KR20080032056A - The system of mobile biochemical gas treatment - Google Patents

The system of mobile biochemical gas treatment Download PDF

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KR20080032056A
KR20080032056A KR1020080018962A KR20080018962A KR20080032056A KR 20080032056 A KR20080032056 A KR 20080032056A KR 1020080018962 A KR1020080018962 A KR 1020080018962A KR 20080018962 A KR20080018962 A KR 20080018962A KR 20080032056 A KR20080032056 A KR 20080032056A
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gas
tower
gas treatment
activated carbon
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윤기섭
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윤기섭
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/02—Separation 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 by adsorption, e.g. preparative gas chromatography
    • B01D53/04—Separation 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 by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0454—Controlling adsorption
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F8/00—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
    • F24F8/10—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
    • F24F8/15—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering by chemical means
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F8/00—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
    • F24F8/10—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
    • F24F8/15—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering by chemical means
    • F24F8/158—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering by chemical means using active carbon
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10—Inorganic adsorbents
    • B01D2253/106—Silica or silicates
    • B01D2253/108—Zeolites
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/30—Physical properties of adsorbents
    • B01D2253/34—Specific shapes
    • B01D2253/342—Monoliths
    • B01D2253/3425—Honeycomb shape

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Analytical Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Treating Waste Gases (AREA)

Abstract

An apparatus for treating biochemical gas is provided to transform harmful gas, which is generated from a biochemical bomb or a germ bomb due to war or terror, into cleaned air promptly. An apparatus for treating biochemical gas comprises a harmful gas-absorbing unit, a preheat exchanger(2), an electric furnace(3), a heat exchanger(4), a nitrification tower(5), an activated carbon-adsorbing tower(6), a back filter(7), a zeolite tower(8), and a chimney(9). All of the constituent components are simultaneously mounted in a 40-feet container.

Description

이동식 생화학 가스 처리장치{The System of Mobile Biochemical Gas Treatment}Mobile Biochemical Gas Treatment

본 발명의 기술 분야는 생화학분야 중 군사장비 기술이다.The technical field of the present invention is the military equipment technology of the biochemical field.

전쟁 또는 테러로 인한 생물학적, 화학적 화생방 오염지역의 공기정화를 위한 재난구호 처리시스템이다.Disaster relief treatment system for air purification of biological and chemical NBC contaminated areas caused by war or terrorism.

본 발명 배경기술은 전시 또는 테러가 발생할 경우 생물학적 공격이나 화학적 피폭에 대응할 수 있는 장치들이 없으며 설령 있다 하더라도 소형이거나 감지수준에 불과하였다.In the background of the present invention, there is no device capable of responding to biological attack or chemical exposure in the event of war or terrorism, and even if it is small, it is only a small detection level.

근래에 들어서는 테러로 인하여 군이나 민간을 가리지 않고 인명을 대량 학살을 목적으로 불특정 다수의 군중 밀집지역인 운동장이나 집회장소 등을 선택하여 무차별 공격하는 의도가 있기에, 이에 대처하는 기술이 필요하게 되었고, 특히 화생방 오염지약까지 신속 대응할 수 있는 기동력이 없었기 때문에 화생방 오염지역 대기오염 정화 처리를 위한 이동식 생, 화학 가스처리 장치의 필요성이 절실한 현실이 본 발명의 배경기술이다.In recent years, due to terrorism, there is an intention to indiscriminately select a playground or a meeting place, which is an unspecified crowded area, for the purpose of mass murder of people, regardless of military or civilian. In particular, since there is no maneuverability capable of quickly responding to the NBC pollution, the background of the present invention is an urgent need for a mobile biochemical and chemical gas treatment device for air pollution purification treatment of NBC pollution area.

