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RISK-BASED INSPECTION METHODOLOGY, PART 3—CONSEQUENCE OF FAILURE METHODOLOGY 3-65Table 4.14—Toxic Impact Criteria for Toxic ChemicalsToxic ComponentProbit ParametersA B NIDLH(ppm)AEGL3-10(ppm)AEGL3-30(ppm)AEGL3-60(ppm)EPA ToxicEndpoint(mg/L)ERPG-3Acrolein −9.93 2.05 1.00 2 — — — 0.50 —Acrylonitrile −29.42 3.01 1.43 85 — — — 0.08 75Aluminum trichloride −14.65 2.00 1.00 — — — — — —Ammonia −35.90 1.85 2.00 10 — — — 0.14 750Benzene −109.8 5.30 2.00 500 — — — 1,000Bromine −9.04 0.92 2.00 3 — — — 0.01 5Carbon monoxide −37.98 3.70 1.00 1,200 1,700 600 330 — 500Carbon tetrachloride −6.29 0.41 2.50 200 — — — — 750Chlorine −8.29 0.92 2.00 10 — 28 20 0.01 20Ethylene glycolmonoethyl ether−15.54 1.00 2.00 — — — — — —Ethylene oxide −6.21 1.00 1.00 800 — — — — —Formaldehyde −12.24 1.30 2.00 20 — — — 0.01 25Hydrogen chloride −16.85 2.00 1.00 50 620 210 100 0.03 150Hydrogen cyanide −29.42 3.01 1.43 50 27 21 15 — 25Hydrogen fluoride −48.33 4.853 1.00 30 170 62 44 —Hydrogen sulfide −31.42 3.01 1.43 100 76 60 50 — 100Methanol — — — — 15,000 15,000 7,900 —Methyl bromide −56.81 5.27 1.00 — — — — — 200Methyl isocyanate −5.64 1.64 0.65 — — — — — —Nitric acid −5.48 1.00 2.00 — — — — — —Nitrogen dioxide −13.79 1.40 2.00 20 — — — — —Phosgene −19.27 3.69 1.00 2 3.6 1.5 0.75 — —Propylene oxide −7.415 0.509 2.00 400 — — — 0.59 750Styrene — — — 700 — — — — 1,000Sulphur dioxide −15.67 2.10 1.00 100 — — — — —Toluene −6.79 0.41 2.50 500 1,600 900 630 — —Toluenediisocyanate−4.49 1.00 2.00 — — — — — —NOTE Shaded areas in the above table designate toxic fluids and toxic impact criteria modeled in the Level 1 consequence analysisdescribed in Section 4.9. In the Level 2 consequence analysis, all data can be considered for all other fluids and toxic impact criteria.
3-66 API RECOMMENDED PRACTICE 581Table 4.15—Example Component Damage CostsEquipmentTypeComponentTypeDamage Cost (2001 U.S. Dollars), holecostSmall Medium Large RuptureCompressor COMPC 10,000 20,000 100,000 300,000COMPR 5,000 10,000 50,000 100,000Heat exchangerHEXSS,HEXTS,HEXTUBE1,000 2,000 20,000 60,000Pipe PIPE-1 5 0 0 20PIPE-2 5 0 0 40PIPE-4 5 10 0 60PIPE-6 5 20 0 120PIPE-8 5 30 60 180PIPE-10 5 40 80 240PIPE-12 5 60 120 360PIPE-16 5 80 160 500PIPEGT16 10 120 240 700PumpPUMP2S,PUMP1S1,000 2,500 5,000 5,000PUMPR 1,000 2,500 5,000 10,000Tank TANKBOTTOM 5,000 0 0 120,000COURSES-10 5,000 12,000 20,000 40,000FINFAN FINFAN_TUBE 1,000 2,000 20,000 60,000VesselFINFANHEADERKODRUM,DRUM1,000 2,000 20,000 60,0005,000 12,000 20,000 40,000FILTER 1,000 2,000 4,000 10,000REACTOR 10,000 24,000 40,000 80,000COLTOP,COLMID,COLBTM10,000 25,000 50,000 100,000
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ForewordNothing contained in any AP
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CONTENTS1 SCOPE ...................
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PART 2PROBABILITY OF FAILURE METHOD
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12.7 Nomenclature .................
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19.6 Determination of the Damage Fa
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CONTENTSTABLE 2.A.1—LEADERSHIP AN
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PART 2, ANNEX 2.BDETERMINATION OF C
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2.B.8 AMINE CORROSION .............
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CONTENTSOVERVIEW ..................
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PART 3CONSEQUENCE OF FAILURE METHOD
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CONTENTS3.A.1 GENERAL .............
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PART 5SPECIAL EQUIPMENT5-1
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Consequence of Failure Methodology
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CONTENTS5.A.1 General .............
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5.A-2 API RECOMMENDED PRACTICE 5815
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5.A-4 API RECOMMENDED PRACTICE 581
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5.A-6 API RECOMMENDED PRACTICE 5815
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