted and attached to the upper part of the dust collecting chamber 31. At this time, the lower part of the filter cloth 32 is open, and the upper part is blocked.

이러한 역기류탈진방식은 특성상 전체 집진장치가 몇 개의 단위 집진실(31)로 구성되어 있으며, 여과속도가 대체로 느려 여과포(32)의 단위면적당 처리가스의 유량이 적으므로 전체 집진장치의 설치면적이 많이 필요해지는 반면에, 낮은 에너지 탈진방식이므로 상기 여과포(32)에 주어지는 탈진강도가 낮아 상기 여과포(32)의 수명이 길며, 집진장치의 운영비용이 적게 소요되는 장점이 있다.The reverse airflow dedusting method is characterized in that the whole dust collecting device is composed of several unit dust collecting chambers 31, and since the filtration speed is generally low, the flow rate of processing gas per unit area of the filter cloth 32 is small, so that the installation area of the whole dust collecting device is On the other hand, since it is a low energy dedusting method, the dedusting strength given to the filter cloth 32 is low, the service life of the filter cloth 32 is long, and the operating cost of the dust collector is low.

또한, 충격기류탈진방식은 여과포표면에 부착된 분진을 분사노즐을 통한 고압의 압축공기(통상 3 내지 7기압)를 이용하여 탈진시키는 것으로서 이러한 방식의 특징은 여과포의 외면에 분진이 포집되는 외면여과방식이며, 여과백은 부직포(felt)를 사용한다는 것이다.In addition, the impact air dedusting method is to dedust dust attached to the surface of the filter cloth by using high pressure compressed air (usually 3 to 7 atmospheres) through the injection nozzle, which is characterized by an outer filtration in which dust is collected on the outer surface of the filter cloth. Method, the filter bag uses a non-woven (felt).

집진실내의 여과포는 내부에 철물지지대(bag cage)가 설치되어 여과포를 지지하며, 상기 여과포의 하부가 막혀있고, 상부는 열려 있으며, 철물지지대를 통하여 집진실상부에 연결되어 있다.The filter cloth in the dust collecting chamber has a bag cage installed therein to support the filter cloth, the lower part of the filter cloth is blocked, the upper part is open, and is connected to the dust collecting chamber upper part through the hardware support.

이러한 방식은 압축공기를 이용한 높은 탈진에너지를 이용하기 때문에 여과속도를 크게 할수 있어 집진기 본체를 작게 할수 있는 장점이 있는 반면에 고압의 압축공기를 사용하므로 집진기의 운영비용이 증가하며, 여과포의 길이를 크게 할 경우에는 여과포의 하단부까지 탈진력이 미치지 못하여 털진이 제대로 이루어지지 않는 문제점이 있었다.Since this method uses high dust extraction energy using compressed air, the filtration speed can be increased and the dust collector main body can be made small. On the other hand, the operation cost of the dust collector increases due to the use of high pressure compressed air, and the length of the filter cloth is increased. When it was enlarged, there was a problem in that the dust was not properly made since the dust removal force did not reach the lower end of the filter cloth.

따라서, 종래 부직포를 사용하는 역기류 탈진식 여과집진기는 내면여과를 이용하고 탈진시에는 저압의 공기를 이용하기 때문에 여과속도를 크게 할수 없어 동일한 배가스량에 대하여 집진기본체가 커지는 문제점을 가지고 있다.Therefore, the conventional backflow dedusting type filter precipitator using the nonwoven fabric uses internal filtration and low pressure air at the time of dedusting, so that the filtration rate cannot be increased.

또한 충격기류탈진식은 여과속도를 크게 할수 있어 동일한 배가스처리량을 기준으로 하여 역기류탈진식보다 집진장치의 크기를 줄일수 있으나 고압의 압축공기의 사용으로 인하여 장치운영비가 과다하게 소요되는 문제점을 가지고 있는 것이다.In addition, the impact air dedusting type can increase the filtration speed, which can reduce the size of the dust collecting device than the backflow dedusting type on the basis of the same exhaust gas throughput, but the operation cost of the equipment is excessive due to the use of high pressure compressed air. will be.

따라서, 본 발명은 이러한 종래의 문제점을 감안하여 안출된 것으로써, 그 목적은, 함진가스내에 함유된 분진을 여과하는 속도가 크고, 저압의 외부공기로서 여과포에 부착된 분진을 탈진할수 있어 집진설비의 운영하는 비용을 줄일 수 있는 집진기의 탈진방법을 제공하고자 한다.Therefore, the present invention has been devised in view of such a conventional problem, and its object is to provide a high speed of filtering dust contained in the dust-containing gas, and to collect dust attached to the filter cloth as low pressure external air, so that dust collection equipment The present invention aims to provide a dust extraction method that can reduce the operating cost of the dust collector.

또한, 본 발명의 또다른 목적은 함진가스내에 함유된 분진을 여과하는 속도가 크고, 저압의 외부공기로서 여과포에 부착된 분진을 탈진할 수 있어 집진설비의 운영하는 비용을 줄일 수 있으며, 설비의 설치공간을 줄일 수 있는 집진기의 탈진장치를 제공하고자 한다.In addition, another object of the present invention is to filter the dust contained in the dust containing gas is high, the dust attached to the filter cloth as a low pressure external air can be dedusted to reduce the operating cost of the dust collection equipment, It is intended to provide a dust collector of a dust collector that can reduce an installation space.

