IMO I104E-1993 IGC Code International Code for the Construction and Equipment of Ships Carrying Liquefied Gases in Bulk (Includes Supplement).pdf
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1、 International Code for the Construction and Equipment of Ships Carrying Liquefied Gases in Bulk (IGC Code) 1993 Edition Supplement The following umendments were adopted by resolution MSC.32(63) on 23 Muy 1994 und entered into force on 1 July 1998: Amendments related to application 1 Existing paragr
2、aphs 1.1.2 and 1.1.3 are replaced by the following: Unless expressly provided otherwise, the Code applies to ships the keels of which are laid or which are at a stage at which: construction identifiable with the ship begins; and assembly of that ship has commenced cornpricing at least 50 tonnes or 1
3、% of the estimated mass of all structural material, whichever is the less; on or after 1 July 1998. Ships constructed before 1 July 1998 are to comply with resolution MSC.5(48) adopted on 17 June 1983 subject to amendments by resolution MSC.30(61) adopted on 11 December 1992. 1.1.3 A ship, irrespect
4、ive of the date of construction, which is converted to a gas carrier on or after 1 July 1998 should be treated as a gas carrier constructed on the date on which such conversion commences.? ?1.1.2 .1 .2 Printed in the United Kingdom by IMO Copyright 0 IMO 2003 (IA104E) Amendments related to filling l
5、imits 2 Existing chapter 15 is replaced by the following: “Chapter 15 Filling limits for carg 15.1 General 15.1.1 No cargo tanks should have a 98% at the reference temperature, 15.1.3. tanks iigher filling limit (Fi) than except as permitted by 15.1.2 The maximum loading limit (LL) to which a cargo
6、tank may be loaded should be determined by the following formula: LL = FLE where: Li = loading limit expressed in percent, which means the maximum allowable liquid volume relative to the tank volume to which the tank may be loaded; FL = filling limit as specified in 15.1 .I or 15.1.3; PR = relative
7、density of cargo at the reference tempera- ture; and pL = relative density of cargo at the loading temperature and pressure. 15.1.3 The Administration may allow a higher filling limit (FL) than the limit of 98% specified in 15.1 .I at the reference tempe- rature, taking into account the shape of the
8、 tank, arrangements of pressure relief valves, accuracy of level and temperature gauging and the difference between the loading temperature and the temperature corresponding to the vapour pressure of the cargo at the set pressure of the pressure relief valves, provided the conditions specified in 8.
9、2.1 7 are maintained. 15.1.4 For the purposes of this chapter only, reference temperature means: the temperature corresponding to the vapour pressure of the cargo at the set pressure of the pressure relief valves when no cargo vapour pressure/temperature control as referred to in chapter 7 is provid
10、ed; the temperature of the cargo upon termination of loading, during transport, or at unloading, whichever is the greatest, when a cargo vapour pressure/tempera- ture control as referred to in chapter 7 is provided. If .I .2 2 this reference temperature would result in the cargo tank becoming liquid
11、-full before the cargo reaches a temperature corresponding to the vapour pressure of the cargo at the set pressure of the relief valves required in 8.2, an additional pressure-relieving system complying with 8.3 should be fitted. 15.1.5 The Administration may allow type C tanks to be loaded accordin
12、g to the following formula provided that the tank vent system has been approved in accordance with 8.2.1 8: LL = FL PL where: iL = loading limit as specified in 15.1.2; FL = filling limit as specified in 15.1.1 or 15.1.3; PR = relative density of cargo at the highest temperature which the cargo may
13、reach upon termination of loading, during transport, or at unloading, under the ambient design temperature conditions described in 7.1.2; and p = as specified in 15.1.2. This paragraph does not apply to products requiring a type 1G ship. 15.2 The maximum allowable loading limits for each cargo tank
14、should be indicated for each product which may be carried, for each loading temperature which may be applied and for the applicable maximum reference temperature, on a list to be approved by the Administration. Pressures at which the pressure relief valves, including those valves required by 8.3, ha
15、ve been set should also be stated on the list. A copy of the list should be permanently kept on board by the master. 15.3 Chapter 15 applies to all ships regardless of the date of construction.” Information to be provided to the master 3 The following words are added at the end of existing paragraph
16、 8.2.17: “at the maximum allowable filling limit (Fi)”. 4 The following new paragraph 8.2.18 is added after existing paragraph 8.2.17: “8.2.18 The adequacy of the vent system fitted on tanks loaded in accordance with 15.1.5 is to be demonstrated using the 3 guidelines developed by the Organization.*
17、 A relevant certifi- cate should be permanently kept on board the ship. For the purposes of this paragraph, vent system means: the tank outlet and the piping to the pressure relief valve; the piping from the pressure relief valve to the location of discharge to the atmosphere and including any inter
18、connections and piping which joins other tanks. This paragraph may apply to all ships regardless of the date of construction.” * Refer to the guidelines to be developed by the Organization. .I .2 the pressure relief valve; .3 Amendments related to cargo tank vent systems Existing paragraph 8.2.3 is
19、replaced by the following: In general, the setting of the pressure relief valves should not be higher than the vapour pressure which has been used in the design of the tank. However, where two or more pressure relief valves are fitted, valves comprising not more than 50% of the total relieving capac
20、ity may be set at a pressure up to 5% above MAWS.” The following sentences are added to existing paragraph 8.2.4: “Valves should be constructed of materials with a melting point above 925C. Consideration of lower melting point materials for internal parts and seals should be given if their use provi
21、des significant improvement to the general operation of the valve.” Existing paragraph 8.2.9 is replaced by the following: Each pressure relief valve installed on a cargo tank should be connected to a venting system which should be so constructed that the discharge of gas will be unimpeded and direc
22、ted vertically upwards at the exit and so arranged as to minimize the possibility of water or snow entering the vent system. The height of vent exits should not be less than B/3 or 6 m, whichever is the greater, above the weather deck and 6 m above the working area, the fore-and-aft gangway, deck st
23、orage tanks and cargo liquid lines.” The following sentences are added to existing paragraph 8.2.16: “The pressure drop in the vent line from the tank to the pressure relief valve inlet should not exceed 3% of the valve set pressure. For unbalanced pressure relief valves the back pressure in the dis
24、charge line should not exceed 10% of the gauge pressure at the relief valve inlet with the vent lines under fire exposure as referred to in 8.5.2.” “8.2.3 “8.2.9 4 The following amendments were adopted by resolution MSC.59(67) on 5 December 1996 and entered into force on 1 July 1998: Chapter I - Gen
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