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Contents

1.
2. UN R67
3. 2 2
4. 2 Classification of pressure equipment pursuant external internal Strength to Articio 3 in connection with Annex Il of inspectio inspectio 9 n n E Tabie 1n Category IV f tno maximum pressura PS 2 years exceeds one bar 2 Tabls 2 in a category IlI if the maximum pressure PS excoods one bar or b category IV 3 Table 3 in a category II if tho maximum pressure PS is more than 500 bar and the product of PS and the volume V exceeds 10 000 bar liter or b category lI if the product of
5. A FE SE CIT IC E M 21 1 2 3 oW E VES
6. 0 25 1 70 BE 0 05 0 05 1 EN10120 2008 1 1 H 7 1 2 1 JISK 7206 1999 VST IS0306 2004
7. 2m 2m 45 2 m 18 2 1
8. gt 8 OUIO 3 1 6 4 9 OUIO OUIO OUIO
9. ASME Certificate Mark ASME DLE 3 1 3 CFR
10. E 4 8 41 50 7 3 LPeG 1 2 1 1
11. 120 ES OFQXF XJOAxhxp 60 Q Fj F Q 15 0 1MPa m min F 15C 0 1MPa
12. lm 1 g 130 25 R R67
13. 6 98 II man D n H 4 S ali ZH E 1 1958 UNECE 1 D 1958 1958
14. ECE TRANS WP29 1059 2 le NS 2 ECE TRANS WP 2971059 2 a b F E
15. c p n c nuc ERI COF d f e A4 LS
16. ali kz 2 1 c TEC A 2
17. AL 1 1 Ix E UE mml EB 17 A EU 41 50 16 2 175
18. ER _LP LP P LP 2 1 26 1 29 2 26 3 3 3 3 1 1 Y MEN 958 1
19. II 10 sc D D ES Af Ec i5 Trade Register
20. moo e S gu gt 2 1 http www unece org fileadmin DAM trans main wp29 wp29regs updates ECE TRANS WP 29 343 Rev 22 pdf http www unece org fileadmin DAM trans doc 2011 wp29other wp29finaldocs 1000s ECE TR ANS WP29 1059e pdf http www unece org fileadmin DAM trans main wp29 wp29resolutions ECE TRANS WP29 78 r3e pdf JN R IH GRIS 3
21. 0 10mm 0 25mm 3 IS02504 1973 6 3 1 1 2 4mm 4 1 4mm 1 14mm 1 3mm mi 2
22. 10 Virginia Department of Labor and Industry Boiler and Pressure Vessel Safety Division 231H 4 1 C do 5 NBBI R 2 2 OUIO AIA
23. A B C D UN A B 18017025 ISO17020 3 TISO17025 ATV ih ISO17020
24. 2 6MPa 3 0MPa 2 6 75MPa 4 0 00005cm 7h Ka X4 V Va pA 60 P X T 101 6 Vi V z P Vi V 7 T
25. UN ra x Q D x A EN B EN EN 1 ISO IEC 17025 2005 3 ISO IEC 17020 2004 3 45012 1998 j EN ISO EC 17020 2004
26. 2 4 UN 2 5 Bc
27. 67 1 1 Technical requirements LPG 4 1 1 Cylinders covered by this annex are as follows 15 LPG 1 Metal containers 1 LPG 4 All Composite containers 41 50 3 6 7
28. 6 75MPa GEIRI o TIt 4 5MPa 20 8 gt 1 15cm h 7 Low temperature test A LPG containing component shall not leak more than 15 cm3 hour with the outlet plugged when submitted to a gas pressure at the minimum operating temperature 20 C equal to the leakage test pressure Table 3 paragraph 5 3 The component shall be conditioned for at least 8 hours at this temperature 8 2 3
29. 3 9 5i 4 1 4 n 11 101 301 701 EJ 100 300 700 12 MPa L 100 30 T OD A TE ARR II m HH p qe aec pud H X IT fH 30
30. 50 mm Z 25 mm 2 JISZ3104 1995 6 ISO 1106 1 1984 1 50 mm XE B ISO 0 10 mm 0 25 mm 3 NN e OO Siocon LU a cg 3 1
31. OUIO 3 1 6 4 NB 371 OUIO NBBI 2013 11 5 um OUIO 3 1 6 4 NB 371 NBBI NBBI 3 1 6
32. 130 130C 30 3 LPG 4 B3 ME dc LM gt 5 9 5 b Is Ep UA BL DYAN IA RERIBNSRSOU DC 8 1 15 DD 8 Fez RENE SEUR UR 3 3
33. 2 3 3 1 A 3 LPG 1 4 LPG 4 1 LPG 1 JIS G 3103 2012 SB410 SB450 SB450M SB480 SB480M JISG3106 1995 SM400A SM400B SM400C SM490A SM490B SM490C SM490YA SM490YB SM520B SM520C SM570 JIS 6 3114 1988 SMA400AP SMA400AW
34. amp 6G GO AIA AIA Ok lE HE LC 25 2 2 v OUIO OUIA NBBI OUIO 3 1 6 NBB NBBI iX 1919 4
35. OSHA HI Pressure vessel safety order E Ca OSHA AHJ Unfired Pressure Vessel Safety Order LPG Pressure Vessel Safety Order Unfired Pressure Vessel Safety Order Petroleum Safety Order National Board R Form NBBI LPG
36. 0 ZLS ZUS PvU
37. MI1 8 M2 8 5 M3 8 5 N1 3 5 N2 3 5 12 NS3 12 O1 0 75 O2 0 7 3 5 O3 3 5 10
38. 3 f SEG Cx Sp ZUS m 10000 0 1000 0 4000 Maximum allowable pressure P S bar 0 1 10 19 0 1nn f innan O 100000 100000 0 Volume V M 4 ZUS ZUS
39. 11 Washington Department of Labor and Industries Boiler Unfired Pressure Vessel Section NBBI R NBIC 2 2 AIA 12 Detroit Michigan FZ LIAK E Department of Building and Safety Engineering EJ ABE x xao
40. 1 IR ZH Xn II 1
41. gt gt ASNT Level II XIM 2 NDE Level II 2 NDE LevelIl 4 NBBI NBBI 2 2
42. R67 3 3 2 4 R67 4 3 2 4 sz lt Fn Eg pn HH Il 15 38
43. 1 R67 PS R67 6 9 1 yia cobro d Se 9 1 9 2 8 10 15 acies cd Me iu BOR l 10 LPG 15 T 1 1 10 2 3 10 2 3 9 5 3 00 kPa 2
44. 3 1 2 6MPa 1 8 Seat leakage test 8 1 The following tests for seat leakage are to be conducted on samples of service valve or filling unit which have previously been subjected to the external leak test of paragraph 5 above 8 1 1 Seat leakage tests are conducted with the inlet of the sample valve connected to a source of aerostatic pressure the valve in the closed position and with the outlet open A positive shut off valve and a pressure gauge having a pressure range of not less than 1 5 times nor more than 2 times the test pressure are to be installed in the pressure supply piping The pressure gauge is to be installed between the positive shut off valve and the sample under test While under the applied test pressure observations for leakage are to be made with the open outlet submerged in water unless otherwise indicated 8 1 2 Conformance with paragraphs 8 2 to 8 8 below is to be determined by connecting a length of tubing to the valve outlet The open end of this
45. ARUBA E NBBI OUIO
46. PAN 17 A 18 T m Q R67 p A ri HE 17 18 f AX T 48 ETA OR
47. C 1 000 1 5 HDIC HD c 0 900 0 25 1 000 0 38 0 612 0 26 0 931 0 39 0 604 14 0 27 0 885 0 40 0 596 0 28 0 845 0 41 0 588 0 005 0 29 0 809 0 42 0 581 C 0 0075 0 30 0 775 0 43 0 576 001 0 800 0 31 0 743 0 44 0 572 13 002 0 32 0 714 0 45 0 570 0 03 0 33 0 687 0 46 0 568 9 0 34 0 667 0 47 0 566 0 35 0 649 0 48 0 565 0 36 0 633 0 49 0 564 12 0 700 0 37 0 621 0 50 0 564 B 0 600 1 0 2 0 21 0 22 0 23 0 24 0 25 0 500 0 25 0 30 0 35 0 40 0 45 0 50 H D H D 1 2 2 10 2 1 11 2 1 3 1 16 2 1 ABRIT TEUER 22 R R67 weld 23 2 R 5 is H
48. 1 ILPG 1 2 8 1 9 62 15 LPG 4 5 2 6 5 2 1 C DC COS DD BUB 1 2 3 2
49. O d 0 W g REH ELE giam 1 SOEBIRGR NER CREE TUY Rheinland KBA SNCH RDW lu eA
50. g NBIC OUIO JH dt h AC Eg i
51. 0 85 1 2 dh X 1281 1 03 uk NY mom B LK X 21 3 HH 4 10
52. gt ZUS PvU ZUS ZUS ZLS
53. 13 6 3 3 0MPa 30 3 1 2 3 14 1 2 AOKK 3E SE EA ER XL
54. 3 3 0MPa 96 1 120 20C 65 4 5 2 s 6 2 7 2 E 10 3 1 5 3 6 3 7 3 18 1 1
55. 22 LPGC 4 115 1 3 2 1 3 0MPa Cb C 7 3 BEN RO f C a amp E ERI h 100 200 95 350 90 600 85 1000 80 1800 75 3200 70 5900 65 11000 60 21000 2 20 2 3 12 2 3 1
56. um JIS K 5627 1995 130 20 2 JIS K 5628 1995 1 1 2 1 16 1 BL H 08 JIS K 5633 1995 JIS K 5572 1995 130 15 1 2 1 16
57. JLT 3 0MPa 6 75MPa 2 gt ITI Z Hi o 1 13mm 1 2 AX
58. Chevron Richmond Subchapter 15 Chevron Richmond API 510 API 580 3 1 7 Los Angels CCR Department of Building and Safety Los Angels LPG
59. 2 2 10 3 0MPa 3 7MPa 11 3 H ODK K ak iR ABR IF HELTIIJI Z 14 1 2 LPG 4 2 L min 15 LPG 1
60. 0 25 PZI 1 70 Tg 0 05 0 05 3 1 EN10120 2008 7 1 2 1 4 1 1 JIS K 7206 1999 72A v2 839p WEZ 7 AT v 27 UA2 v Fb amp 8IEdH E VST IS0306 2004 ZZ 2A v Z hup HEHE X3 h RAE VST 90 u 100 2 4 Arai E JIS R 3420 2013 Ob CHATE 3 CE JE JIS R 3413 2012 3 7 A amp 0 4 2013 ASTM
61. h gt BR il t 2 3 2 2 3 3 1 3 LPG 1 4 LPG 4 1 LPG 1 R R67 2 3 4 2 1 2 JI
62. Ew 7d 20 icit uoc EN R67 aL en des a 7 2 ISO20826 nc pua R67 10 R67 3 0 MPa 2 9 MPa 2 32 MPa LN H 2 7 0 1 MPa 10 II 34 fi
63. HB E RIADIT 3 WP29 Noise GRB dur MO dude Lighting and Light Signalling GRE iu 3 2014 4 E 1 30 Pollution and Energy GRPE 3 6 eu Brakes and Running Gear GRRF General Safety Provisions GRSG Passive Safety GRSP 1 EU 1958 I 1 2 3 5 6 7 8 10 11
64. p 15 4 10 JARIS002 2 3 16 1 2 6 2 7 2 8 2 2 12 2 13 2 14 2 15 2 16 2 KRE 2 5 2 9 2 10 2 11 RE R R67 17 2 18
65. uu RM IN m M gt 25mm 5 1 65m 6 10cm 7 8 165cm 9 165cm
66. ji 8 1 15 DD 8 3 i m nns LH s7 X ng vA xis ex v2 iN F m Hg i SE E don mh Xn eH zt m X oo 2 d m sto N c Y xu fv n H gY gu ox S S DN Pl o
67. 4 ESN 12 13 1 lm 4 5 6 7 8 9 10 11 4 15 16 17 13 N Hl 14
68. ZA ka 4 ZM rj 7 Bunte CU DEUS 49 RO ZM ri 7 8 R67 3 1 7
69. C 0 50 30 165 cm 165 cm ROREM
70. 10mm aul io EN 6 2 LPG 1 4 m Bv E
71. d ZLS BAuA WEB 2 BetrSichV section17 26 1 ZUS http www baua de de Produktsicherheit Produktinformationen pdf Pruefstellen 01 pdf blob p ublicationFile amp v 13 2 PvU http www baua de de Produkt
72. 3 JIS Z 2241 2011 2 a b 1 3 1 a 1 b ISO 6892 1 2009 4 1 1 3 1 f J EN10002 1 2001 1 BR Hr PEN x 2 1 2 Types of tests and evaluation of test results 2 1 2 1 Each sample container is subjected to the following tests 2 1 2 1 1 Containers with longitudinal and cir
73. lt 1958 EU KBA Eu LION zn at EU US SEDE eu enterprise sectors _ automotive index en htm EA Y EBA http www kba de EN Home en homepage _ node html nnn true BW Te rdw nl englishinformation P aginas default aspx SAI oo Du be Dun Y UOS kerti fication Automotive Certification asDx VCA http www dft gov uk vca index asp SNCH http www snch lu ROETE BE htt
74. 1 2 15 2 3 1 15 3 31 LPG 1 2 7 200 1 1 3 2 16 2 3 1 16 3 32 LPG 1 3 mu
75. 3 d m 2B uu Address of Manufacturer and manufacturer s Logo Minist re du D veloppement durable et des Your letior dated February 01 2014 Infrastructures Contact Mr Yamada D partement des transports Telephone 4 Place de l Europe L 2940 Luxembourg Re Application for ECE approval Dear Sir or Madam We hereby apply for the L3 granting of an L EEC approval granting of an extension Lj ECE approval Roference LPG vehicles Regulation ECE R 67 01 Type 1234 Wo confirm that the application lor above the mentioned type has nol been submitted to any other Member State nor has any other Member State granted a c
76. 8 6 1 2 2 10 2 11 2 3 12 2 13 4 amp 88 2 3H 38 14 2 15 2 No 2 17 2 6 1 3 22 2 H 2 27 2 28 2 2 3 2 31 2 32 zi x x yiri 3 51 3 1 3 3 7 1 2 13 1 3
77. sou ERER zam MM RER amame gem E R67 Annex Annex3 Annex3 Annex3 Annex7 3 FFAS 3 1 3MPa 3MPa 3MPa 3MPa BERR 4 AlS4 O O O a AISS O O O 6 A156 O O O 0 7 A15 7 O O O 8 Ais O O O I 30 _ O ESSE O2 amp 9 A15 9 E O O A3 7 7 O 10 4 A15 10 O 2 9 x 11 A15 11 O O O O 12 13 A15 12 O O O O MHERARR 14 AISI3 O O O 15 A15 14 O O O O 16 A15 15 O O O 17 A15 16 O O O 1 R67 WP 3MPa 0 WP
78. LTIT m 3 4 6 75MPa 1 o 1 3 4 Overpressure test under hydraulic conditions A LPG containing component shall withstand without any visible evidence of rupture or permanent distortion a hydraulic test pressure which is determined by Table 1 of 2 25 times the maximum classification pressure during minimal 1 minute with the outlet of the high pressure part plugged The samples previously subjected to the durability test of paragraph 9 are to be connected to a source of hydrostatic pressure A positive shut off valve and a pressure gauge having a pressure range of not less than 1 5 times nor more than 2 times the test pressure are to be installed in the hydrostatic pressure supply piping Table 2 shows the classification pressure and the pressures to be used in the over pressure test according to the cl
79. 3 Hori JEL CIT Ds Fak 15cm3 h 3 cH v T T N rH HH 65 6 75MPa Xi IE FZ do o X X 4 5MPa 8
80. 20 17 17 per cent if the length of the metal container is equal to or less than the diameter 8 per cent in the case of a special metal container as shown in Appendix 5 page 1 Figures A B and C 2 2 3 3 The burst test must not cause any fragmentation of the container 2 2 3 3 The main fracture must not show any brittleness i e the edges of the fracture must not be radial but must be at an angle to a diametrical plane and display a reduction of area throughout their thickness 2 2 3 3 2 For metal containers the fracture must not reveal an inherent defect in the metal The weld must be at least as strong as the original metal but preferably stronger For all composite containers the fracture shall not reveal any defects in the structure 13 6 2
81. NBBI NBBI OUIO OUIO OUIO NB 263 NBBI OUIO NB 371 1 J
82. i l 3 i l 2 G SE i i l i l 5 Ef 3 1 2 3 9 1 EU EU 2007 46 EC Whole Vehicle Type approval X 61 UN UN EC WVTA UN 1998 EU 2s X C EC WVTA 7
83. 1 2 3 1 10 11 101 100 300 301 701 mur 2 1 1 3 0MPa 2 3 3 0MPa C MPa L 100
84. 17 LPG 1 6 3 2 3 1 1 4 18 ER AR i 3 LPG 4 pu 16 3 sz uH
85. AIA OUIO Q 12 BAG 1 4 gt 1 gt Power Boiler AWS 2 gt 3 gt 4 1 4 ELT 1 1 gt gt gt 50 000lbs h
86. 10 Subchapter 1 LPG W Wc 364 LPG W I 21 Subchapter 15 API 510 API 580 API 379 NBIC
87. TR sz 67 e 9 2 7 E s Dira HB
88. HH FOE 3 AUNTZ EE TEV AZ ARBRRAA R67 ZE R67 nn 95 R67 1 MITRO EL HAE R67 DBK DKN A E 85 FL ii 9 8 1
89. N HT D L5R P m PAD a L5R Z P PhD 15R CL a Pj D b R Z r R HEU CX f ikoX a mm P 3 0 3 0 MPa D mm b mm Re N mm Z 30 1 1 0 85 30 1 3 1 5 r mm R mm H mm
90. 2 NBBI NB 263 Rules for National Board Inservice and New Construction Commissioned Inspectors NB 263 3 Part 1 General Requirements RG Part 2 Inservice Commission RT Part 3 New Construction Commission RN ASME BPV Code A amp s NBIC Part 3 NB 263 RG 2 2 Eligibility Requirements
91. 4 EC WVTA E XE 2 EC WVTA EC WVTA EU R67 1 EU 7 E MN EU EU Ju EU EC WVTA 3 1958 1992 92 53 EEC
92. o de m ZLS ZLS lH Es b 2 2o I 34 ZUS ZUS PvU PvU ZUS
93. 2 IS01431 1 2012 1 JIS K 6259 2004 JIER A K OE a RAE T 20 40C 5 000ppm 72 3 1 NM 14 Ozone ageing 14 1 The test has to be in compliance with ISO 1431 1 The test piece which has to be stressed to 20 per cent elongation shall be exposed to air at 40 C with an ozone concentration of 50 parts per hundred million during 72 hours 14 2 No cracking of the test piece is allowed 16 3 3
94. OUIO NB 371 6 0 NB 371 f ke OUIO MZ NBBI pem Ro TIHE ERREA LC w AC E LC RIE
95. 27 LPG 1 2 7 200 1 1 3 4 20 O1 AeA C N 2 13 2 H 0 JJ 10 2 1 10 3 1 2
96. j GE k NBBI NBBI HX E organization NBBI j OUIO jvc Er s L1 gm Ed
97. 2 3 1 Ep 4 1 26 Q Q
98. 4 1 t SRAE A H Z b UNS E EE fE assa dc a E b
99. 7 JIS G 3454 1988 JIS G 3457 1988 JIS G 3460 1988 2 LPG 4 JISH3250 2010 C3604 C3712 C3771 C4641 C4622 C6782 2 1 2
100. ISO9001 a EE RA US MR manager uu Quality manager b ex
101. 5H 3 1 1 4 2 5 Examination on the outside of the weld for metal containers 2 5 1 This examination is carried out when the weld has been completed The welded surface examined must be well illuminated and must be free from grease dust scale residue or protective coating of any kind 2 5 2 The fusion of the welded metal with the parent metal must be smooth and free from etching There must be no cracks notching or porous patches in the welded surface and the surface adjacent to the wall The welded surface must be regular and even Where a butt weld has been used the excess thickness must not exceed 1 4 of the width of the weld 18 LPG 4 3
