KR100287286B1 - System and method for removing dust and desulfurizing of flue gas during steelmaking and combustion of bunker-c oil - Google Patents

System and method for removing dust and desulfurizing of flue gas during steelmaking and combustion of bunker-c oil Download PDF

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KR100287286B1
KR100287286B1 KR1019980049320A KR19980049320A KR100287286B1 KR 100287286 B1 KR100287286 B1 KR 100287286B1 KR 1019980049320 A KR1019980049320 A KR 1019980049320A KR 19980049320 A KR19980049320 A KR 19980049320A KR 100287286 B1 KR100287286 B1 KR 100287286B1
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water
sludge
dust
exhaust gas
desulfurization
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KR1019980049320A
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Korean (ko)
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KR19990014503A (en
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권기성
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신승근
포철로재주식회사
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • B01D53/50Sulfur oxides
    • 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
    • B01D39/16Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
    • 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
    • B01D46/56Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/06Spray cleaning
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • B01D53/78Liquid phase processes with gas-liquid contact
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/66Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/40Alkaline earth metal or magnesium compounds
    • B01D2251/402Alkaline earth metal or magnesium compounds of magnesium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/60Inorganic bases or salts
    • B01D2251/604Hydroxides

Abstract

PURPOSE: System and method are provided to exhaust air in the clean state by removing dust and sulfur oxides in the flue gas during steelmaking and combustion of bunker-C oil, and recycles the used cleaning water after water treatment. CONSTITUTION: The system for removing dust and desulfurizing of flue gas during steelmaking and combustion of bunker-C oil comprises a collection unit(10) collecting and removing dust of a large particle from a contaminant generation source; a cooling unit(20) on which a plurality of spray nozzles are arranged to rapidly cool the flue gas having a high temperature passing through the collection unit(10); a dust removal and desulfurizing unit(30) equipped with a filling material(30a), a spray nozzle(30b), an eliminator(30c) and demister(30d); a reservoir(40) supplying clean water with the spray nozzle(30b) and an eliminator(30c) of the dust removal and desulfurizing unit(30); a neutralizer storage tank(50) in which a neutralizer is stored to increase a hydrogen ion concentration of the clean water contained in the reservoir(40) so as to supply the neutralizer into the reservoir(40); an oxidation unit(60) oxidizing sulfite magnesium remained in waste water with magnesium sulfate by forcibly receiving oxygen from the outer part, and recirculating the clean water into the reservoir(40) by separating sludge from water; a cooling tower(70) cooling wastewater generated after the clean water of the reservoir(40) is circulated into the dust removal and desulfurizing unit(30); a purification unit(80) neutralizing wastewater by receiving wastewater from the oxidation unit(60) and receiving the neutralizer from the neutralizer storage tank(50); and a dehydration unit(90) caking the sludge by lowering a moisture content of a concentrate sludge after receiving the concentrated sludge from the oxidation unit(60).

Description

철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 설비와 그 방법Facilities and methods for dust removal and desulfurization of flue gas during steel production and bunker seed oil combustion

본 발명은 철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 설비와 그 방법에 관한 것으로, 보다 상세하게는 제철·제강 및 벙커씨유 연소시에 발생 배출되는 배가스중의 먼지와 황산화물을 제거하여 청정상태의 공기로 방출하고, 이때 사용된 세정수를 수처리후 재사용할 수 있도록 하는 철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 설비와 그 방법에 관한 것이다.The present invention relates to a facility for dust removal and desulfurization of flue gas during steel production and bunker seed oil combustion, and more particularly, to dust and sulfur oxides in flue gas emitted during steelmaking, steelmaking and bunker seed oil combustion. The present invention relates to a method and a method for dust removal and desulfurization of exhaust gas during steel production and bunker seed oil combustion which removes and releases the air as clean air and reuses the washing water used after treatment.

일반적으로 석탄이나 벙커씨유를 연료로 사용하는 제철 및 제강설비, 그리고 벙커씨유를 연료로 하는 여타의 산업에 있어서, 연소후 배출되는 배가스중에는 분진과 함께 다량의 황산화물이 함유되어 있는데, 이들 분진과 황산화물이 함유된 배기가스를 그대로 대기중에 배출시킨다면 환경규제가 강화되고 있는 현실정에서 큰 문제점이 아니라 할 수 없을 것이다.In steelmaking and steelmaking facilities, which typically use coal or bunker seed oil as fuel, and in other industries fueled by bunker seed oil, flue gases emitted after combustion contain large amounts of sulfur oxides together with dust. If the exhaust gas containing dust and sulfur oxides is discharged to the atmosphere as it is, it will not be a big problem in the reality that environmental regulations are being strengthened.

