E:전기염 에너지(J)C:정전 용량 V:방전 전압 Q:전기량 2. 탱크 시험자의 필수 장비, 필요한 장비 ① 필수 장비:자기 탐상 시험기, 초음파 두께 측정기, 영상 초음파 시험기 또는 방사선 투과 시험기 및 초음파 시험기 ② 필요 장비 미츠루, 수압 시험 기밀 시험 또는 내압 시험 – 진공 능력 53kPa이상의 진공 누설 시험기, 기밀 시험 장치 수직 수평도 시험:수직 수평도 측정기 3. 위험물 중 I등급 정의 4종류의 위험물의 위험물의 위험물을 작성한다.5O2→ 2CO2+H2O, 연소 범위 2.5~81%5. 수송 취급소┗ 설치 제외 장소 ① 철도 및 도로 터널 내 ② 고속 국도, 자동차 전용 도로의 차도, 긴 참깨 및 중앙 분리대 ③ 호수, 저수지 등에서 수리의 수원이 되는 곳 ④ 급경사지로 붕괴 위험이 있는 지역┗ 재해 방지 조치
진도계 5 이상 펌프정지 및 긴급차단밸브 폐쇄진도계 4 이상 해당 지역에 대한 지진재해 정보를 계속 수집하고, 그 상황에 따라 펌프정지 및 긴급차단밸브 폐쇄배관 관계가 과도하고 강한 지진동을 받았을 때 해당 배관에 관한 최대 상용압력의 1.5배의 압력으로 4시간 이상 수압시험하여 이상 없음을 확인할 것 진도계 5 이상 펌프정지 및 긴급차단밸브 폐쇄진도계 4 이상 해당 지역에 대한 지진재해 정보를 계속 수집하고, 그 상황에 따라 펌프정지 및 긴급차단밸브 폐쇄배관 관계가 과도하고 강한 지진동을 받았을 때 해당 배관에 관한 최대 상용압력의 1.5배의 압력으로 4시간 이상 수압시험하여 이상 없음을 확인할 것
인기글
┗ 특정 수송 취급소 위험물을 이송하기 위한 배관 연장 해당 배관의 기점과 종점이 두개 이상인 경우에는 임의의 기점에서 임의의 종점까지 해당 배관 연장 중 최대의 것을 말한다.이하 동일)이(15)km를 넘거나 위험물을 이송하기 위한 배관에 관련된 최대 상용 압력이(950)kPa이상이고 위험물을 이송하기 위한 배관 연장이(7)km이상임 ┗ 해상 배관(3개 이상 암기)① 배관은 지진, 풍압, 파도 등에 대해서 안전한 구조의 지지물에 의한 지지하는 것 ② 배관은 선박 등의 항행에 의한 손상을 받지 않도록 수면 사이에 필요한 공간을 확보하고 설치하기 ③ 선박의 충돌 등에 의한 배관 또는 그 지지물이 손상을 받을 우려가 있는 경우에는 견고하고 내구력 있는 보호 설비를 설치하는 것 ④ 배관은 다른 공작물(해당 배관 지지물을 제외)에 대해서 배관의 유지 관리상 필요한 간격을 유지하기┗ 설치 허가긴급 차단 밸브 차단 밸브자 서류
구조(부대설비 포함) 설명서 강도에 관한 설명서 기능설명서 제어계통도 밸브의 종류, 형식 및 재료에 대해서 기재한 서류 구조(부대설비 포함) 설명서 강도에 관한 설명서 기능설명서 제어계통도 밸브의 종류, 형식 및 재료에 대해서 기재한 서류
┗위치 및 주의표지 ┗위치 및 주의표지
위치 표시 배관 경로 약 100m마다 수평곡관부 기타 안전상 필요한 곳 기재사항 배관의 상황, 기점과 거리, 매설위치, 연도, 배관의 축방향, 이송자 명주의 표시 지하 매설 배관의 바로 위(배관 상부와 0.3m 이상) 내구성을 가진 합성수지(황색) 배관의 외경 이상 이송 배관의 매설된 상황주의 표지 지상 매설 배관의 경로 일반인이 접근하기 쉬운 장소 및 안전상 필요한 장소의 배관 최근하도 참조 금속제판은 백색 역삼각형, 반사형, 황색각형 반사재, 기타 반사재는 황색이다 위치 표시 배관 경로 약 100m마다 수평곡관부 기타 안전상 필요한 곳 기재사항 배관의 상황, 기점과 거리, 매설위치, 연도, 배관의 축방향, 이송자 명주의 표시 지하 매설 배관의 바로 위(배관 상부와 0.3m 이상) 내구성을 가진 합성수지(황색) 배관의 외경 이상 이송 배관의 매설된 상황주의 표지 지상 매설 배관의 경로 일반인이 접근하기 쉬운 장소 및 안전상 필요한 장소의 배관 최근하도 참조 금속제판은 백색 역삼각형, 반사형, 황색각형 반사재, 기타 반사재는 황색이다
6. 니트로글리세린 ┗분해반응식 C3H5(ONO2)3 → 3CO2+2.5H2O+1.5N2+0.25O2 ┗니트로글리콜6.니트로글리세린 ┗분해반응식 C3H5(ONO2)3 → 3CO2+ 2.5H2O+ 1.5N2+ 0.25O2 ┗니트로글리콜
색순수한 것은 무색, 공업용은 담황색 또는 핑크색 액체 비중 1.5액체 폭속 7,800m/s융점 -22℃ 제조법 에틸렌글리콜+질산+황산용해도수에 불용, 알코올 아세톤벤젠에 잘 녹는다 색순수한 것은 무색, 공업용은 담황색 또는 핑크색 액체 비중 1.5액체 폭속 7,800m/s융점 -22℃ 제조법 에틸렌글리콜+질산+황산용해도수에 불용, 알코올 아세톤벤젠에 잘 녹는다
7. 분말소화약제 ┗1종(중탄산나트륨, NaHCO3) 백색 B, C등급 270℃ 2NaHCO3 → Na2CO3 + CO2 + H2O 850℃ 2NaHCO3 → Na2O + 2CO2 + H2O ┗ 2종(중탄산칼륨, KHCO3) 등급 190℃ 2KHCO3 → K2CO3 → 2O3 + CO2 + CO2 + HO+H590 2KH CO 3 담 2色, 담홍색,4종,p-)┗4종 (중탄산칼륨+요소)2NaHCO3+(NH2)2CO→ K2CO3+2CO2+2NH3 ┗저장용기 충전비7.분말소화약제 ┗1종(중탄산나트륨, NaHCO3) 백색 B, C등급 270℃ 2NaHCO3 → Na2CO3 + CO2 + H2O 850℃ 2NaHCO3 → Na2O + 2CO2 + H2O ┗ 2종(중탄산칼륨, KHCO3) 등급 190℃ 2KHCO3 → K2CO3 → 2O3 + CO2 + CO2 + HO+H590 2KH CO 3 담 2色, 담홍색,4종,p-)┗4종 (중탄산칼륨+요소)2NaHCO3+(NH2)2CO→ K2CO3+2CO2+2NH3 ┗저장용기 충전비
1종 2,3종 4종 0.85 이상 1.45 이하 1.05 이상 1.75 이하 1.5 이상 2.5 이하 1종 2,3종 4종 0.85 이상 1.45 이하 1.05 이상 1.75 이하 1.5 이상 2.5 이하
방사압력 방사시간 전역 방출식 이산화탄소 고압식 2.1MPa 이상 60초 이내 저압식 1.05MPa 이상 60초 이내 불활성가스(IG-55,100,541) 1.9MPa 이상 95% 이상 60초 이내 국소 방출식 이산화탄소와 동일 30초 이내 방사압력 방사시간 전역 방출식 이산화탄소 고압식 2.1MPa 이상 60초 이내 저압식 1.05MPa 이상 60초 이내 불활성가스(IG-55,100,541) 1.9MPa 이상 95% 이상 60초 이내 국소 방출식 이산화탄소와 동일 30초 이내
