資料4-5 リスクアセスメント・ガイドライン
Contents
1.2.
3. 34 3 8 a 3 1974 6
4. b
5. E E 4
6. a b c DPT
7. 1 y lin
8. 33 7
9. 2
10. 38 12 H ISO Guide 73 2009 JIS Q 0073 3 ln TL
11. gt 3 3
12. 8 79
13. 0 1 0 1 1 2
14. 20 RISCAD lin RIM 1996 4 29 1973 7 RIM Reaction Injection Molding
15. ES 11 7 h E
16. FTPLC 1 2 E HAZOP 16 HAZOP 6 HAZOP
17. 3 2 ISO 31000 2009 JIS Q 31000 2010 0 J 1
18. 4 TL x
19. HAZOP HAZOP 25 No Less More 15 HAZOP HAZOP 15 HAZOP Sooner than Later than Longer than
20. 2
21. A gt B BA a
22. HAZOP What if Checklist i 3 HSE
23. 1 2 3 4 5
24. 4
25. f NR OE CM EN
26. Dow 15 4 2 6 7
27. Risk Assessment and Risk Management for the Chemical Process Industry Stone amp Webster Engineering Corporation o 10 8 9 10 9 2
28. 17 3 30 86 3 1 3 3 2 3
29. 10 3 3 1 E 2
30. HAZOP What if Checklst 3 42
31. 1 2 1 2
32. 2 1 1
33. i Nr N 4M Man Machine Material Method 1
34. HAZOP F PG 1 5 HAZOP 6
35. 3 1 2 3
36. V3 V2 V2 GAS 3 No Less Other than Sooner than No Less Sooner than V2 V2 V3 V2 V2 V2 30 5 4 ESD HAZOP 8 ESD ESD
37. 1 FE E Eg 5 1
38. RR i NE 6 i a CN RM EO i IH
39. 26 3 16 4 PG 1 E V1 i 7 17 3 3
40. a 2 0 8MPa 100 C 3 13 14 5 1 HAZOP E No Less
41. 1961 2 1971 3 ln 1MPa 0 7SMPa
42. 20 28 1 E 6 28 5 4 DD pH lt
43. 12 13 No Less More 2 2 12 HAZOP WA RTE NO NOT MORE LESS REVERSE AS WELL AS
44. 4 4 24 HAZOP 5 2 3 HAZOP HAZOP
45. 3 I n 2 a b ec d e 1D g
46. 1 3 2 a RISCAD 1973 10 18 198 1 ECH
47. 11 RIM HH 11 2
48. DMSO 1993 7 4 1996 7 17 DMSO 2 SAHD THF NAH SAH DMSO NAH THF 2 3
49. Xk hn 3 3 4 A B AB
50. XV 1 XV 2 P 1 31 8 ESD HAZOP XV 1 LtY SS 2 A XV 2 3 AN ON P 1 KK P 2 el 9 ESD HAZOP 18 ESD HAZOP No
51. NE _ 100 20 100 9 gt
52. E 37 10 11
53. 7 JX Ver1 OR 0 RC PP 1 gt E
54. 1 5 1 6 7 23 T 2 2 1 19
55. 4 FTA wt AND OR E ETA FMEA
56. E 20 5 2 HAZOP What if FTA 5 5 2 1 HAZOP HAZOP 4 ESD HAZOP HAZOP HAZOP 4 2 HAZOP HAZOP HAZOP HAZOP re HAZOP HAZOP HAZOP ESD HAZOP 4 HAZOP HAZOP
57. 3 1 3 12 4 3 ISO 31000 4 1 5 ISO 31010 2009 JIS Q 31010 2012
58. 1 eo 2 39 40 13 2 3 6 8 3 2 2012
59. 6 1 Catastrophic 1 I Severe 1 1 ll Moderate 1 1 1 IV Slight 1 Risk Assessment and Risk Management for the Chemical Process Industry Stone amp Webster Engineering Corporation 7 1 1 1 10 1 10 100 1 nn 100 10000