102. Ei A gt HE LB CU C rk 8 HEN i XE HA 8 Tig i 1 ZLS BetrSichV ProdSG y Brandenburg Humburg BetrSichV uq f 1072 Ek ZLS
103. 11 3 3 lt 2 1 bun RED INE E 10cm 2 2
104. ZUS ZUS it E Ur PvU ZLS EL
105. Amnex 10 OR 2 Annex10 2 11 R67 Annex 10 9 1 3 1 62 12 33 25 13 29 23 ICE ARR SAXA 14 2 6 18 34 2 3 6 1 19 s 2 3 6 2 20 2 3 6 3 2 3 64 ENS 21 2 3 6 5 22 T 2 3 6 6 23 2
106. 3 2 6 1 2005 12 GSG T V 2006 1 ZUS Adoption of GSG 31 12 2005 31 12 2007 Single room maaping 1 Old plant model j Cost regulation Cost regulation 1 only for oid piants ccreditation accroditation requirements of ZUS ZUS arc able to work Adoption of the BetrSichV 5 2 ZUS 2 ZUS Z0S PvU 533
107. es She ae Sa Tha QNERGIDCS SBD TERN Gits 2 11 b Ls 1 5 The heat treatment procedures on metal containers only shall be according to the following requirements 1 2 VA E DM 2 n E 1 5 1 The heat treatment shall be carried out on the parts or on the complete container 6 3 4 1 52 Those parts of a container having been deformed by more than 5 per cent must be submitted to the 1 7 2 2 following heat treatment normalize 1 1 5 3 Containers with a wall thickness z5 mm must be submitted to the following heat treatment 5 6 2 2
108. s 7 BE E E43 R67 2 6 Annex 2A Arrangement of the LPG equipment type approval mark See paragraph 5 4 of this Regulation T R 6012439 CLASS m lm 2 5mm The above approval mark affixed to the LPG equipment shows that this equipment has been approved in the Netherlands E4 pursuant to Regulation No 67 under approval number 012439 The first two digits of the approval number indicate that the approval was granted in accordance with the requirements of Regulation No 67 as amended by the 01 series of amendments 6 X
109. 3 125 LPG Dispensing units trap tanks and skid tanks 3 5 Storage tanks vapor storage 5 XE ZR Subchapter 15 LPG API 510 3 6 10
110. 4 2 2 75 cm P apo BE 25 mm RADEN 5 1 65 m 6 10 cm 7 2 6 Bonfire test 2 6 1 General The bonfire test is designed to demonstrate that a container complete with the fire protection system specified in the design will prevent the burst of the container when tested under the specified fire conditions The manufacturer shall
111. 50km h 3 20 2 3 1 24 LPGc 4 1 3 1 2 3 2 1 2 3 2m
112. 20mm 49Nm 54Nm 4 1 3 1 2 8MPa 130 2 3 CRR E ARW EIE URZ2 ORA 1 3 1C
113. tn mm D mm 3 LPG 4 3 10 3 0MPa 3 0MPa 5 3 3 1 LPG 1 2 10 1
114. E fc 4 4 2 API 510 2003 API 580 2002 15 LPG E E TY 10 Subchapter 1 H 3
115. R R67 2 1 2 1 2 Containers with circumferential welds only two sections on test pieces taken from the places shown in Figures 2a and 2b of Appendix 2 to this annex The tests as specified in paragraph 2 1 2 1 1 above with the exception of c e and f which are not applicable The test piece for the tensile test on parent material shall be taken from a or b as mentioned in paragraph 2 1 2 1 1 above 2 1 2 1 3 Test pieces which are not sufficiently flat must be flattened by cold pressing 2 1 2 1 4 In all test pieces containing a weld the weld 1s machined to trim the surplus 2 1 2 2 Tensile test 2 1 2 2 1 Tensile test on parent metal 2 1 2 2 1 1 The tensile test shall be carried out in accordance with Euronorms EN 876 EN 895 and EN 10002 1 2 1 2 2 1 2 The values determined for yield stress tensile strength and elongation after break must comply with the characteristics of the metal as required in paragraph 1 3 of this annex 2 1 2 2 2 Tensile test on welds T PURA AA z T pee m 2 1 2 2 2 1 This tensile test perpendicular to the weld must be carried out on a test piece having a reduced 11 1
116. o 6 75MPa 1 Ju 3 5 3 3 2 1 20 65 C
117. 3 7 1 2 13 1 US OUS 3 29 RE 1 3 4 7 1 3 10 1 3 11 1 1 4 1 12 1 3 18 1 3 27 1 3 4 28 1 1 4 5 33 1 3 4
118. 3 1 5 3 6 3 7 3 16 Temperature cycle test A non metallic part containing liquid LPG shall comply with the leakage tests mentioned in paragraphs 5 6 and 7 after having been submitted to a 96 hours temperature cycle from the minimum operating temperature up to the maximum operating temperature with a cycle time of 120 minutes under maximum working pressure R67 18 1 1
119. N E 1 1 1 EP an R67 UN 1 9 3 9 8 E CA 4
120. 2 1 2 0 3MPa 3 0MPa 10 20 000 3 1 sz HH C Jim lk 2 10 000 19 LPG 41 3 2 1 1 2
121. b NB 371 c B d e NBBI NBBI f
122. us 3 1 6 la X 2010 3 29 OUIO
123. 2 W W kai o 29 3 3 1 13 3 30 LPG 1 2 7 200 1 1 3 1
124. 82 0 3MPa 3 0MPa 4 10 000 FT 20 0 3MPa 3 0MPa 6 ps 4 10 000 3 ASTM B154 12 ik 10ml 30 3 0MPa 1 3 1 1 2 200cm h Ey 10g 70 2
125. D door Bi cpu yg G 2 3 16 1 2
126. JN g 10 000 a E huh Ei Xr S EE ml Zu N pressure cycling test according to the requirements of paragraph 2 3 6 1 of this annex The container shall be sectioned and the liner end boss interface shall be inspected 2 3 6 5 2 Test interpretation The container shall comply with the ambient temperature pressure cycling test requirements Inspection of the liner end boss interface of the container shall not reveal any evidence of deterioration such as fatigue cracking or electrostatic discharge 2 3 6 5 3 Retesting Retesting 1s permitted for the LPG cycling test A second test shall be performed on two containers which have been produced successively to the first container within the same batch If the results of these tests are satisfactory the first test shall be ignored In the event where one or both of the retests fail to meet the requirements the batch shall be rejected Z 22
127. R67 AVR 1 R67 DLPG 1 Metal containers DRR KS LPG 4 All Composite containers 15 S special vessels S RERRJEIA OO 8 68 3 RER VS EST Annex 10 Appendix 5 Q Annex 10 2 2 6 9
128. in 4 Idaho Idaho Division of Building Safety Industrial Safety Section 231H HATO 5 2010 3 29 OUIO 3 1 81 2 5 Illinois Office of the Illinois State Fire Marshal Division of Boiler and Pressure Vessel Safety ETOD SN du 3
129. 2 1 2 6 75MPa 120 96 3 5 2 6 2 7 2 3 1 5 3 6 3 7 3 15 Creep A non metallic part containing liquid LPG shall comply with the leakage tests mentioned in paragraphs 5 6 and 7 after having been submitted to a hydraulic pressure of 2 25 times the maximum operating pressure at a temperature of 120 C during min
130. more than 2 times the test pressure are to be installed in the pressure supply piping The pressure gauge is to be installed in the piping between the valve being tested and the positive shut off valve Start todischarge and resealing pressure resealing pressure are to be observed through a water seal not over 100 mm in depth 10 1 2 4 After recording the start to discharge pressure of the valve the pressure is to be increased sufficiently T a l above the start to discharge pressure to ensure unseating of the valve The shut off valve is then to be closed Q Fy XFX JO1x hxp tightly and the water seal as well as the pressure gauge are to be observed closely The pressure at which TS 60 E PER vg bubbles through the water seal cease is to be recorded as the resealing pressure of the valve TQ Fa Fa h RO p
131. Wi H OUIO 3 1 6 4 NBBI NBBI I 18 D OUIO 3 1 6 4
132. m ZUS T V PvU 3 ZLS ZUS ZLS ZLS ZUS BetrSichV ZLS KO PvU ZUS
133. 236 13 Retesting 2 1 Retesting is permitted for the ambient temperature pressure cycling test ET E c En A second test shall be performed on two containers which have been produced successively to the first 3 4 HEA Jarzyna iB 2 container within the same batch If the results of these tests are satisfactory the first test shall be ignored In the event where one or both of the retests fail to meet the requirements the batch shall be rejected 4 21 R R67 35 7 2 BE 5
134. B NBBI CalOSHA B E Chevron Richmond OUIO OIUO CaOSHA B OUIO OUIO
135. ELE 10 11 101 301 100 300 700 A 10 cp 23 ccs DEPXWO IC E 7 F 2 2 1 3 1 2 74Nm 78Nm
136. A cus NB 369 OO GO OG 3 NB 374 Checklist of Quality Program Elements for Accreditation of AIAs NBBI NB 369 AIA NBBI WEB 3 los 1 Rev Q0134E5 11 2 Rev 0 2003 4E 8 4 OUIO
137. 20mm 49Nm 54Nm 4 1 3 1 2 8MPa 1 30 2 a 3 RE dE IRU Z PAIF LID DIR C 1 3 1C 4
138. D WE PVU ZUS 13 I 31 14 1 BetrSichV Section21 Mr 2 5
139. H Q LPG 4 7 3 1 2 2 3 2 3 4 1 2 5 Q 3 4 2
140. c The openings plate for accessories metal ring KHKSO121 S zx Su eue in case of metal containers 2 3 f The heat treatment in case of metal containers l g The production line Q 4 h The nominal wall thickness 4 i The diameter 2 5 j The height in case of special containers QD 10 R R67 C 5
141. 2013 OUIO CR M OIUO v NBBI NBBI HP OUIO OUIO IDAHO 2 OUIO SES
142. E 1 2 ISO9001 TSO9001 ALTOR E o HES 2 Doo NUTUS 2 1 1
143. 1 TOt more than 105 per cent of the set pressure marked on the valve blow down pressure Om 2 10 1 2 2 The resealing pressure ofa pressure relief valve before being subjected to a flow capacity test shall be not less than 50 per cent of the initially observed start to discharge pressure pe me ERN S PE TA 10 1 2 3 A pressure relief is to be connected to an air or other aerostatic supply source capable of being 2 EFKE maintained at a pressure of at least 500 kPa effective pressure above the marked set pressure of the valve being 10 1 3 9 120 tested A positive shut off valve and a pressure gauge having a pressure range of not less than 1 5 times nor
144. 11 N 3 1 2 1 1 2 3 1 c 1 d 2 d 1 5 2 mm E T Th ig E T 3 JE BENBIXSASRU OC BXtid 5600tv mREIXRRMOomzzctbgys6ort3T5 4 JIS Z 3121 2013 IS05178 2001 TS04136 Ih 2012 p Az
145. 3 1 1 25 9 2 10 30 15 fes J 3 3 1 3 2 1IS01431 1 2012 1 H E cO gam vw ARETA
146. 15cm h 3 Ter I H HH 6 75MPa 4 5MPa 20C 8 4 3 3 Dira 8 3 Av E dU E 1 HH H UC 3 Es Afl mu GU Mr VM 2 1 2 3 4 3 1 2
147. 3 17 7m min 10 66A0 82 A Q 15C 0 1MPa m min A m 4 Q Z 2 73xA 4 3 3 2 1 2 3 MG 2i MEE em 1 I 6 75MPa
148. Em i g zy ud s A 1 4 h
149. 1 lam Et HH TL 4 IRTO UN RO ZOR h 1 EZS a gt 3 1958 UN UN UNECE BCE TRANS WP 297343 1 hints di 26 2 0 E
150. UN 67 2 V 3 1958 A a 3 1938
151. m 3 1 4 CFR NBIC API 510 Pressure Vessel Inspection Code cm e Maintenance Inspection Rating Repair and Alteration 3 1 CFR
152. 1 CCR Title8 Chapter4 3 1 8 1 NBBI 1055 Crupper Avenue Col David A Douin Executive Director umbus Ohio 43229 1183 Charles Withers Assistant Executive Director TECHNICAL Richard L Allison Assistant Executive Director ADMINISTRATIVE D OUIO OUIO X 1977 ZEC 2 OUIO OUIO DRA 79 Ee us AH Me C ESTEE
153. Circular Letter Circular Letter PV 2006 2 Repairs amp Alteration to Boilers and Pressure Vessels Circular Letter PV 2006 3 Repair Organizations Obtaining Jurisdictional Acceptance Circular Letter PV 2007 1 LP Gas Systems in California Subchapter 1 LPG Hr LPG Subchapter 1 Subchapter 15 Subchapter 1 LPG
154. 18 5 12 3 2 2 3 3 3poW 23 LPG 4 1 3 2 H 1 0 568kg L 80 DEP UON NEP MAMMA MM MEM 2 Zz ai H X X
155. PvU PvU PvU PvU PvU PvU ZLS st uu ff 3 EA 6 7
156. gt Subchapter 2 Boiler and Fired Pressure Vessel Safety Order gt Subchapter 1 Unfired Pressure Vessel Safety Order Section460 Subchapter 1 Unfired Pressure Vessel Safety Order LPG CNG LNG NH E Subchapter 15 Petroleum Safety Orders Refining Transportation and Handling NBIC 2004 E Subchapter 2 Boiler and Fired Pressure Vessel Safety Order W gt gt AIA gt AIA gt Subchapter 15 Petroleum Safety Orders Refining Transportation and Handling NBIC
157. 2 10 2 10 R67 2 sa AEE 10 R67 R6 3 2 2 ES R67 1 2 R67 Annex 10 Provisions regarding the approval of LPG containers 6 Annex 10 Annex 10
158. 9 Endurance test 9 1 A filling unit or service valve shall be capable of conforming to the applicable leakage test requirements of paragraphs 5 and 8 above after being subjected to a number of cycles of opening and closing as mentioned in the annexes to this Regulation 9 2 A shut off valve is to be tested with the valve outlet plugged The valve body filled with n hexane and the valve inlet subjected to a pressure of 3 000 kPa or of WP in accordance with the classification pressure of the valve 9 3 An endurance test is to be conducted at a rate not faster than 10 times per minute For a shut off valve the closing torque is to be consistent with the size of handwheel wrench or other means employed to operate the valve 9 4 The appropriate tests for external and seat leakage as described under external leakage test under paragraph 5 and seat leakage test under paragraph 8 are to be conducted immediately following the endurance test 9 5 Endurance for 80 per cent stop valve 9 5 The 80 per cent stop valve shall be capable to withstand 6 000 complete filling cycles to the maximum filling degree 9 6 Endurance test for pressure regulator and vaporizer The regulator shall be able to withstand 50 000 cycles without any failure when tested according to the following procedure a Recycle the regulator for 95 per cent of the total number of cycles at room
159. NB 345 The National Board Body of Knowledge for ASME and National Board Review Team Leaders E1 Rev 3 2003 8 20 H2 Rev 5 2011 11 1 Im 3 1 7 OUIO 1 OUIO OUIO Statutes of Alaska Alaska 4 Title 18 Labor and Workforce Development Arizona Revised Statutes Arizona 4 Title 23 Labor Arkansas Code Arkansas 1 20 23 101et seq and 5 64 1301 through 1303 f f California Code of Regulations California 13 P Title 8 Chapter 4 Division of Industrial Safety Colorado Revised Statutes Colorado 2 k f Title 9 Safety Industrial and Commercial f Official Code of Georgia Annotated Georgia 2 i Title 34 Labor n Statutes of Hawaii Hawaii 3
160. UN No13 H 9 A UN No 13 H EC No 661 2009 13 4A E UN No 18 9 2 MI TR a o 1
161. 11 2 10 a 3 lt Ix Zy cu lt JIS Z 2241 2011 1 e HE 1 ds gt 5 9 amp 2 20 a XlX b EN10002 1 2001 A 20 1 21 1 1 4 1 Rn
162. 4 30 5 3 1 2 10 R R67 1 2 S TETOR RU peg BEZONT 3
163. 20 0 3 95 5wt 2 40 90 95 168 4 3 55C 1 4 4 4 2 5 2 6 2 7 2 5 7 wE TiiIRSXERIX JIS H 3300 2012 7 13 IS06957 1988 24 6 4 2 5 2 6 2 7 2 X 3
164. EF zl H NBBI Tal Ei MA E gt Ls NBBI NBBI NBBI NBBI IA Ei E NBBI OUIO D RA H ZE hn alli
165. 3 4 3 2 C 10
166. JIS K 5572 1995 130 15 2 Ab 1 16 pep BERI O WL RESG5zqgomKL liu Jvodoliciuo tei rn cnll lm 1 g 130 25 1 dues JIS K 5651 1992 120 20 1 5 EE 130 130C 30 P 3 LPG 4