┗전역방출 불말소화 약제 저장량 ┗전역방출 불말소화 약제 저장량
종별 분말 소화 약제 저장량(kg/m3) 개구부 가산량(kg/m2) 1종 0.64.52종, 3종 0.362.74종 0.241.8 종별 분말 소화 약제 저장량(kg/m3) 개구부 가산량(kg/m2) 1종 0.64.52종, 3종 0.362.74종 0.241.8
┗국소방출분말소화약제저장량 ┗국소방출분말소화약제저장량
1종 분말 2,3종 분말 4종 분말 액체 위험물을 상부를 개방한 용기에 저장하는 경우 등 화재시 연소 면이 온통 한정되어 위험물이 반입될 우려가 없는 경우, 면적식 보호 대상물 표면적(m2)*8.8kg/m2*1.1*계수 표 면적(5.2*1*계수 표 면적(3.6*1.1*계수 기타의 용적식 방호 공간 용적(m3)*(X-Y(a/A)(m/A)(가중 거리)각 M6m2). 43.31.1할론13014.03.01.25
┗이동식 할로겐 화합물 소화설비 ┗이동식 할로겐 화합물 소화설비
소화약제의 양분당 방사량 하론 240~250kg 이상 45kg 이상 하론 121145kg 이상 40kg 이상 하론 130135kg 이상 소화약제의 양분당 방사량 하론 240~250kg 이상 45kg 이상 하론 121145kg 이상 40kg 이상 하론 130135kg 이상
┗청정소화약제 성분비 ┗청정소화약제 성분비
IG-01Ar 100%IG-100N2 100%IG-55N2 50% Ar 50%IG-541N2 52% Ar 40% CO2 8% IG-01Ar 100%IG-100N2 100%IG-55N2 50% Ar 50%IG-541N2 52% Ar 40% CO2 8%
┗할로겐 화합물 소화 설비입니다 ┗할로겐 화합물 소화 설비입니다
FC-3-1-10C4F4F4FK-5-1-12C(O)CF2C(O)2HCFC BLEND AHCFC-123(CHCI2) : 4+75% HCFC-22(CCF)75% HCFC-124CHCIFC3HFC-125CHF2HFC-227eaCF3HFC-236FC-13I
9. 아세트알데히드 인화점 -39℃(책마다 다름, 국가위험물정보센터에는 -40℃) ┗비점 21℃ 휘발성이 강함 과일 냄새 수용성 ┗ 제조법 ①에탄올 산화②에틸렌+산소+촉매(PdCl2) 반응┗는 거울 반응–CH3CHO+2Ag(NH3)2OH→CH3COOH+2Ag+4NH3+H2O┗ 저장 탱크①는 수은, 구리, 마그네슘 또는 그 합금을 사용하지 않을 것②증기 폭발 방지 장치의 불활성화를 취급할 경우는 봉입 방지한다, 단, 지하탱크 저장시설로서 저온유지되는 경우를 제외한 ④ 옥외저장탱크 또는 옥내저장탱크 중 압력탱크는 섭씨 40℃ 이하 유지⑤ 보냉장치가 있는 이동저장탱크는 끓는점 이하 유지(21℃) ⑥보냉장치 없는 이동저장탱크는 섭씨 40℃ 이하 유지 ┗아세트알데히드 이동저장탱크의 구조 ①탱크(맨홀, 주입관 뚜껑 포함)는 두께 3.2mm 이상 강판으로 위험물이 새지 않도록 제작하고 불연성 가스를 봉입할 수 있는 구조일 것. ②냉압 시험 장치는 0kg분. 3kg 압력 십분 수압 10.3류 운반용기 9. 아세트알데히드 인화점 -39℃(책마다 다름, 국가위험물정보센터에는 -40℃) ┗비점 21℃ 휘발성이 강함 과일 냄새 수용성 ┗ 제조법 ①에탄올 산화②에틸렌+산소+촉매(PdCl2) 반응┗는 거울 반응–CH3CHO+2Ag(NH3)2OH→CH3COOH+2Ag+4NH3+H2O┗ 저장 탱크①는 수은, 구리, 마그네슘 또는 그 합금을 사용하지 않을 것②증기 폭발 방지 장치의 불활성화를 취급할 경우는 봉입 방지한다, 단, 지하탱크 저장시설로서 저온유지되는 경우를 제외한 ④ 옥외저장탱크 또는 옥내저장탱크 중 압력탱크는 섭씨 40℃ 이하 유지⑤ 보냉장치가 있는 이동저장탱크는 끓는점 이하 유지(21℃) ⑥보냉장치 없는 이동저장탱크는 섭씨 40℃ 이하 유지 ┗아세트알데히드 이동저장탱크의 구조 ①탱크(맨홀, 주입관 뚜껑 포함)는 두께 3.2mm 이상 강판으로 위험물이 새지 않도록 제작하고 불연성 가스를 봉입할 수 있는 구조일 것. ②냉압 시험 장치는 0kg분. 3kg 압력 십분 수압 10.3류 운반용기
3류 자연발화성 불활성 기체를 봉입하여 밀봉하는 등 공기와 접촉 금지 3류 자연발화성 외 파라핀, 경유, 등유 등 보호액/불활성 기체로 밀봉 수분방지 3류 알킬알루미늄등운반용기 내용적 90% 이하, 50℃ 5% 공간 용적 유지하도록 3류 자연발화성 불활성 기체를 봉입하여 밀봉하는 등 공기와 접촉 금지 3류 자연발화성 외 파라핀, 경유, 등유 등 보호액/불활성 기체로 밀봉 수분방지 3류 알킬알루미늄등운반용기 내용적 90% 이하, 50℃ 5% 공간 용적 유지하도록
┗운반용기 외부표시 주의사항 ┗運搬容器 외부표시 주의사항
1류 알칼리 금속 과산화물화기·충격주의물화기 엄금 가연물 접촉주의 기타 물화기·충격주의 가연물 접촉주의 2류 철 금마화기 주의 물화기 엄금 인화성 고체화기 엄금 기타 물화기 주의 3류 자연 발화성 화기 엄금 공기 접촉 금지금 수성 물엄금 4류 화기 엄금 5류 화기엄금, 충격주의 6류 가연수 접촉주의 1류 알칼리 금속 과산화물화기·충격주의물화기 엄금 가연물 접촉주의 기타 물화기·충격주의 가연물 접촉주의 2류 철 금마화기 주의 물화기 엄금 인화성 고체화기 엄금 기타 물화기 주의 3류 자연 발화성 화기 엄금 공기 접촉 금지금 수성 물엄금 4류 화기 엄금 5류 화기엄금, 충격주의 6류 가연수 접촉주의
┗운반용기 외부표시 주의사항 예외사항(UN의 위험물 운송에 관한 권고, 소방청장) ┗운반기준 ┗운반용기 외부표시 주의사항 예외사항(UN의 위험물 운송에 관한 권고, 소방청장) ┗운반기준
차광성 1류, 3류(자연발화성), 4류(특수인화물), 5류, 6류 방수성 1류(알칼리금속 과산화물), 2류(철금마), 3류(금수성물질) 5류 55℃ 이하 온도분해의 우려물질은 보냉컨테이너등 적정한 관리충격방지 액체위험물 또는 위험등급Ⅱ 고체위험물을 기계로 하역 차광성 1류, 3류(자연발화성), 4류(특수인화물), 5류, 6류 방수성 1류(알칼리금속 과산화물), 2류(철금마), 3류(금수성물질) 5류 55℃ 이하 온도분해의 우려물질은 보냉컨테이너등 적정한 관리충격방지 액체위험물 또는 위험등급Ⅱ 고체위험물을 기계로 하역
재질. 재질.