도 1(a)(b)(c)는 일반적인 역기류방식의 집진기를 도시한 개략도,Figure 1 (a) (b) (c) is a schematic diagram showing a dust collector of a general reverse air flow type,

도 2도는 본 발명에 따른 집진기의 탈진장치를 도시한 사시도,Figure 2 is a perspective view showing a dust collector of the dust collector according to the present invention,

도 3은 본 발명에 따른 집진기의 탈진장치를 도시한 개략도,3 is a schematic view showing a dust extraction apparatus of the dust collector according to the present invention;

도 4는 본 발명에 따른 집진기의 탈진장치를 이용하여 연속적으로 집진, 탈진작업을 수행한 실험결과를 도시한 그래프Figure 4 is a graph showing the results of the experiment to perform the dust-collecting, dust-dusting operation continuously using the dust collector of the dust collector according to the present invention

* 도면의 주요부분에 대한 부호의 설명** Explanation of symbols for the main parts of the drawings *

11 .... 집진실 12 .... 여과포11 .... Dust collection room 12 .... Filter cloth

17 .... 분진배출구 19 .... 집진후드17 .... Dust outlet 19 .... Dust collection hood

21 .... 흡입팬?? 22 .... 흡입라인21 .... suction fan ?? 22 .... suction line

23,27 .... 댐퍼 25 .... 역세팬23,27 .... Damper 25 .... Backwash Fan

26 .... 역세라인 29 .... 차압계26 .... Backwash Line 29 .... Differential Pressure Gauge

30 .... 제어기 34 .... 스택30 .... Controller 34 .... Stack

상기 목적을 달성하기 위한 기술적인 구성으로써, 본 발명은,As a technical configuration for achieving the above object, the present invention,

함진가스내의 분진을 집진하여 탈진하는 방법에 있어서,In the method for collecting dust in dust-containing gas and dedusting,

흡입팬의 흡입력에 의해 집진실내로 유입되는 함진가스중의 분진을 여과포의 외부면에 부착하여 집진하고, 분진이 여과된 청정가스를 스택으로 배출하는 집진단계;A dust collecting step of attaching dust in the dust-containing gas introduced into the dust collecting chamber by the suction force of the suction fan to the outer surface of the filter cloth and collecting the dust-filtered clean gas into the stack;

상기 여과백에 부착되는 분진에 의해 발생되는 상기 집진실내에서의 압력손실을 차압계로서 측정하고, 상기 차압계의 측정값을 근거로 하여 상기 흡입팬의 구동을 중지하고, 역세팬을 가동시켜 집진실내로 외부공기를 역세공급하는 역세단계; 및,The pressure loss in the dust collecting chamber caused by the dust attached to the filter bag is measured as a differential pressure gauge, the driving of the suction fan is stopped based on the measured value of the differential pressure gauge, and the reverse washing fan is operated to enter the dust collecting chamber. A backwashing step of backwashing the external air; And,

상기 집진실내로 강제 유입되는 역세공기에 의해 상기 여과백의 외면에 부착된 분진을 하부로 탈락제거하여 탈진하는 탈진단계;를 포함함을 특징으로 하는 집진기의 탈진방법을 마련함에 의한다.It is provided by a dust extraction method of a dust collector; comprising a dust-removing step of dropping and removing the dust attached to the outer surface of the filter bag to the lower by the backwash air forcibly introduced into the dust chamber.

또한, 상기 목적을 달성하기 위한 기술적인 구성으로써, 본 발명은,In addition, as a technical configuration for achieving the above object, the present invention,

집진발생원으로부터 함진가스가 투입되는 집진후드와, 복수개의 여과백을 내장한 집진실과, 탈진된 분진이 배출되는 분진배출구를 갖추어 함진가스내의 분진을 제거하는 집진설비에 있어서,In the dust collecting equipment which removes the dust in the dust containing the dust collection hood which the dust-containing gas is input from the dust generating source, the dust chamber which has a plurality of filter bags built-in, and the dust discharge port which exhausted dust is discharged,

상기 집진후드를 통하여 함진가스를 상기 집진실내로 흡입할수 있는 흡입력을 발생시키고, 상기 여과백을 통과하면서 여과된 가스를 외부로 배출할 수 있도록상기 집진실의 일측 외부면에 설치되는 흡입라인에 갖추어지는 집진팬;Equipped with a suction line installed on one side of the dust collecting chamber so as to generate a suction force to suck the dust containing gas into the dust collecting chamber through the dust collection hood and to discharge the filtered gas to the outside while passing through the filter bag. Losing dust collecting fan;

상기 여과백에 부착된 분진을 탈락시킬수 있도록 외부공기를 상기 집진실내로 공급할수 있도록 상기 집진실의 타측 외부면에 설치된 역세라인에 갖추어지는 역세팬; 및,A backwash fan provided in a backwash line installed on the other outer surface of the dust collecting chamber to supply external air into the dust collecting chamber so that dust attached to the filter bag can be dropped; And,

상기 집진실내의 압력손실을 측정하는 차압계의 측정값을 수신하여 상기 흡입, 역세라인에 설치된 댐퍼의 개도, 집진후드, 역세배기라인에 설치된 댐퍼의 개도 및 상기 흡입팬,역세팬의 기동을 제어하는 제어기;를 포함함을 특징으로 하는 집진기의 탈진장치를 마련함에 의한다.Receiving the measured value of the differential pressure gauge for measuring the pressure loss in the dust collecting chamber to control the opening degree of the damper installed in the suction, backwash line, the dust collection hood, the opening degree of the damper installed in the backwash exhaust line, and the starting of the suction fan and backwash fan. By providing a dust collector of the dust collector, characterized in that it comprises a controller.

이하, 본 발명의 바람직한 일실시예를 첨부된 도면에 의거하여 보다 상세하게 설명하고자 한다.Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.

도 2는 본 발명에 따른 집진기의 탈진장치를 도시한 사시도이고, 도 3은 본 발명에 따른 집진기의 탈진장치를 도시한 개략도이다.Figure 2 is a perspective view showing a dust collector of the dust collector according to the present invention, Figure 3 is a schematic diagram showing a dust collector of the dust collector according to the present invention.