본 발명에서 해결하고자 하는 기술적 과제는 화생방 오염지역의 재난구호를 위한 방법으로, 우선 신속한 기동력을 위해 모든 장비는 40피트의 컨테이너에 장착하고, 유입되는 가스 또는 분말(Powder)이 산성인지 알칼리성인지를 구별하도록 하고, 감지 자동센서가 장착되어 실시간 메인 컴퓨터에 전송되면 주 처리장치에서 중화 처리하는 구조로 이루어진다.The technical problem to be solved in the present invention is a method for disaster relief in a biohazardous contaminated area. First, all the equipment is installed in a container of 40 feet for quick maneuverability, and whether the incoming gas or powder is acidic or alkaline. It is distinguished, and is equipped with a detection automatic sensor is sent to the real-time main computer, the neutralization processing in the main processing unit is made.

또한 유입가스 또는 분말이 전기로에 유입되면 1,200℃ 이상이 유지되므로 생물학적 세균이나 탄저균, 바이러스 등 생체미생물 균들은 모두 사멸되고 화학적 가스나 분말들도 중화 탑을 통과함으로서 부식성이나 기타 화학적 특성들을 중화 처리하고 특정 독성을 제외한 부분적 안정화가 이루어지도록 하였다.In addition, when the incoming gas or powder is introduced into the electric furnace, the temperature is maintained at 1,200 ° C or higher. Therefore, all biological microorganisms such as biological bacteria, anthrax, and viruses are killed, and chemical gases or powders are passed through the neutralization tower to neutralize corrosive or other chemical properties. Partial stabilization was allowed except for specific toxicity.

본 발명의 화생방 오염지역 재난구호를 위한 기술적 과제의 해결 수단으로 다음 아홉 단계로 구성되어 있다.The present invention consists of the following nine steps as a means of solving the technical problems for disaster relief zone of the NBC pollution.

제1단계에서는 유해가스를 흡입하여 인터록 및 컨트롤시스템(Interlock and Control System)을 통하여 유입가스가 산성인지 알칼리성분인지를 분석, 확인하도록 하고(도면번호 1), In the first step , the harmful gas is sucked in and analyzed and confirmed whether the inflow gas is an acid or an alkali component through an interlock and control system (Fig. 1).

제2단계에서는 예열교환기를 통하여 흡입, 분석된 가스를 예열하고 (도면번호 2) In the second stage , the gas sucked and analyzed through the preheat exchanger is preheated (No. 2).

제3단계에서는 유해가스를 태울 수 있는 전기로(Refractory)를 설치하였다.(도면번호 3) In the third step , an electric furnace (Refractory) was installed to burn harmful gases (No. 3).

제4단계에서는 3단계에서 타고나오는 가스를 냉각할 수 있는 열교환기(Heat Exchanger)를 통하게 한 다음(도면번호 4) In the fourth stage , a heat exchanger capable of cooling the gas discharged in the third stage is passed (No. 4).

제5단계에서는 중화 탑을 설치하여 냉각된 가스를 산성과 알칼리성으로 중화 할 수 있도록 하고 (도면번호 5) In the fifth step , a neutralization tower is installed to neutralize the cooled gas with acid and alkali (Fig. 5).

제6단계에서는 활성탄 흡착탑(A/C Carbon Filter)을 설치하여, 냉각된 가스 중 유독물질을 흡착할 수 있도록 하였다.(도면번호 6) In the sixth step , an activated carbon adsorption tower (A / C Carbon Filter) was installed to adsorb toxic substances in the cooled gas (Fig. 6).

제7단계에서는 백 필터(Bag Filter Unit)로 미세한 재 또는 먼지 등을 여과할 수 있는 집진장치를 설치하고 (도면번호 7) In the seventh step , a dust collecting device for filtering fine ash or dust with a bag filter unit is installed (Fig. 7).

제8단계에서는 제올라이트 타워를 통하여 다이옥신과 세란. 퓨란 등 유해 가스를 처리할 수 있도록 하고(도면번호 8) In the eighth step , dioxin and seran via zeolite tower. To handle harmful gases such as furan (Fig. 8)

제9단계에는 연돌(굴뚝)을 설치하여 최종 처리된 청정 공기를 대기로 배출하도록 하였다.(도면번호 9) In the ninth step , a stack (chimney) was installed to discharge the final clean air to the atmosphere (Fig. 9).