30L유리(10L) 섬유판 강판 플라스틱 (10L) 삼우 알루미늄판 고무류 짚풀불판 종이목 금속판 철재 드럼 (250L) 합성섬유 30L유리(10L) 섬유판 강판 플라스틱 (10L) 삼우 알루미늄판 고무류 짚풀불판 종이목 금속판 철재 드럼 (250L) 합성 섬유
11.트리에틸알루미늄(에탄의 위험도3~12.4%) 11.트리에틸알루미늄(에탄의 위험도3~12.4%)
연소 2(C2H5)3Al + 21O2→Al2O3 + 15H2O + 12CO2물(C2H5)3Al + 3H2O →Al(OH)3 + 3C2H6염산(C2H5)3Al + 3HCl→AlCl3 + 3C2H6염소(C2H5)3Al + 3Cl2→AlCl3 + 3C2H5Cl메탄올(C2H5)3Al + 3CH3OH→Al(CH3O)3 + 3C2H6에탄올(C2H5)3Al + 3C2H5OH→Al(C2H5O)3 + 3C2H6 연소 2(C2H5)3Al + 21O2→Al2O3 + 15H2O + 12CO2물(C2H5)3Al + 3H2O →Al(OH)3 + 3C2H6염산(C2H5)3Al + 3HCl→AlCl3 + 3C2H6염소(C2H5)3Al + 3Cl2→AlCl3 + 3C2H5Cl메탄올(C2H5)3Al + 3CH3OH→Al(CH3O)3 + 3C2H6에탄올(C2H5)3Al + 3C2H5OH→Al(C2H5O)3 + 3C2H6
12. POTASSIUM PEROXIDE K2O2 colorless or orange determination ┗Dissolved K2O2 → K2O + O2 ┗ objects K2O2 + H2O → 2KOH + 0.5O 2 + Fever ┗CO 2 K2O 2 + 0.5O 2 ┗acetic acid K 2 O 2 + 2CH3COOH → 2CH3COOK + H3CO OK + H2 O┗塩酸 K2+HCl→H3CO+H4 Sulfur→H413 OH3+H3+H3+HSO413.3 OK412. PotASS PEROXIDE K2O2 colorless or orange determination ┗Dissolved K2O2 → K2O + O2 ┗ objects K2O2 + H2O → 2KOH + 0.5O 2 + Fever ┗CO 2 K2O 2 + 0.5O 2 ┗acetic acid K 2 O 2 + 2CH3COOH → 2CH3COOK + H3CO OK + H2 O┗塩酸 K2+HCl→H3CO+H4硫黄→H413 OH3+H3+H3+HSO413.3 OK4
Release Rate (L/m2*min) Radiation Time (min) Type I, III, IV Special Type I, III, IV Special Type I Oil 4483055302 Stone Oil 44820203, 448152515 Water-soluble Type I Type II Type IV 8882040 Release Rate (min) Radiation Time (min) Type I, III, IV Special Type I Oil 44830553025, IV Oil 448203025
III TYPE FLUOROPROTEIN PACKAGE, AQUEOUS MEMBRANE PACKAGE AND OTHER FLUOROPROTEIN PACKAGE, AQUEOUS MEMBRANE PACKAGE AND FIRE EXTINGUISHING AGENT FOR WATER-SOLUBLE III TYPE FLUOROPROTEIN PACKAGE, AQUEOUS MEMBRANE PACKAGE AND OTHER FLUOROPROTEIN PACKAGE, AQUEOUS MEMBRANE PACKAGE AND FIRE EXTINGUISHING AGENT FOR WATER-SOLUBLE
┗water source ┗water source
Fixed gun discharge port gun water volume (see front) * Tank surface area m2 auxiliary gun fire hydrant N (up to 3) * 400 L/min * 20 min gun head surface area * 6.5 (L/min * m2) * 10 min gun monitor N (up to 4) * 400 L/min * 30 min surface hydrant (up to 4) N (up to 30 min fire hydrant), Up to 4)*400L/min *30min
14. Calculation of volume pressure specific gravity – Solve a lot 15. Criteria for determining multiple products (oxidation, ignition < self-reaction, spontaneous ignition, gold water) (1,6<2,4<3,5) ① Oxidative solid + flammable solid = 2 ② Oxidative solid + self-reaction = 5 자기 14. Calculation of volume pressure specific gravity – Solve a lot 15. Criteria for determining multiple products (oxidation, ignition < self-reaction, spontaneous ignition, gold water) (1,6<2,4<3,5) ① Oxidative solid + flammable solid = 2 ② Oxidative solid + self-reaction = 5 자기
Oxygen 2Al + 1.5O2 → Al2O3 Water Al + 3H2O → AI(OH)3 + 1.5H2 hydrochloride Al + 3HCl → AlCl3 + 1.5H2 sulfate Al + 1.5H2SO4 → 0.5Al2(SO4)3 + 1.5H2 sodium hydroxide solution Al + NaOH+H2O → 1.5H2 is produced except for NaAlO 2+1.5H2 combustion reaction, so fine-tuning method is applied Oxygen 2Al + 1.5O2 → Al2O3 Water Al + 3H2O → AI(OH)3 + 1.5H2 hydrochloride Al + 3HCl → AlCl3 + 1.5H2 sulfate Al + 1.5H2SO4 → 0.5Al2(SO4)3 + 1.5H2 sodium hydroxide solution Al + NaOH+H2O → 1.5H2 is produced except for NaAlO 2+1.5H2 combustion reaction, so fine-tuning method is applied
┗Thermit reaction (thermit welding) When iron oxide and aluminum powder are combined and ignited, the thermite reaction produces 2,800℃ 17. PotASS NITRATE DECOMPOSITION REACTION TYPE ┗ DECOMPOSITION REACTION TYPE KNO3→KNO2+0.5O218. FIREPROOFING FENCE HEIGHT ┗Thermit reaction (thermit welding) When iron oxide and aluminum powder are combined and ignited, the thermite reaction produces 2,800℃ 17. PotASS NITRATE DECOMPOSITION REACTION TYPE ┗ DECOMPOSITION REACTION TYPE KNO3→KNO2+0.5O218. FIREPROOFING FENCE HEIGHT
For H<=pD2+a If h=2H>pd2+a h=H-p(D2-d2) For H<=pD2+a If h=2H>pd2+a h=H-p(D2-d2)
┗calculation formula ┗name of curve focal line:corrected combustion limit curve solid line:combustion limit curve Slanted area: Combustion hazard range of protected objects ┗calculation formula ┗name of curve focal line:corrected combustion limit curve solid line:combustion limit curve Slanted area: Combustion hazard range of protected objects
19.Fikuric acid (trinitrophenol) ┗ astrophase – yellow precipitated crystal, pure water colorless, industrial bright yellow, cold water-free hot water, alcohol, ether, benzene, etc. – boiling point of DDNP, etc. – melting point 122.5°C. flash point 150°C. Specific gravity 1.8┗ manufacturing method – benzene is produced by reacting mercury with catalyst 20. Calculation of the Explosive Range of Mixed Gas L= lower limit, U= upper limit, V=volume 19.Fikuric acid (trinitrophenol) ┗ astrophase – yellow precipitated crystal, pure water colorless, industrial bright yellow, cold water-free hot water, alcohol, ether, benzene, etc. – boiling point of DDNP, etc. – melting point 122.5°C. flash point 150°C. Specific gravity 1.8┗ manufacturing method – benzene is produced by reacting mercury with catalyst 20. Calculation of the Explosive Range of Mixed Gas L= lower limit, U= upper limit, V=volume
21. Sodium Peroxide 21. Sodium Peroxide
Water Na2O2 + H2O → 2NaOH + 0.5O2 carbon dioxide Na2O2 + CO2 → Na2CO3 + 0.5O Na2O2 acetate 2 + 2CH3COOH → 2CH3COONA + H Na2O2 hydrochloride + 2HCl → 2NaCl + H2O2 water Na2O2 + H2O → 2NaOH + 0.5O2 carbon dioxide Na2O2 + CO2 → Na2CO3 + 0.5O Na2O2 acetate 2 + 2CH3COOH → 2CH3COONA + Na2O2 H hydrochloride + 2HCl → 2NaCl + H2O2