본 발명에 따른 집진기의 탈진방법은 함진가스의 여과속도를 높이고, 설치운영비용을 줄일 수 있도록 집진단계, 역세단계 및 탈진단계로 구성되는바, 함진가스내에 함유된 분진을 여과하는 집진단계는 집진실(11)에 연결된 흡입라인(22)의 흡입팬(21)을 작동시켜 분진발생원으로부터 집진후드(19)를 통하여 함진가스를 상기 집진실(11)내로 흡입하고, 상기 집진실(11)내로 흡입된 함진가스는 여과백(12)을 통과하면서 분진은 상기 여과백(12)에 부착되고, 분진이 제거된 청정가스는 댐퍼(23)가 개도된 흡입라인(22) 및 흡입팬(21)을 통과하면서 외부로 청정가스를 배기하는 것이다.Dust collection method of the dust collector according to the present invention is composed of a dust collection step, backwashing step and dust removal step to increase the filtration rate of the dust containing gas, and reduce the installation operating cost, the dust collecting step of filtering the dust contained in the dust containing gas By operating the suction fan 21 of the suction line 22 connected to the truth 11, the dust-containing gas is sucked into the dust collecting chamber 11 from the dust generating source through the dust collecting hood 19, and into the dust collecting chamber 11. The suctioned dust gas passes through the filter bag 12 and the dust is attached to the filter bag 12, and the clean gas from which the dust is removed is the suction line 22 and the suction fan 21 in which the damper 23 is opened. Exhaust the clean gas to the outside while passing through.

그리고, 상기 역세단계는 상기 집진실(11)내로 저압의 외부공기를 공급하는 것으로서, 그 시기는 상기 여과백(12)의 외면에 부착되는 분진의 부착량이 많아지면서 상대적으로 높아지는 상기 집진실(11)내에서의 압력손실을 수시로 측정하는 차압계(29)의 측정값을 근거로 하여 상기 측정값이 설정값이상이 될 때 상기 차압계(29)의 측정값을 수신하여 설정값과 비교하는 제어기(30)에서 상기 흡입팬(21)의 구동을 중지하고, 상기 흡입라인(22)의 댐퍼(23)를 차단한 다음에 역세라인(26)에 설치된 댐퍼(27)를 개도하고, 역세팬(25)를 작동시켜 상기 집진실(11)내로 외부공기를 공급하는 것이다.In addition, the backwashing step is to supply low-pressure external air into the dust collecting chamber 11, and the dust collecting chamber 11 is relatively increased as the amount of dust attached to the outer surface of the filter bag 12 increases. The controller 30 which receives the measured value of the differential pressure gauge 29 and compares it with the set value when the measured value becomes more than the set value based on the measured value of the differential pressure gauge 29 which measures the pressure loss in the. Stop the driving of the suction fan 21, cut off the damper 23 of the suction line 22, and then open the damper 27 installed in the backwash line 26, and backwash fan 25 To operate to supply external air into the dust collecting chamber (11).

연속하여 상기 탈진단계는 상기 집진실(10)내로 강제 유입되는 외부의 역세공기를 상기 여과백(12)의 개방된 상부로 공급함으로서 상기 여과백(12)의 외면에 부착된 분진을 하부로 ??락제거하고, 분진배출구(17)에 모아진 일정량 모아진 분진을 외부로 배출하는 것이다.Continuously, the dust exhausting step supplies dust backing to the outer surface of the filter bag 12 by supplying external back air forced into the dust collecting chamber 10 to the open upper portion of the filter bag 12. ? Clear and discharge the dust collected in a certain amount collected in the dust outlet 17 to the outside.

한편, 본 발명에 따른 집진기의 탈진장치는 도 3에 도시한 바와같이, 집진발생원으로부터 함진가스가 투입되는 집진후드(19)와, 복수개의 여과백(12)을 내장한 집진실(11)과, 탈진된 분진이 배출되는 분진배출구(17)를 갖추어 함진가스내의 분진을 제거하는 집진실(11)에 갖추어는 것으로서, 흡입팬(21), 역세팬(25), 제어기(30)등으로 구성된다.On the other hand, the dust collector of the dust collector according to the present invention, as shown in Figure 3, the dust collection hood 19, the dust collecting gas is introduced from the dust generating source, the dust collecting chamber 11 containing a plurality of filter bags 12 and , Equipped with a dust discharge port 17 through which dust is discharged and provided in a dust collecting chamber 11 for removing dust in the dust containing gas, comprising a suction fan 21, a backwash fan 25, a controller 30, and the like. do.

즉, 상기 흡입팬(21)은 상기 집진후드(19)를 통하여 분진발생원으로 부터함진가스를 상기 집진실(10)내로 흡입할수 있도록 흡입력을 발생시키고, 상기 여과포(12)을 통과하면서 여과된 청정가스를 외부로 배출할 수 있도록 상기집진실(11)의 일측 외부면에 설치되고, 댐퍼(23)가 설치된 흡입라인(22)에 장착된다.That is, the suction fan 21 generates a suction force to suck the dust gas from the dust generation source through the dust collection hood 19 into the dust chamber 10, and cleans the filter while passing through the filter cloth 12. It is installed on the outer surface of one side of the dust collecting chamber 11 to discharge the gas to the outside, the damper 23 is mounted to the suction line 22 is installed.

이때, 상기 여과백(12)은 백케이지(bagcage) 또는 리테이너(retainer)와 같은 상부지지대(15)로서 상부는 열려있고, 하부는 닫혀져 있도록 복수개 설치되어 분진이 외부면에 부착여과될 수 있는 부직포로 구성된다.In this case, the filter bag 12 is a non-woven fabric which is provided with a plurality of upper supports 15, such as a bagcage or a retainer, the upper part of which is open and the lower part of which is closed so that dust is attached to the outer surface. It consists of.