60. HAZOP HAZOP HAZOP 3 ESD HAZOP ESD ON OFF ESD HAZOP
61. PART OF OTHER THAN 13 22 NN Temperature Pressure Level Composition No More Less Reverse As Well As Part of Other than 23 gt 2 2 14 14
62. 4 2 2 AI 3
63. MM RT bn DCS gt FTPLC 29 gt V1 V2 PG 1 lt gt V1 V2 PG 1 lt gt 6 HAZOP
64. Shorter than 5 3 HAZOP F E HAZOP
65. 2 3 4 5 6 7 35 Rt E FE 36 9 19
66. 1 2 3 4 1 2 3 4
67. DMSO NRN lt ECH ECH ECH ECH ECH DMSO 2 2 2
68. 4 yu E HAZOP 4 7 FTPLC 1 HAZOP 27 E E FTPLC 16
69. FTPLC OC 1 gt lt 2 gt e e 3 gt 4 gt 35 HAZOP 1 1 4
70. Ver 1 27 3 26 26 NE
71. E IM 1 E
72. E 1 2012 HAZOP 2010 TIS Q 31000 I Vol 53 JIS Q 0073 ISO Guide 73 2 2012 SO 31000 2010 No 4 2014 2006 41 2010 23 2
73. 3 XV 1 No Less Part of 3 XV 2 No 4 Less Part of 15 Cw P 01 No 6 0 SMPaG PS 1 PS 1 Less 7 PS 1 More 32 6 oR et a BN OS ie 1
74. 4 1 2 3 5 104C 1 6 E 800 900C EE E
75. 3 ESD 4 5 6 7
76. ESD ESD HAZOP 9 ESD ESD 18 XV 1 XV 2 P 1 PCL 1 ESD ESD
77. 1 2 1 RN 1 2 SS 2 2 iS 2 82 3 2 0 SS RN 9 3 11 3 1 832 RE iE Gs 2 11 8 snubs Reaaaeaat 12 Ti 14 JRO NN 14 42 EE 16 8 ii 16 OU 17 5 ET 19 51 iri 19 5 2 21 5 3 HAZOP 26 5 4 ESD HAZOP ee 31 6 RMN SRE 33 7 Greco 34 8 35 9 ER 37 10 ER 38 Oh 38 2 39 9 KKKKKMKMN NR 41 ee 42 3 1 2
78. More HAZOP HAZOP x HAZOP HAZOP Sooner than Longer than HAZOP HAZOP What if
79. 5 2 2 HAZOP EE 6 E 4 HAZOP p HAZOP HAZOP HAZOP FTPLC v 5 21 HAZOP E
80. 1 2 a 2 NE NR
81. E 10000 1 Risk Assessment and Risk Management for the Chemical Process Industry Stone Webster Engineering Corporation 4 3 6 7 1 4 8 16 8
82. 23 1 EN OO OO A NH TI 0
83. Unacceptable 6 1 3 Undesirable 12 3 Acceptable with controls Acceptable as is Risk Assessment and Risk Management for the Chemical Process Industry Stone amp Webster Engineering Corporation 1
84. 3 1 4 4 17 18 5 v E EF
85. 4 ISO 31000 2009 JIS Q 3100 11 0 2010 1 3 3 TISO 31000 2009 2
86. 4 4 2 2 E g H E E E 1
87. 19 PFD Process flow diagram P amp ID Piping and instrumentation diagram I SDS E 8 2 4 lt
88. 4 Dry Gas Y1 V5 V2 V3 V4 or 3 7 17 NN EN Dry GAS 1 No V1 V4 VS V5 Less No Less Other than No Less Other than Sooner than VS VS VS V2
89. 2 3 pH F I
90. FTPLC HAZOP HAZOP HAZOP HAZOP HAZOP ESD HAZOP 1 HAZOP HAZOP No Less Other than 2 HAZOP
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