따라서, 제철 및 제강설비, 그리고 벙커씨유를 사용하는 설비에는 필수적으로 집진장치와 탈황장치가 구비됨으로써, 상기 집진장치에서 분진을 모아 처리하고, 탈황장치에서 황산화물을 처리하는 과정을 거치게 되어 어느 정도 배출가스를 정화시킨다.Therefore, the steelmaking and steelmaking facilities, and the equipment using bunker seed oil are essentially provided with a dust collector and a desulfurization device, so that the dust is collected and treated in the dust collector, and sulfur oxides are treated in the desulfurization device. Purify the exhaust gas.

그러나, 이와 같이 종래에 제철·제강설비와 벙커씨유를 사용하는 설비에 구비되는 집진장치와 탈황장치는 단순히 집진과 탈황이라는 단편적인 기능만을 수행할 뿐, 배출가스의 청정화 그리고, 집진 및 탈황에 이용된 세정수의 수처리후 재사용이라는 유기적인 시스템은 제시되지 못하여, 보다 바람직한 제진 및 탈황 그리고 이와 연계된 환경상의 과제를 만족시킬 수 없는 문제점이 대두되었다.However, the dust collector and the desulfurization apparatus which are conventionally provided in a facility using steelmaking and steelmaking facilities and bunker seed oil merely perform a fractional function of dust collection and desulfurization, and clean the exhaust gas, and The organic system of reuse after water treatment of the used washing water has not been proposed, and thus problems that cannot be satisfied with more preferable dust removal and desulfurization and related environmental problems have emerged.

본 발명은 전술한 바와 같은 문제점을 해소하기 위해 안출된 것으로, 제철·제강 및 벙커씨유 연소시에 발생 배출되는 배가스중의 먼지와 황산화물을 제거하여 청정상태의 공기로 방출하고, 이때 사용된 세정수를 수처리후 재사용할 수 있도록 유기적인 시스템을 갖춘 철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 설비와 그 방법을 제공하는 데에 목적이 있다.The present invention has been made to solve the problems described above, and removes dust and sulfur oxides in the exhaust gas generated during the combustion of steelmaking, steelmaking and bunker seed oil to be discharged as clean air, It is an object of the present invention to provide a method and method for dedusting and desulfurizing flue gas during the production of steel and burning bunker seed oil with an organic system to reuse the water after water treatment.

위와 같은 목적을 달성하기 위한 본 발명에 따른 철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 설비는, 오염물질 발생원으로부터 큰 입자의 분진을 포집·제거하는 집진장치와; 이 집진장치를 거쳐온 고온의 배가스를 송풍팬에 의해 송급받아 급냉시킬 수 있도록 다수의 스프레이노즐이 배치되어 있는 냉각장치와; 이 냉각장치에 의해 급냉되고서 인입되는 다습한 배가스에 대하여 제진 및 탈황을 시키는 충진물층, 이 충진물층 사이에서 세정수를 분사시키는 스프레이노즐, 다습한 배가스중의 미세한 오염물질을 굵은 물방울로 포집하여 적하시키는 엘리미네이터, 이 엘리미네이터를 통과하는 분무상태의 수분과 극히 미세한 분진이나 황산화물을 제거하는 디미스터가 구비된 제진및탈황장치와; 이 제진및탈황장치의 스프레이노즐과 엘리미네이터로 세정수를 공급하는 집수조와; 이 집수조에 담긴 세정수의 수소이온농도를 높이기 위한 중화제가 저장됨으로써 상기 집수조로 중화제를 송급하는 중화제저장조와; 상기 집수조의 세정수에 함유된 아황산마그네슘을 용해성이 우수한 황산마그네슘으로 산화시키는 산화장치와; 상기 집수조의 세정수가 상기 제진및탈황장치를 순환하고서 발생되는 폐수를 냉각시키는 냉각탑과; 상기 산화장치로부터 폐수를 송급받고 상기 중화제저장조로부터 중화제를 공급받아 폐수를 정화시키고, 폐수를 상기 산화장치로 순환시키면서 산소를 취입받아 폐수중에 잔류하는 아황산마그네슘을 황산마그네슘으로 산화시키며, 슬러지를 물과 분리시켜 청정수를 상기 집수조로 재순환시키는 정수장치와; 이 정수장치로부터 농축슬러지를 송급받아 농축슬러지의 함수율을 낮추어 슬러지를 케이크화시키는 탈수장치로 이루어지는 것을 특징으로 한다.Facilities for dust removal and desulfurization of flue gas during steel production and bunker seed oil combustion according to the present invention for achieving the above object, and a dust collecting device for collecting and removing large particles of dust from the pollutant source; A cooling device in which a plurality of spray nozzles are arranged to quench the high-temperature exhaust gas passing through the dust collector by a blowing fan; Filling layer to dampen and desulfurize the humidified flue gas quenched and introduced by this cooling device, spray nozzle for spraying washing water between the packed layer, and fine contaminants in the humid flue gas are collected by thick water droplets. A dust removal and desulfurization apparatus equipped with an eliminator for dropping, a demister for removing water in an atomized state passing through the eliminator and extremely fine dust or sulfur oxides; A water collecting tank for supplying washing water to the spray nozzle and eliminator of the dust removal and desulfurization apparatus; A neutralizing agent storage tank for supplying neutralizing agents to the water collecting tank by storing a neutralizing agent for increasing the hydrogen ion concentration of the washing water contained in the water collecting tank; An oxidation apparatus for oxidizing magnesium sulfite contained in the washing water of the sump to magnesium sulfate having excellent solubility; A cooling tower for cooling the wastewater generated by circulating the dust removal and desulfurization apparatus in the water collecting tank; The wastewater is supplied from the oxidizer, the neutralizer is supplied from the neutralizer storage tank to purify the wastewater, the oxygen is blown into the oxidizer by bleeding the magnesium sulfite remaining in the wastewater into magnesium sulfate, and the sludge is separated from the water. A water purification device for separating and recirculating clean water to the sump tank; It is characterized by comprising a dewatering device for feeding the sludge from the water purification device to lower the water content of the concentrated sludge to cake the sludge.