22. oil repellent 22. oil repellent
Material: Non-flammable and impermeable structures (reinforced concrete, etc.) on the ground surface between reinforced concrete and tanks. However, if the height of the stairway oilproof agent that can be used as soil is not less than 1 m, not more than 0.5 m and not more than 3 m Material: Non-flammable and impermeable structures (reinforced concrete, etc.) on the ground surface between reinforced concrete and tanks. However, if the height of the stairway oilproof agent that can be used as soil is not less than 1 m, not more than 0.5 m and not more than 3 m
23. classification of fire extinguishing difficulty level 23. classification of fire extinguishing difficulty level
Manufacturing and General Handling Offices INDOOR ELECTRIC, OUTDOOR ELECTRIC, (FLAME OF SMOKE) SKUK, WATER SPRAY Manchuria Oil Handling Office (Building Only) and Small Manual Fire Extinguisher (Building, Structures, Dangerous Goods Required Units Only) INDOOR STORAGE STORAGE STORAGE STORAGE STORAGE STORAGE STORAGE INSTALLED IN BUILDING WITH PART OF OTHER USE ① SCU, FIRE EXTINGUISHING EQUIPMENT SUCH AS MOBILE WATER SPRAYING ① + OUTDOORS INSTALLATION TANK (OUTTER FIRE HYDRANT INSTALLED OUTDOORS + WATER SPRAY) Outside the fixed tank, outside the water tank), mobile water tank, mobile, mobile (fire, split, minute), indoor electricity at outdoor storage and transportation facilities, outdoor electricity, (fear of smoke), water spray, dark spot sulfur spray fire extinguishing equipment Manufacturing and General Handling Offices INDOOR ELECTRIC, OUTDOOR ELECTRIC, (FLAME OF SMOKE) SKUK, WATER SPRAY Manchuria Oil Handling Office (Building Only) and Small Manual Fire Extinguisher (Building, Structures, Dangerous Goods Required Units Only) INDOOR STORAGE STORAGE STORAGE STORAGE STORAGE STORAGE STORAGE INSTALLED IN BUILDING WITH PART OF OTHER USE ① SCU, FIRE EXTINGUISHING EQUIPMENT SUCH AS MOBILE WATER SPRAYING ① + OUTDOORS INSTALLATION TANK (OUTTER FIRE HYDRANT INSTALLED OUTDOORS + WATER SPRAY) Outside the fixed tank, outside the water tank), mobile water tank, mobile, mobile (fire, split, minute), indoor electricity at outdoor storage and transportation facilities, outdoor electricity, (fear of smoke), water spray, dark spot sulfur spray fire extinguishing equipment
28. Water reaction products (water reaction memorization) 28. Water reaction products (water reaction memorization)
K, Na, CaCaH NaH hydrogen Ca3P2 Ma3P2 AlPPH3 (phosphine) CaC2 Li2C2H2 (acetylene) Al4C3 trimethylaluminum methane triethylaluminum ethane K, Na, CaCaH NaH hydrogen Ca3P2 Ma3P2 AlPPH3 (phosphine) CaC2 Li2C2C2H2 (acetylene) Al4C3 trimethylaluminum methane triethylaluminum ethane
29. Diethyl ether flash point -40°C ┗ boiling point 34.5°C ignition point 180°C, starry, volatile Strong, colorless and transparent, distinctive fragrance ┗Temperature of moving tank, ┗Dissolved into direct sunlight and produced peroxide upon air contact, put it in a brown bottle and store it in a cool dark place ┗ 10% peroxide detection: yellow removal method within 1 minute METHOD FOR PREVENTING IRON SULFATE OR REDUCED IRON SUL 40 Mesh Copper mesh stored together ┗ Manufacturing method: Dissolve yellow phosphorus by heating ethyl alcohol with thick sulfuric acid ┗Combustion reaction type CS2 + 3O2 → CO2 + 2SO2 ┗Outdoor storage tank wall floor thickness 0.2, water leakage X iron cone tank, public knowledge, ventilation pipe, automatic measuring device omitted 31. Safety education target ① Safety supervisor ② Safety tester = Dangerous goods carrier 32 N = Drainage multiple of designated quantity 29. Diethyl ether flash point -40°C ┗ boiling point 34.5°C ignition point 180°C, starry, volatile Strong, colorless and transparent, distinctive fragrance ┗Temperature of moving tank, ┗Dissolved into direct sunlight and produced peroxide upon air contact, put it in a brown bottle and store it in a cool dark place ┗ 10% peroxide detection: yellow removal method within 1 minute METHOD FOR PREVENTING IRON SULFATE OR REDUCED IRON SUL 40 Mesh Copper mesh stored together ┗ Manufacturing method: Dissolve yellow phosphorus by heating ethyl alcohol with thick sulfuric acid ┗Combustion reaction type CS2 + 3O2 → CO2 + 2SO2 ┗Outdoor storage tank wall floor thickness 0.2, water leakage X iron cone tank, public knowledge, ventilation pipe, automatic measuring device omitted 31. Safety education target ① Safety supervisor ② Safety tester = Dangerous goods carrier 32 N = Drainage multiple of designated quantity
33. Calculation tank volume in oval tank = Intra-tank volume – space volume of tank (5% or 0.1%) 33. Oval tank volume calculation tank volume = In-tank volume – the space volume of the tank (5% or 0.1%)
a —Tank height b — width l of the tank; the length of the middle part of a tank, l1, l2 : the length of the round part of the tank Phosphorus Sulfide ┗Stars a : Tank Height b — width l of the tank; the length of the middle part of a tank, l1, l2 : the length of the round part of the tank 34.Phosphorus sulfide ┗starlike
P4S3 phosphorus trisulfide P2S5 phosphorus pentasulfide P4S7 phosphorus pentasulfide yellow crystal pale yellow crystal Specific gravity 2.03 2.092.19 Ignition 100°C 142°C-boiling point 407°C 514°C melting point 172.5°C 290°C 310°C spontaneous ignition (modulation property) X) P2S5+8H2O→5H2S+2H3PO4CS2, alkali, nitric acid and green alcohol, CS2 minutes or decomposed water and alkaline water P4S3 phosphorus trisulfide P2S5 phosphorus pentasulfide P4S7 phosphorus sulfide yellow crystal pale yellow crystal Specific gravity 2.03 2.092.19 Ignition 100°C 142°C-boiling point 407°C 514°C melting point 172.5°C 290°C 310°C spontaneous ignition (modulation property) X) P2S5+8H2O→5H2S+2H3PO4CS2, alkaline, nitric acid and green alcohol, CS2 minutes or decomposed water with alkaline water, gradually greening water, alkaline water