167. 2 3 12 3 5 E 2 3 6 6 High temperature creep test 2 3 6 6 1 General This test shall only be performed on all composite containers with a resin matrix having a glass transition temperature TG below the design temperature 50 C 2 3 6 6 2 Test procedure One finished container shall be tested as follows a The container shall be pressurized to 3 000 kPa and held at a temperature defined according to Table 3 on the basis of the test period duration Table 3 Test temperature relating to the High temperature creep test duration T C Exposure time h 100 200 95 350 90 600 85 1000 80 1800 75 3200 70 5900 65 11000 60 21000 b The container shall be submitted to an external leak test 2 3 6 6 3 Test interpretation The maximum allowed volume increase is 5 per cent The container shall meet the requirements of the external leak test as defined in paragraph 2 4 3 of this annex and the burst test as defined in paragraph 2 2 of this annex 2 3 6 6 4 Retesting Retesting 1s permitted for the high temperature creep test A second test shall be performed on two containers wh
168. AIA 2 California Cal OSHA 3 1 8 2 1 13 3 Hawaii Hawaii Department of Labor and Industrial Relations 231H 4 f C do 2 NBIC NBBI R NBIC Part3 2 4 AIA
169. C OUIO CCR OUIO OIUO Chevron Products Company Richmond Refinery AF Chevron Richmond 2012 8 6 CSB WEB 3 13 OUIO NBBI CalOSHA m CalOSHA OUIO
170. 19 48 49 15 3 26 R67 2 8MPa 4 1 R R67 R R67
171. recen fen ps ned zen C 0 20 0 25 1 1 0 25 0 50 1 2 0 003D b 0 08D ZST M Z Cli rz0 1D RED HZ0 18D rZ2b hZ4b KK O h 0 15D HZ0 18D hZ4b RKU h 0 15D r mm mm mm mm mm mm T Hox 2 1 5mm posee uu 250
172. 1 2 3 1 20 1 1
173. 10 1 3 5 A flow capacity test on a pressure relief valve is to be conducted by utilizing a properly designed and calibrated orifice flowmeter of the flange type connected to a source of air supply of adequate capacity and 3 po 1 pn 1 pressure Modifications of the flowmeter from that described herein and an aerostatic flow medium other than air may be used provided the end results are the same 3 1 10 1 3 6 The flowmeter is to be arranged with sufficiently long lengths of pipe both preceding and following the orifice or other arrangements including straightening vanes to assure no disturbance at the orifice place for 0 1 E the ratios of orifice to pipe diameters to be employed E o Ea Flanges between which the orifice plate is located and clamped are to be provid
174. 1958 Es X IH 12S RIC HEIZE VY E AES TES 131 UN AH cr PO Fl HI E nj Ps ji Ic DAE go WET A A83 Eg 3 1998 1958 HJ 1958 4 ECC 1958 4 Eii HH FE E fri I4 2 1958 1 1958 4j HED HB E IE 1958 4 E UN EE AES D
175. H Ex aj 2 Lt gt 3 2 1 4 3 2 1 5 LPG 1 f 6 75MPa u 1 LPG 4 6 7 LPG 1
176. 1 2 3 1 10 15 20 25 2 1 1 2 3 4 5 pira 3 B 1 2 3 4 5 E 3 0MPa 3 0MPa 1 2
177. 12 14 15 22 23 24 13 21 Dira 19 20 ed E H 23 3 1 1 SN LI 1 DX LLEEEELELELLLLLL T TE ENBNENBENENBEEBHENHHENER CU JJ LELLLILLLILLELELLLS 02 021 02 023 024 025 H D S 1 H D 23 0 20 UE 0 25 C 1 000 0 500 1T T TITTIETgIILlt e ER KS EA FE EE Ht ME 0 25 0 30 0 35 0 40 0 45 0 50 H D Y2 HID 0 25 0 50 24 qm 11 2 1 3 B RJT O TR RM E 3 2 Y weld 25
178. 17 1 3 2 5 17 1 4 1 2 2 6 5 1 3 OB 3 OUS 3 17 1 5 E 5B
179. 2 200cm h 10 Operational tests 11 3 3 10 1 Operation test of the gas tube pressure relief valve 10 1 1 In the case of pressure relief valves three samples of each size design and setting are to be used for 10 2 d ed pum Exe Miss san E of three valves is to be used for flow capacity tests 2 b
180. 33 LPG 4 2 7 200 1 1 3 4 2 12 2 3 1 12 3 1 20 D 98 4 4 1 22 3 4 Retesting for the burst test Retesting is permitted for the burst test A second burst test shall be performed on two containers which have MA Z3 BA LOmEL 75 s gt gt ERANA ZAER iT 2 1 ERV BEOWRHABR
181. D NBBI NB 371 OUIO NBBI WEB 3 NBBI 1 Rev 2013 11 2 NBBI R NB 415 Accreditation of R Repair Organization Zw 3 http www nationalboard org Index aspx pageID 67 ID 121 n 5 NBBI NBBI NB 290 Qualification of National Board Team Leaders and National Board Representatives NBBI
182. UN ENI M ax e E ds WP29 BEI WAE UN M Il M UN T ES E x EJIIS VE BEZTA z 1AE 4 UR MA
183. F 15C 7 h p 3 CE 1 1 3 Eus II wik V JE aa 3 4 KO kPa EJ iE E 2 50 Vice LM E RAM M OQ 1 3 3 J JI 2 8MPa 3 3 1 Ts 1 1
184. 29 1 3 4 7 1 3 10 1 3 11 1 1 4 1 12 1 3 18 1 3 TH 27 1 3 4 28 1 1 4 5 33 1 3 4 34 1 3 4 2 5 7 1 4 1
185. 3 DAY NS lt m 2 HETS 3 3 5 ZLS 18 4 5
186. WT gt m NBIC NBBI NBBI B NBIC B NBBI R LPG
187. cm K A kPa 3 3 2 1 3 2 3 9 M 1 10 2 10 Eg n Hun Iz 200 3 5 2
188. n 7 25 LPG 4 1 3 2 1 2 2 3 20 2 3 1 2 9 Boss torque test 2 9 1 Test procedure The body of the container shall be restrained against rotation and a torque of 2 times the valve or PRD installation torque specified by the manufacturer shall be applied to each end boss of the container first
189. 152 7 1 2 MAN 4 mm 1 4 mm 1 3 mm 2 325mm 6 mm A 2 1 1 5 mm 2 25 mm 6 mm EL 4 j d uu Lu n 12 100 mm 4 mm 4 1 2 mm
190. E Part 2 Gnspection 3 FFS Part 3 repairs and alternations
191. PvU B B ZUS PvU gt ZUS 20 gt gt 2 gt ZUS
192. Approved body Approved by Inspection of installations subject to expert competent monitoring and work equipment zUS authority Nominated by Inspection of installations subject to operating company monitoring and work equipment qualified via special training Nominated by Inspection of work equipment Competent person operating company 3 Competent person 1 ZUS ZUS ProdSG ZLS ZUS ZUS BetrSichV ProdSG ZLS ZUS 3 2 6 2 2
193. 19 4 2m 5 45 2m 6 18 2 3 1 1 R REZXDLRVLIE 2 10 000 25 LPG 4 1 3 Vs 2 1
194. SQVIA SQVIB SQV2A SQV2B SQV3A SQV3B TISG3126 2000 SLA360 SLA410 JIS G 3127 2000 SL3N440 SL5N590 SL9 JISG3445 1988 AY 7 JIS G 3454 1988 JIS G 3457 1988 JIS G 3460 1988 C3771 C4641 C4622 C6782 T SLA235A SLA235B SLA325A SLA325B SL2N255 SL3N255 SL3N275 520 SL9N590 STKM19A STKM19C STKM20A LPG 4 JIS H 3250 2010 C3604 C3712 1
195. 1 3 2 3 6 3 External leak test 2 3 6 3 1 Test procedure While under 3 000 kPa pressure the container shall be submerged in soapy water to detect leakage bubble test 2 3 6 3 2 Test interpretation The container shall not show any leakage 2 3 6 3 3 Retesting Retesting 1s permitted for the external leak test A second test shall be performed on two containers which have been produced successively to the first container within the same batch If the results of these tests are satisfactory the first test shall be ignored In the event where one or both of the retests fail to meet the requirements the batch shall be rejected 1 21 4 i 1 2
196. 3 2 4 2 4 3 ss jaa 19 1 1 3 1 20 21 101 301 701 100 300 700 2
197. 3 2 4 3 4 1 R67 R67 1 1 2 R67 8 1 18 1 29 2 8MPa
198. 23 1 3 24 1 3 25 1 3 26 1 3 28 1 2 4 5
199. 3 XT 5 1 2 3 4 E FH 2 6MPa 3 0MPa 2
200. EI gt J 5 8 1 20 1 2 7 17 1 6 21 1 1 2 2 3 8 17 1 7 1 11 1 3 21 1 3 4 4 2
201. 2 8 Drop Test 2 8 1 Test procedure One finished container shall be drop tested at ambient temperature without internal pressurization or attached valves The surface onto which the containers are dropped shall be a smooth horizontal concrete pad or flooring The drop height Hd shall be 2 m measured to the lowest point of the container The same empty container shall be dropped a In a horizontal position b Vertically on each end c At an angle of 45 Following the drop test the containers shall be submitted to an ambient temperature pressure cycling test according the requirements of paragraph 2 3 6 1 of this annex 2 8 2 Test interpretation The containers shall comply with the requirements of the ambient temperature pressure cycling test according the requirements of paragraph 2 3 6 1 of this annex 2 8 3 Retesting Retesting 1s permitted for the drop test A second test shall be performed on two containers which have been produced successively to the first container within the same batch If the results of these tests are satisfactory the first test shall be ignored In the event where one or both of the retests fail to meet the requirements the batch shall be rejected 18 R R67 2 10 000
202. During the bonfire test the following items shall be measured NM bur Dk below the container along the bottom of the container at minimum two locations b The wall temperature in the bottom of the container 2 c The wall temperature within 25 mm from the pressure relief device e i arai _ d The wall temperature on the top of the container in the centre of the fire source OZ PONES VC S Escdbo CH KIRO HX BIRRET DEFORE e The pressure inside the container 2 Metallic shielding shall be used to prevent direct flame impingement on the thermocouples Alternatively ES DS pts uu ERES Ms INT _ thermocouples may be inserted into blocks of metal measuring less than 25 mm2 During the test the 10 PEE S and the container pressure shall be recorded at intervals of 2 seconds or l
203. 1958 2 1 1 1 EU UN ISO9001 ISO9001 ISO TS16949 ISO9001 IAF International Accreditation Forum TISO TS16949 IATF
204. 2 2 IE 17 1 7 17 1 6 21 1 1 7 3 H 6 15 8 2 The pressure relief valve shall be so designed as to open at a pressure of 2 700 100 kPa 6 15 8 3 The flow capacity of the pressure relief valve determined with compressed air at a pressure which is 20 per cent higher than the normal operating pressure must be at least Ay Para Av m u zy IRE a D gt RL IPEA X 2 10 A0 82 D 11 1 3 Q 10 66 A08 S Af E 1 3 4 4
205. 2 11 2 3 11 3 4 1 11 4 5 1 2 1 2 2 1 2 4 Retesting for the tensile and bend tests 2 1 2 4 1 Retesting is permitted for the tensile and bend test A second test shall consist of two test pieces taken from the same container If the results of these tests are satisfactory the first test shall be ignored In the event where one or both of the retests fail to meet the requirements the batch shall be rejected 29 3 SN 2 13
206. 30 d The severity of the test conditions shall not be mitigated by ambient conditions e g rain moderate high L min wind etc 2 6 6 Test results a A burst of the container shall invalidate the test result b A pressure of more than 3 700 kPa i e 136 per cent of the set pressure of the PRV 2 700 kPa during the test shall invalidate the test result A pressure between 3 000 and 3 700 kPa shall only invalidate the test result in case visible plastic deformation is observed c In case the behaviour of the protection system does not comply with the specification of the manufacturer and it leads to a mitigating test condition the result shall be invalidated d For a composite container a release of LPG via the surface is accepted in case of a controlled release A release of gaseous LPG within 2 minutes after the start of the test or a release capacity of more than 30 litres per minute shall invalidate the test result e The results shall be presented in a test summary and shall include the following data for each container as a minimum 1 Description of the container configuration ii Photo of the container set up and PRD 11 Applied method including time interval between measurements iv The elapsed time from ignition of the fire to the start of venting of LPG and actual pressure v Time to reach atmospheric pressure vi Pressu
207. S 5 2 5 5 I 33 ZUS OX E rp srt pPvU H HUZzVN 2 5 ZUS 3 ZUS ZUS
208. 1 2 3 0MPa 3 1 21 LPG 4 1 I 1 4
209. 3 o 2 1 2 3 1 1 2 0 3 MPa 3 0 MPa 10 20 000 10 000 2 3 6 Additional hydraulic tests to be performed on all composite containers 2 3 6 1 Ambient temperature pressure cycling test 2 3 6 1 1 Test procedure The finished container shall be pressure cycled to a maximum of 20 000 cycles according to the following procedure a Fill the container to be tested with a non corrosive fluid such as oil inhibited water or glycol b Cycle the pressure in the container betw
210. R67 R67 LESS 1958 ali 1958 N zl l JENE R67 LH
211. ArbSchG Act ProdSG Act RU BImSchG Act BetrSichV National Ordience Pe Special Laws ArbSchG 3 WHG GGBefG ArhStBttV 3 ef GGVSE ProdSG rwV GGVBinSch ProdSV TA Luft GGVSee BetrSichV lt GGKontrollV ZustVO For construction and operation 2 3 3 2 6 3 2 2 BetrSichV Section14 3 2 3 B m 000 i NERIS d o ons m
212. HHI EC No 661 2009 12 RIZ UN No 67 UN No 110 UN EC No 661 2009 TIV 2 840 kg TESC HO EC 7 sw EC HHJ EC No 661 2009 ii 12 UN 13 21 UN No 13 EC No 661 2009 13 ESX ESC
213. NBBI 5 National Board Pressure Equipment Inspector National Board Pressure Equipment Inspector 1 Rev 8 2013 9 30 2 NBBI NBIC ASME BPVC NB 438 The National Board Pressure Equipment Inspector Program 3 AIA NBBI NB 369 1 Qualifications and Duties for Authorized Inspection Agencies Performing Inservice Inspection Activities and Qualifications for Inspectors of Boilers and Pressure Vessels AIA NB 369 NB 381 Quality Program Elements for AIAs accredited to NB 369
214. 1 BTE 4 3 2 1 BR 2 5 LPG 1 LPG 4 w R67 6 75 MPa 6 9 7 2 4 Type of container means containers which do not differ in respect to the following characteristics as 9 LPG 1 9 specified in Annex 10 5 9 a The trade name s or trade mark s U b The shape cylindrical special shape
215. 4 2 8MPa 120 10 3 22 17 2 us 2
216. R R67 and resealing pressures recorded under test No 1 of paragraph 10 1 2 10 1 4 2 These tests are to be conducted approximately 1 hour after the flow capacity test and the test procedure is to be the same as described under test No 1 of paragraph 10 1 2 12 3 prre UJ RICT boR 3 2 ISO01817 1999 JIS K 6258 2003 8 CD un c il E 23 2 n 72
217. 4 2 3 pm 4 C 4 5 GR 10 5 f O
218. VST 1 3 1 The material used for the manufacture of the stress resistant container shells must be steel as specified in Euronorm EN 10120 however other materials may be used provided that the container has the same safety characteristics to be certified by the authorities granting type approval 4 KHKS0128 R R67 90 100C 2 JIS R 3413 2012 4 E JIS R 3420 2013 ASTM D 2343 2008 1400N mm UF TE JISK7010 1995 S JIS R 3420 2013
219. 2 5 2 6 2 7 2 8 2 9 2 10 2 1 1 2 12 2 13 2 14 2 15 2 16 2 17 2 18 2 19 2 20 2 1 4 3 1 4 21 2 3 4 1 3 2 17 1 1 1 3 10 1 3 18 1 3 20 1 1 2 5 pira 3 17 1 2
220. R R67 2 WEF 2 ERO 6 75MPa L3 3 0MPa 1 Zt 4 cm 0 00005cm h 60 273 P exe xo LloXicdwcW Vet TRO V V t T K P kPa T ambient temperature during test in K 8 1 3 Instead of the method described above leakage may be measured by a flowmeter installed on the inlet side of the valve under
221. 19 1 3 4 17 1 3 6 1 3 7 1 3 9 1 H EX 3 10 1 3 12 1 3 13 1 3 14 1 3 15 1 3 16 1 3
222. E 3 Rev 0 2002 3 4 http www nationalboard org Index aspx pageID 123 NBBI NB 371 Accreditation of Owner User Inspection Organization OUIO NB 371 NBBI OUIO D OUIO NBIC R CR Certficate 5