또한, 본 발명에 따른 철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 방법은, 배가스중에 함유된 큰 입자의 분진을 1차적으로 포집·제거하는 단계와; 배가스를 냉각수로 급냉시켜 다습한 배가스로 만드는 단계와; 다습한 배가스에 중화제로 중화된 세정수를 분사시키면서 충진물층으로 통과시켜 제진 및 탈황하고, 다습한 배가스중의 미세한 오염물질은 엘리미네이터로써 굵은 물방울로 적하시키며, 분무상태의 수분과 극히 미세한 분진이나 황산화물은 디미스터로써 포집 제거하여 배가스를 청정화시키는 단계와; 배가스의 청정화로 발생되는 폐수를 냉각시키는 단계와; 냉각된 폐수를 중화시키고, 산소를 취입하여 폐수중의 아황산마그네슘을 황산마그네슘으로 산화시키며, 슬러지를 물과 분리시켜 폐수를 청정화하여 청정수를 재순환시키는 단계와; 슬러지의 함수율을 낮추어 슬러지를 케이크화시키는 단계로 이루어지는 것을 특징으로 한다.In addition, the method for dust removal and desulfurization of flue gas during steel production and bunker seed oil combustion according to the present invention comprises the steps of: first collecting and removing dust of large particles contained in the flue gas; Quenching the exhaust gas with cooling water to produce a humid exhaust gas; Dehumidification and desulfurization by passing through the filling layer while injecting the neutralized washing water into the humidified flue gas as a neutralizing agent. Or sulfur oxides are collected and removed with a demister to purify the exhaust gas; Cooling the wastewater generated by the purification of the exhaust gas; Neutralizing the cooled wastewater, blowing oxygen to oxidize magnesium sulfite in the wastewater to magnesium sulfate, separating the sludge from the water to purify the wastewater, and recycling the clean water; It characterized by consisting of the step of lowering the water content of the sludge to cake the sludge.

도 1은 본 발명에 따른 배가스의 제진 및 탈황을 위한 설비를 나타낸 도면,1 is a view showing a facility for dust removal and desulfurization of exhaust gas according to the present invention,

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

10 : 집진장치 20 : 냉각장치10: dust collecting device 20: cooling device

30 : 제진및탈황장치 40 : 집수조30: dust removal and desulfurization device 40: water collection tank

50 : 중화제저장조 60 : 산화장치50: neutralizer storage tank 60: oxidizer

70 : 냉각탑 80 : 정수장치70: cooling tower 80: water purifier

90 : 탈수장치90: dewatering device

이하 본 발명의 바람직한 실시예를 상세히 설명하면 다음과 같다.Hereinafter, the preferred embodiment of the present invention will be described in detail.