본 발명에서 얻고자 하는 기대효과는 환경적으로는 화생방 오염지역을 신속히 정화하는 대기오염 정화효과가 있고, 군사적 또는 민간의 재난 구조팀들이 적 또는 재난으로부터 생물학적 세균탄이나 화학탄의 피폭을 받았을 때, 신속하고 안전하게 즉시 현장에 투입하여 가스 및 세균의 종류를 파악하고, 시스템의 가동 후, 처리 효율도 어느 정도인지 배기가스 측정 장치를 통해 알 수 있도록 하는 재난구호 장비로서의 효과가 있다.The expected effect to be obtained in the present invention is environmentally effective to clean air pollution pollution area, and when military or civil disaster rescue teams have been exposed to biological bacterial coal or chemical coal from enemy or disaster, It is effective as a disaster relief equipment that can quickly and safely enter the site immediately to determine the type of gas and bacteria, and after the operation of the system, the degree of treatment efficiency can be known through the exhaust gas measuring device.

본 발명의 작용을 살펴보면 본 시스템에 유입되는 분말(Powder) 가스의 종류가 어떤 것인지를 구별하는 자동센서(Interlock and Control System)가 장착되어 실시간(Real Time) 주 컴퓨터(Main Computer)에 전송되면 주 처리장치(CPU)에서는 산성이 유입될 때는 알칼리성을 분사하여 중화처리하고, 알칼리성이 유입될 때는 산성이 분사되어 중화되는 구조로 이루어진다.Looking at the operation of the present invention is equipped with an automatic sensor (Interlock and Control System) for distinguishing what kind of powder gas flowing into the system (Real Time) is transmitted to the main computer (Real Time) In the processing unit (CPU), when acid flows in, it is neutralized by spraying alkaline, and when alkaline flows, acid is injected and neutralized.

본 발명의 구성에 대한 상세한 내용을 설명하기 위하여 다음과 같이 실시 예를 첨부하였다.In order to explain the details of the configuration of the present invention, the following examples are attached.

[실시예 1]Example 1

유해가스 흡입장치 (Interlock and Control System : 도면번호 1)에 유입된 가스(Gas) 또는 분말(Powder)이 어떤 성분인지를 분석하여 실시간 주 컴퓨터에 전송하면, 중앙처리장치(CPU)에서는 예열교환기(도면번호 2)를 통해 성분에 따른 처리방법을 지시하도록 하였다.When the gas or powder introduced into the noxious gas suction device (Interlock and Control System: No. 1) is analyzed and transmitted to the main computer in real time, the central processing unit (CPU) provides a preheat exchanger ( Through reference numeral 2) to indicate the treatment method according to the component.

예열기의 용도는, 외부에서 유해물질이 바로 전기로로 유입될 수도 있지만 본 시설은 전기로 후단에 있는 열교환기에 1차로 유해 물질을 통과시켜 처리온도를 상승시키기 위한 시설로 열교환기와 일체형으로 구성 하였다.The preheater can be used to directly introduce harmful substances from the outside, but this facility is a facility to increase the treatment temperature by first passing harmful substances through the heat exchanger at the rear of the furnace.

[실시예 2]Example 2

전기로시스템(도면번호 3) 내부에는 전기로 내부를 시각적으로 모니터링하기 위하여 핀홀카메라(Two Pin Hole Cameras) 2세트를 설치하고, 용용온도 측정용 적외선 온도계와, 내부온도 측정용 6개의 열전대(6 Thermocouples) 및 차등압력계(Differential Pressure Gauge)를 통한 유입가스의 특성 분석과 전기로의 작동을 정확히 하였다.Inside the furnace system (Fig. 3), two sets of two pin hole cameras are installed to visually monitor the inside of the furnace, an infrared thermometer for measuring the melting temperature, and six thermocouples for measuring the internal temperature. The characteristics of the inlet gas through the differential pressure gauge and differential pressure gauge and the operation of the electric furnace were corrected.