┗comparison of red and yellow scales ┗comparison of red and yellow scales
Chemical chromotoxicity CS2 solubility hazard grade yellow phosphorus P4 white, pale yellow OO1 red phosphorus P dark red x2 Chemical chromotoxicity CS2 solubility hazard grade yellow phosphorus P4 white, pale yellow OO1 red phosphorus P dark red x2
Halon 2402 Pressurized (discharge valve) 0.51 or more and 0.67 or less Pressure accumulation 0.67 or greater and 2.75 or less Halon 12110.7 or greater and 1.4 or less Halon 1301, HFC-227ea 0.9 or greater and 1.6 or less HFC-23, 1251.2 or higher and 1.5 or lower Halon 2402 Pressurized (discharge valve) 0.51 or more and 0.67 or less Pressure accumulation 0.67 or greater and 2.75 or less Halon 12110.7 or greater and 1.4 or less Halon 1301, HFC-227ea 0.9 or greater and 1.6 or less HFC-23, 1251.2 or higher and 1.5 or lower
┗pressure (nitrogen) of a pressure storage vessel ┗pressure (nitrogen) of a pressure storage vessel
1301, HFC-227ea1211 Low Pressure 2.5MPa1.1 High Pressure 4.22.51301, HFC-227ea1211 Low Pressure 2.5MPa1.1 High Pressure 4.22.5
40.4 Name, product name, chemical formula, presence or absence of defenders, specific gravity – separately organized 41. Combination of air bubble extinguishing agents 40.4 Name, product name, chemical formula, presence or absence of defenders, specific gravity – separately organized 41. Combination of air bubble extinguishing agents
A part of the water discharged from the pump is fed to an inhaler installed in the middle of a pipe connecting a pump discharge pipe and a suction pipe, and the required amount of fire extinguishing agent adjusted by a concentration control valve is fed from a fire extinguisher tank to a pump suction side, Mixing ratio Most constant compressed air gun mixing chamber gun aqueous solution with compressed air or nitrogen as a pressurized source and release (high pressure vessel, regulator) * New introduction, clean air, good quality gun, drug saving (3-6%/0.3-1%) and long distance adjustment A part of the water discharged from the pump is fed to an inhaler installed in the middle of a pipe connecting a pump discharge pipe and a suction pipe, and the required amount of fire extinguishing agent adjusted by a concentration control valve is fed from a fire extinguisher tank to a pump suction side, Mixing ratio Most constant compressed air gun mixing chamber gun aqueous solution with compressed air or nitrogen as a pressurized source and release (high pressure vessel, regulator) * New introduction, clean air, good quality gun, drug saving (3-6%/0.3-1%) and long distance adjustment
42.PotASSIUM PERMANGANATE ┗Dissolved 2KMnO4 → K2MnO4 + MnO2 + O2 ┗Thin sulfate 4KMnO4 + 6H2SO4 + 4MnSO4 + 6H2O + 5O2┗Dense sulfate 2KMnO4 + H2SO4 + 2HMnSO4 (potaluminous sulfate) 43. Tank-only room ┗塊 Phosphorus sulfide, phosphorus subsulfate, phosphorus monosulfate, sulfurous, and mass of sulphuric acid when not faulted 42.PotASSIUM PERMANGANATE ┗Dissolved 2KMnO4 → K2MnO4 + MnO2 + O2 ┗Thin sulfate 4KMnO4 + 6H2SO4 + 4MnSO4 + 6H2O + 5O2┗Dense sulfate 2KMnO4 + H2SO4 + 2HMnSO4 (potaluminous sulfate) 43. Tank-only room ┗塊 Phosphorus sulfide, phosphorus subsulfate, phosphorus monosulfate, sulfurous, and mass of sulphuric acid when not faulted
2 seats (38 or higher), 3 seats, 4 seats, 1st floor of animals and plants, 40 times more than 20,000 L, 10 times more than 2 floors and 10 times more than 5,000 L, 10 times more than 5,000 L 2 seats (38 or higher), 3 seats, 4 seats, 1st floor of animals and plants, 40 times more than 20,000 L, 10 times more than 2 floors and 10 times more than 5,000 L, 10 times more than 5,000 L
┗CHAMBER PUMP FACILITY FOR TANK ONLY Step Height – Non-combustible material 0.2 m or more 44. Magnesium reaction formula ┗CHAMBER PUMP FACILITY FOR TANK ONLY Step Height – Non-combustible material 0.2 m or more 44. Magnesium reaction formula
Combustion Mg + O2 → 2MgO Water 3Mg + H2O → Mg(OH)2 + H2HCl → MgCl2 + H2Sulfate Mg + H2SO4 → MgSO4 + H2 Nitrogen Mg + N2/→ Mg3N2/carbon dioxide Mg + CO 2 → MgO + CO Combustion Mg + O2 → 2 MgO Water 3 Mg + H2O → Mg(OH)2 + H2HCl → MgCl2 + H2Sulfate Mg + H2SO4 → MgSO4 + H2 Nitrogen Mug + N2/MgO Water 3N 2 Carbon Dioxide mg+CO 2 → MgO + CO
┗Water, nitrogen, carbon dioxide, combustion 45. Indoor storage safe distance Exclusion Criteria ① 4 seats, maximum number of indoor storage facilities for storing and handling animal and plant oils = less than 20 times the designated quantity ② 20 times the designated quantity (50 times the bottom 150 m2) or less ┗Water, nitrogen, carbon dioxide, combustion 45. Indoor storage safe distance Exclusion Criteria ① 4 seats, maximum number of indoor storage facilities for storing and handling animal and plant oils = less than 20 times the designated quantity ② 20 times the designated quantity (50 times the bottom 150 m2) or less