첨부도면 도 1은 본 발명에 따른 배가스의 제진 및 탈황을 위한 설비를 나타낸 도면으로서, 도시된 바와 같이 본 발명에 따른 철강제조 및 벙커씨유의 연소시 배가스의 제진 및 탈황을 위한 설비는, 오염물질 발생원으로부터 큰 입자의 분진을 포집·제거하는 집진장치(10)와; 이 집진장치(10)를 거쳐온 고온의 배가스를 송풍팬(11)에 의해 송급받아 급냉시킬 수 있도록 다수의 스프레이노즐(20a)이 배치되어 있는 냉각장치(20)와; 이 냉각장치(20)에 의해 급냉되고서 인입되는 다습한 배가스에 대하여 제진 및 탈황을 시키는 충진물층(30a), 이 충진물층(30a) 사이에서 세정수를 분사시키는 스프레이노즐(30b), 다습한 배가스중의 미세한 오염물질을 굵은 물방울로 포집하여 적하시키는 엘리미네이터(30c), 이 엘리미네이터(30c)를 통과하는 분무상태의 수분과 극히 미세한 분진이나 황산화물을 제거하는 디미스터(30d)가 구비된 제진및탈황장치(30)와; 이 제진및탈황장치(30)의 스프레이노즐(30b)과 엘리미네이터(30c)로 세정수를 공급하는 급수펌프(41)를 구비한 집수조(40)와; 이 집수조(40)에 담긴 세정수의 수소이온농도를 높이기 위한 중화제가 저장됨으로써 펌프(51)에 의해 상기 집수조(40)로 중화제를 송급하는 중화제저장조(50)와; 블로어(61)를 통하여 외부로부터 산소를 강제 취입받아 폐수중에 잔류하는 아황산마그네슘을 황산마그네슘으로 산화시키며, 슬러지를 물과 분리시켜 청정수를 상기 집수조(40)로 재순환시키는 산화장치(60)와; 상기 집수조(40)의 세정수가 상기 제진및탈황장치(30)를 순환하고서 발생되는 폐수를 펌프(42)로 이송받아 냉각시키는 냉각탑(70)과; 상기 산화장치(60)로부터 펌프(62)를 통해 폐수를 송급받고 상기 중화제저장조(50)로부터 중화제를 공급받아 폐수를 정화시키는 정수장치(80)와; 상기 산화장치(60)로부터 펌프(63)에 의해 농축슬러지를 송급받아 농축슬러지의 함수율을 낮추어 슬러지를 케이크화시키는 탈수장치(90)로 이루어진다.1 is a view showing the equipment for dust removal and desulfurization of the exhaust gas according to the present invention, as shown, the equipment for dust removal and desulfurization of the exhaust gas during the production of steel and combustion of bunker seed oil according to the present invention, contaminants A dust collecting device 10 for collecting and removing large particles of dust from the source; A cooling device 20 in which a plurality of spray nozzles 20a are disposed to quench the high-temperature exhaust gas passing through the dust collector 10 by quenching the fan 11; Filling layer 30a for dedusting and desulfurizing the humid exhaust gas quenched by the cooling device 20 and spray nozzle 30b for spraying the washing water between the filling layer 30a and humid An eliminator (30c) that collects and drips fine contaminants in the exhaust gas into coarse droplets, and a demister (30d) that removes water in the sprayed state and extremely fine dust or sulfur oxides passing through the eliminator (30c). Is provided with a vibration suppression and desulfurization device (30); A water collecting tank 40 having a water supply pump 41 for supplying washing water to the spray nozzle 30b and the eliminator 30c of the vibration suppression and desulfurization apparatus 30; A neutralizing agent storage tank 50 for supplying neutralizing agents to the water collecting tank 40 by a pump 51 by storing a neutralizing agent for increasing the hydrogen ion concentration of the washing water contained in the water collecting tank 40; An oxidizer 60 forcibly drawing oxygen from the outside through the blower 61 to oxidize magnesium sulfite remaining in the waste water to magnesium sulfate, separating sludge from water, and recycling clean water to the sump 40; A cooling tower (70) for cooling the waste water generated by circulating the dust removal and desulfurization apparatus (30) of the water collecting tank (40) by being transferred to a pump (42); A water purifier (80) for supplying wastewater from the oxidizer (60) through a pump (62) and receiving a neutralizer from the neutralizer storage tank (50) to purify the wastewater; The dehydration apparatus 90 receives the concentrated sludge by the pump 63 from the oxidizer 60 and lowers the water content of the concentrated sludge to cake the sludge.

여기서, 상기 냉각장치(20)에는 대략 200∼250℃정도의 고온이면서 황산화물을 함유한 배가스를 60℃이하로 냉각시킴과 아울러 황산으로 하기 위해 세정수를 분사하는 스프레이노즐(20a)이 냉각장치(20)의 원주방향으로 6개 정도씩 5단으로 구비되되, 살수반경내에서 다방향으로 세정수를 골고루 분사할 수 있고 미세한 이물질에 의해 분사구가 잘 막히지 않는 풀콘타입(Full Cone Type)으로서, 그 재질은 산에 의한 부식을 막을 수 있는 테프론으로 되어 있다.Here, the cooling device 20 has a spray nozzle 20a for cooling the exhaust gas containing sulfur oxides at a high temperature of about 200 to 250 ° C. to 60 ° C. or less and spraying washing water to make sulfuric acid. As a full cone type, which is provided in five stages of about six in the circumferential direction of 20, it can evenly spray the washing water in multiple directions within the spraying radius and the nozzle is not blocked by fine foreign matter. The material is made of Teflon which can prevent corrosion by acid.