전기로 내부규격은 0.8m x 0.8m x 1.2m의 크기로 직사각형 모양의 물로 냉각하도록 하고, 최대 작동온도는 1,400℃-OFF, 1,200℃-On으로 중앙위치에서 측정하도록 하였다.The internal dimensions of the furnace were 0.8m x 0.8m x 1.2m and cooled in rectangular water, and the maximum operating temperature was 1,400 ℃ -OFF and 1,200 ℃ -On.

[실시예 3]Example 3

열교환기(Electric Refractory : 도면번호 4)에 유입된 가스 또는 분말은 1,200℃ 이상의 온도를 유지하여 생물학적 세균이나 탄저균, 바이러스 등 생체 미생물 균들을 모두 사멸되도록 하였다.The gas or powder introduced into the heat exchanger (Electric Refractory: No. 4) was maintained at a temperature of 1,200 ° C. or higher to kill all biological microorganisms such as biological bacteria, anthrax, and viruses.

[실시예 4]Example 4

중화조의 탑(도면번호 5)은 전기로 전단에서 유해물질에서 냉각된 가스를 산성과 알칼리성을 분석하여 중화할 수 있도록 하였다.The tower of the neutralization tank (fig. 5) was able to neutralize the gas cooled from harmful substances at the front of the furnace by analyzing acidity and alkalinity.

[실시예 5]Example 5

활성탄 흡착탑(A/C Carbon Filter 도면번호 6)은 4 x 8 Mesh로 하고 차압 게이지를 설치하여 다이옥신과 세린, 퓨란과 같은 유독 물질을 흡착, 탈취할 수 있도록 하였다.Activated carbon adsorption tower (A / C Carbon Filter No. 6) was 4 x 8 Mesh and the differential pressure gauge was installed to adsorb and deodorize toxic substances such as dioxins, serine and furan.

[실시예 6]Example 6

백 필터(Air Pulse Bag Filter Unit : 도면번호 7)에는 정확한 오염공기처리를 위하여 백 외면에 부착된 먼지에 순간적인 펄스제트 기류를 주어 충격력과 역 기류에 의해 털어내도록 하고, 사용온도 180℃의 Nomex와 구경 25A의 펄스 밸브(Diaphrgm v/v), Bag cage와 Venturi는 STS 304 재질로 하고 Air Unit와 0 - 300mmAq의 Manometer 및 6개의 Timer를 장착하여 집진 효율이 높고 안정된 연속운전이 가능하도록 하였다.Air Filter Bag Filter Unit (No. 7) is provided with instantaneous pulse jet air flow to dust attached to the outside of bag for accurate polluted air treatment, and it is shaken off by impact force and back air. Pulse valve (Diaphrgm v / v) with a diameter of 25A, Bag cage and Venturi are made of STS 304 material and equipped with Air Unit, 0-300mmAq Manometer and 6 Timers for high dust collection efficiency and stable continuous operation.

[실시예 7]Example 7

또한 사용하는 Fan은 임펠라 타입의 모터와 방전가드, 방진 스프링으로 운전 중의 오류를 방지하도록 하고, 멀티가스분석기(Multi Gas Analyzer)를 설치하여 Nox, SOx, CO, O2를 분석하도록 했으며, 50RT의 냉각장치시스템(Chiller System)을 설치하여 정확성을 유지하도록 하였다.In addition, the fan used is an impeller-type motor, discharge guard and vibration spring to prevent errors during operation, and a multi gas analyzer is installed to analyze Nox, SOx, CO, O 2 , and 50RT A chiller system was installed to maintain accuracy.

[실시예 8]Example 8

중화 탑에는 화학적 가스(Chemical Gas)나 분말(Powder)들도 통과하도록 하여 부식성이나 기타 화학적 특성들을 중화하도록 특수한 독성을 제외한 부분적 안정화가 이루어지도록 하였다.The neutralization tower also allows chemical gas or powder to pass through, allowing partial stabilization except for specific toxicity to neutralize corrosive or other chemical properties.

[실시예 9]Example 9

2단계 과정의 활성탄 흡착 탑을 통과하도록 하여 유독성이나 기타 유해 물질들을 흡착하고 다이옥신 등 염소 화합물들이 특별히 선택적으로 제거되도록 하였다.The adsorption column was passed through a two-stage activated carbon adsorption tower to absorb toxic and other harmful substances and to specifically remove chlorine compounds such as dioxins.