그리고, 상기 흡입팬(21)과 반대로 작동되는 역세팬(25)은 상기 여과백(12)에 부착된 분진을 탈락시킬수 있는 외부역세공기를 상기 집진실(11)내로 공급할수 있도록 상기 집진실(11)의 타측 외부면에 설치되고, 댐퍼(27)가 설치된 역세라인(26)에 장착된다.In addition, the reverse washing fan 25, which is operated opposite to the suction fan 21, may supply the external backwashing air capable of dropping dust attached to the filter bag 12 into the dust collecting chamber 11. It is installed on the other outer surface of 11), and is attached to the back washing line 26 provided with the damper 27.

또한, 상기 흡입팬(21)과 역세팬(25)의 기동을 제어하는 제어기(30)는 상기 여과백(12)에서의 집진이 이루어지면서 상승되는 집진실(11)내에서의 압력손실을 수시로 측정할수 있도록 검출단이 상기 여과백(12)의 상,하부에 각각 배치되는 차압계(29)와 전기적으로 연결되어 상기 차압계(29)의 측정값을 수신함으로서 상기 차압계(29)의 측정값에 따라 상기 흡입, 역세라인(22)(26)에 설치된 댐퍼(23)(27)의 개도를 제어하고, 집진후드(19), 역세배기라인(18)에 설치된 댐퍼(19a)(18a)의 개도를 제어하는 한편, 상기 집진실(11)내에서 집진이 가능하도록 흡입력을 발생시키는 흡입팬(21), 외부로부터 역세공기를 공급하는 역세팬(25)의 작동을 제어한다.In addition, the controller 30 which controls the start of the suction fan 21 and the backwash fan 25 frequently receives a pressure loss in the dust collecting chamber 11 which is raised as dust is collected in the filter bag 12. The detection stage is electrically connected to the differential pressure gauge 29 disposed at the upper and lower portions of the filter bag 12 so as to receive the measured value of the differential pressure gauge 29 according to the measured value of the differential pressure gauge 29. The opening degree of the dampers 23 and 27 installed in the suction and backwashing lines 22 and 26 is controlled, and the opening degree of the damper 19a and 18a provided in the dust collecting hood 19 and the backwashing line 18 is controlled. On the other hand, while controlling the operation of the suction fan 21 for generating a suction force to enable the dust collection in the dust collecting chamber 11, and the reverse washing fan 25 for supplying the backwash air from the outside.

도 3에서 미설명 부호 7은 분진주입기이고, 8은 압축공기라인이다.In FIG. 3, reference numeral 7 denotes a dust injector, and 8 denotes a compressed air line.

상기한 바와같은 구성으로 이루어진 본 발명의 작용을 설명한다.The operation of the present invention having the configuration as described above will be described.

먼저, 집진실(11)내에서의 집진작업은 역세라인(26)의 댐퍼(27)는 닫혀지고,역세배기라인(18)의 댐퍼(18a)가 닫혀진 초기상태에서, 댐퍼(23)가 개방된 흡입라인(22)의 흡입팬(21)을 기동시켜 상기 집진실(11)내에 흡입압력을 발생시키면, 댐퍼(19a)가 개도된 집진후드(19)를 통하여 분진발생원으로부터 함진가스가 집진실(11)내로 강제 유입된다.First, in the dust collecting chamber 11, the damper 27 of the backwash line 26 is closed, and the damper 23 is opened in the initial state in which the damper 18a of the backwash line 18 is closed. When the suction fan 21 of the suction line 22 is activated to generate the suction pressure in the dust collecting chamber 11, the dust-containing gas is collected from the dust generating source through the dust collecting hood 19 in which the damper 19a is opened. (11) is forced to flow into.

그리고, 상기 집진실(11)내로 유입된 함진가스는 상기 집진실(11)내부에 상부가 개방되고, 하부가 밀폐되도록 상부지지대(15)에 장착된 여과백(12)을 통과하여 상부로 흡입되면서, 분진은 부직포로 이루어진 여과백(12)의 외면에 부착되고, 분진이 여과된 청정공기는 흡입라인(22),흡입팬(21)을 통하여 스택(34)을 거쳐 외부로 배출된다.In addition, the dust-containing gas introduced into the dust collecting chamber 11 is sucked upward through the filter bag 12 mounted on the upper support 15 so that the upper part is opened inside the dust collecting chamber 11 and the lower part is sealed. While the dust is attached to the outer surface of the filter bag 12 made of a non-woven fabric, the dust is filtered clean air is discharged to the outside through the stack 34 through the suction line 22, the suction fan 21.

여기서, 상기 집진실(11)의 여과백(12)에 함진가스의 분진이 여과되는 집진작업동안에, 상기 여과백(12)의 상,하부에 검지단이 설치된 차압계(29)에 의해서 일정시간간격으로 압력손실을 측정하고, 측정된 압력손실의 측정값은 제어기(30)측으로 전송되며, 상기 제어기(30)에서 측정값이 설정값 이상되면, 이는 상기 여과백(12)에 부착된 분진량의 과다해져 더 이상의 집진이 곤란하는 것으로 판단할수 있기 때문에 상기 집진실(11)내로 역세공기를 주입하여 역세작업을 수행한다.Here, during the dust collecting operation in which dust of the dust-containing gas is filtered in the filter bag 12 of the dust collecting chamber 11, the differential pressure gauge 29 is provided at the upper and lower portions of the filter bag 12 for a predetermined time interval. Pressure loss is measured, and the measured value of the pressure loss is transmitted to the controller 30, and when the measured value is more than the set value in the controller 30, it is excessive of the amount of dust attached to the filter bag 12. Since it can be determined that further dust collection is difficult, backwashing air is injected into the dust collecting chamber 11 to perform backwashing.