또한, 상기 제진및탈황장치(30)는 분진을 포집할 수 있도록 기체와 액체간의 접촉효율이 좋은 충진물층(30a)이 상하로 다층 배열된 구조를 가지면서, 각 충진물층(30a)의 구간에는 다수의 스프레이노즐(30b)이 취부되고, 최상단의 충진물층(30a) 상측에는 상하로 경로가 연장되도록 지그재그형상을 갖는 엘리미네이터(30c)가 배치되고, 이 엘리미네이터(30c)의 상측에는 그물형상의 폴리프로필렌을 여러겹으로 적층한 디미스터(30d)가 배치된다.In addition, the dust removal and desulfurization apparatus 30 has a structure in which the filling layer 30a having a good contact efficiency between the gas and the liquid is arranged up and down so as to collect dust, and in each section of the filling layer 30a. A plurality of spray nozzles 30b are mounted, and an eliminator 30c having a zigzag shape is disposed above the filler layer 30a at the uppermost end so as to extend a path up and down, and above the eliminator 30c. The demister 30d which laminated | stacked several layers of mesh polypropylenes is arrange | positioned.

또한, 상기 중화제저장조(50)에 저장하여 사용할 중화제로는 중화제사용으로 인한 2차 슬러지 발생을 방지할 수 있는 해수 수산화마그네슘(Mg(OH)2)으로 한다.In addition, the neutralizing agent to be stored and used in the neutralizing agent storage tank 50 is made of seawater magnesium hydroxide (Mg (OH) 2 ) which can prevent the secondary sludge generation due to the use of the neutralizing agent.

또한, 상기 산화장치(60)는 공기와 물의 접촉을 극대화하기 위해 미세한 구멍을 여러개 형성한 산기배관을 수중에 설치한 구조로 되어 있으며, 상기 정수장치(80)는 그 내부에 활성탄과 분진제거용 필터가 설치된 구조를 갖는다.In addition, the oxidizer 60 has a structure in which an acid pipe formed with a plurality of fine holes in the water in order to maximize the contact between air and water, the water purifier 80 is for removing activated carbon and dust therein It has a structure in which a filter is installed.

이와 같이 이루어진 본 발명에 따른 철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 설비의 작용을 설명하면 다음과 같다.Referring to the operation of the facility for dust removal and desulfurization of the exhaust gas during steel production and bunker seed oil combustion according to the present invention made as follows.

먼저, 집진장치(10)는 오염물질 발생원으로부터 배출되는 배가스에 포함되어 있는 분진중 입자가 조대한 분진을 포집하여 적하시키고, 미세한 분진이 포함된 고온의 배가스는 송풍팬(11)을 이용하여 냉각장치(20)로 이송시킨다.First, the dust collector 10 collects and drops coarse dust particles in the dust included in the exhaust gas discharged from the pollutant generating source, and the high temperature exhaust gas containing the fine dust is cooled by using the blower fan 11. Transfer to (20).

또, 상기 냉각장치(20)는 스프레이노즐(20a)을 통해 분사되는 세정수로 대략 200∼250℃정도의 고온이면서 황산화물(SO2)을 함유한 배가스를 60℃이하로 급냉시키며 유황성분을 황산으로 변화시킨다.(SO2+ H2O → H2SO3)In addition, the cooling device 20 is a washing water sprayed through the spray nozzle 20a to quench the exhaust gas containing sulfur oxide (SO 2 ) at a temperature of about 200 to 250 ° C. to 60 ° C. or less, and remove sulfur components. Change to sulfuric acid (SO 2 + H 2 O → H 2 SO 3 )

또, 제진및탈황장치(30)는 상기 냉각장치(20)에 의해 급냉된 배가스에 대하여 충진물층(30a)과 스프레이노즐(30b)로부터 분사되는 세정수에 의해 제진 및 탈황을 실시하고, 엘리미네이터(30c)에서 미세한 분진이 포함된 작은 물방울을 굵은 물방울로 포집하여 적하시키며, 엘리미네이터(30c)를 통과하는 분무상태의 수분과 극히 미세한 분진이나 황산화물은 디미스터(30d)에서 제거하게 된다.In addition, the vibration suppression and desulfurization apparatus 30 performs dust removal and desulfurization by the washing water injected from the filling layer 30a and the spray nozzle 30b with respect to the exhaust gas quenched by the cooling apparatus 20, and elimine Small droplets containing fine dust are collected and dropped into the coarse droplets from the emitter 30c, and the sprayed water passing through the eliminator 30c and the extremely fine dust or sulfur oxides are removed from the demister 30d. do.