Gasoline Handling Office Dangerous Goods Gasoline Handling Office Black Characters White local liquor office gasoline-powered ENGINE STOP BLACK CHARACTER YELLOW BASE MANUFA Equalizer strictly prohibited white Ground manufacturing equalizer caution white character red background manufacturing plant ISOLATED WATER-PROHIBITED WHITE CHARACTER BLUE GROUND MOVING TANK dangerous yellow reflective paint black background Gasoline Handling Office Dangerous Goods Gasoline Handling Office Black Characters White local liquor office gasoline-powered ENGINE STOP BLACK CHARACTER YELLOW BASE MANUFA Equalizer strictly prohibited white Ground manufacturing equalizer caution white character red background manufacturing plant ISOLATED WATER-PROHIBITED WHITE CHARACTER BLUE GROUND MOVING TANK dangerous yellow reflective paint black background
Class 1 Class 2 Class 3 Class 4 Class 5 Class 6 grayish blue Red Recommended yellow blue Excluded the front and back of the tank Up to 40% of the area can be painted in different colors Class 1 Class 2 Class 3 Class 4 Class 5 Class 6 grayish blue Red Recommended yellow blue Excluded the front and back of the tank Up to 40% of the area can be painted in different colors
┗mobile tank storage station for storing or handling alkylaluminum, etc ┗mobile tank storage station for storing or handling alkylaluminum, etc
HYDRAULIC TEST OF STEEL SHEET (TANK, MANHOLE, INJECTION PORT COVER) WITH THICKNESS OF 10mm OR MORE (TANK, INERT GAS SEALING DEVICE OF OPERATION DEVICE WITH PRESSURE EXCEEDING 2/3 OF WATER PRESSURE TEST PRESSURE OF 1900L AND NOT EXCEEDING 4/5 INSTALLATION OUTER SURFACE COATING INERT GAS ENCLOSURE DEVICE OF OPERATION DEVICE WITH PRESSURE EXCEEDING 2/3 OF WATER PRESSURE TEST PRESSURE OF RED COLOR STEEL SHEET (TANK, MANHOLE, INJECTION PORT COVER) UNDER 1900L OF 10 MINUT CAPACITY Installation outer surface paint color red
┗Certificate of completion inspection of two documents in the mobile tank storage station, periodic inspection records ┗Safety device operating pressure 20 kPa to 24 kPa, normal pressure 20 kPa to 1.1 times ┗Alkylaluminum, etc. ①Inert gas at 200 kPa or less at the same time ┗Certificate of completion inspection of two documents in the mobile tank storage station, periodic inspection records ┗Safety device operating pressure 20 kPa to 24 kPa, normal pressure 20 kPa to 1.1 times ┗Alkylaluminum, etc. ①Inert gas at 200 kPa or less at the same time
FREE ALKYL ALUMINUM AND ALKYL LITHIUM REINFORCING LIQUID OF TWO OR MORE FIRE EXTINGUISH 8L24021L Dry sand 150L Carbon dioxide 3.2kg 12112L Expanded pearl rock 640L Fire extinguishing powder 3.3kg 13012L Vehicle fire extinguisher FREE REINFORCEMENT OF TWO OR MORE ALKYL ALUMINUM AND ALKYL LITHIUM 8L24021L Dry sand 150L Carbon dioxide 3.2kg 12112L Expanded pearl rock 640L Fire extinguishing powder 3.3kg 13012L
51. Standard for stationary refueling facilities ① Keep a distance of more than 4m to the road boundary, a distance of more than 2m to the building wall, a distance of more than 4m to the road boundary, a distance of more than 1m to the building wall 51. Standard for stationary refueling facilities ① Keep a distance of more than 4m to the road boundary, a distance of more than 2m to the building wall, a distance of more than 4m to the road boundary, a distance of more than 1m to the building wall
以上20 times the volume of the evacuation center per hour 以上18 m3 per 1 m2 以上18 m3 per 1 m2 局所20 times the volume of the evacuation center per hour 以上18 m3 per 1 m2 全域18 m3 per 1 m2 倍1 hour of the local system
┗If the whole area type is possible (basically local type) ①If the whole area type is valid due to the structure of the building, distribution of the work place, etc. ┗Place to be installed: Building that may cause combustible steam or differentiation ┗Ventilation and exhaust facilities inspection chart of manufacturing and general handling place ┗If the whole area type is possible (basically local type) ①If the whole area type is valid due to the structure of the building, distribution of the work place, etc. ┗Place to be installed: Building that may cause combustible steam or differentiation ┗Ventilation and exhaust facilities inspection chart of manufacturing and general handling place
DAMAGE AND CLOGGING OF DEFORMATION, DAMAGE AND FIXED STATE OF SUITABLE EYE FLASH PREVENTION NET, DAMAGE AND CLOGGING OF SIX EYE FLASH PREVENTION NET, DAMAGE AND CLOGGING OF SIX EYE FLASH PREVENTION NET, DAMAGE OF SIX EYE FLASH DAMPER, DAMAGE OF FUNCTION
Fire Extinguishing Water Bottle 8L0.3 Water Tank (Including 3 Water Bottle) 80L1.5 Water Tank (Including 6 Water Bottle) 190L2.5 Dry Sand (Including 1 shovel) 50L0.5 Expanded Nitrite or Pearl Rock (Including 1 shovel) 160L1.0 Fire Extinguishing Water Bottle 8L0.3 Water Tank (Including 3 water Bottle) 190L2.5 Dry Sand (Including 1 shovel) 50L0.5 Expanded Nitrite or Pearl Rock (Increte 160)
55. Other capacity units of fire extinguishing equipment 56. Types of hazardous substances (i) Chlorates (super, salt, tea, sub), inorganic peroxides and other hazardous substances with a designated quantity of 50 kg among hazardous substances of indoor storage are 10 kg. Administrative Disposition Standards (Location, Structure, or Equipment Change 1, 2, and 3rd Dispositions of Manufacturing Plants, etc.) 55. Other capacity units of fire extinguishing equipment 56. Types of hazardous substances (i) Chlorates (super, salt, tea, sub), inorganic peroxides and other hazardous substances with a designated quantity of 50 kg among hazardous substances of indoor storage are 10 kg. Administrative Disposition Standards (Location, Structure, or Equipment Change 1, 2, and 3rd Dispositions of Manufacturing Plants, etc.)
