Section 7 Pumping and piping
Clasification Society 2024 - Version 9.40
Clasifications Register Rules and Regulations - Rules and Regulations for the Classification of Naval Ships, January 2023 - Volume 2 Machinery and Engineering Systems - Part 12 Emissions Abatement Plant - Chapter 1 Emissions Abatement Plant for Combustion Machinery - Section 7 Pumping and piping

Section 7 Pumping and piping

7.1 General

7.1.1 Pipe work and transfer systems which may carry chemical substances are to meet the requirements of Vol 2, Pt 7, Ch 1 Piping Design Requirements, Vol 2, Pt 7, Ch 2 Ship Piping Systems and Vol 2, Pt 7, Ch 3 Machinery Piping Systems, as applicable. Lining steel pipe systems with corrosion-resistant materials is subject to special approval. The elasticity of the lining is not to be less than that of the supporting boundary material.

7.1.2 Pipe systems carrying sea-water or fresh water are to meet the requirements of Vol 2, Pt 7, Ch 1 Piping Design Requirements, Vol 2, Pt 7, Ch 2 Ship Piping Systems and Vol 2, Pt 7, Ch 3 Machinery Piping Systems. Where there is a risk of fresh-water or sea-water systems becoming contaminated with process chemicals, substances or effluent, pipe systems are to comply with Vol 2, Pt 12, Ch 1, 7.1 General 7.1.1.

7.1.3 Chemical transfer and control arrangements are to be provided with one stop-valve capable of being manually operated on each tank filling and discharge line, located near the tank penetration, plus one stop valve at each chemical-hose loading connection. The stop valve for the chemical tank discharge line is additionally to the quick closing type and is to meet the requirements of Vol 2, Pt 12, Ch 1, 9.1 General 9.1.6.

7.1.4 Bilge and effluent pumping and piping systems in the emissions abatement plant spaces are to be constructed of materials suitable for any chemicals or substances used by the emissions abatement plant, any effluent that is produced or any combination of substances on board which might result from accidental admixture.

7.1.5 Arrangements are to be provided for the control of the bilge and effluent pumping and piping system. They are to be installed in the emissions abatement plant spaces from within these spaces and also from a position outside the spaces.

7.1.6 Bilge and effluent pumping and piping systems for hazardous materials should, wherever possible, be installed in the space associated with the particular hazard.

7.1.7 Where chemicals or wash water are injected into exhaust piping then the exhaust piping is to be suitable for such chemicals and wash water, see Vol 2, Pt 12, Ch 1, 3.3 Chemical substances 3.3.1.

7.1.8 Where filters are used, they are to be capable of being removed for cleaning and replaced safely without interrupting emissions abatement plant or combustion machinery operations.

7.1.9 Where scrubbers are used, the following apply:

  1. Closed loop wet scrubbers are to have natural gravity fall drainage from the wet sump of the scrubber to the process tank or circulating pump suction, with the drain line dimensioned to accommodate 125 per cent of the maximum pumping capacity of the installed water pump(s). No valves are to be fitted to the drain line from the scrubber sump to the process tank unless it can be demonstrated that suitable precautions are in place to prevent the possibility of the scrubber filling with water and reverse-flowing into the combustion machinery exhaust duct. Where a valve is fitted to this line, the system is to be protected as for the overboard discharge valve of an open loop system, in accordance with Table 1.9.1 Machinery emissions to air abatement plant: alarms and safeguards.

  2. For open loop wet scrubbers, the overboard discharge valve and any other sea-water valves downstream of the scrubber are to be protected in accordance with Table 1.9.1 Machinery emissions to air abatement plant: alarms and safeguards. The sea suction valve(s) are also to have position indicators which are to give remote indication of valve position. The scrubber is to be mounted above the waterline under all normal ship operating conditions to prevent sea-water ingress into the scrubber.

  3. For wet scrubbing systems (open loop and closed loop), an overflow line is to be fitted to prevent the risk of reverse flow of water to combustion machinery. This overflow is to be dimensioned to accommodate 125 per cent of maximum capacity of installed water pumps and is to have no impairment to flow. This overflow line is to be directed to the process tank in closed loop or hybrid installations. On open loop installations, it is to be directed overboard. The overboard discharge is to have an effective means of preventing reverse flow of seawater. Alternative arrangements to prevent the risk of reverse flow are subject to special consideration.

  4. Overboard discharge connections from scrubbers are to be positioned below the lowest operating waterline and are to be internally protected from effluent-induced corrosion.

7.1.10 Where applicable, tanks are to be maintained within the temperature limits of the chemicals and substances they contain so as to avoid risks of boiling, stress corrosion, freezing and other temperature-sensitive processes.


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