223. EE 1 2 3 4 1 2 2 1 e Ff 2 T JIS 23122 2013 Amd1 2011 IS07799 1985 4 amp 3mm EN876 1995 3 BU IS07438 2005 fi ix L N mm
224. NBBI g N o NB 371 C NB 371 NB 371 NBBI NB 234 OUIO En ma NBBI 8 us 9 OUIO OUIO NBBI
225. TRBS AD2000 PvU ZUS I 32 B B W DOC 3 ZUS Module Minimum time period of training within the approved body 1 9 Months thereof 6 months of practical training basic module f
226. 25mm 12 6mm 2 100mm 2 4 u j 4mm 1 2mm A T Js H 1 2mm 1 1 5mm 2 25mm j 12 f 100mm LPG 1 EE 16 3 2 1 p nu DT J 2
227. 34 1 3 A 5 7 1 4 15 1 3 16 1 3 17 1 3 30 1 3 31 1 3 32 1 3 6 7 1 6 11 1 2 4 2 14 1 3 19 1
228. 1 2 10 E 200 PILER 0 RT 3 2 IH OR 5 E 3 3 RA H E EE 1 3 2 3 FH E 10 g 2 1 5 3 3
229. UN 131 UN Eu e UN UN 1958 2 UN UN EAH ZA KO
230. in Which m 9 e 2 How of air 1n standard m3 min a absolute and temperature o 21 588 eb o S AUS 4 A uL PERAR C BESNSRI ETI Q flow of dard m3 min 100 kPa absol d temp f 15 C UE e A exterior surface of the container in m2 2 The flow test results must be corrected to standard conditions 3 17 7m min DA Air pressure of 100 kPa absolute and temperature of 15 C en the pressure relief valve is considered as a pressure relief device the flow shall be at least 17 7 standar When the p lief valve i idered p lief device the fl hall be at 1 17 7 dard Q 10 66A082 m3 min Q A j 9 MS SEE Jus Baa Emo wg 6 15 8 5 The pressure relief device fuse shall be designed to open at a temperature of 120 10 C d Mb Me z4 E Z Q He 19 0 1MPa 6 15 8 6 The pressure relief device fuse shall be designed to have when opened a m min u 3 flow capacity of A
231. 2 1 2 34 LPG 4 2 7 200 1 5 1 3 4 22 2 3 18 2 1 1 E 4 4 7 2 AX NER WERB d d EZ
232. R Form Cal OSHA ASAP Regal Request Cal OSHA Petroleum Safety Order 1 http wwwr dir ca gov databases dosh pv DOSH PV html 2 http wwwr ci richmond ca us index aspx2NID 2628 3 http www csb gov chevron refinery fire I 25 3 2 ArbSchG Arbeitssc
233. ZLS ZUS ETAZ LD I 35 18 ZLS ZLS BetrSichV U ProdSG ZUS ZLS gd xe LCSHaBZz3 2 D 4 5 ZUS ZUS ZLS
234. Il 21 polle 2 EC WVTA E Me Tac e E ER gt 1 2 3 1 2 3 Oi O 04 1 70 157 EEC X X X X X X 2 Buro 5 6 EC No 715 2007 x x x x 3 70 221 EEC x xO x xO xXO X X X X X 3A PA X X X X X X X X XX 3B RUPD URU EC No 661 2009 X X X X X X X X XX RUP AM 4 70 222 EEC X X XX X X X X XX P EC No661 2009 EN ease eec ebd l zs ets EU No 1003 2010 5
235. 1 2 1 Em 3 2 80 3 5 590
236. E 1 2 80 3 5 590 4 2
237. R OUIO NB 371 OUIO personnel OUIO Ok PA OUIO EE odes NBBI OUIO NB 371 OUIO a k a NB 371
238. CA AER IERE KRIER 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 36 2 7 14 1 4 1 FE H D
239. 1 rea dni 2 1 2 3 3 1 2 3 LPG 4 115 3 3 0 MPa nl CC AW b 100 200 95 350 90 600 85 1000 80 1800 75 3200 70 5900 65 11000 60 21000 20 2 12 2 1 1
240. 8 6 3 9 2 3 1 E 3 4 6 9 10 O 1 2 Ra LPG 1 1 VB 3 2 ARII IRR 2 2
241. P 1958 ECE TRANS WP29 1059 ECE TRANS WP 29 78 Rev 3 R E 3 UN RE3 1 ECE TRANS WP29 1059 1 UN RE3 1 10
242. UN No 85 2 610 kg 2 610 kg 2 840 kg EC No 595 2009 2 9A EC No 715 2007 UN No 64 EC No661 2009 15 3A 3B 4A 5A 6A 6B 7A 8A 9A 9B 10A 12A 13A 13B 14A 15A 15B 16A 17A 17B 18A 19A 20A 21A 22A 22B 22C 23A 24A 25A 25B 25C 25D 25E 25F 26A 27A 28A 29A 30A 31A 32A 33A 34A 35A 36A 37A 38A 42A 43A 44A 45A 46A 46B 46C 46D
243. d OUIO 1 W B NBBI CaUOSHA OUIO B OUIO OUIO ua Ri idee 3 1 24
244. u 2 mm C 12 100 mm 2 2 4 Non destructive examination 2 4 1 Radiographic examination 2 4 1 1 Welds must be radiographed in compliance with ISO specification R 1106 using classification B 2 4 1 2 When a wire type indicator is used the smallest diameter of the wire visible may not exceed the value of 0 10 mm When a stepped and holed type indicator is used the diameter of the smallest hole visible may not exceed 0 25 mm 2 4 1 3 Assessment of the weld radiographs must be based on the original films in compliance with the practice recommended in standard ISO 2504 paragraph 6 2 4 1 4 The following defects are not acceptable Cracks inadequate welds or inadequate penetration of the weld 2 4 1 4 1 For the container wall thickness Z4 mm the inclusions listed below are regarded as acceptable Any gas inclusion measuring not more than a 4 mm Any gas inclusion measuring more than a 4 mm but not more than a 3 mm which is more than 25 mm away from other gas inclusion measuring more than a 4 mm and measuring not more than a 3 mm Any elongated inclusion or any group of rounded inclusions in a row where th
245. 10 AIA 9 Utah Utah Labor Commission H 34 HETO 2 API 510 9 Secton 8 A NBBI R 1 2 E eaa a REB NSLAL310 E AIA
246. 2 0 Pa 65C 95 48 0 3 MPa 3 0 MPa fj 10 3 600 3 20 2 4 12 2 3 1 1 2 2 3 3 4 85 2 3 6 2 High temperature pressure cycling test 2 3 6 2 1 Test procedure Finished containers shall be cycle tested without showing evidence of rupture leakage or fibre unravelling as follows a Fill the container to be tested with a non corrosive fluid such as oil inhibited water or glycol b Condition for 48 hours at 0 kPa 65 C and 95 per cent or greater relative humidity c Hydrostatically pressurize for 3 600 cycles not exc
247. 2 Hf 26 3 5 H CK The National Board of Boiler and Pressure Vessel Inspectors ASME 26 3 6 The Division of Occupational Safety and Health Department of Industrial Relations Labor and Workplace Development Agency California State Government 3 3 A ANSI A ASNT A W S Cal OSHA zo E Z 1 I P WH A A 1 A Authorized Inspection Agency American Society of Mechanical Engineers
248. Av E ES Rd 3 1 LU s 1 mm BS TA En 1 2 1 LH A RE 5 0MPa 6 75MPa
249. ISO188 2007 JIS K 6257 2010 JIRET D M UFLA ME T A MEEUBHIEOK C X 03x88 Zi E 656C 168 3 1 1 25 2 10 309 equal to the maximum operating temperature for 168 hours The allowable change in tensile strength should not exceed 25 per cent The allowable change in ultimate elongation shall not exceed the following values Maximum increase 10 per cent Maximum decrease 30 per cent 15 3 3 WRN ZCOOT KERU 3
250. gt T 1 2 3
251. R67 R67 3 2 4 R67 LPG R67 R67 R67 3 4 2 R67 R67
252. Subchapter 1 LPG uk Circular Letter PV 2006 2 W NBIC E Subchapter 15 Petroleum Safety Orders Refining Transportation and Handling NBIC 2004 APIS10 8 hk 2003 8 APIS10
253. 1 Fz 3 R67 R67 LPG E SEA sz 80 80 3 R67 Adm gh R671 2 15 j f 3 ERICK VR
254. EC No 661 2009 UN No 12 II 22 WVTA E TRE Mi M M Ni N N 0 10 10 15 74 408 EEC xI X X XI X X EC No 661 2009 15A X X X X X X UN No 17 Y 3 EC No 661 2009 15B X X UN No 80 16 74 483 EEC X RAJ EC No 661 2009 16A 2 X 2 UN No 26 _ 17 n 75 443 EEC X X X X XIX erm ROSRSEH EC No 661 2009 X X X X X X i i EU No 130 2012 EC No 661 2009 17B X X X X X X UN No 39 18 76 114 EEC X X xi
255. EC No 661 2009 22B Mond X X X X X Xx UN No 87 EC No 661 2009 22C u X X X X X X X X X X UN No 91 23 F 76 759 EEC X X X X X X X X X EC No 661 2009 QAM TETTE p X X X X X X X X X X UN No 6 24 76 760 EEC X X X X X X X X X X EC No 661 2009 24A m X X X X X X X X X X UN No 4 25 76 761 EEC X X X X X X WVTA et E Mi M M Ni N N 0 01 o Se EC No 661 2009 Seb ee ce elt n
256. Pressure relief device Xe cfe 2 120 Annex15 10 3 1 1 1 uH B 0 3A JU TS Annex 3
257. 1 H 2 3 1 10 20 1 1
258. 2 1 40 2 3 1 2 m0 2s 1 2 LPG 4 o E S X N BITAR 1 80 500 8 18 2 2 3 6 4 Permeation test 2 3 6 4 1 Test procedure All the tests shall be performed at 40 C on a containe
259. LPG 4 1 1 3 AR S 1 2 3 2 3 4 1 G 3 RS 4 2 3 4 3
260. n 2 3 3 Batch of containers means a maximum of 200 containers of the same type produced consecutively on the same production line 2 1 2 4 Retesting for the tensile and bend tests 2 1 2 4 1 Retesting is permitted for the tensile and bend test A second test shall consist of two test pieces taken from the same container If the results of these tests are satisfactory the first test shall be ignored In the event where one or both of the retests fail to meet the requirements the batch shall be rejected 28 LPG 1 2 7 200 1 1 4 19 R R67 5
261. 1 1 1 En 1 Federal law State Law C St Occupational Safety and Health Act of 1970 Z 7 n CFR OSHA standards in Title 29 Labor PART 1910 Occupational Safety and Health Standards 29 CFR Part1910 29 CFR Part1910 M ASME 1968 Department of Labor DOL Occupational Safety and Health Administration OSHA 2 NB 370 National Board Synopsis of Boiler and Pressure Vessel Laws Rules and
262. EC No 595 2009 x x x x9 x x 42 89 297 EEC X X xl x m EC No 661 2009 42A 4 X X XI X UN No 73 43 91 226 EEC X X X X X X X E EC No 661 2009 43A X X X X X X X EU No 109 2011 44 ES 92 21 EEC x TA EC No 661 2009 44A i X EU No 1230 2012 45 92 22 EEC xi x xl x x x x xl xl x EC No 661 2009 45A X x X x X x x x X X n fer UN No 43 46 92 23 EEC X X x xix x xi x xl X A EC No 661 2009 46A S X X X X X X x X X X EU No 458 2011 EC No 661 2009 46B X X x x C1 UN No 30 4gc B EC No 661 2009 6 X x X X X x xX C2 C3 UN No 34 JHJ EC No 661 2009 Eie EN VE A o 46D URGREDNOTIS X X X X X X X X X X z S O C1 C2 C3 Sa gc No 661
263. m Q2273 A 4 in which 5 2 Annex3 7 7 d R R67 Q 2 7 3XA Q flow of air in standard m3 min 100 kPa absolute and temperature of 15 C A exterior surface of the container in m2 The flow test must be carried out at an upstream air pressure of 200 kPa absolute and at temperature of 15 C The flow test results must be corrected to standard conditions Air pressure of 100 kPa absolute and temperature of 15 C 2 3 4 3 3 1 6 75MPa 2
264. 3 EZS N 1 EJO 85 1 EID 80 3 12 3 2 Para 2320C Z 48 dr HH A IH PS 3 1 E A Er 3 JIS K 6258 2003 Jim 2 A XQ up B 5 13 6 0318 8 IS01817 1999
265. 1 1 9 14 E 1 1 1 b 2 aR HR uA BR DAVE OD gx R 360L 2 gt 3 4 H zne 3 1 WB 2 D iA c EXER UT TE E N ETRHEUT D C CXe ot IS06892 1 2009 H Zu on D R Aa IZ 4
266. 70 311 EEC X X X X X X X X X X SA Bn a X X X X X X X X XX 6 70 387 EEC X X X XxX SS EC No 661 2009 ai ida RAJ EU No 130 2012 o c Nat A 6B HH EC No 661 2009 2 UN No 11 7 70 388 EEC X X X X XX us Te EC No 661 2009 7A UN No 28 X X X X X X 8 KS 2003 97 EC X X X X XX PM Tm EC No 661 2009 8A UN No 46 X X X XX X 9 mig 71 320 EEC X X X X x X X X xl X 9A E RI XO x9 x XC xX x9 x0 x9 x UN No 13 mr HH EC No 661 2009 y y UN No 13 H 10 72 245 EEC XI X X X X X X X X X 10A Mu Ia X X X X X X X X X X No 10 12 74 60 EEC X EC No 661 2009 12A X UN No 21 13 74 61 EEC X X X X XI X 13A CN A KOA KOA KON K UN No 18 EN EC No 661 2009 13B X X No 116 14 74 297 EEC X X i
267. EN 895 1995 3 1 2 1 ARAIA 2 3 1 e f 1 g h 2 g h 2 2 N Sh iy 10 R R67 3 JIS Z 3122 2013 Amd1 2011 IS0 7799 1985
268. 2 2E 3 0MPa C RI 15cm h Aic IR BEZCT KO 2 hc E 4 EP E RO LV RFL MAH EE BaidockAAwy Lr 13 F BA DIU
269. 2 17 2 3 RE DEL RUE 3 33 LPG 4 2 7 200 1 1 3 4 2 12 2 3 1 12 3 1 4 4 1
270. 6 sz HH 30 3 2 1 2 100mm 3 100mm 50mm 25 mm 2 JIS Z 3104 1995 6 IS01106 1 1984 1 50mm B ISO gt J B BEST IEH
271. 10 1 3 Flow capacity of pressure relief valves test No 2 Q 15C 0 1MPa 10 1 3 1 The flow capacity of each of three samples of a pressure relief valve of a specific size design and R R67 m min setting shall fall within a range of 10 per cent of the highest observed capacity F mE 15C 0 1MPa 10 1 3 2 During flow capacity tests on each valve there shall be no evidence of chattering or other abnormal F 15C BE operating condition h kPa 10 1 3 3 The blow down pressure of each valve shall be not less than 65 per cent of the initially recorded kPa start to discharge pressure 10 1 3 4 A flow capacity test on a pressure relief valve is to be conducted at a flow rating pressure of 120 per Dp cent of the maximum set pressure E s
272. 2 EE SET 2S 3 6 75MPa 4 5MPa 4 3 Para a 6 2 2 3 3 Dira T 1 2 B J We vea Pora E EX Ex A E ES 1 1 GE BOUT ITE 1 IH PS B 2 1 2 3
273. 6 3 4 1 22 20 3 5mm 5mm 4 5 6 55 7 A oi 5 Ra LPG 1 1 3
274. AIA 6 Mississippi Mississippi States Department of Health Boiler and Pressure Vessel Safety Branch 2348 4 EE C E NBIC cur uult c us 2
275. H http ec europa eu consumers safety rapex alerts main index cfm event main listNotifications amp CFID 5015348 amp CFTOKEN 17948973 amp jsessionid 09008caf093c08255dDc2226544a58435 db5 II 37 3 4 R67 R67 3 4 1 1 44 WA HH au DE 48 2 BR SS ZM ri
276. H z0 18D 4b h 50 15 D not applicable for containers as shown in Appendix 2 to this annex Figure 2a Er 1 6 1 2 3 The thickness of these barrelled ends must not in toto be less than the figure calculated by means of the following formula The shape factor C to be used for full ends is given in the table and in the graphs contained in Appendix 4 to this annex The wall thickness of the cylindrical edge of the ends may not be less or differ more than 15 per cent from the smallest wall thickness of the shell 1 6 1 3 The nominal wall thickness of the cylindrical part and of the barrelled end may not under any circumstances be less than tm mm D mm with a minimum of 1 5 mm 1 6 1 4 The shell of the container may be made up of one two or three parts When the shell is made up from two or three parts the longitudinal welds must be shifted rotated with a minimum of 10 times the thickness of the container wall 10 X a The ends must be in one piece and convex 3 LPG 4 165 Calculation of the parts un
277. 1 12 1 3 1 1 2 15 2688 2 10 3 1 15 3 1 6 1 1 2 Containers with longitudinal welds a z 0 85 where the manufacturer radiographs each weld intersection and 100 m of the adjacent longitudinal weld and 50 mm 25 mm each side of the intersection of the adjacent circumferential weld This test has to be performed per machine at the beginning and
278. L amp LPG T 8 VANS D 300L 8 UN UN DIESEN
279. LL H 440 440 520 3 520 4 5 hr 12 EN895 1995 1 g h 2 g h IS05173 2009 H l 3 i LAB D1 3a 4 1 1 1 1 2 1 2 EM 12 2 LPGC 4
280. 3 2 1 2 3 4 5 6 3 1 4 3 5 3 6 3 7 3 IEC 60068 2 52 1996 2 IS09227 2012 JIS Z 2371 2000 KARRDI k 144 Kb JIS C 0024 2000 IEC 60068 2 52 1996 JI
281. 40 48 3 1 5 20 11 LPG compatibility tests for synthetic materials 11 1 A synthetic part in contact with LPG liquid shall not show excessive volume change or loss of weight Resistance to n pentane according to ISO 1817 with the following conditions a Medium n pentane b Temperature 23 C tolerance acc to ISO 1817 c Immersion period 72 hours 11 2 Requirements Maximum change in volume 20 per cent After storage in air with a temperature of 40 C for a period of 48 hours the mass compared to the original value may not decrease more than 5 per cent TC JIS K 6250 6 1 13 6 3 ROT voe EHE CHA OS PR OO E Ze H TRE 3 cg LH I5 HEB