또, 집수조(40)는 중화제저장조(50)에 저장된 중화제 즉, 수산화마그네슘을 송급받아 중성의 세정수로 하여 상기 제진및탈황장치(30)의 스프레이노즐(30b)과 엘리미네이터(30c)로 공급한다.(Mg(HSO3) + Mg(OH)2→ 2MgSO3+ 2H2O)In addition, the water collection tank 40 receives neutralizing agent, that is, magnesium hydroxide, stored in the neutralizing agent storage tank 50 as neutral washing water to the spray nozzle 30b and the eliminator 30c of the dust removal and desulfurization apparatus 30. (Mg (HSO 3 ) + Mg (OH) 2 → 2MgSO 3 + 2H 2 O)

또, 산화장치(60)는 산소를 강제 취입받아 폐수중에 잔류하는 아황산마그네슘(MgSO3)을 황산마그네슘(MgSO4)으로 산화시키며(MgSO3+ 1/2O2→ MgSO4), 슬러지를 물과 분리시킴으로써 청정수를 상기 집수조(40)로 재순환시킨다.In addition, the oxidizer 60 is forcibly blown oxygen to oxidize the magnesium sulfite (MgSO 3 ) remaining in the waste water to magnesium sulfate (MgSO 4 ) (MgSO 3 + 1 / 2O 2 → MgSO 4 ), the sludge and water By separating, the clean water is recycled to the sump 40.

또, 냉각탑(70)은 상기 제진및탈황장치(30)를 순환함으로써 분진과 유황성분이 함유된 폐수를 냉각시킨다.In addition, the cooling tower 70 circulates the dust removal and desulfurization apparatus 30 to cool the wastewater containing dust and sulfur components.

또, 정수장치(80)는 상기 산화장치(60)로부터 송급된 폐수에 상기 중화제저장조(50)로부터 공급된 중화제를 첨가하여 폐수를 중화시킨다.In addition, the water purifier 80 neutralizes the wastewater by adding the neutralizer supplied from the neutralizer storage tank 50 to the wastewater supplied from the oxidizer 60.

또, 탈수장치(90)는 상기 정수장치(80)에서 물과 분리된 슬러지를 농축상태에서 탈수,건조함으로써 수분을 제거하여 케이크화한다.In addition, the dewatering device 90 dehydrates and dries the sludge separated from the water in the water purifying device 80 in a concentrated state to remove moisture and cakes.

한편, 본 발명에 따른 철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 방법은, 집진장치를 이용하여 배가스중에 함유된 큰 입자의 분진을 1차적으로 포집·제거하는 단계와; 냉각장치를 이용하여 배가스를 스프레이노즐을 통해 분사되는 냉각수로 급냉시켜 다습한 배가스로 만드는 단계와; 충진물층과 스프레이노즐과 엘리미네이터 및 디미스터를 구비한 제진및탈황장치를 이용하여, 다습한 배가스에 중화제로 중화된 세정수를 스프레이노즐을 통해 분사시키면서 충진물층으로 통과시켜 제진 및 탈황하고, 다습한 배가스중의 미세한 오염물질은 엘리미네이터로써 굵은 물방울로 적하시키며, 분무상태의 수분과 극히 미세한 분진이나 황산화물은 디미스터로써 포집 제거하여 배가스를 청정화시키는 단계와; 냉각탑을 이용하여 배가스의 청정화로 발생되는 폐수를 냉각시키는 단계와; 산화장치 및 정화장치를 이용하여, 냉각된 폐수를 중화제로써 중화시키고, 산소를 취입하여 폐수중의 아황산마그네슘을 황산마그네슘으로 산화시키며, 슬러지를 물과 분리시켜 폐수를 청정화하여 청정수를 재순환시키는 단계와; 탈수장치로써 슬러지의 함수율을 낮추어 슬러지를 케이크화시키는 단계로 이루어진다.On the other hand, the method for dust removal and desulfurization of the flue gas during steel manufacturing and bunker seed oil combustion according to the present invention comprises the steps of: collecting and removing dust of large particles contained in the flue gas primarily by using a dust collector; Quenching the exhaust gas with the cooling water injected through the spray nozzle using the cooling device to produce a humid exhaust gas; Using a dedusting and desulfurization device equipped with a filling layer, a spray nozzle, an eliminator and a demister, dehumidifying and desulfurizing by passing the cleaning water neutralized with a neutralizing agent through humidifying flue gas through the spray nozzle, Fine contaminants in the humid flue gas are dropped into coarse droplets as an eliminator, and the water in the sprayed state and extremely fine dust or sulfur oxides are collected by a demister to purify the flue gas; Cooling the wastewater generated by the purification of the exhaust gas using a cooling tower; Neutralizing the cooled wastewater with a neutralizer using an oxidizer and a purifier, blowing oxygen to oxidize magnesium sulfite into magnesium sulfate, separating sludge from water, and purifying the wastewater to recycle clean water; ; The dewatering device consists of lowering the water content of the sludge to cake the sludge.