[실시예 10]Example 10

3단계의 처리과정으로 활성탄 흡착 탑을 통과한 유독 가스 등은 백 필터(Back Filter)를 통과하도록 하여 미세입자들과 먼지 등 물리 화학적 분말(Powder)이나 미생물의 사체(Ash)들이 여과되도록 하였다.Toxic gas that passed through the activated carbon adsorption tower through the three-stage process was passed through the back filter to allow physicochemical powders such as microparticles and dust or ashes of microorganisms to be filtered.

[실시예 11]Example 11

3단계 백 필터를 통과한 가스들은 최종단계로 제4단계 처리장치인 합성 제올라이트 탑을 통과하도록 하고. 본 과정은 4 - 10mm의 합성 제올 라이트로서 구형(원/공)의 4- 10A' (옹그스트롬)의 기공을 가진 물질로서 유독성과 맹독성 물질들과 다이옥신 등의 물질들을 흡착하고 화학물질의 이온화 결합을 교환시키도록 하였다.The gases passed through the three-stage bag filter are passed through the synthetic zeolite tower, the fourth stage treatment unit, to the final stage. This process is a 4-10mm synthetic zeolite with spherical (circle / hole) pores of 4-10A '(angstrom), adsorbing toxic and highly toxic substances and dioxin and ionizing chemicals. Was exchanged.

[실시예 12]Example 12

연돌(굴뚝 : 도면번호 9)은 높이가 높을수록 효율이 좋은 것이지만 이동식 차량의 특성상 높이 올릴 수 없으므로 2 - 3단계의 접이식으로 설치하여 이동 간에는 슬라이드 게이트(Slide Gate)를 닫고 시설 운전시에만 상부로 1- 2m 올려서 사용하도록 하였다. 본 단계까지의 처리공정을 거치면 대부분 청정공기로 판정된다.The higher the chimney (chimney: No. 9), the more efficient it is.However, due to the characteristics of the mobile vehicle, the stack cannot be raised, so it is installed in two or three stages of folding. It was used to raise 1-2m. After the treatment process up to this stage, most of the clean air is determined.

[실시예 13]Example 13

이 모든 장치는 40피트 컨테이너에 장착하고 이 처리시스템의 처리용량은 250CFM (7.1m3/min)가 되도록 하였다.All of these units were mounted in a 40 foot container and the treatment system had a capacity of 250 CFM (7.1 m 3 / min).

[실시예 14]Example 14

활성탄흡착 탑은 상부 투입, 하부 토출방식으로 구성되어 새로운 활성탄은 상부에서 투입하고, 제거하는 활성탄은 하부로 떨어뜨려 제거하도록 했으며 그 규격은 200mm x 200mm 3 set로 STS 316 재질로 구성하였다.Activated carbon adsorption tower is composed of top input and bottom discharge method, new activated carbon is injected from the top, and removed activated carbon is dropped to the bottom to remove and the standard is 200mm x 200mm 3 sets composed of STS 316 material.

[실시예 15]Example 15

백 필터에는 유해물질 중 먼지는 하부로 떨어지고 깨끗한 유해물질은 Dust로 배출되도록 하고 Dust의 처리방법은 하단에 슬라이드 Box를 만들어 Dust포집을 하도록 하였다. 백 필터의 치수는 1,450mm x 660mm x 3set STS316 재질로 하였다.In the bag filter, dust falls to the bottom of the harmful substances and clean hazardous substances are discharged to the dust, and the dust treatment method is to collect the dust by making a slide box at the bottom. The bag filter was made of 1,450mm x 660mm x 3set STS316 material.