282. 2 7 200 1 1 3 20 R R67 2 16 2 3 1 16 3 32 LPG 1 3 2 17 2 3 1 17 3
283. 24 es 2 8 25 2 9 26 m 2 10 3 2 3 1 R67 R67 Cli 2 5 Sun Os dE TE D80 per cent stop valve Level indicator Pressure relief valve ZEF EU 6 3 3 4 E E Remotely controlled service valve with excess flow valve GAWIE FIT S kahi Fuel pump Multivalve Gas tight housing Power supply bushing Non returm valve
284. ASTM D 2343 2008 2800N mm AF TS 3 4 3 2 1 LPG 1 ATF TEER UD BAD FER 4H p P D LSR 4P P D
285. IS06957 1988 4 2 5 2 EE IH PES 6 2 7 2 55C 1 w 12 Corrosion resistance 12 1 A metal LPG containing component shall comply with the leakage tests mentioned in 4 5 6 and 7 and after having been submitted to 144 hours salt spray test according to ISO 9227 with all connections closed Or an optional test 12 1 1 A metal LPG containing component shall comply with the leakage tests mentioned in 4 5 6 and 7 and after having been submitted to a salt spray test according to IEC 68 2 52 Kb Salt Spray Fog Test Test procedure Before the test the component shall be cleaned according to the instructions of the manufacturer All the connections shall be closed off The component shall not be operated during the test Subsequently the component shall be submitted during 2 hours to spraying with a solution of salt containing 5 per cent NaCl mass per cent with less than 0 3 per cent contamination and 95 per cent distilled or demineralized water at a temperature of 20 C After the spraying the co
286. 1 219 20 100 2 12 2 3 1 85 2 10 Acid environment test 2 10 1 Test procedure A finished container shall be exposed for 100 hours to a 30 per cent sulphuric acid solution battery acid with specific gravity of 1 219 while pressurized to 3 000 kPa During the test a minimum of 20 per cent of the total area of the container has to be covered by the sulphuric acid solution Then the container shall be submitted to a burst test as defined in paragraph 2 2 of this annex 2 10 2 Test interpretation The burst pressure measured shall be at least 85 per cent of the container burst pressure 2 10 3 Retesting Retesting is permitted for the acid environment test A second test shall be performed on two containers which have been produced successively to the first container within the same batch If the results of these tests are satisfactory the first test shall be ignored In the event where one or both of the
287. 20 17 R67 R67 R67 R67 EN10120 2008 Steel sheet and strip for welded JISG3116 gas cylinders 4 4 O SUE T E EL FERT EN10120 steel name N mm 3 tz5
288. Nmm P245NB 245 360 to 450 34 P265NB 265 410 to 500 32 P310NB 310 460 to 550 28 P355NB 355 510 to 620 24 JIS G 3116 hrs Na Nmm doe SG255 255 400 28 SG295 295 440 26 SG325 325 490 22 SG365 365 540 20 4 18 E R67 ISO20826 2006 Automotive LPG components Containers ISO20826 S
289. R67 2 alli II 31 Toroidal Vessel with torispherical shell torispherical Form 7 value kPa N mm mm mm mm H mm mm mm
290. 1 2 28 LPG 1 2 7 200 1 1 4 5 11 2 11 3 1 11 4 1 2 1
291. 2 8MPa 11 R67 20 10 3 R67 R67 22 17 2
292. 3 R R67 R R67 ik EE UN R67 3 Hr m 3 i HEISE 67
293. 30 o 4 ye une fup 5 21 noc un 1 jam 1 20 3 3 4
294. R67 7 LPG RE Ms R67 2 5 0045 000 25 e II 17 5 RTRA TUV Rheinland KBA SNCH RDW i ISO9001 i TRO n mmi ni mei jm
295. 12 13 14 16 17 18 19 20 21 22 23 24 25 26 277 28 29 3 1 CTO 34 36 We 39 TNNT NEU RON D CUI MEN 2 e 4 62 4 351 52 53 7 40 BU 42 43 6 38 WP29 UN 21958
296. 2 m2 1 ml gt 3 ml m2 2 JISG 0553 1996 3 1 2 4 2 Macroscopic examination The macroscopic examination of a full transverse section of the weld must show a complete fusion on the surface treated with any acid from the macropreparation and must not show any assembly fault or a significant inclusion or other defects In case of doubt a microscopic examination should be made of the suspect area 17 3 LPG 1 6 2
297. 3 2 4 2 3 4 3 Z 19 5 E 3 19 1 J 1 i Ic E 2 x 10 3 1 20 21 101 301 701 100 300 700 2
298. XX 200 1 10 2 1 2 1 10 2 1 2 1 9 8 DE 2 1 2 4 1 UT Wy pera IEEE a EE 123485 er S ases zzi seu m quaes rar E E etes mme oT mag EET CT ZT 95 Luc MEE IEEE E R1 TXEcuegoaesemu2s50rTs2 2 1 2 mur ponen p EC AWREXISIT V7TRY sno mm CTS EZ ELE RENNES CN 77771 amna O CO ETT A FE semen A ME CE E zsh Jt EC EE E ET e DE E 0 C ME E a E exem emmmwrxi ME uae 4 6
299. KHKS0121 2010 5 70MPa KHKS 0128 2010 3 1 LPG 1 Annex 10 1 R67 Annex 10 9 1 3 1 6 1 10 27 2 1 2 2 11 28 2 1 2 3 12 2 2 13 29 2 3 JC ARSB SA 14 x 2 6 24 1 15 30 1 6 1 1 2 1 7 2 3 16 31 2 4 2 17 32 2 5 2 LPG 4
300. 2 1 1 3 000 kPa 9 6 30 3 000 LPG kPa tW 2 2 0 0 3 000 kPa 9 6 1 30 LPG WP R67 200 10 2 4 1 1 1 10 2 4 1
301. 3 3 2 3 3 1 1 2 2 3 4 5 LPG 1 20 zz Hd ZA 17
302. II 39 R67 49 2 4 18 2 R67 29 R67 2 8MPa 2 6 1 2 8 2 13 2 2 30 m
303. The butt welds on the stress resistant shell may not be located in any area where there are changes of profile RREI Vene MHIL UE C E Angle welds may not be superimposed on butt welds and must be at least 10 mm away from them Ski 1 fi Welds joining parts making up the shell of the container must satisfy the following conditions see figures given as examples in Appendix 1 of this annex 10mm Longitudinal weld this weld is executed in the form of a butt weld on the full section of the material of the wall m en this Pise in B a asl on the full section of the material of the 4 AM i iis T wall A joggle weld is considered to be a special type of butt weld m 2 s LI mi Welds the studded valve plate or ring shall be PE out according to Appendix 1 Figure 3 nir FC o m A weld fixing the collar or supports to the cont
304. 2 3 1 5 3 3 3 1 2 3 2 1 3 0MPa 90 24 10 1 2
305. 2 0ml 1 M ZA IN 6mm 2 sz HH Faran 1 nm 2 2 m2 1 ml 3 ml m2 2 2 JIS G 0553 1996 6 3 1
306. 3 R R67 4 R I 1 1 E BG E FOr
307. m 1 1 1 W NBBI 3 Cal OSHA LTH m B Chevron Richmond NBBI Cal OSHA OUIO Cal OSHA NBBI 1 NBBI 3 NBBI 1 5 He
308. 3 21 1 2 4 2 22 1 3 23 1 R R67 3 24 1 3 26 1 3 28 1 2 7 7 1
309. 4 cross section 25 mm in width for a length extending up to 15 mm beyond the edges of the weld as shown in Figure 2 of Appendix 3 to this annex Pu Ne fe EE pe ERES Beyond this central part the width of the test piece must increase progressively 2 1 2 2 2 2 The tensile strength value obtained must meet the minimum levels required by EN 10120 1 2 1 2 3 Bend test SN RAT SA 5 The bend test shall be carried out in accordance with standards ISO 7438 2005 and ISO 7799 1985 and ISO nnus N B ij gt KA 2p PAN o 2 RARA n OS RE ero 5173 2009 Amd 1 2011 for welded parts The bend tests shall be carried out on the inner surface in tension 2 1 and the outer surface in tension 1 2 3 The bend tests shall be carried out on the
310. EU Her ORE eX 96 The rapid alert system for non food dangerous products RAPEX The Sustainable EU Ir 4 2004 2005 2014 13 856 1 239 762 2 1 S BTE m ok me A E noe
311. 17 1 3 6 1 3 7 1 3 9 1 3 10 1 3 12 1 3 13 1 3 E 14 1 3 15 RE 1 3 16 5 6 7 1 3 en
312. ISO 5173 2009 FHR ISO 7438 2005 3 mm 4 N mm 440 2 440 520 3 520 4 5 3 4 1 1 1 1 uc ues 2 1 2 EAR HR TTE n x AAR CENDELO E 2 2 Burst test under hydraulic pressure
313. M i pu Annex 10 1 6 1 2 2 0 003 D lt b lt 0 08 D lt 300 lt 20 00 R lt D 250 Annex 10 H2 0 18 D 6502 gt r22 b 31 gt h gt 4 b 20 gt h lt 0 15 D lt 1 6 1 2 3 o 9 x E Jui D E n 38 b gt Ph D C 1500 Re 3 gt 202 Annex 10 1 6 1 3 C 4 dg EJ IE b gt D 250 imm 3 gt 2 b gt 1 5 mm 3 gt 1 5 2 3 A CNG CHG LP q Ta 3 12
314. OUIO OUIO W gt ASME gt NBBI gt ASME Section IX Subchapter 15 Petroleum Safety Orders Refining PA imi 3E TN I 22 Transportation and Handling C 1f
315. 1 CN SD s Id JIS K 5627 1995 130 20 JIS K 5628 1995 1 1 i 1 16 qoa dm 1 JISK 5633 1995
316. 17 1 3 17 1 A a 2 1 2 5 1 3 17 1 5 8 1 3 20 1 2 5r KC O98 3 5
317. 2 2 R67 7 R67 44 A 8 4 R67 17 3
318. AIA T 7 Ohio Ohio Department of Commerce Division of Industrial Compliance 23TH 4 Z5 C do 2 8 Oklahoma Department of Labor Safety Standard Division 23TH 4 HAE C do 5 NBBI API VN 3 1 3
319. HAIJ EC No 661 2009 x 9 e e e Hj EU No 1008 2010 II 24 E ut H WVTA E Mi M M Ni N N 0 10 10 36 2001 56 EC xi xi x xi x xi xi xi xi x X EC No 661 2009 36A x x x x x x x X X X ici UN No 122 37 78 549 EC x EC No 661 2009 37A X EU No 1009 201 38 78932 EEC x SRM EC No 661 2009 38A d i4 x XI X X x x VLA o 40 80 1269 EEC XN XO XO XO x xo 41 2005 55 EC x9 x9 X x X X EuroIV XU V iid 41A Euro VD
320. 0Pa 65C 95 E 48 0 3MPa 3 0MPa iG ONE Ice SNE 3 20 2 4 12 2 3 1 1 2 2 3 3 4 85 20 LPG 4 3 jum E 5bIAILEAAESXERXE TTC Lnd CER 5
321. 2 19 2 20 2 1 4 3 1 4 ES 2 3 17 1 1 7 21 2 3 4 1 3 Erp 1 3 10 1 18 1 3 20 RE 1 1 2 5 3 4 17 1 2 19 1 3 2 0
322. 2 5 26 3 I E u hRoNELDLISIL ET 1 E rip erc er E 1 UE LI EIC E 2 Sh oc dibsds AS orere ieai TRA S nA ER Ree X UH IRR SG RUM RUE 2 2 RAZBATE uxerume qeeoxbrk esa e des RA De RES uw NU RR EE E 26 WE S er 31 II 1 enm HH 1 2 een n IH hmm hn 1 3 nn HI IH hehehe 3 3 1 1958 3 3 2 eee HH Inn nn nnn 28 3 3 enne 36 3 4 38 1 R R67 2 R
323. M Ave RLE EOD 1 E i5 ej 1 2 2 1 3 1 2 74Nm 78Nm
324. 10 7 Wr 8 9 8 2 1 2 3 11 10 3 ps 3A SR C r1 7 1 7 E ts 3 o D 7 oux 2 2 X E 7 EI y CA XE E B d 7 sz A dm gt N 3 n naL HX n LPG II RI aA BR Hr 1 EX K
325. 3 3MPa 2 3 R67 10 3 2 4 1 1 R67 Annex 10 Appendix 5 1
326. 2 3 1 13 3 30 LPG 1 200 1 2 7 1 3 1 0 85
327. O 10 EEs 50 30 165cm 165cm Zt
328. OUIO PA mE X Hx diae fT 4 5 NBBI NBBI R NBBI Cal OSHA DRA NBBI OIUO H OUIO 23 8 E B W a E ull E RJ ii OUIO B
329. 0 A 3 0MPa ml of nitric acid per litre of solution Following the immersion the pressure relief device shall be leak tested by 4 10 000 applying an aerostatic pressure of 3 000 kPa for one minute during which time the component shall be checked Ho 20C 0 3MPa 3 0MPa for external leakage Any leakage shall not exceed 200 cm3 h 4 10 000 d Exposed stainless steel pressure retaining components of pressure relief device shall be made of an alloy 3 type resistant to chloride induced stress corrosion cracking ASTM B154 12 10g L 70 10ml 30 3 0MPa 1 3 1 1
330. 2 4 5 6 7 8 9 10 11 12 13 14 15 16 17 12 4 R 3 USE R Euri
331. 7 lt 25 1 3 ES HX n 4 5 20 1 3 21 1 1 4 1 8 2 7 2 7 9 7 B 1 9 360L 2 14
332. HB EC No 661 2009 x0 x x05 x x05 x x05 x05 x x05 ike EC No 661 2009 64 X EU No 65 2012 E EC No 661 2009 65 X x X x EU No 347 2012 s HERBA ATA EC No 661 2009 D 2 x x X EU No 351 2012 a LPG EC No 661 2009 67 NUR X x x X XIX UN No 67 ER EC No 661 2009 68 QS LATUS VAS X X UN No 97 69 RAZA HHI EC No 661 2009 X X X UN No 100 Eur us 28 CNG EC No 661 2009 UN No 110 S Eo MS Bn C X 1 Q 6 4B UN No 80 G 6 8 9 10 11 2 5t 12 13 14 70 220 EEC I 5 3 1 4 1 N1 1 2 610 kg LPG CNG
333. R67 R67 P R67 m R LPG ED MPa kPa 7 maximum degree of filling 80 RATAR 80 fil 99 01 3 4 EE PUMP INSIDE
334. The component shall be conditioned for at least 8 hours at this temperature R R67 3 1 15cm h 2 3 6 75MPa GEIRI o TIt 4 5MPa 65 8 2 3 7 3 3 H 1 2 3
335. a Phk D b R Z r R H C a mm Pi 3 0 3 0 MPa D mm b mm R N mm Z MEDRE 30 2878 1 1 0 85 30 1 3 1 mm mm mm H H R b RD Rr 2 205 C H D 0 20 0 25 1 H D 230 25 0 50 1 0 003D b 0 08D LLICCSJGIJ C oCHXrz0O1DRED Hz0 8D rz2b hZ4b h 0 15D r R H 1 2 2N 1 6 Calculation of the parts under pressure 1 6 1
336. 2 2 3 20 2 3 1 26 LPG 4 1 3 2 1 3 0MPa 30 1 219 20 E E2 2 amp 8E amp v5 ko5idgiEEUL 1008RgRIEL Ef amp fed 5 2 12 2 3 1 85
337. 2013 Regulations 2012 10 29 ch PH M Di fi i R 7 Tr A c B il m A H c las 38 0 10 JD 2 9 1 Connecticut Florida Louisiana Michigan Montana New Mexico South Carolina n 3 2013 South Dakota Texas West Virginia 2 Idaho Wyoming Albuquerque New Mexico Buffalo New York Chicago Illinoi Detroit Michigan Los Angeles California NB 370 JREF x Miami Florida Miami Dade Florida Milwaukee Wisconsin New Orleans Louisiana New York New York Omaha Nebraska Puerto Rico Commonwealth 4 Seattle Washington Spokane Washington St Louis Missouri Washington D C Federal District 3 1 2 CFR
338. 3 5 12 2 LPG 4 1 31 3 2 E A 3 3 1 1 2 2 3 4 2 2 1 Test conditions Containers subjected to this test must bear the inscriptions which it is proposed to affix on the section of the container subjected to pressure 2 2 1 1 The burst test under hydraulic pressure must be carried
339. E n 72 20 FE 3 50 kPa E E H t f zu gt Bx XE 10 65 El E lZ 3 Eom K V AEA W 5 EF WE 05 m E 0E 4 0C
340. SMA400BP SMA400BW SMA400CP SMA400CW SMA490AP SMA490AW SMA490BP SMA490BW SMA490CP SMA490CW SMA570P SMA570W JIS G 3115 2000 J X zs M Sik SPV235 SPV315 SPV355 SPV410 SPV450 SPV490 JISG3116 2000 pe SGC255 SG295 SG325 SG365 JISG3118 2000 Ed HE 4H pss SUD SGV410 SGV450 SGV480 JIS G 3119 1987 3 SBV1A SBV1B SBV2 SBV3 JIS G 3120 1987 SQV1A SQV1B SQV2A SQV2B SQV3A SQV3B Y JISG3126 2000 SLA235A SLA235B SLA325A SLA325B SLA360 SLA410 JISG3127 2000 SL2N255 SL3N255 SL3N275 SL3N440 SL5N590 SL9N520 SL9N590 JIS G 3445 1988 STKM19A STKM19C STKM20A
341. Title 12 Department of Labor and Industrial Relations Idaho 2 n Illinois Compiled Statutes Illinois 3 Health and Safety Chapter 430 Public Safety Indiana Administrative Code Indiana 2 Title 680 Boiler and Pressure Vessel Rules Board LEEN Mississippi Code Mississippi 3 f Title 45 Public Safety and Good Order Nevada Administrative Code Nevada 1 Title 455C Safety and Health New Jersey State Statutes New Jersey 1 Title 34 Labor and Workers Compensation North Dakota Statutes North Dakota 1 Title 26 1 Insurance J Ohio Revised Code Ohio 3 Title 41 Labor and Industry Oklahoma State Statutes Oklahoma 4 Title 40 Labor The Pennsylvania Code Pennsylvania 1 No 85 Boiler and Unfired Pressure Vessel Law South Carolina 1 Tennessee Code Annotated Tennessee 1 A Title 68 Health Safety and Environmental Protection Utah Condensed Constitution Utah 3 Title 34A Utah Labor Code dog Code of Virginia Virginia 3 Title 40 Labor and Employment Washington Administrative Code Chapter 296 104 Washington 7 Revised Code of Washington Chapter 70 79 West Virginia 1 Detroit B City of Detroit Municipal Code Michigan Chapter 11 Buil
342. 1 4 3 5 3 6 3 7 3 X 14 3 3 3 2 TIS0188 2007 JIS K 6257 2010 JI fii A K OVE RT BE c A SAX ER TEOGR I IC KU EXER 65C 168
343. 2 3 5 2 6 2 7 2 3 1 5 3 6 3 7 3 17 3 3 1 ma H N 2 2
344. 46E 47A 48A 49A 50A 50B 51A 52A 52B 53A 54A 56A 57A 64 70 3 2 3 2 1 R67 2 1 I R67 NV Ws 2 10 OD ge n EF R67 LH pe i EO OR DUE AR TR TERES CUR
345. Hob ROS 2 F AA 13 Los Angeles California Department of Building and Safety AIA E d HH