즉, 정상적인 집진작업시 150 ㎜Aq이하의 압력손실을 갖던 상기 집진실(11)에서의 압력손실이 상기 여과백(12)에서의 집진이 과다해져 상기 집진실(11)내의 압력손실을 측정한 값이 200 내지 300㎜Aq이상이 되면, 원하는 흡입력에 의한 풍량이 발생되지 않기 때문에 상기 흡입팬(21)의 기동을 중단하고, 흡입라인(22)의 댐퍼(23), 집진후드(19)의 댐퍼(19a)를 닫은 반면에 역세라인(27)의 댐퍼(27), 역세배기라인(18)의 댐퍼(18a)를 개방한 상태에서 역세팬(25)을 작동시켜 저압의 외부공기를 상기 집진실(11)내로 공급한다.That is, the pressure loss in the dust collecting chamber 11, which had a pressure loss of 150 mmAq or less in the normal dust collecting operation, was excessively collected in the filter bag 12, and the pressure loss in the dust collecting chamber 11 was measured. When the value is 200 to 300 mmAq or more, since the air volume due to the desired suction force is not generated, the start of the suction fan 21 is stopped, and the damper 23 and the dust collection hood 19 of the suction line 22 are stopped. While the damper 19a is closed, the backwash fan 25 is operated while the damper 27 of the backwashing line 27 and the damper 18a of the backwashing line 18 are opened to operate the low pressure external air. Feed into the truth (11).

연속하여, 상기 집진실(11)내로 저압의 역세외부공기가 공급되면, 여과백(12)의 외면에 부착된 분진은 역세되는 외부공기에 의해서 하부로 탈락제거되고, 제거된 분진은 분진배출구에 모아지며, 모아진 분진은 개도되는 로타리밸브에 의해서 외부로 배출처리되며, 상기 여과백의 외면에 부착된 분진을 탈락시키도록 이를 통과한 역세공기는 댐퍼(18a)가 개도된 역세배기라인(18)을 통하여 스택(35)을 거쳐 외부로 배기처리된다.Subsequently, when the low pressure backwashing outside air is supplied into the dust collecting chamber 11, the dust attached to the outer surface of the filter bag 12 is eliminated and removed downward by the backwashed outside air, and the removed dust is discharged to the dust outlet. The collected dust is discharged to the outside by an open rotary valve, and the backwashing air passing through this to remove the dust attached to the outer surface of the filter bag passes through the backwashing line 18 having the damper 18a opened. Through the stack 35 is exhausted to the outside.

여기서, 탈진시 사용되는 상기 역세팬(25)의 역세풍량은 크면 클수록 여과백(12)에 부착된 분진을 탈진하는 작업에는 유리하나 탈진에 소요되는 운영비용이 증가하므로 상기 집진팬(21)의 집진풍량보다 작게 설정하는 것이 바람직하다.Here, the greater the backwashing amount of the backwashing fan 25 used for dedusting is advantageous for the work of dedusting dust attached to the filter bag 12, but the operating cost required for dedusting increases, so that It is preferable to set smaller than the amount of dust collection winds.

<실시예><Example>

집진실(11)에 여과백(12)을 9개 장착하고, 집진팬(21)의 최대집진풍량을 40m3/min, 역세팬(25)의 최대역세풍량을 30m3/min 으로 하고, 집진실험에 이용된 분진은 소결공장의 실제 여과집진기에서 포집된 분진을 샘플링하여 사용하였으며, 하기와 같은 실험조건으로 실험을 수행하였다.Nine filter bags 12 are mounted in the dust collecting chamber 11, and the maximum amount of dust collecting air of the dust collecting fan 21 is 40 m 3 / min, and the maximum amount of back washing air of the back washing fan 25 is 30 m 3 / min. The dust used in the experiment was used by sampling the dust collected in the actual filter dust collector of the sintering plant, the experiment was carried out under the following experimental conditions.

- 여과백 사양-Filter bag specification

1) 여과백 타입: 부직포, 2) 여과백크기 : 직경 150mm, 3)길이 3000mm, 4)총여과면적 12.72,1) Filter bag type: Non-woven fabric, 2) Filter bag size: Diameter 150mm, 3) Length 3000mm, 4) Total filtration area 12.7 2 ,

- 집진실험조건-Dust collection test condition

1) 집진풍량 : 19m3/min 2)여과속도 :1.5m/min 3)유입가스 온도 : 26℃ 4)입구농도 :10g/Nm35) 분진종류 : 소결분진 6) 분진특성 : 평균입도 29.2㎛, 진비중 3.3g/cm37) 역세풍량 8.4m3/min 8)역세시간 : 60초1) Air collection volume: 19m 3 / min 2) Filtration speed: 1.5m / min 3) Inlet gas temperature: 26 ℃ 4) Inlet concentration: 10g / Nm 3 5) Dust type: Sintered dust 6) Dust characteristics: Average particle size 29.2 ㎛, true specific gravity 3.3g / cm 3 7) backwash flow rate 8.4m 3 / min 8) back washing time: 60 seconds

여과집진기의 성능에서 가장 중요한 것은 탈진성능이며, 탈진성능을 판단??수 있는 기준은 압력손실이다. 통상적인 여과집진기의 운전중 압력손실의 관리기준은 150mmAq이하며, 압력손실이 200 내지 300mmAq이상이되면, 원하는 풍량이 나오지 못하므로 여과백(12)을 교체하게 된다.The most important factor in the performance of bag filter is the dust removal performance, and the criterion for determining the dust removal performance is the pressure loss. The standard of the management of the pressure loss during operation of the conventional filter dust collector is 150mmAq or less, if the pressure loss is 200 to 300mmAq or more, the desired air volume does not come out to replace the filter bag (12).