위의 각 단계별 작용설명은 전술한 본 발명에 따른 철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 설비에 대한 구성 및 작용설명에 갈음한다.Each step described above is replaced with the description of the configuration and operation of the facility for dust removal and desulfurization of the exhaust gas during the manufacturing and bunker seed oil combustion according to the present invention described above.

이상에서 설명한 바와 같이, 본 발명에 따른 철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 설비와 그 방법에 의하면, 제철 및 제강시에 발생 배출되는 배가스중의 먼지와 황산화물을 제거하여 청정상태의 공기로 방출하고, 이때 사용된 세정수를 수처리후 재사용할 수 있도록 함으로써, 환경보전에 일익을 하게 되는 효과를 갖는다.As described above, according to the present invention and a method for dust removal and desulfurization of the exhaust gas during the production of steel and bunker seed oil according to the present invention, by removing dust and sulfur oxides in the exhaust gas generated during steelmaking and steelmaking Emitted as a clean air, and can be reused after the water treatment at this time, it has the effect of doing a good job of environmental conservation.

Claims (4)

오염물질 발생원으로부터 큰 입자의 분진을 포집·제거하는 집진장치(10)와;A dust collecting device 10 for collecting and removing large particles of dust from the pollutant generating source; 상기 집진장치(10)를 거쳐온 고온의 배가스를 송급받아 급냉시킬 수 있도록 다수의 스프레이노즐(20a)이 배치되어 있는 냉각장치(20)와;A cooling device 20 in which a plurality of spray nozzles 20a are disposed to quench and receive the high-temperature exhaust gas passed through the dust collector 10; 상기 냉각장치(20)에 의해 급냉되고서 인입되는 다습한 배가스에 대하여 제진 및 탈황을 시키는 충진물층(30a)과, 이 충진물층(30a) 사이에서 세정수를 분사시키는 스프레이노즐(30b)과, 다습한 배가스중의 미세한 오염물질을 굵은 물방울로 포집하여 적하시키는 엘리미네이터(30c)와, 이 엘리미네이터(30c)를 통과하는 분무상태의 수분과 극히 미세한 분진이나 황산화물을 제거하는 디미스터(30d)가 구비된 제진및탈황장치(30)와;A filling layer 30a for dedusting and desulfurizing the humidified exhaust gas quenched by the cooling device 20 and a spray nozzle 30b for spraying washing water between the filling layer 30a; An eliminator (30c) that collects and drops fine contaminants in humid exhaust gas with coarse droplets, and a demister (removal of sprayed water and extremely fine dust or sulfur oxides) passing through the eliminator (30c). A dust removal and desulfurization apparatus 30 provided with 30d; 상기 제진및탈황장치(30)의 스프레이노즐(30b)과 엘리미네이터(30c)로 세정수를 공급하는 집수조(40)와;A water collecting tank 40 for supplying washing water to the spray nozzle 30b and the eliminator 30c of the vibration removing and desulfurization apparatus 30; 상기 집수조(40)에 담긴 세정수의 수소이온농도를 높이기 위한 중화제가 저장됨으로써 상기 집수조(40)로 중화제를 송급하는 중화제저장조(50)와;A neutralizer storage tank 50 for supplying a neutralizer to the water collection tank 40 by storing a neutralizing agent for increasing the hydrogen ion concentration of the washing water contained in the water collection tank 40; 외부로부터 산소를 강제 취입받아 폐수중에 잔류하는 아황산마그네슘을 황산마그네슘으로 산화시키며, 슬러지를 물과 분리시켜 청정수를 상기 집수조(40)로 재순환시키는 산화장치(60)와;An oxidizer 60 forcibly drawing oxygen from the outside to oxidize magnesium sulfite remaining in the waste water into magnesium sulfate, separating sludge from water, and recycling clean water to the sump 40; 상기 집수조(40)의 세정수가 상기 제진및탈황장치(30)를 순환하고서 발생되는 폐수를 냉각시키는 냉각탑(70)과;A cooling tower (70) for cooling the waste water generated by circulating the dust removal and desulfurization apparatus (30) of the washing water of the water collecting tank (40); 상기 산화장치(60)로부터 폐수를 송급받고 상기 중화제저장조(50)로부터 중화제를 공급받아 폐수를 중화시키는 정수장치(80)와;A water purifier (80) for supplying wastewater from the oxidizer (60) and receiving a neutralizer from the neutralizer storage tank (50) to neutralize the wastewater; 상기 산화장치(60)로부터 농축슬러지를 송급받아 농축슬러지의 함수율을 낮추어 슬러지를 케이크화시키는 탈수장치(90)로 이루어진 철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 설비.Equipment for dust removal and desulfurization of the exhaust gas during bunker-seed oil combustion and consisting of a dewatering device (90) for feeding the sludge from the oxidizing device (60) to lower the water content of the concentrated sludge to cake the sludge. 