346. be radiographed 151 quim iS 18020826 2006 Automotive LPG components Containers je 2 1 7 2 3 14 R R67 16 S LPG 1 1 3 2 2 1 m2 1 A 2 D 6 Fii IRS 20 ml es
347. 2 b One specimen shall be fatigue tested at a pressure cycling rate not to exceed 4 cycles per minute as follows 3 1 Held at 82 C while pressured for 10 000 cycles between 300 and 3 000 kPa 2 G Held at 20 C while pressured for 10 000 cycles between 300 and 3 000 kPa As At the end of this test there shall be no leakage or any visible sign of extrusion of any fusible metal used in the 8 y 8 y 1 3 0MPa 90 24 design c Exposed brass pressure retaining components of pressure relief device shall withstand without stress 2 corrosion cracking a mercurous nitrate test as described in ASTM B154 The pressure relief device shall be BASRAN SJE lt c lt immersed for 30 minutes in an aqueous mercurous nitrate solution containing 10 g of mercurous nitrate and 10 82 C
348. D 2343 2008 58 1400N mm UF TE JIS K 7010 1995 E JISR 3420 EMI S ASTM D 2343 2008 2800N mm S 4 1 Vy 3 2 LPG 1 sz HH
349. H pany pun na n ng JU Im ini DM D INFORMATION DOCUMENT relating to type approval and referring to specific components of motor vehicles using liquefied petroleum gas LPG or compressed natural gas CNG in their propulsion system 2A001 2A001 51 2A001 52 2A001 53 ECE R110 R67 2A001 54 2A001 55 2A001 56 amendment 00 8 supplement 9 ABC Co Ltd Yokohamai shi 2A001 Kanagawa 243 000 Not applicable Japan Interface Control Moduie i Name and address of manufactures Not applicable authorized representative General information Essential characteristics of the CNG and LPG component System description Explanation of versions ICM system diagram Source of interface and protection parts Fuel cut timing chart 9 pages include this cover page 2 2 2
350. I AIA NBBI E Not for Profit Organization ASME Chief Inspector NBBI WEB 1 NBIC NBIC ANSI NBIC 3 Part 1 installation TE http www nationalboard org ViewMembers aspx
351. International Automotive Task Force ISO9001 ISO TS16949 DRET ISO9001 ISO9001
352. Tra R JIS K 6259 2004 E 20 1 5 000ppm 72 3 1 40 3 16 3 3 2 1 H 0 fj Jg wb Ed amp nico vC KAROR 6 75MPa 120C 96
353. end of each work shift period from continuous production b z 1 where each weld intersection and 100 mm of the adjacent longitudinal weld and 50 mm 25 each side of the intersection of the adjacent circumferential weld is spot radiographed This test has to be performed at 10 per cent of the container production the containers to be tested are chosen randomly Should these radiograph tests reveal unacceptable defects as defined in paragraph 2 4 1 4 all the necessary steps must be taken to examine the production run in question and eliminate the defects 1 7 2 3 Inspection of welds The manufacturer must ensure that the welds show continuous penetration without any deviation of the weld seam and that they are free from defects likely to jeopardize the safe use of the container For containers in two pieces a radiographical test has to be performed on the circumferential butt welds over 100 mm with the exception of the welds in conformity with joggle weld on page 1 of Appendix 1 of this annex On one container selected at the beginning and end of each shift period from continuous production and in the event of production being interrupted for a period of more than 12 hours the first container welded should also be radiographed ITUBIS 1 6 1 1 2 a 1 2 gt 1 723 1 3 1 6 1 1 2 b 31 LPG 1
354. gu A5 AR 348 O0 TyLew e vy RIi 3 2 1 IS09227 2012 A IL 02 B x DERI K A ERARA L I4 JIS Z 2371 2000 14 4 IEC60068 2 52 1996 2 Kb JIS C 0024 2000 REAR TES ETE K CERE UO Z7 7v 2 IEC60068 2 52 1996 2 Kb JIS C 0024 2000
355. i 9 16 17 18 rei zn 25 26 36 14 2 7 BOR D ZA COE Z amp Ok A i BR SX SR EA 9 0o I 18 3 2 1 2 H 11
356. in the direction to tighten a threaded connection then in the untightening direction and finally again in the tightening direction The container shall then be subjected to an external leak test in accordance with the requirements shown in paragraph 2 3 6 3 of this annex 2 9 2 Test interpretation The container shall comply with the requirements of the external leak test as shown in paragraph 2 3 6 3 of this annex 2 9 3 Retesting Retesting 1s permitted for the boss torque test A second test shall be performed on two containers which have been produced successively to the first container within the same batch If the results of these tests are satisfactory the first test shall be ignored In the event where one or both of the retests fail to meet the requirements the batch shall be rejected 26 LPG 4 1 OUR 3 2 1 3 MPa 30
357. mentioned in the annexes to this Regulation 200 10 R R67 room temperature and at the temperature of 120 C 7 7 Pressure relief device fuse requirements 10 1 Pressure relief device fuse specified by the manufacturer shall be shown to be compatible with the service 3 conditions by means of the following tests 4A MESE a One specimen shall be held at a controlled temperature of not less than 90 C and a pressure not less than CH 1 test pressure 3 000 kPa for 24 hours At the end of this test there shall be no leakage or visible sign of MUN b extrusion of any fusible metal used in the design
358. of tha EU GG German Basic Law TRBS Technical Rules of industrial safety and health VdTUV Organization of TUV VDE Association for Electrical Technologies Ant ot Pariamant VDI Association of German Engineers tational Orinanns BG Employer s Liability and Statutes Insurance Association Constitutions of the Federal States Federal State Law mandatory Sta e d DIN EN TRBS nondntndaeny National Standards e g VDE VDI Rules BG Rules VdTUV Merkhlatt Industrial Standards 1 EU 1 EU 97 23 EC PED I IV 4 2 ProdSG Act ProdSV National Ordience
359. out with equipment which enables the pressure to be increased at an even rate until the container bursts and the change in pressure over time to be recorded The maximum flow rate during the test should not exceed 3 per cent of the capacity of the container per minute 2 2 2 Test interpretation 2 2 2 1 The criteria adopted for the interpretation of the burst test are as follows 2 2 2 1 1 Volumetric expansion of the metal container it equals volume of water used between the time when the pressure starts to rise and the time of bursting 2 2 2 1 2 Examination of the tear and the shape of its edges 2 2 2 1 3 Bursting pressure 2 2 3 Test acceptance conditions 2 2 3 1 The measured bursting pressure Pr must not under any circumstances be less than 2 25 X 3 000 6 750 kPa 2 2 3 2 The specific change in the volume of the metal container at the time of bursting must not be less than 20 per cent if the length of the metal container is greater than the diameter 8 11 R R67 5 LPG 1
360. to be decreased until there is no further discharge from the valve The pressure at which this occurs is to be recorded as the blow down pressure of the valve 10 1 3 10 From the recorded data and the known orifice coefficient of the flowmeter the air flow capacity of the pressure relief valve tested is to be calculated using the following formula where Q Flow capacity of pressure relief valve in m3 min of air at 100 kPa absolute and 15 C Fb Basic orifice factor of flowmeter at 100 kPa absolute and 15 C Ft Flowing air temperature factor to convert recorded temperature to base of 15 C h Differential pressure across orifice of meter in kPa p Flowing air pressure to pressure relief valve in kPa absolute recorded gauge pressure plus recorded barometric pressure 60 Denominator to convert equation from m3 hour to m3 min 10 1 3 11 The average flow capacity of the three pressure relief valves rounded off to the nearest five units is to be taken as the flow capacity of the valve of that specific size design and setting 10 1 4 Recheck start to discharge and resealing pressures of pressure relief valves test No 3 10 1 4 1 Subsequent to flow capacity tests the start to discharge pressure of a pressure relief valve shall be not less than 85 per cent and the resealing pressure shall be not less than 80 per cent of the initial start to discharge
361. 0 Do a P stress relieve or normalize M 3 5mm 5mm 27 ateria ota Cr erenf and norma Ize P 1 5 4 The manufacturer must submit the procedure for the heat treatment used 4 ds EE ADSIDUE 43 e ERA OS 1 5 5 Localized heat treatment of a completed container is not permitted EDEA JO o 5 6 Jedes gg 1 2 Dimensions 1 7 2 4 CHAHE For all dimensions without indication of tolerances general tolerances of EN 22768 1 shall apply MERE OHNE 7 3 5 LPG 1 2 1 1 7 2 4 Outofroundness eu HD jay The out of roundness of the cylindrical shell of the container must be limited so that the
362. 1 H 1 41 50 6 17 2 1 2 1 3 4 1
363. 1998 1 EC WVTA EU EC WVTA EU 2007 2007 A6 EC AY EC WVTA 3 EC WVTA UN 4 EU 2007 46 EC IV 1I EC WVTA EU 1 H EU UN 2 UN EC WVTA 1958 ECE TRANS WP29 78 Rev 3 Consolidated Resolution on the Construction of Vehicles R E 3
364. 2 2 1 1 80 40 2 500 8 3 1 2 1 18 2 2 4 1 1 0 15g h 2 10 000
365. 2009 46B TTY 2 xa XA qum 47 92 24 EEC X x x x EC No 661 2009 47A HORE RIE X X X X epe UN No 89 j 44 oa 8 B4 97 27 EC X X X X X X X X X r xh EC No 661 2009 48A g X X X X X X X X X EU No 1230 2012 49 92 114 EEC X X X EC No 661 2009 49A x x X UN No 61 II 25 WVTA A Mi M Mi Ni N 5 00 0 0 04 50 94 20 EC x09 x09 ya yay xA X X X X X x EC No 661 2009 50A UN No 55 xA xA xA xA x0 x X x X X CCD EC No 661 200
366. 3 0MPa 3 30 3 1 2 3 Hydraulic test 2 3 1 The containers representative of the type of container submitted for approval without accessories but with the outlets closed off shall withstand an inner hydraulic pressure of 3 000 kPa without leakages or becoming permanently distorted according to the following requirements 2 3 2 The water pressure in the container must increase at an even rate until the test pressure of 3 000 kPa is reached 2 3 3 The container must remain under the test pressure long enough to make it possible to establish that the pressure is not falling off and that the container can be guaranteed leakproof 2 3 4 After the test the container must show no signs of permanent deformation 2 3 5 Any container tested which does not pass the test must be rejected 2 30 fb Ze TH Gica au 2 18 6 Ina Gt HE ge AR Lc H J 5 IDE ARR AUR 14
367. 5 1 3 16 1 3 17 1 3 30 1 3 31 1 3 32 1 3 6 7 1 6 11 1 2 4 2 14 1 3 19 1 3 21 1 2 4 2 22 1 3
368. 9 m 50B CCD UN No 102 ES dile 51 95 28 EC X FENTY O D 0 v E D EC No 661 2009 51A X UN No 118 52 2001 85 EC X X P EC No 661 2009 X X E 3 UN No 107 si T EC No 661 2009 52B X X UN No 66 53 96 79 EC x NUUS EC No 661 2009 53A xe UN No 94 54 96 27 EC xe XS 54A EC No 661 2009 P RITE ZEE A UN No 95 id 55 56 98 91 EC X03 x09 x03 x03 x03 x03 x03 EC No 661 2009 56A UN N M X05 X05 X03 KEA 303 X033 x03 VLA O 57 ed 2000 40 EC x x FUPD AE dn pae kh HI 57A PRI EC No 661 2009 FUP UN No 93 58 EC No 78 2009 X X 59 2005 64 EC X X 60 61 2006 40 EC X X 4 62 RAJ EC No 792009 X X xl xix X 63
369. AIOLI ISC been produced successively to the first container within the same batch 2 If the results of these tests are satisfactory the first test shall be ignored In the event where one or both of the retests fail to meet the requirements the batch shall be rejected NS 34 LPG 4 2 7 200 1 5 1 3 4 2 18 2 3 1 18 3 4 1
370. Calculation of the parts under pressure for metal containers 1 6 1 1 The wall thickness of the cylindrical shell of the containers must not be less than that calculated by the formula 1 6 1 1 1 Containers without longitudinal welds 2x 1 6 1 1 2 Containers with longitudinal welds 2x a z 0 85 where the manufacturer radiographs each weld intersection and 100 m of the adjacent longitudinal weld and 50 mm 25 mm each side of the intersection of the adjacent circumferential weld This test has to be performed per machine at the beginning and end of each work shift period from continuous production b z 1 where each weld intersection and 100 mm of the adjacent longitudinal weld and 50 mm 25 each side of the intersection of the adjacent circumferential weld is spot radiographed This test has to be performed at 10 per cent of the container production the containers to be tested are chosen randomly Should these radiograph tests reveal unacceptable defects as defined in paragraph 2 4 1 4 all the necessary steps must be taken to examine the production run in question and eliminate the defects 1 6 1 2 Dimensions and calculations of ends see figures in Appendix 4 to this annex 1 6 1 2 1 The container ends shall be in one piece shall encave to the pressure and shall have either a torispherical or an elliptical form examples are given in Appendix 5 1 6 1 2 2 The container ends must fulfil the following conditio
371. D 2 CalOSHA 1515 Clay Street Suite 1622 A Oakland California 94612 Donald C Cook Principal Safety Engineer CCR Title 8 Chapter 4 Division of Industrial Safety AIC Ov CI LC S Subchapter 1 3 1 2 ASME Certificate Mark LPG LPG CalOSHA CalOSHA WEB Subchapter 14 15 CCR Circular Letter Cal OSHA
372. E 2 1958 1958 4 UN UN 3 UN E HEDE E 26 amp 8 E 1 30 E HEHEH O A HSF 4 R O HEO TER 1958 51 UN ALBEN
373. E qnc c du E eus UE min idi ein E HS Hz R67 1 n p ES Em mi T LPG LPG NA yN AER Ane EAE 2
374. NBBI OUIO NB 371 6 0 1 3 1 2 1 2
375. No 1005 2010 28 77 538 EEC X x X x X x X x X X 5778 EC No 661 2009 28A D x x x x x x x X X X UN No 38 29 77 539 EEC x xl xi x x xi x xi x x 578 7 EC No 661 2009 29A NH x x x x X x x X X X UN No 23 30 77 540 EEC X X X X X X H EC No 661 2009 30A sr X x x X XIX A UN No 77 31 77 541 EEC xc cel XIX XJ X EC No 661 2009 31A ii pq PE e X X X X x X Isofix UN No 16 32 77 649 EEC X EC No 661 2009 32A X UN No 125 33 K B 78 316 EEC x x X X X X 3 pit yF Bar huka 77 yp EC No 661 009 33A X X X X X X M UN No 121 34 ERE ERG 78 317 EEC xlo oj o gu N B Hi BERUR EC No 661 2009 Saele a SELWATA SHI EU No 672 2010 35 78 31 8 EEC xl 9 0 6 6 D Co EE HI doi
376. S 6 3103 2012 Gam SB450 SB450M SB480 SB480M JISG3106 1995 RHR E SB410 SM400A SM400B SM400C SM490A SM490B SM490C SM490YA SM490YB SM520B SM520C SM570 JIS G 3114 1988 SMA400AP SMA400AW SMA400BP SMA400BW SMA400CP SMA400CW SMA490AP SMA490AW SMA490BP SMA490BW SMA490CP SMA490CW SMA570P SMA570W JIS G 3115 2000 SPV490 SPV235 SPV315 SPV355 SPV410 SPV450 JISG3116 2000 JIS G 3118 2000 GSG255 SG295 SG325 SG365 SGV410 SGV450 SGV480 JIS G 3119 1987 SBV2 SBV3 JIS G 3120 1987 SBV1A SBV1B H
