Материал: Gas SIR CDI 9th edition

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Section 5.

 

CARGO OPERATIONS

 

 

 

 

 

Gas

 

 

 

 

 

 

 

5.1

Ref.

Cargo Transfer Operations

Yes

No

N/A

Cat

Gp

5.1.40IGC (16) 3.6. EGC 3.6.3

5.1.41IGC (16) / EGC 13.3 13.1.3

5.1.42IGC (16) 13.3 / EGC

5.1.43

5.1.44IGC (16) 13.4 / EGC 13.1.

13.1.4

There are records to indicate the regular testing of air lock

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alarms and interlocks

 

 

There are records to indicate the regular testing of high level

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alarms

 

 

There are records to indicate the testing/function of

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independent high level shutdown system

 

 

There are records indicating that the cargo tank filling valves

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are tested at intervals not exceeding one week

 

 

There are records indicating the regular testing of high and low

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pressure alarms

 

 

5.1.45

5.1.46

5.1.46

5.1.47

5.1.47IGC 13.1.4 IGC (16)13.1. EGC

There are records indicating the inspection / checking of inert

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gas system non-return valves

 

 

Procedures are in place to fully segregate the inert gas piping

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from hold spaces when the system is connected to the cargo

 

 

system.

 

 

Segregation is through the use of a spectacle flange or

 

 

removal of spool pieces.

 

 

There are records indicating that calibration checks have been

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carried out on cargo plant instrumentation

 

 

There are procedures requiring records of calibration checks

 

 

on the following:-

 

 

5.1.48IGC13.1.4 IGC (16) 13.1 13.1.2 EGC

5.1.49

5.1.49IGC 5.6.4 IGC (16) 18 EGC

5.3.3

5.1.50

5.1.50IGC (16) 13.4 / EGC 13.1.4

5.1.51SOLAS IX ISM 10.1

5.1.52SOLAS IX ISM 10.1

5.1.53

5.1.53IGC 9.1.2 IGC (16) 18.9

- Level indicators

Coppola

 

- overflow control

 

- pressure gauges

 

- temperature indicating devices - gas detecting equipment

ESD fusible elements are in satisfactory condition

Cargo plant instrumentationMassimilianoappears in good operating condition

ESD fusible elements should be free from paint

All high and low pressure alarms appear to be in a good

Hold space seals and rubber skirting for Cargo tank domes, if fitted, appear in good order

operational condition

by

 

May not be fitted to an “existing ship”. In this case question to

be marked N/A.

 

Tank dome fittings appear in good order

Purchased

 

When not in use, sample points are closed and capped

Quick coupling connections should not be used. Caps must be screwed/threaded and tightened properly when sample points are not in use.

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Gas

SIR Page 66

Rev. CDI 8/19

(C) 2019 Chemical Distribution Institute

Section 5.

 

CARGO OPERATIONS

 

 

 

 

 

Gas

 

 

 

 

 

 

 

5.1

Ref.

Cargo Transfer Operations

Yes

No

N/A

Cat

Gp

5.1.54

 

Means for the connection of sampling equipment, liquid or

 

 

 

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vapour, appears to be satisfactory

 

 

 

 

 

5.1.54

SIGTTO

Pipework to be of robust construction to withstand up to 3.5 kg

 

 

 

 

 

 

LPG

weight of a sample cylinder.

 

 

 

 

 

 

Sampling

 

 

 

 

 

 

Proc.

IACS 114

5.1.55

5.1.55

5.1.56

5.1.57SOLAS IX ISM 10.1

5.1.58SOLAS IX ISM 10.1

5.1.59

5.1.60IGC 5.2.1.3 IGC (16) 5 EGC 5.2.2

5.1.61

5.1.62IGC 5.2.1.2 IGC (16) 5, EGC 5.2.1b

5.1.63

5.1.63IGC 5.2.1.2 IGC (16) 5.8.4 EGC 5.2.1b TSG (G) 5.3.9

The sampling connection should be isolated by two needle valves or one needle valve and one ball valve (not 2 ball valves) fitted at least 500 mm apart.

There should be a clearance of at least 250mm around the stub piece connection to allow spanner access.