도 4는 본 발명에 따른 집진기의 탈진장치를 이용하여 연속적으로 집진, 탈진작업을 수행한 실험결과를 도시한 그래프로서, 집진시에는 주어진 조건에서 120mmAq의 압력손실까지 분진을 투입한 후 주어진 역세조건으로 탈진을 수행할 경우 압력손실이 20 내지 30mmAq로 감소하는 것으로 나타났다.Figure 4 is a graph showing the results of the experiment to perform the dust-collecting, dust-collecting operation continuously using the dust collector of the dust collector according to the present invention, when dust is dusted up to 120mmAq pressure loss in a given condition at a given backwash condition When exhaustion was carried out, the pressure loss was found to decrease to 20 to 30mmAq.

이와 같은 결과는 5회의 연속실험을 수행하였을 경우 매우 유사하게 나타났으며, 계속적으로 집진 및 탈진실험을 수행하여도 매우 유사한 경향이 나타날것으로 판단된다.These results were very similar when five consecutive experiments were carried out, and it would be expected that similar trends would occur even if the dust collection and exhaustion experiments were carried out continuously.

상기의 실험조건에서 주목할 만한 점은 집진시 여과속도 1.5m/min 는 통상적인 역기류 탈진시 여과집진기의 여과속도 0.9 내지 1.2m/min 보다도 큰 범위의 여과속도이므로 기존방식보다 여과속도를 크게할수 있다는 것을 보여주고 있다. 이에 따라 상기 실험결과는 본 발명의 탈진장치를 갖는 집진기가 종래의 집진기에 비하여 우수하는 것을 보여주고 있다.It is remarkable in the above experimental conditions that the filtration rate of 1.5m / min at the time of dust collection is larger than the conventional method since the filtration rate of the dust collector is larger than 0.9 to 1.2m / min at the time of normal backflow dust extraction. It is showing that there is. Accordingly, the experimental results show that the dust collector having the dust extraction device of the present invention is superior to the conventional dust collector.

상술한 바와같은 구성을 갖는 본 발명에 의하면, 집진이 외면여과로 이루어지고, 저압의 외부공기를 역세하여 탈진이 이루어짐으로서, 동일한 배가스처리를 기준으로 하여 종래의 역기류탈진식보다 여과속도를 크게 할수 있기 때문에 장치의 현저히 설치공간을 줄일 수 있고, 저압의 외부공기로서 탈진을 수행할수 있기 때문에 종래의 충격기류식에 비하여 운영비용을 현저히 낮출수 있는 효과가 얻어진다.According to the present invention having the above-described configuration, the dust collection is made by the outer filtration, and the dust is removed by backwashing the low pressure external air, so that the filtration rate is larger than the conventional backflow dedusting based on the same exhaust gas treatment. Since it is possible to significantly reduce the installation space of the device, since the dust can be carried out as low pressure external air, the effect that the operating cost can be significantly lowered compared to the conventional impact air type.

Claims (5)