377. S C 0024 2000 Kb ETNE 20C 0 3 95 Bii LC HERE L7 GERD 5wt 2 40 90 95 168 4 4 4 2 5 2 6 2 7 2 JIS H 3300 2012 7 13 RR 24
378. The American Society for Nondestructive testing American Welding Society The Division of Occupational Safety and Health Department of Industrial Relations American National Standards Institute I American Petroleum Institute ASME Labor and Workplace Development Agency California State Government California Code of Regulation Code of Federal Regulation U S Chemical Safety Board The National Board of Boiler and Pressure Vessel Inspectors N B I C National Board Inspection Code American National Standard ANSI NB 23 NBBI O U I A Owner User Inspection Agencies O U I O Owner User Inspection Organizations 3
379. UE I 9 S RS E brun cus Not less than two successive start to discharge and resealing pressure observations are to be made on each of D nb nd 1 KEFA F RUKE IRIZ the three test valves under test No 1 and 3 of paragraphs 10 1 2 and 10 1 4 below 10 4 10 1 2 Start to discharge and resealing pressures of pressure relief valves test No 1 10 1 2 1 Before being subjected to a flow capacity test the start to discharge pressure of each of three samples 10 5 ofa pressure relief valve of a specific size design and setting shall be within 3 per cent of the average of the T zu Wed ZAZ N p ressures but the start to discharge pressure of any one of the three valves shall be not less than 95 per cent P gep y P
380. a maximum radius of 2 5 mm The length of the wedge L shall be at least equal to the width of the container in respect to its movement during the test The height H of the wedge shall be at least 600 millimetres Figure 1 Description of the impact test procedure In the case where a container can be installed in more than one position in the vehicle each position shall be tested After this test the container shall be submitted to an external leak test as defined in paragraph 2 3 6 3 of this annex 2 7 3 Test interpretation The container shall comply with the external leak test requirements as defined in paragraph 2 3 6 3 of this annex 2 7 4 Retesting Retesting 1s permitted for the impact test A second test shall be performed on two containers which have been produced successively to the first container within the same batch If the results of these tests are satisfactory the first test shall be ignored In the event where one or both of the retests fail to meet the requirements the batch shall be rejected 24 1 2 3 2 1 2 3 4 5 6 3 1 E LPG 4 1 OUS 3
381. ainer shall be either a butt or angle weld Welded mounting supports shall be welded in the circumferential way The welds shall be strong enough to Eo withstand vibration braking actions and outside forces of at least 30 g in all directions XBHEHSEEBUIU AST0IARSOTERUE RATRAT L m this case of butt welds the misalignment of the joint faces may not exceed one fifth of the thickness of the M 2 LPG 1 walls 1 5 a m2 4 R R67 Noe nm 2 1
382. akage or any other equivalent test method flow measurement or pressure drop cn 5 4 The external leakage must be lower than the requirements stated in the annexes or if no requirements are mentioned the external leakage shall be lower than 15 cm hour with the outlet plugged when submitted to a gas pressure equal to the leakage test pressure 2 6 3 3 1 HH 6 High temperature test A LPG containing component shall not leak more than 15 cm3 hour with the outlet plugged when submitted to a gas pressure at maximum operating temperature as indicated in the annexes equal to the leakage test pressure Table 3 paragraph 5 3
383. assification cl 2 5 3 3 1 20C 65 2 3 1 4 3 1 15cm H 6 75MPa 4 5MPa
384. cumferential welds three sections on test pieces taken from the places shown in Figure 1 of Appendix 2 of this annex 2 1 1 2 All the mechanical tests for checking the properties of the parent metal and welds of the stress resistant shells of the container are carried out on test pieces taken from finished containers 2 1 2 Types of tests and evaluation of test results 2 1 2 1 Each sample container is subjected to the following tests 2 1 2 1 1 Containers with longitudinal and circumferential welds three sections on test pieces taken from the places shown in Figure 1 of Appendix 2 of this annex a One tensile test on parent material the test piece to be taken in the longitudinal direction if this is not possible it may be taken in a circumferential direction b One tensile test on parent material of the bottom c One tensile test perpendicular to the longitudinal weld d One tensile test perpendicular to the circumferential weld e One bend test on the longitudinal weld the inner surface in tension f One bend test on the longitudinal weld the outer surface in tension g One bend test on the circumferential weld the inner surface in tension h One bend test on the circumferential weld the outer surface in tension and 1 One macroscopic test of a welded section ml m2 A minimum of two macroscopic tests of valve boss plate sections in case of the sidewall mounted valves referred to in paragraph 2 4 2 below
385. der pressure for all composite containers 3 The stresses in the container shall be calculated for each container type The pressures used for these 6 9 calculations shall be the design pressure and burst test pressure The calculations shall use suitable analysis 3 10 techniques to establish stress distribution throughout the container 3 0MPa 3 0MPa TREET A RV 1 6 1 4 The shell of the container may be made up of one two or three parts When the shell is made up from 5 3 3 two or three parts the longitudinal welds must be shifted rotated with a minimum of 10 times the thickness of the container wall 10 X a The ends must be in one piece and convex 1 LPG 1 4 d PUEDE AAR TETO EAE a SO MN HE ien eed er NS welding process HA DS s BA nens dus ones
386. describe the behaviour of the complete fire protection system including the designed drop to atmospheric pressure The requirements of this test shall be deemed to be fulfilled for any container having the following characteristics in common with the parent container a Same type approval owner b Same shape cylindrical special shape c Same material d Same or greater wall thickness e Same or smaller diameter cylindrical container f Same height or smaller height special container shape g Same or smaller external surface h Same configuration of accessories fitted to the container 2 6 2 Container set up a The container shall be placed in the designed position by the manufacturer with the container bottom approximately 100 mm above the fire source b Shielding shall be used to prevent direct flame impingement on the fusible plug PRD if present The shielding shall not be in direct contact with the fusible plug PRD c Any failure during the test of a valve fitting or tubing that is not part of the intended protection system for the design shall invalidate the result d Containers with a length of less than 1 65 m The center of the container shall be positioned over the center of the fire source e Containers with a length equal to or larger than 1 65 m If the container is fitted with a pressure relief device at one side the fire source shall commence at the opposite side of the container If the c
387. difference between the maximum and minimum outside diameter of the same cross section is not more than 1 per cent of the average of those diameters R R67 A 3 8 6 1 2 2 10 2 11 2 3 12 2 13 2 14 2 15 2 16 2 17 2 18 2 19 2 20 2 21 2 3 22 2 23 2 24 2 25 2 26 2 27 2 28 2 3 29 2 30 2 31 2 32 2 33 2 34 2 2 2 7 1 1 3 1 3
388. ding and Safety Regulations Los Angeles i Los Angeles Municipal Code California Chapter IX Building Regulations 1 Alaska Alaska Department of Labor and Workforce Development 231H 4 2 C do 2 zn uH E AIA NBBI 1 5
389. e length represented over a weld length of 12a is not greater than 6 mm Gas inclusions over any 100 mm weld length where the total area of all the figures is not greater than 2a mm 2 4 1 4 2 For the container wall thickness 4 mm the inclusions listed below are regarded as acceptable Any gas inclusion measuring not more than a 2 mm Any gas inclusion measuring more than a 2 mm but not more than a 1 5 mm which is more than 25 mm away from other gas inclusion measuring more than a 2 mm and measuring not more than a 1 5 mm Any elongated inclusion or any group of rounded inclusions in a row where the length represented over a weld length of 12a is not greater than 6 mm Gas inclusions over any 100 mm weld length where the total area of all the figures is not greater than 2a mm 1 7 2 3 Inspection of welds The manufacturer must ensure that the welds show continuous penetration without any deviation of the weld seam and that they are free from defects likely to jeopardize the safe use of the container For containers in two pieces a radiographical test has to be performed on the circumferential butt welds over 100 mm with the exception of the welds in conformity with joggle weld on page 1 of Appendix 1 of this annex On one container selected at the beginning and end of each shift period from continuous production and in the event of production being interrupted for a period of more than 12 hours the first container welded should also
390. ed with pressure take off lines 2 8MPa 5 connected to a manometer This instrument indicates the pressure differential across the orifice plate and the 3 3 reading is used in the flow calculation A calibrated pressure gauge is to be installed in that portion of the meter roues 50 pipe downstream of the orifice plate This gauge indicates the flow pressure and the reading is also used in the 2 2 flow calculation Pe 10 1 3 7 A temperature indicating instrument is to be connected to the meter pipe downstream of the orifice 3 10 plate to indicate the temperature of the air flowing to the safety valve The reading of this instrument is to be 1 65 integrated in the calculation to correct the temperature of the air flow to a 15 C base temperature A barometer
391. eeding 10 cycles per minute between not more than 300 kPa and not less than 3 000 kPa at 65 C and 95 per cent humidity Following the pressure cycling at high temperature containers shall be submitted to the external leak test and then hydrostatically pressurized to failure in accordance with the burst test procedure 2 3 6 2 2 Test interpretation The container shall comply with the external leak test requirements as defined in paragraph 2 3 6 3 The container shall achieve a minimum burst pressure of 85 per cent of the burst pressure 2 3 6 2 3 Retesting Retesting 1s permitted for the high temperature pressure cycling test A second test shall be performed on two containers which have been produced successively to the first container within the same batch If the results of these tests are satisfactory the first test shall be ignored In the event where one or both of the retests fail to meet the requirements the batch shall be rejected 3 3 R67 20 2 3 0MPa lt 3 1 LPG 4
392. een not more than 300 kPa and not less than 3 000 kPa at a rate not to exceed 10 cycles per minutes This cycle shall be performed at least 10 000 times and continued until 20 000 times unless a leak before break appears c The number of cycles to failure shall be reported along with the location and description of the failure initiation 2 3 6 1 2 Test interpretation Before reaching 10 000 cycles the container shall not fail or leak After completing 10 000 cycles the container may leak before break 15 R R67 19 LPG 4 1 3 2 1
393. ess 3 0MPa 3 7MPa 2 6 5 General test requirements a Container shall be filled with 80 per cent in volume of LPG commercial fuel and tested in the horizontal 1 position at working pressure 11 b Immediately following the ignition the fire shall produce flame impingement on the surface of the container along 1 65 m length of the fire source across the container i c Within 5 minutes of ignition at least one thermocouple shall indicate the temperature of fire just below the 3 1 v e container of at least 590 C 1 This temperature shall be maintained for the remaining duration of the test namely until when no overpressure m ux b is present in the container 2 LPG 4 2
394. h 3 4 The test period for leakage and hydrostatic strength tests shall be not less than 1 minute 3 5 All tests shall be performed at a room temperature of 20 5 C unless otherwise stated 5 External leakage test 5 1 A component shall be free from leakage through stem or body seals or other joints and shall not show evidence of porosity in casting when tested as described in paragraph 5 3 at any aerostatic pressure between 0 and the pressure shown in Table 3 The above prescriptions are deemed to be satisfied if the provisions of paragraph 5 4 are met 5 2 The test shall be performed at the following conditions a At room temperature b At the minimum operating temperature c At the maximum operating temperature The maximum and minimum operating temperatures are given in the annexes 5 3 During this test the equipment under test EUT will be connected to a source of aerostatic pressure of 1 5 times the maximum pressure and in the case of a Class 3 component 2 25 times the maximum classification pressure A positive shut off valve and a pressure gauge having a pressure range of not less than 1 5 times nor more than 2 times the test pressure are to be installed in the pressure supply piping The pressure gauge is to be installed between the positive shut off valve and the sample under test While under the applied test pressure the sample should be submerged in water to detect le
395. hutzgesetz B A u A Bundesanstalt f r Arbeitsschutz und Arbeitsmedizin BetrSichV Betriebssicherheitsverordnung BlmSchG Bundesimmissionsschutzgesetz B M W A Bundesministerium fur Wirtschaft und Arbeit E U European Union G P S G Geraet und Produktsicherheitgezetzes G S G Geratesicherheitsgesetz P ro d S G Produktsicherheitsgesetz P v U Pr fstellen von Unternehmen R B S Technische Regeln f r Betriebssicherheit Technischer Uberwachungsverein Zentralstelle der L nder f r Sicherheitstechnik Zugelassene berwachungsstelle L NN H H 3 2 1 German Basic Law BEU EU EU ECL Treatigs