For threaded sampling couplings, a positive means to prevent the coupling from rotating should be provided and regular inspections of the tightness of the connection should be performed and recorded. This is to prevent the fittings and/or valve from being unscrewed by the normal action of making and breaking connections.

The connection should be clearly labelled as to its point of origin, i.e. tank number and location, top, middle or bottom.

The use of a drain valve as a sample point is not acceptable.

system should be obtained by connectingCoppolathe container outlet valve to a vapour sample connection point or vent system.

Sampling can be achieved by a closed loop system, keeping the length of sampling line as short as practically possible

In connection with toxic and flammable cargoes, a closed loop

Local pump controls are accessibleMassimiliano

When possible, sampling through the use of the cargo pump

can allow return of cargo back to the vapour space of the cargo tank, minimizing release to the atmosphere.

Local pump controls appear in good condition

Electrical equipment, glandsby and seals appear well maintained

Suitable weatherPurchasedprotection is provided for electrical fittings on

deck

Cargo pipework is isolated from ordinary steel to prevent brittle fracture, where appropriate

Cargo pipework insulation is intact

Cargo and vapour pipelines are free to move inside supporting collars

Expansion bellows are only fitted on cargo vapour lines, are correctly supported and aligned with the pipes they are connected to

Only Industry Standard expansion bellows are accepted, and they may only be used on cargo vent lines .

5.1.64

 

Condition of expansion devices appears satisfactory

5.1.64

SOLAS IX

There should be no evidence of damage or distortion.

 

ISM 10.1

 

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Gas

SIR Page 67

Rev. CDI 8/19

(C) 2019 Chemical Distribution Institute

Section 5.

 

CARGO OPERATIONS

 

 

 

 

 

Gas

 

 

 

 

 

 

 

5.1

Ref.

Cargo Transfer Operations

Yes

No

N/A

Cat

Gp

5.1.65SOLAS IX ISM 10.1 TSG (G)

3.7.1

5.1.66

5.1.66SOLAS IX ISM 10.1

5.1.67

5.1.68SOLAS IX ISM 10.1

5.1.69IGC 5.4.2.3., IGC (16) 5.8.2.3

Cargo pipe work electrical bonding arrangements appears in

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good condition

 

 

Cargo pipe work is free of leaks and does not appear to be

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corroded

 

 

If NO then quantify and specify accordingly

 

 

Cargo pipework does not have temporary repairs

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All other aspects of cargo pipework, including proper service

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marking and piping supports, appear in good condition

 

 

Screwed couplings are only used for accessory lines and

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instrumentation lines with external diameters of 25 mm or less

 

 

5.1.70

Screwed fittings for accessory or sampling lines are locked or

 

additionally secured to prevent inadvertent unscrewing.

5.1.70IACS 114

5.1.71

5.1.71IGC / EGC 7.2.2.

5.1.72

5.1.73

SSSCL

A

 

14

 

5.1.74IGC (16) 13.4 / EGC 13.4.3

5.1.75SOLAS IX ISM 10.1

5.1.76SOLAS IX ISM 10.1

5.1.77

5.1.77SIGTTO Manifold Recommendati ons

5.1.78

5.1.78

For threaded fittings, a positive means to prevent the coupling from rotating should be provided and regular inspections of the tightness of the connection should be performed and recorded. This is to prevent the fittings and/or valve from being unscrewed by the normal action of making and breaking connections.

When applicable, segregation between grades is achievable without risk of liquid or vapour contamination

If the ship is only certified to carry one grade at a time this question to be marked “N/A”.

Manifold reducers are correctly rated for pressures achievable

during loading and discharging

Coppola

 

Manifolds not in use have fully bolted blanks fitted

A local pressure gauge is fitted outboard of manifold valves

Manifold pressure gauge(s) appears to be in a good operating condition

There is no indication of pressure build-up or cargo leakage in

unused manifold connections.Massimiliano

Liquid spill containment arrangements at the manifold are

 

 

by

adequate and suitable for the temperature of cargoes the ship

may carry

 

 

If portable containment is in use it must be appropriately

 

Purchased

 

secured. For low-temperature liquids, the sheathing should extend longitudinally for a distance of at least 1.5 metres beyond the outermost edge of the outermost manifold flange. The sheathing should also extend to at least 0.5 metres inboard of the innermost manifold valve, transversely from the ship's side. In addition, in the case of other transfer line layouts, the sheathing should extend over any other areas that may be subject to spillage.