함진가스내의 분진을 집진하여 탈진하는 방법에 있어서,In the method for collecting dust in dust-containing gas and dedusting, 흡입팬(21)의 흡입력에 의해 집진실(11)내로 유입되는 함진가스중의 분진을 여과포(12)의 외부면에 부착하여 집진하고, 분진이 여과된 청정가스를 스택(34)으로 배출하는 집진단계;The dust in the dust-containing gas introduced into the dust collecting chamber 11 by the suction force of the suction fan 21 is attached to the outer surface of the filter cloth 12 and is collected, and the dust is filtered and discharged to the stack 34. Dust collecting step; 상기 여과백(12)에 부착되는 분진에 의해 발생되는 상기 집진실(11)내에서의 압력손실을 차압계(29)로서 측정하고, 상기 차압계(29)의 측정값을 근거로 하여 상기 흡입팬(21)의 구동을 중지하고, 역세팬(25)을 가동시켜 집진실(11)내로 외부공기를 역세공급하는 역세단계; 및,The pressure loss in the dust collecting chamber 11 generated by the dust attached to the filter bag 12 is measured as a differential pressure gauge 29, and the suction fan (based on the measured value of the differential pressure gauge 29) A backwashing step of stopping the driving of the 21 and operating the backwash fan 25 to backwash the outside air into the dust collecting chamber 11; And, 상기 집진실(11)내로 강제 유입되는 역세공기에 의해 상기 여과백(12)의 외면에 부착된 분진을 하부로 탈락제거하여 탈진하는 탈진단계;를 포함함을 특징으로 하는 집진기의 탈진방법.And a dust removal step of dropping and removing the dust attached to the outer surface of the filter bag (12) by the back washing air forced into the dust collecting chamber (11) to remove the dust. 집진발생원으로부터 함진가스가 투입되는 집진후드(19)와, 복수개의 여과백(12)을 내장한 집진실(11)과, 탈진된 분진이 배출되는 분진배출구(17)를 갖추어 함진가스내의 분진을 제거하는 집진설비에 있어서,Dust collecting hood 19 into which the dust-containing gas is introduced from the dust generating source, dust collecting chamber 11 having a plurality of filter bags 12 therein, and dust discharge port 17 through which the dust is discharged are provided, In the dust collection equipment to remove, 상기 집진후드(19)를 통하여 함진가스를 상기 집진실(11)내로 흡입할수 있는 흡입력을 발생시키고, 상기 여과백(12)을 통과하면서 여과된 가스를 외부로 배출할 수 있도록 상기 집진실(11)의 일측 외부면에 설치되는 흡입라인(22)에 갖추어지는집진팬(21);The dust collecting chamber 11 generates a suction force capable of sucking the dust containing gas into the dust collecting chamber 11 through the dust collecting hood 19, and discharges the filtered gas to the outside while passing through the filter bag 12. A dust collecting fan 21 provided on the suction line 22 installed on one side of the outer surface; 상기 여과백(12)에 부착된 분진을 탈락시킬수 있도록 외부공기를 상기 집진실(11)내로 공급할수 있도록 상기 집진실(11)의 타측 외부면에 설치된 역세라인(26)에 갖추어지는 역세팬(25); 및,A backwashing fan provided on the backwashing line 26 provided on the other outer surface of the dust collecting chamber 11 to supply external air into the dust collecting chamber 11 so that dust attached to the filter bag 12 may be eliminated ( 25); And, 상기 집진실(11)내의 압력손실을 측정하는 차압계(29)의 측정값을 수신하여 상기 흡입, 역세라인(22)(26)에 설치된 댐퍼(23)(27)의 개도, 집진후드(19), 역세배기라인(18)에 설치된 댐퍼(18a)(19a)의 개도 및 상기 흡입팬(21),역세팬(25)의 기동을 제어하는 제어기(30);를 포함함을 특징으로 하는 집진기의 탈진장치.Receiving the measured value of the differential pressure gauge 29 for measuring the pressure loss in the dust chamber 11, the opening degree of the dampers 23, 27 installed in the suction, backwash line 22, 26, dust collection hood 19 And a controller (30) for controlling the opening degree of the dampers (18a) and (19a) installed in the backwashing line (18) and the starting of the suction fan (21) and the backwashing fan (25). Dust removal device. 제 2항에 있어서,The method of claim 2, 상기 여과백(12)은 백케이지(bagcage) 또는 리테이너(retainer)와 같은 상부지지대(15)로서 상부는 열려있고, 하부는 닫혀져 있도록 복수개 설치되어 분진이 외부면에 부착여과될 수 있는 부직포로 구성됨을 특징으로 하는 집진기의 탈진장치.The filter bag 12 is an upper support 15 such as a bagcage or a retainer, the upper part of which is open, and the lower part of the filter bag 12 is installed in a plurality of non-woven fabrics to which dust can be attached to the outer surface. Dust collector of the dust collector, characterized in that. 제 2항에 있어서The method of claim 2 상기 역세팬(25)의 역세풍량은 상기 집진팬(21)의 집진풍량보다 작게 설정함을 특징으로 하는 집진기의 탈진장치.Dust collecting device of the dust collector, characterized in that the backwashing air amount of the backwashing fan (25) is set smaller than the amount of dust collecting air of the dust collecting fan (21). 제 2항에 있어서The method of claim 2 상기 집진실(11)내의 압력손실을 측정한 값이 200 내지 300㎜Aq이상이 되면, 원하는 흡입력에 의한 풍량이 발생되지 않기 때문에 상기 흡입팬(21)의 기동을 중단하고, 흡입라인(22)의 댐퍼(23), 집진후드(19)의 댐퍼(19a)를 닫은 반면에 역세라인(27)의 댐퍼(27), 역세배기라인(18)의 댐퍼(18a)를 개방한 상태에서 역세팬(25)을 작동시켜 저압의 외부공기를 상기 집진실(11)내로 공급함을 특징으로 하는 집진기의 탈진장치.When the value of the pressure loss measured in the dust collecting chamber 11 is 200 to 300 mmAq or more, the air flow due to the desired suction force is not generated. Therefore, starting of the suction fan 21 is stopped, and the suction line 22 is stopped. The damper 23 of the dust collector 19, the damper 19a of the dust collection hood 19 is closed, while the damper 27 of the backwash line 27 and the damper 18a of the backwash line 18 are opened. 25) to operate the dust collector of the dust collector, characterized in that for supplying low-pressure external air into the dust chamber (11).
KR10-1999-0063121A 1999-12-27 1999-12-27 Method and apparatus for remove dust in filtering machine KR100460666B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR10-1999-0063121A KR100460666B1 (en) 1999-12-27 1999-12-27 Method and apparatus for remove dust in filtering machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR10-1999-0063121A KR100460666B1 (en) 1999-12-27 1999-12-27 Method and apparatus for remove dust in filtering machine

Publications (2)

Publication Number Publication Date
KR20010060712A true KR20010060712A (en) 2001-07-07
KR100460666B1 KR100460666B1 (en) 2004-12-09

Family

ID=19630505

Family Applications (1)

Application Number Title Priority Date Filing Date
KR10-1999-0063121A KR100460666B1 (en) 1999-12-27 1999-12-27 Method and apparatus for remove dust in filtering machine

Country Status (1)

Country Link
KR (1) KR100460666B1 (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100409215B1 (en) * 2000-11-29 2003-12-18 두산중공업 주식회사 Apparatus And Method For Maintaining Constant Velocity Of Cyclone Inlet Gas In A Circulating Fluidized Bed Combustor And Incinerators
KR20180080010A (en) * 2017-01-03 2018-07-11 (주)에어릭스 Filtration and Dust Collection System and Apparatus for controlling Dust Collection System
CN109381933A (en) * 2018-12-24 2019-02-26 永兴特种不锈钢股份有限公司 A kind of cleaner and equipment operation method applied to steel rolling line reversable mill
CN109779672A (en) * 2019-03-23 2019-05-21 福州大学 Mining impact water bath dust-extraction unit and its working method
CN110270188A (en) * 2019-07-08 2019-09-24 广州市旗兴精密器材有限公司 A kind of dust-extraction unit
CN110575716A (en) * 2019-10-11 2019-12-17 江苏润广环保科技有限公司 Environment-friendly dust collection and filtration device
EP3871751A4 (en) * 2018-10-26 2022-06-29 Zhejiang Hongsheng New Material Technology Group Co., Ltd Modularized dust collector system and control method thereof
KR102483349B1 (en) * 2022-05-09 2022-12-30 (주)태진기연 Air blower dedusting type filtering system
KR20230161734A (en) 2022-05-19 2023-11-28 주식회사 씨케이월드 Pulse-jet type dust collector made by remodeling reverse air type dust collector, shaking type dust collector or electrostatic precipitator
CN117258940A (en) * 2023-08-31 2023-12-22 重庆市药研院制药有限公司 Reducing mechanism with dust removal function