Failure to obtain permission to change location, structure, or equipment of a manufacturing plant, etc. on the 15th day of suspension of use, repair, remodeling, or use of a manufacturing plant on the 90th day of suspension, or use of a product on the 10th day of suspension Failure to obtain permission to change location, structure, or equipment of a manufacturing plant, etc. on the 15th day of suspension of use, repair, remodeling, or use of a manufacturing plant on the 90th day of suspension, or use of a product on the 10th day of suspension
58.3 Hazardous Substances Reaction Type 59. Benzene Reaction Type – Utilization of water and carbon dioxide generation TBD Water Opening Method 60. Installation Criteria for fire extinguishing equipment (1) Pressurized water supply equipment, manual open valves and fire extinguishing agent mixing equipment. 61. Acetyl peroxide structural type – Operation part of separate arrangement equipment, 62. Installation capacity of alkyl equipment, and 63 manufacturing facilities of alkyl equipment are stored 58.3 Hazardous Substances Reaction Type 59. Benzene Reaction Type – Utilization of water and carbon dioxide generation TBD Water Opening Method 60. Installation Criteria for fire extinguishing equipment (1) Pressurized water supply equipment, manual open valves and fire extinguishing agent mixing equipment. 61. Acetyl peroxide structural type – Operation part of separate arrangement equipment, 62. Installation capacity of alkyl equipment, and 63 manufacturing facilities of alkyl equipment are stored
Heating facilities for storage or handling houses (excluding central heating facilities for public housing) – Manufacturing facilities for military or military purposes, such as livestock, marine heating or drying facilities – Storage facilities, etc-
65. Construction of the building ① Walls, columns, floors, beams, rafters, stair non-combustible materials, fireproof structural walls with no openings other than entrances, in this case, asphalt and other non-corrosive materials. ② Roof (top floor roof) shall be covered with non-combustible materials. ③Window or entrance glass ④ Non-penetrating material for handling liquid hazardous materials, minimum inclined oil collection facilities * -2 (excluding powder conditions, flammable solids), 4 stone, flora and fauna oil, 6 buildings – iron cone structure, hydrogen peroxide (stabilizer: phosphoric acid) ┗ hydrazine 2H2H2O2N+2H2N+2N+2N+2 65. Construction of the building ① Walls, columns, floors, beams, rafters, stair non-combustible materials, fireproof structural walls with no openings other than entrances, in this case, asphalt and other non-corrosive materials. ② Roof (top floor roof) shall be covered with non-combustible materials. ③Window or entrance glass ④ Non-penetrating material for handling liquid hazardous materials, minimum inclined oil collection facilities * -2 (excluding powder conditions, flammable solids), 4 stone, flora and fauna oil, 6 buildings – iron cone structure, hydrogen peroxide (stabilizer: phosphoric acid) ┗ hydrazine 2H2H2O2N+2H2N+2N+2N+2
In the event that a person who has succeeded to the establishment status of a Do Governor’s Manufacturing Plant, etc. within 30 days without changing the location, structure, or equipment subject to reporting (~** days prior to) is dismissed or re-elected (above) tank tester within 30 days Designated institution closed Closed: Designated organization closed fire fighting during a holiday In the event that a person who has succeeded to the establishment status of a Do Governor’s Manufacturing Plant, etc. within 30 days without changing the location, structure, or equipment subject to reporting (~** days prior to) is dismissed or re-elected (above) tank tester within 30 days Designated institution closed Closed: Designated organization closed fire fighting during a holiday
┗Re-appointment of safety supervisor, re-appointment period, persons concerned, within 30 days of appointment ┗ Violation of gasoline handling station use abolition, violator, fine-related person, over-application deadline, 300,000 won fine ┗ Qualification ① Dangerous Goods Technician = All Dangerous Goods = Class 4 Firefighters (3 years) = 4 years ┗Re-appointment of safety supervisor, re-appointment period, persons concerned, within 30 days of appointment ┗ Violation of gasoline handling station use abolition, violator, fine-related person, over-application deadline, 300,000 won fine ┗ Qualification ① Dangerous Goods Technician = All Dangerous Goods = Class 4 Firefighters (3 years) = 4 years
enura plate + CONTACT ENURER PLATE FOR FACING MATERIAL ON BACK SURFACE OF ENURER PLATE + FACE-TO-FACE WELDING OR OVERLAP WELDING LOWER PLATE WITH MATERIAL ON BACK SURF + WELDING LEAF PLATE FOR NEURA PLATE + HORIZONTAL PLATE PART ON LOWER PLATE + INSERTION ALIGNMENT WELDING FOR COMPLETE VERTICAL AND HORIZONTAL JOINT OF LOWER LATERAL enura plate + CONTACT ENURER PLATE FOR FACING MATERIAL ON BACK SURFACE OF ENURER PLATE + FACE-TO-FACE WELDING OR OVERLAP WELDING LOWER PLATE WITH MATERIAL ON BACK SURF + WELDING LEAF PLATE FOR NEURA PLATE + HORIZONTAL PLATE PART ON LOWER PLATE + INSERTION ALIGNMENT WELDING FOR COMPLETE VERTICAL AND HORIZONTAL JOINT OF LOWER LATERAL
76. Separation embankment (oil-proof agent for outdoor storage tanks with capacity of 10 million L or more) ① Height of partition embankment: 0.3 m (total capacity of 200 million L or more, but 0.2 m or lower than oil-proof) ② Material: soil or iron cone ③ Capacity: 10% or more of tank capacity 77. Method and Criteria ① Vertical noise are welded by welder 76. Separation embankment (oil-proof agent for outdoor storage tanks with capacity of 10 million L or more) ① Height of partition embankment: 0.3 m (total capacity of 200 million L or more, but 0.2 m or lower than oil-proof) ② Material: soil or iron cone ③ Capacity: 10% or more of tank capacity 77. Method and Criteria ① Vertical noise are welded by welder
Bottom 2 or more steps 10 mm or less Any position of all vertical connections 10 to 25 or less per location Two of all vertical connections, but one of them is the junction point of all vertical horizontal connections at the bottom and any of all vertical connections 100% (full length) of all vertical connections exceeding 25mm per location Bottom 2 or more steps 10 mm or less Any position of all vertical connections 10 to 25 or less per location Two of all vertical connections, but one of them is the junction point of all vertical horizontal connections at the bottom and any of all vertical connections 100% (full length) of all vertical connections exceeding 25mm per location
Place 2ml of 1 atmospheric pressure in a sample cup, ignite the set temperature immediately on the lid for 1 minute, lower the set temperature for 2.5 seconds after 4mm1 minute, repeat 1 atmospheric pressure, 2ml in the sample cup, and lower the set temperature for 2.5 seconds after 4mm1 minute
┗クリーブランド ┗クリーブランド