1. 민간 밀집지역 즉 운동장, 지하철, 대형극장 및 건물 지역 재난구호 공기 정화시설1. Disaster relief air purification facilities in private dense areas such as sports grounds, subways, large theaters and

2. 대기 오염지역의 공기 정화시설2. Air purification facility in air pollution area

도 1은 본 발명에 따른 이동식 생, 화학 가스처리 시스템1 is a mobile raw, chemical gas treatment system according to the present invention

도 2는 본 발명에 따른 이동식 생, 화학 가스처리 시스템의 설비운영 기반장치 (전원공급방치, 가스, 용수, 압축공기, 전산시설과 GPS 등)Figure 2 is a facility operating infrastructure of mobile raw, chemical gas treatment system according to the present invention (power supply, gas, water, compressed air, computing facilities and GPS, etc.)

Claims (5)

이동식 생, 화학 가스처리장에 있어서In mobile raw and chemical gas treatment plants 제1단계 유해가스 흡입장치, 제2단계 예열교환기,1st stage harmful gas suction device, 2nd stage preheat exchanger, 제3단계 전기로, 제4단계 열교환기,Third stage electric furnace, fourth stage heat exchanger, 제5단계 중화탑, 제6단계 활성탄 흡착탑,5th stage neutralization tower, 6th stage activated carbon adsorption tower, 제7단계 백 필터, 제8단계 제올라이터 탑.7th stage bag filter, 8th stage zeolite tower. 제9단계 연돌(굴뚝) 등 모든 장치들이 40피트용 컨테이너에 동시에 탑재하고 세균이나 화학탄의 피폭에 대한 생화학적 유해가스 처리시스템과,All devices such as the 9th stack (chimney) are simultaneously mounted in a 40-foot container, and the biochemical hazardous gas treatment system for the exposure of bacteria and chemical coal, 청구항 1에 있어서The method according to claim 1 제3단계 전기로에서 가스의 흐름을 통과시키는 통로를 6각형의 벌집 모양(하니 컴)으로 통과시켜 고온에서 가스처리 상승효과를 얻을 수 있도록 한 구조와In the third stage electric furnace, a passage through which gas flows is passed through a hexagonal honeycomb (honeycomb) to obtain a synergistic effect of gas treatment at high temperature. 청구항 2에 있어서The method according to claim 2 자동온도 측정기를 통하여 로 내의 온도를 자유자재로 조정할 수 있는 장치와.A device that can freely adjust the temperature in the furnace through the automatic temperature measuring device. 청구항 1에 있어서The method according to claim 1 제5단계의 중화탑에서 자동 폐하(Ph) 측정 장치에 의해 유입가스가 산성 또 는 알칼리성으로 감지될 때 그 반대되는 약품을 분사시키는 페하( ph)를 중성인 7로 유지시켜주는 조절 장치(알칼리 -＞ 산성액 분사 : 산성일 때 -＞ 알칼리 액 분사) 와Adjusting device that maintains neutral pH 7 when the incoming gas is detected as acidic or alkaline by automatic pH measurement device in the fifth stage of neutralization tower (ph) -> Injection of acidic liquid: When acidic-> Injection of alkaline liquid) and 청구항 1에 있어서The method according to claim 1 제6단계에서 활성탄 흡착탑과 제7단계에서 백 필터와 제8단계에서의 제올라이트 탑을 통과하는 동안 독성 가스를 흡착 제거하는 시스템을 채택하는 연속처리장치.And a system for adsorbing and removing toxic gas while passing through the activated carbon adsorption tower in step 6, the bag filter in step 7, and the zeolite tower in step 8.
KR1020080018962A 2008-02-29 2008-02-29 The system of mobile biochemical gas treatment KR20080032056A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20160094797A (en) 2015-02-02 2016-08-10 이미숙 Portable measuring radioactivity and toxic gas processing device and processing system
KR101654900B1 (en) 2016-02-04 2016-09-07 주식회사 한국루베 Decontaminant composition
KR20160117399A (en) 2016-09-29 2016-10-10 이미숙 Portable measuring radioactivity and toxic gas processing device and processing system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20160094797A (en) 2015-02-02 2016-08-10 이미숙 Portable measuring radioactivity and toxic gas processing device and processing system
KR101654900B1 (en) 2016-02-04 2016-09-07 주식회사 한국루베 Decontaminant composition
KR20160117399A (en) 2016-09-29 2016-10-10 이미숙 Portable measuring radioactivity and toxic gas processing device and processing system

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