リスクアセスメント・ガイドライン （概要版）
Contents
1.2.
3.
4.
5.
6. 4M Man Mach
7. 0
8. HAZOP What if Checklist 3
9. 37 10
10. FTPLC HAZOP 16 HAZOP 6
11. 5 1 11 1 5
12. 2 1 1
13. 4 a 4
14. HSE 1 23
15. BCH ECH ECH ECH ECH DMSO 2 2
16. 34 8 CY A gt Ct ON RO ON 6 5 4 6 28
17. 11
18. a RISCAD 1973 10 18 1985 1 ECH DMSO
19. 33 7
20. 4
21. 3 NO R TT 1 2
22. 2 2
23. 0 1 0 1 40 13 1 2 2012 2 2 2012 3 2010 4 JIS Q 31000 ISO 31000
24. 2 3 3 4 A B AB
25. 1 2 1 2
26. 4 9 100 20C 9 100 CE
27. 42
28. 17 3 30 86 3 1 2
29. RD a 10 3 3 1
30. 36 9 19 19 PFD Process flow diasram P amp ID Piping and instrumentation diagram lt SDS
31. DPT 3 DMSO 1993 7 4 1996 7 17 DMSO 2 DM
32. HAZOP 5 21 1 gt 2 gt lt 3 gt 4 gt HAZOP 1 1
33. 2 3
34. 1 4 TISO 31000 2009JIS Q 31000 2010 11 1 3 3 ISO 31000 2009
35. HAZOP No Less Other than 2 HAZOP HAZOP HAZOP HAZOP 3 BSD HAZOP ESD
36. 1 x 1961 2 1971 3 We
37. 25 NN Flow Temperature Pressure Level Composition No More Less Reverse As Well As Part of Other than 23 2 2 14 14 B
38. E 6 Ff 3 ETA FMEA Du Dow
39. I I 3 3 4 4
40. EEC PD 9 3 2 ISO 31000 2009 JIS Q 31000 2010 0
41. 1 2 1 39 3 4 us
42. 0 75MPa 1MPa a RISCAD RIM
43. po 6 A NY DCS gt V1 V2 G 1 lt gt V1 V2
44. 3 1 3 12 3 0 2 0 8MPa 100 C 1 2MPa
45. No Less More 12 13 22 I 12 HAZOP A NO NOT B E MORE B FE REVERSE oe AS WELL AS B PART OF OTHER THAN 13
46. 24 HAZOP o 5 2 3 HAZOP HAZOP ETPLC HAZOP HAZOP HAZOP HAZOP HAZOP ESD HAZOP 1 HAZOP
47. 1 1
48. 11 7 20 5 2 5 2 1 HAZOP What if FTA 5 HAZOP 4 HAZOP HAZOP HAZOP HAZOP
49. 6
50. 4 1 2 3 5 800 900C 104 1 6
51. 4 Acceptable as is Risk Assessment and Risk Management for the Chemical Process Industry Stone amp Webster Engineering Corporation 1 3 1
52. 2 3 1 4
53. 2 3 Pa 2 1 1 a
54. 8 2 3 1 2
55. 9 MM i NE
56. 6 7 23 2 2 1 RIM
57. 27 3 26
58. 11 1 2 3 ESD
59. FE More 1 No Ei HAZOP HAZOP HAZOP
60. b c e f g h I i k m 5 n 2 a b 2
61. 1 2 3 4 1 ay 2 lt 3 4
62. 1996 4 29 1973 7 RIM Reaction Injection Molding 1 3 2 SN
63. 20 28 A pH a
64. 3 13 4 ISO 31000 4 1 5 ISO 31010 2009 JIS Q 31010 2012 14 HAZOP lan K 5 l Less
65. ESD 8 ESD HAZOP 31 XV 2 pio N P 1 P 2 ee 9 ESD HAZOP 18 ESD HAZOP No 1 1 XV 1
66. 2010 1 2012 6 HAZOP Vol 53 No 4 2014 7 2006 8 IS Q 0073 SO Guide 73 2010 41 23
67. HAZOP What ifF Checklist 3 2 2 2 i 2 9 3 3 1 i OU APO EK KK K KM UK OO 0 7 KK KKK KK KKK 77 TKT KR 9 KKKKO YA A A KTN KANKWKAWKWVN N N5j 7 RE 8UN EE RMK NQN NN Mb 5 NM Ns 5 Ran naa 5 2 i 59 12 5 4 ESD HAZOP 7
68. E H 15 4 2 6 7 6 I
69. 38 12 ISO Guide 73 2009 JIS Q 0073 3 9 2 1 3 4 5
70. 4 HAZOP PG 1 V1 PG 1 5
71. HAZOP 6 HAZOP 7 FTPLC 1 HAZOP
72. 1 2 HAZOP 26 3 16 7 17
73. 1 4 8 16 Va 8 4 Risk Assessment and Risk Management for the Chemical Process Industry Stone amp Webster Engineering Corporation 8 I 9 22 Unacceptable 6 3 Undesirable 12 nb et Acceptable with controls
74. JX LP
75. Catastrophic 1 I Severe 1 1 I Moderate 1 1 1 IV Slight 1 ek L Risk Assessment and Risk Manasement for the Chemical Process Industry Stone amp Webster Engineering Corporation 7 1 1 1 10 1 10 100 1 100 10000 1 E 10000 1 Risk Assessment and Risk Management for the Chemical Process Industry Stone amp Webster Ensineerins Corporation On rH 4 3 6 7
76. HAZOP ESD HAZOP HAZOP JI HAZOP HAZOP ESD HAZOP 4 HAZOP HAZOP HAZOP HAZOP 5 2 2 HAZOP HAZOP HAZOP FTPLC HAZOP FTPLC
77. HAZOP HAZOP Longer than Sooner than a I What if FTA AND OR 4
78. 10 18 5
79. 4 4 17 ON NR ee oN 10
80. ON OFF ESD HAZOP HAZOP HAZOP
81. ESD ESD ESD ESD HAZOP 9 18 ESD XV 1 P 1 PCI 1 ESD XV 1 XV 2 P 1 a
82. 25 No Less More 15 HAZOP HAZOP 15 HAZOP WA Pa Sooner than Later than Longer than Shorter than 5 3 HAZOP HAZOP
83. V2 GAS 3 Less No Less Other than No Less Other than Sooner than No Less Other than Sooner than No Less Sooner than 30 VS VS VS V2 V2 V3 V2 V2 V2 5 4 ESD HAZOP 8
84. FTPLC 27 5 NG 0 A B BA
85. No 1 2 Less Part of 1 3 XV 2 No 1 4 Less Part of 1 5 CW P 01 No 1 6 0 5MPaG PS 1 PS 1 Less 1 7 PS 1 More 32 6 i 0
86. PG 1 FTPLC 6 HAZOP 29 Dry Gas 7 17 2 Ni Dry GAS 1 No V1 V4 VS VS V2 V3 V2
87. SO AH THFE NAH SAH DMSO NAH THF 2 3 H
88. ine Material Method 1 2 3 4 5 6 7 NNN Ss 2 35
89. ti 8 9 kk 12 kk 18 NRN CRP 3 17 42 1
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