The test site shall move horizontally above the upper edge of the sample cup (2) mm or less if the test site is filled with a windless (1 atmospheric pressure) and the surface bubble removal flame is adjusted to a diameter of (4 mm). If the difference between the passing flash point and the set value does not exceed 4°C for each 2°C increase in the temperature of the test product, the temperature flammers and excess flammers shall be re-applied The test site shall move horizontally above the upper edge of the sample cup (2) mm or less if the test site is filled with a windless (1 atmospheric pressure) and the surface bubble removal flame is adjusted to a diameter of (4 mm). If the difference between the passing flash point and the set value does not exceed 4°C for each 2°C increase in the temperature of the test product, the temperature flammers and excess flammers shall be re-applied
85. Qualitative and quantitative risk assessment and analysis techniques 86. Sodium bicarbonate decomposition reaction formula 87. Chemical fire engine fire extinguishing capability facility standard 85. Qualitative and quantitative risk assessment and analysis techniques 86. Sodium bicarbonate decomposition reaction formula 87. Chemical fire engine fire extinguishing capability facility standard
A fire extinguishing chemical tank and a fire extinguishing chemical mixing device having a radiation capacity of 以上2,000 L per minute, a powder tank with a radiation capacity of 以上35 kg per second, a halogen compound radiation capacity of 以上1,000 kg per second, and a halogen compound radiation capacity of 以上40 kg per second A fire extinguishing chemical tank and a fire extinguishing chemical mixing device having a radiation capacity of 以上2,000 L per minute, a powder tank with a radiation capacity of 以上35 kg per second, a halogen compound radiation capacity of 以上1,000 kg per second, and a halogen compound radiation capacity of 以上40 kg per second
88. INSTALLATION STANDARD FOR WATER STRUCTURE AND FIXED OILING EQUIPMENT 89. CARBON DIOXIDE FIRE EXTINGUISHING EQUIPMENT ┗MANUAL STARTING DEVICE Checklist 88. INSTALLATION STANDARD FOR WATER STRUCTURE AND FIXED OILING EQUIPMENT 89. CARBON DIOXIDE FIRE EXTINGUISHING EQUIPMENT ┗Manual Boot Device Checklist
EXISTENCE OF OBSTACLE AROUND OPERATION PART EXISTENCE OF OBSTACLE DAMAGE AND EXISTENCE OF OBSTACLE MARKING AND EXISTENCE OF OBSTACLE EXISTENCE OF OBSTACLE AROUND OPERATION PART EXISTENCE OF OBSTACLE DAMAGE AND EXISTENCE OF OBSTACLE MARKING AND EXISTENCE OF OBSTACLE
┗Installation Criteria 91. Calculation Formula for Ozone Depletion Index, Explanation ┗Installation Criteria 91. Calculation Formula for Ozone Depletion Index, Explanation
An indicator indicating the ozone destruction capacity of a substance (considering chlorine and bromine mass ratio, ozone destruction capacity, etc.), and a reference substance CFC-11’s ozone destruction capacity is determined to be 1. Pressurized water feeder An indicator indicating the ozone destruction capacity of a substance (considering chlorine and bromine mass ratio, ozone destruction capacity, etc.), and a reference substance CFC-11’s ozone destruction capacity is determined to be 1. Pressurized water feeder
Indoor Fire hydrant Manufacturing Plant, etc – PRESSURE FEEDING DEVICE FOR INDOOR FIRE HYDRANT WITH HORIZONTAL DISTANCE OF 25 METHOD OR LESS FROM PROTECTIVE OBJECT TO ONE HOSE CONNECTION PORT FOR EACH FLOOR OF BUILDING AND WITH AT LEAST ONE OR MORE INSTALLATION – To prevent waterproofing pressure from exceeding 0.7 kPa from the tip of a nozzle Distance to indoor hydrant outdoor hydrant hose connection port 25m40m nozzle tip waterproof pressure 0.35MPa0.35MPa water content 7.8m3 (maximum 5) 13.5m3 (maximum 5) = 260 minutes / 30m3m3 / 3m3 / m3 / m3 / m3 / 3 / 3 / 3/ m/3/ 3/3 minutes. PRESSURIZED WATER FEEDER OF 5 M OR LESS Expensive water tank H=h1+h2+35mh1: Friction loss of fire hose head(m)h2: Friction loss of pipe head(m)water gauge, drain pipe, overflow drain pipe, supply pipe, manhole installation pressure tank P=p1+p2+p3+0.35MPap1: Friction loss of pipe head pressure p2: Fliction loss of pipe head pressure p3: Water pump=h+ indoor fire hydrant, etc – PRESSURE FEEDING DEVICE FOR INDOOR FIRE HYDRANT WITH HORIZONTAL DISTANCE OF 25 METHOD OR LESS FROM PROTECTIVE OBJECT TO ONE HOSE CONNECTION PORT FOR EACH FLOOR OF BUILDING AND WITH AT LEAST ONE OR MORE INSTALLATION – To prevent waterproofing pressure from exceeding 0.7 kPa from the tip of a nozzle Distance to indoor hydrant outdoor hydrant hose connection port 25m40m nozzle tip waterproof pressure 0.35MPa0.35MPa water content 7.8m3 (maximum 5) 13.5m3 (maximum 5) = 260 minutes / 30m3m3 / 3m3 / m3 / m3 / m3 / 3 / 3 / 3/ m/3/ 3/3 minutes. PRESSURIZED WATER FEEDER OF 5 M OR LESS Expensive water tank H=h1+h2+35mh1: Friction loss of fire hose head(m)h2: Friction loss of pipe head(m)water gauge, drain pipe, overflow drain pipe, supply water pipe, manhole installation pressure tank P=p1+p2+p3+0.35MPap1: Friction loss of pipe head pressure p2: Friction loss of pipe head pressure p3: Water head pump=h+h+h+h1
Safety distance holding manufacturing plant OO (indoor, outdoor) storage plant OO (indoor, underground, simple, moving) tank storage plant XX (oil, sale, transfer) storage plant XX (indoor, outdoor) storage plant OO (indoor, underground) storage tank storage plant XX (oil, sale and transfer) storage plant XX
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29. HALOGEN COMPOUND 30. TRANSPORTATION CONTAINER Performance Standards ① Mechanical Loader – Comply with the standards set by the Fire Department Director for pressure test, stack test, drop test, airtightness test ② Mechanical Loader, Lower Lift Test, Upper Lift Test, Fall Test, Breakdown Test 31 29. HALOGEN COMPOUND 30. TRANSPORTATION CONTAINER Performance Standards ① Mechanical Loader – Comply with the standards set by the Fire Department Director for pressure test, stack test, drop test, airtightness test ② Mechanical Loader, Lower Lift Test, Upper Lift Test, Fall Test, Breakdown Test 31
DANGEROUS MATERIAL MANUFACTURING PLANT OF OIL PROTECTION PERIOD 2 OR MORE outdoor tank DANGEROUS MATERIAL MANUFACTURING PLANT WITH TANK CAPACITY*0.5 OR MORE MAXIMUM TAN*0.5 + REMAINING*0.1 OR MORE Dangerous Goods Outdoor Tank Storage Station Tan*1.1 (Non-flammable 1) or higher than indoor tank Tan or greater than maximum tank capacity Maximum tan*1.1 (non-flammable 1) or higher DANGEROUS MATERIAL MANUFACTURING PLANT OF OIL PROTECTION PERIOD 2 OR MORE outdoor tank DANGEROUS MATERIAL MANUFACTURING PLANT WITH TANK CAPACITY*0.5 OR MORE MAXIMUM TAN*0.5 + REMAINING*0.1 OR MORE Dangerous Goods Outdoor Tank Storage Station Tan*1.1 (Non-flammable 1) or higher than indoor tank Tan or greater than maximum tank capacity Maximum tan*1.1 (non-flammable 1) or higher
32. Manufacturing of Dangerous Goods 32. Manufacturing of Dangerous Goods
Picklesambenzene + mercury nitrate catalyst TNT toluene + sulfuric acid catalyst diethyl ether ethanol + toluene benzene + toluene benzene + aluminum chloride chloride catalyst chlorobenzene + iron chloride catalyst nitrobenzene + aniline nitrate + ethanol acetate Picklesambenzene + mercury nitrate catalyst TNT toluene + sulfuric acid catalyst diethyl ether ethanol + toluene benzene + toluene benzene + aluminum chloride chloride catalyst chlorobenzene + iron chloride catalyst nitrobenzene + aniline nitrate + ethanol acetate
33. Iron Reaction Formula 33. Iron Reaction Formula
Combustion 2Fe + 1.5O2→Fe2O3 Water vapor 3Fe + 4H2O→Fe3O4 + 4H2 Hydrochloride Fe + 2HCl→FeCl2 + H2 Combustion 2Fe + 1.5O2→Fe2O3 Water vapor 3Fe + 4H3O4 Hydrochloride Fe + 2HCl→FeCl2+H2