The company has written procedures for safe connection/disconnection, draining and purging of cargo loading/discharging arms

These procedures may include:

-Safety precautions during cargo operations.

-General arrangement of manifold pipeline area.

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Gas

SIR Page 68

Rev. CDI 8/19

(C) 2019 Chemical Distribution Institute

Section 5.

 

CARGO OPERATIONS

 

 

 

 

 

Gas

 

 

 

 

 

 

 

5.1

Ref.

Cargo Transfer Operations

Yes

No

N/A

Cat

Gp

-Checking integrity of draining and purging pipeline, and valve arrangements (ensuring that draining/purging is never carried out with a single valve acting as a separation).

-Description of atmosphere testing equipment.

-Supply of purging medium from shore or vessel plant.

-Monitoring of operation and effective communication with terminal.

5.1.79

 

 

 

 

A leak test of the cargo arm/hose connection to the manifold is

 

 

conducted prior to commencing the cargo transfer.

5.1.79

 

The completion of the test should be recorded onboard the

 

 

vessel.

5.1.80

SSSI LPG

Safe access is provided for connecting and disconnecting

 

 

arms / hoses

5.1.81

SSSI LPG

The manifold area is clear of any obstructions which may

 

 

interfere with the safe automatic release of a hard arm

5.1.82

 

A temperature sensor is fitted at or near the manifold to

 

 

monitor the cargo temperature during cargo transfer

5.1.83

 

If yes, the minimum permitted cargo temperature is displayed

 

 

at or near the control position and at the manifold

5.1.84

5.1.85SOLAS IX ISM 10.1

5.1.86

5.1.86IGC (16) 3 / EGC 3.3.3

5.1.87

5.1.87IGC 12.1 IGC (16) 8

TSG (G) 6.4.4

 

Coppola

A cargo compressor room/ space is fitted

If Yes:

 

Bulkhead seals appear in good condition

The arrangements of the cargo compressor room/ space

 

Massimiliano

are in compliance with the requirements.

The requirements include:-

- Arrangement allows safe unrestricted access for personnel wearing protective clothing and breathing apparatus, and in the event of an injury, to allow unconscious personnel to be removed.

- All valves necessaryby for cargo handling should be

readily accessable to personnel wearing protective clothing.Purchased

- Suitable arrangements should be made to deal with drainage of compressor rooms

The ventilation system appears to be operating correctly

Should be operating in extraction mode in the Compressor room and the Motor room should be under positive pressure.

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Gas

SIR Page 69

Rev. CDI 8/19

(C) 2019 Chemical Distribution Institute

Section 5.

 

CARGO OPERATIONS

 

 

 

 

 

Gas

 

 

 

 

 

 

 

5.1

Ref.

Cargo Transfer Operations

Yes

No

N/A

Cat

Gp

5.1.88

5.1.88SOLAS IX ISM 10.1

5.1.89SOLAS IX ISM 10.1

5.1.90TSG (G) 1.4.1

5.1.91

5.1.91IGC (16) 17.8

All protective devices appear operational

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This refers to high/low oil pressures in compressors, high gas

 

 

pressure in the compressor, no-flow etc..

 

 

Compressors and associated equipment in the cargo system

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appear fully operational

 

 

Procedures are available detailing when freezing point

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depressants may be used when a means of hydrate control is

 

 

provided

 

 

When applicable, a Certificate of Protection (Inhibitor

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Certificate) is available

 

 

A Certificate must be provided to the vessel prior to departure.

 

 

Care shall be taken to ensure that the cargo is sufficiently inhibited to prevent self-reaction (e.g. polymerization or dimerization) at all times during the voyage. Ships shall be provided with a certificate from the manufacturer stating:

.1 name and amount of inhibitor added;

.2 date inhibitor was added and the normally expected duration of its effectiveness;

.3 any temperature limitations affecting the inhibitor; and

.4 the action to be taken should the length of the voyage exceed the effective lifetime of the inhibitors.

 

 

Coppola

 

by

Massimiliano

Purchased

 

 

 

Copy of Massimiliano Coppola

Gas

SIR Page 70

Rev. CDI 8/19

(C) 2019 Chemical Distribution Institute