제1항에 있어서, 상기 제진및탈황장치(30)의 충진물층(30a)은 상하로 다층 배열되고, 상기 스프레이노즐(30b)은 상기 각 충진물층(30a)의 구간에 다수개가 취부되며, 상기 최상단의 엘리미네이터(30c)는 상하로 경로가 연장되도록 지그재그형상으로 되어 상기 최상단의 충진물층(30a) 상측에 배치되고, 상기 디미스터(30d)는 그물형상의 폴리프로필렌을 여러겹으로 적층한 것으로서 상기 엘리미네이터의 상측에 배치되는 것을 특징으로 하는 철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 설비.The method of claim 1, wherein the filling layer (30a) of the dust removal and desulfurization device 30 is arranged in a multi-layered up and down, a plurality of spray nozzles (30b) are mounted in the section of each of the filling layer (30a), The uppermost eliminator 30c is zigzag-shaped so as to extend the path up and down, and is disposed above the uppermost filling layer 30a, and the demister 30d is formed by stacking multiple layers of mesh polypropylene. And an apparatus for dust removal and desulfurization of exhaust gases during steel production and bunker seed oil combustion, which is disposed above the eliminator. 제1항에 있어서, 상기 중화제저장조(50)에 저장하여 사용될 중화제는 해수 수산화마그네슘인 것을 특징으로 하는 철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 설비.The apparatus for dust removal and desulfurization of exhaust gas during steel production and bunker seed oil combustion according to claim 1, wherein the neutralizing agent used in the neutralization storage tank (50) is seawater magnesium hydroxide. 배가스중에 함유된 큰 입자의 분진을 1차적으로 포집·제거하는 단계와;Collecting and removing the large particles of dust contained in the flue gas firstly; 배가스를 냉각수로 급냉시켜 다습한 배가스로 만드는 단계와;Quenching the exhaust gas with cooling water to produce a humid exhaust gas; 다습한 배가스에 중화제로 중화된 세정수를 분사시키면서 충진물층으로 통과시켜 제진 및 탈황하고, 다습한 배가스중의 미세한 오염물질은 엘리미네이터로써 굵은 물방울로 적하시키며, 분무상태의 수분과 극히 미세한 분진이나 황산화물은 디미스터로써 포집 제거하여 배가스를 청정화시키는 단계와;Dehumidification and desulfurization through the filling layer while injecting the neutralized washing water into the humidified flue gas as a neutralizing agent. Or sulfur oxides are collected and removed with a demister to purify the exhaust gas; 배가스의 청정화로 발생되는 폐수를 냉각시키는 단계와;Cooling the wastewater generated by the purification of the exhaust gas; 냉각된 폐수를 중화시키고, 산소를 취입하여 폐수중의 아황산마그네슘을 황산마그네슘으로 산화시키며, 슬러지를 물과 분리시켜 폐수를 청정화하여 청정수를 재순환시키는 단계와;Neutralizing the cooled wastewater, blowing oxygen to oxidize magnesium sulfite in the wastewater to magnesium sulfate, separating the sludge from the water to purify the wastewater, and recycling the clean water; 슬러지의 함수율을 낮추어 슬러지를 케이크화시키는 단계로 이루어지는 철강제조 및 벙커씨유 연소시 배가스의 제진 및 탈황을 위한 방법.A method for dedusting and desulfurization of flue-gas during steelmaking and bunker seed oil combustion, comprising the step of lowering the water content of the sludge to cake the sludge.
KR1019980049320A 1998-11-17 1998-11-17 System and method for removing dust and desulfurizing of flue gas during steelmaking and combustion of bunker-c oil KR100287286B1 (en)

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WO2006104304A1 (en) * 2005-03-29 2006-10-05 Dai Sung Engineering Environment Co., Ltd. Wet type scrubber for exhaust gas
WO2006118369A1 (en) * 2005-04-30 2006-11-09 Dai Sung Engineering Environment Co., Ltd. Hybrid-type apparatus for treating exhaust gas having a condenser
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Publication number Priority date Publication date Assignee Title
KR100460743B1 (en) * 2002-07-22 2004-12-09 주식회사 포스코 Apparatus for secondary dedusting of exhausted gas from shaft kiln
WO2006104304A1 (en) * 2005-03-29 2006-10-05 Dai Sung Engineering Environment Co., Ltd. Wet type scrubber for exhaust gas
WO2006118369A1 (en) * 2005-04-30 2006-11-09 Dai Sung Engineering Environment Co., Ltd. Hybrid-type apparatus for treating exhaust gas having a condenser
KR101398191B1 (en) 2013-02-27 2014-05-27 (주)대우건설 High temperature purification system for simultaneously removing desulphurization and desalination in synthetic gas using fixed bed single reactor

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