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101560598B1 (en) 2015-06-30 2015-10-16 이선영 Back flow preventing system for dust collector

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5445874A (en) * 1977-09-17 1979-04-11 Toyota Motor Corp Bag filter type dust collector and method of collecting dust therefor
JPS6029534B2 (en) * 1978-02-03 1985-07-11 株式会社豊田中央研究所 Bag filter cleaning device
JP2518576B2 (en) * 1991-11-08 1996-07-24 株式会社プランテック Control method of bag filter device
JPH0838837A (en) * 1994-08-03 1996-02-13 Zemuko Internatl Kk Filter cleaning of dust collector and its device
KR200288785Y1 (en) * 1998-12-21 2002-10-19 주식회사 포스코 Counterflow Dust Filter Type
KR20010018238A (en) * 1999-08-18 2001-03-05 이구택 A Reverse Air Cleaning Bag House System Using Outside Filtration

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100409215B1 (en) * 2000-11-29 2003-12-18 두산중공업 주식회사 Apparatus And Method For Maintaining Constant Velocity Of Cyclone Inlet Gas In A Circulating Fluidized Bed Combustor And Incinerators
KR20180080010A (en) * 2017-01-03 2018-07-11 (주)에어릭스 Filtration and Dust Collection System and Apparatus for controlling Dust Collection System
EP3871751A4 (en) * 2018-10-26 2022-06-29 Zhejiang Hongsheng New Material Technology Group Co., Ltd Modularized dust collector system and control method thereof
CN109381933A (en) * 2018-12-24 2019-02-26 永兴特种不锈钢股份有限公司 A kind of cleaner and equipment operation method applied to steel rolling line reversable mill
CN109779672A (en) * 2019-03-23 2019-05-21 福州大学 Mining impact water bath dust-extraction unit and its working method
CN109779672B (en) * 2019-03-23 2024-02-06 福州大学 Mining impact water bath dust removal device and working method thereof
CN110270188A (en) * 2019-07-08 2019-09-24 广州市旗兴精密器材有限公司 A kind of dust-extraction unit
CN110575716A (en) * 2019-10-11 2019-12-17 江苏润广环保科技有限公司 Environment-friendly dust collection and filtration device
KR102483349B1 (en) * 2022-05-09 2022-12-30 (주)태진기연 Air blower dedusting type filtering system
KR20230161734A (en) 2022-05-19 2023-11-28 주식회사 씨케이월드 Pulse-jet type dust collector made by remodeling reverse air type dust collector, shaking type dust collector or electrostatic precipitator
CN117258940A (en) * 2023-08-31 2023-12-22 重庆市药研院制药有限公司 Reducing mechanism with dust removal function

Also Published As

Publication number Publication date
KR100460666B1 (en) 2004-12-09

Similar Documents

Publication Publication Date Title
KR100855012B1 (en) Dust removal apparatus for filter dust collector
KR101962186B1 (en) Bag-filter washing system and bag-filter washing method for air conditioning system to remove ultra fine dust
KR100460666B1 (en) Method and apparatus for remove dust in filtering machine
KR102021551B1 (en) Bag filter pulse control system
KR100935548B1 (en) A jet nozzle for the bagfilter cleaning and a dust filtration collector equipped the same
JP2015160210A (en) Fabric filter system and method for cleaning the fabric filter system
KR101883974B1 (en) dust collector having apparatus for removing dust
TWI813149B (en) Concentrated dedusting filter dust collector capable of removing nanoparticle-grade fine dust and method thereof
KR100845958B1 (en) Filter fixing structure for a dust collector
KR100815456B1 (en) Dust collector having a dust removal parts at both ends
CN216572239U (en) Dust filtration equipment for marble processing
KR102328699B1 (en) Dust filter recycling device using removable blow pipe
CN113521899B (en) Ash removal method of bag type dust collector
KR101639010B1 (en) Dust Collector Apparatus
KR20040083565A (en) Anti-Refly, Anti-Reattachment Bagfilter Dust Collector for High Efficiency Dust Removal
CN216092762U (en) Novel high-efficient dust remover
CN110338738A (en) The dust of dust collect plant brushes lightly the method for falling
CN107456811A (en) A kind of sack cleaner
CN212017095U (en) Pulse bag dust collector
KR200288785Y1 (en) Counterflow Dust Filter Type
CN109603330A (en) Automatically cleaning sack cleaner
CN109833675A (en) A kind of high-efficiency multi-function deduster
KR20030089791A (en) Anti-Refly, Anti-Reattachment Bagfilter Dust Collector
CN117046228B (en) Self-cleaning industrial cloth bag dust remover
JP3177160B2 (en) Operating method of back pressure collapsible bag filter

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20121102

Year of fee payment: 9

FPAY Annual fee payment

Payment date: 20131202

Year of fee payment: 10

FPAY Annual fee payment

Payment date: 20141201

Year of fee payment: 11

FPAY Annual fee payment

Payment date: 20161129

Year of fee payment: 13

LAPS Lapse due to unpaid annual fee