396. ich have been produced successively to the first container within the same batch If the results of these tests are satisfactory the first test shall be ignored In the event where one or both of the retests fail to meet the requirements the batch shall be rejected ds 23 2 1 LPG 4 1 TE 0 568 kg L ETATS 1 3 pu o s c lt 80 2 7 Impact test 2 7 1 General At the choice of the manufacturer all the impact tests may be carried out on one container or each may be carried out on a different container 2 7 2 Test procedure For this test the fluid medium shall be water glycol mixture or another liquid having a low freezing point which does not change the properties of the conta
397. imal 96 hours Water or any other suitable hydraulic fluid may be used as a test medium 17 3 3 2 1 2 3 3 0MPa 96 1 120 20 65 4 5 2 6 2 7 2
398. iner material A container filled with the fluid medium to the weight that equals the filling with 80 per cent of LPG with a reference mass of 0 568 kg l 1s projected parallel to the length axle x axis in Figure 1 of the vehicle in which it is intended to be fitted at a velocity V of 50 km h against a solid wedge fixed horizontally perpendicular to 17 R R67 2 4 H 2 3 3 50 km 20 2 1 the movement of the container The wedge shall be installed so that the centre of gravity c g of the container hits the centre of the wedge The wedge shall have an angle a of 90 degrees and the point of impact shall be rounded with
399. inner surface in tension and the outer surface in tension 1 098 1 ad un 2 pa dy an 1 2 1 2 3 2 Cracks must not appear in the test piece when it is bent round a mandrel as long as the inside edges c x Hoo are separated by a distance not greater than the diameter of the mandrel 3a see Figure 1 in Appendix 3 of this annex RS ui 2 1 2 3 3 The ratio n between the diameter of the mandrel and the thickness of the test piece must not exceed 2 PORRE OBI HAS 5 the values given in di following table i mm Actual tensile strength Valnet T Rt in N mm2 is up to 440 inclusive 2 lb m above 440 to 520 inclusive 3 above 520 4 3 4 JIS Z 3121 2013 ISO 5178 2001 TSO 4136 2012 EN 876 1995
400. is to be available for indicating the prevailing atmospheric pressure Eo e m PN The reading of the barometer is to be added to the indicated air flow gauge pressure This absolute pressure is 3 3 15g c4ov CBE S quf ol similarly to be integrated in the flow calculation The air pressure to the flowmeter is to be controlled by a DEJO i suitable valve installed in the air supply piping ahead of the flowmeter The pressure relief valve under test is to 4 3 1 be connected to the discharge end of the flowmeter 80 10 1 3 8 After all preparations for flow capacity tests have been made the valve in the air supply line is to be opened slowly and the pressure to the valve under test is to be increased to the appropriate flow rating pressure During this interval the pressure at which the valve pops open is to be recorded as the popping pressure 10 1 3 9 The predetermined flow rating pressure is to be maintained constant for a brief interval until the readings of the instruments become stabilized Readings of the flow pressure gauge pressure differential manometer and the flowing air temperature indicator are to be recorded simultaneously The pressure is then
401. m py 8A GR HL EIE O BOR Ix A CR 1 2 8 1 l 15 LPG 4 9 62 LC 7 E 67
402. mponent is stored at temperature of 40 C and 90 95 per cent relative humidity for 168 hours This sequence shall be repeated 4 times After the test the component shall be cleaned and dried during 1 hour at 55 C The component shall now be conditioned to reference conditions during 4 hours before submitting it to further testing 12 2 A copper or brass LPG containing component shall comply with the leakage tests mentioned in 4 5 6 and 7 and after having been submitted to 24 hours immersion in Ammonia according to ISO 6957 with all connections closed 14 13 Resistance to dry heat The test has to be done in compliance with ISO 188 The test piece has to be exposed to air at a temperature R R67 3 3 3 2
403. ns Torispherical ends simultaneous limits 0 003 D Sb 0 08 D r 0 1D R ED H z0 I8D rec2b h z4b h 50 15 D not applicable for containers as shown in Appendix 2 to this annex Figure 2a Elliptical ends simultaneous limits 0 003 D Sb lt 0 08 D R R67 2 HZz0 18D hZ4b h 0 15D r R D H h b mm 1 5mm r mm R mm D mm H h mm b mm ps Ia tm D
404. ontainer is fitted with pressure relief devices at both sides or at more than one location along the length of the container the center of the fire source shall be centered midway between the pressure relief devices that are separated by the greatest horizontal distance 2 6 3 Fire source A uniform fire source of 1 65 m length shall provide direct flame impingement on the container surface across 1 7 4 12 R R67 rd its entire diameter o 2t e 5 b Any fuel may be used for the fire source provided that it supplies uniform heat sufficient to maintain the 8 165 cm Xm specified test temperatures until the container is vented The arrangement of the fire shall be recorded in sufficient detail to ensure that the rate of heat input to the container 1s reproducible Any failure or BH n M inconsistency of the fire source during a test shall invalidate the result AI E X Za HH j 3 e RUI gt JE DEM 2 165 cm ACTIO LIB UL B RES NEKEP 2 6 4 Temperature and pressure measurements
405. or the other modules 2 additionally 3 months in total 12 months thereof 2 months of practical training 3 additionally 3 months in total 12 months thereof 2 months of practical training 4 additionally 6 months in total 18 months thereof 4 months of practical training module 4 is available only after module 3 4 ZUS Module 4 Inspections Module 1 Module 2 Module 3 water tube Shell Boiler boiler External inspection 10 20 5 Strength inspection 30 8 5 Internal inspection 40 10 10 Inspection of breathing ca 100 P n apparatus Inspection prior to putting into service 20 10 2 Recurrent inspections 20 B ZUS a b c ZU p
406. orresponding type approval Sincerely yours signature Name of responsible person for homologation 3 2 6 2 7 ER LPG R67 2B 5 1958 2 E ECE 324 E ECE TRANS 505 Rev 2 2 UN
407. outlet tube is to be located within an inverted graduated cylinder which is calibrated in cubic centimetres The inverted cylinder is to be closed by a water seal The apparatus is to be adjusted so that a The end of the outlet tube is located approximately 13 mm above the water level within the inverted graduated cylinder and b The water within and exterior to the graduated cylinder is at the same level With these adjustments made the water level within the graduated cylinder is to be recorded With the valve in the closed position assumed as the result of normal operation air or nitrogen at the specified test pressure is to be applied to the valve inlet for a test period of not less than 2 minutes During this time the vertical position of the graduated cylinder is to be adjusted if necessary to maintain the same water level within and exterior to it At the end of the test period and with the water within and exterior to the graduated cylinder at the same level the level of water within the graduated cylinder is again recorded From the change of volume within the graduated cylinder the leakage rate is to be calculated according to the following formula where V1 leakage rate cubic centimetres of air or nitrogen per hour Vt increase in volume within graduated cylinder during test t time of test minutes P barometric pressure during test in kPa
408. p www aegpl eu lpg an exceptional AEGPL energy what is lpg used for move with lpg aspx 2 2 7bary 1 LPG AEGPL 2013 Alternative An LPG Industry Roadmap 2013 Edition EU 28 31 1 000 2 EU CNG LPG JL H Autogas in Europe qi
409. r fuelled with commercial propane at 80 per cent of its water capacity The test shall be held during at least 8 weeks until the steady state permeation of the structure is observed during at least 500 hours Then the rate of the container weight loss shall be measured The graph of mass change per number of days shall be recorded 2 3 6 4 2 Test interpretation The rate of mass loss shall be less than 0 15 g hour 2 3 6 4 3 Retesting Retesting 1s permitted for the permeation test A second test shall be performed on two containers which have been produced successively to the first container within the same batch If the results of these tests are satisfactory the first test shall be ignored In the event where one or both of the retests fail to meet the requirements the batch shall be rejected 2 3 6 5 LPG cycling test 2 3 6 5 1 Test procedure A container having successfully passed the permeation test shall be submitted to an ambient temperature 2 3 6 4 Permeation test 2 3 6 5 LPG cycling test 16 R R67 4 1 2 1 o 0 15 gh
410. re and temperature diagrams 1 Additional accessories modifications and extensions of the accessories fitted to the container 1s possible without retesting if notified to the Type Approval Authority which approved the container considered to be unlikely to have an appreciable adverse effect The Type Approval Authority may require a further test report from the Technical Service responsible The container and its configurations of accessories will be indicated in Appendix 1 to Annex 2B 13 R R67 15 OUR 3 1 LPG 1 ZR 100mm 6 2 2 dE AR 100mm 3
411. retests fail to meet the requirements the batch shall be rejected 27 LPG 1 2 7 200 1 1 3 4 2 10 2 3 1 10 3 4 1 2 1 2
412. s UN No 31 SB rd EC No 661 2009 25B X X X X X X X X X X NM UN No 37 EC No 661 2009 25C 2 M 2 TT x X X X X X UN No 98 uu 7 EC No 661 2009 25D UN No 99 x X X X XIX 1 SEIEN VLA NO LED T x Le e EC No 661 2009 25E UN No 112 x XI X X XIX pt VUA 9 EC No 661 2009 25F x X X X X X AFS UN No 123 26 76 162 EEC X X X X X X EC No 661 2009 26A x X X XIX X TW UN No 19 27 77 389 EEC X X X X xl X FEER EC No 661 2009 27A j X X X X XI X im EU
413. s de R67 8 10 1 6 29 E 3 1 2 10 EEs Ai ind SH HIE Puri R67 2 m EE Heep c i4
414. sicherheit Produktinformationen pdf Pruefstellen 02 pdf blob p ublicationFile amp v 10 4 1 2
415. temperature and at the classification pressure Each cycle shall consist of flow until stable outlet pressure has been obtained after which the gas flow shall be shut off by a downstream valve within 1 s until the downstream lock up pressure has stabilized Stabilized outlet pressures are defined as set pressure 15 per cent for at least 5 s b Cycle the inlet pressure of the regulator for 1 per cent of the total number of cycles at room temperature from 100 per cent to 50 per cent of the classification pressure The duration of each cycle shall be no less than 10 s c Repeat the cycling procedure listed in sub paragraph a at 120 C at the classification pressure for 1 per cent of the total number of cycles d Repeat the cycling procedure listed in sub paragraph b at 120 C at the classification pressure for 1 per cent of the total number of cycles e Repeat the cycling procedure listed in sub paragraph a at 20 C and 50 per cent of classification pressure for 1 per cent of the total number of cycles f Repeat the cycling procedure listed in sub paragraph b at 20 C and 50 per cent of classification pressure for 1 per cent of the total number of cycles g At the completion of all tests indicated in sub paragraphs a b c d e and f the regulator shall be leak proof as described under external leakage test under paragraph 5 at the temperatures of 20 C at the a number of cycles of opening and closing as
416. test The flowmeter shall be capable of indicating accurately for the test fluid employed the maximum leakage flow rates permitted 8 2 The seat of a shut off valve when in the closed position shall be free from leakage at any aerostatic pressure between 0 to 3 000 kPa or from 0 to WP in accordance with the classification pressure of the valve 8 3 A non return valve provided with a resilient seat when in the closed position shall not leak when subjected to any aerostatic pressure between 50 and 3 000 kPa 8 4 A non return valve provided with a metal to metal seat when in the closed position shall not leak at a rate exceeding 0 50 dm hour when subjected to an inlet pressure up to the test pressure according to Table 3 in paragraph 5 3 8 5 The seat of the upper non return valve used in the assembly of a filling unit when in the closed position shall be free from leakage at any aerostatic pressure between 50 and 3 000 kPa 8 6 The seat of a service coupling when in the closed position shall be free from leakage at any aerostatic pressure between 0 to 3 000 kPa 8 7 The gas tube pressure relief valve shall not have internal leakage up to 3 000 kPa or up to WP in accordance with the classification pressure of the valve 8 8 The pressure relief valve discharge valve shall not have internal leakage up to 2 600 kPa 2 3 9
417. the maximum pressure PS and the volume V exceeds 10 000 bar liter n a category if the maximum pressure PS is more than 1 000 bar and the product of PS and the volume V exceeds 10 000 barditer or b category II 5 Table5in 1 year a category Ill if the product of the maximum pressure PS and the volume V exce 1 000 bareliter or b category IV 5 Table6 in 5 years a category I if the pipeline is used for very toxic fiuids or b catogory li cr II If tho pipeline is used for very toxic fluids or other fluids if the product of the maximum pressure PS and the nominal size DN exceeds 2 000 bar 7 lable al category I it the product of the maximum pressure PS and the nominal size DN exceeds 2 000 bar or b ca li oc Hil 8 Table 8 in category I II or III 9 Table 9 in category I or II 3 2 4 BetrSichV TRBS TRBS 3 2 5 BetrSichV ZUS competent person
418. x X X x xIx x T EC No 661 2009 Se hl EU No 19 2011 19 76 115 EEC X X X X X X 6 EC No 661 2009 19A Isofix M X X X X XIX Isofix DR 20 23 a 76 156 EEC X X X X X X X X X X EC No 661 2009 2 AS es X X X X X X X X X X UN No 48 21 76 757 EEC XI X X X X X X X X X dix EC No 661 2009 MI AM SI al UN No 3 22 76 758 EEC x X X x X X X X X X EC No 661 2009 22A OAM ONE X X X X X X X X X X UN No 7

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