Part 1 - Test and Performance Specifications for Type Approval of 15 ppm Bilge Separators
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Statutory Documents - IMO Publications and Documents - Resolutions - Marine Environment Protection Committee - Resolution MEPC.107(49) - Revised Guidelines and Specifications for Pollution Prevention Equipment for Machinery Space Bilges of Ships - (adopted on 18 July 2003) - Annex - Revised Guidelines and Specifications for Pollution Prevention Equipment for Machinery Space Bilges of Ships - Annex - Part 1 - Test and Performance Specifications for Type Approval of 15 ppm Bilge Separators

Part 1 - Test and Performance Specifications for Type Approval of 15 ppm Bilge Separators

1.1 General

  1.1.1 These Test and Performance Specifications for Type Approval relate to 15 ppm Bilge Separators. In addition, the electrical and electronic systems of the 15 ppm Bilge Separator should be tested in accordance with the Specifications for Environmental Testing contained in part 3 of this annex.

  1.1.2 The 15 ppm Bilge Separator being tested should comply with the relevant requirements of the technical specifications contained in section 4.1 of these Guidelines and Specifications.

1.2 Test Specifications

  1.2.1 These Specifications relate to 15 ppm Bilge Separators. 15 ppm Bilge Separators should be capable of producing an effluent for discharge to the sea containing not more than 15 ppm of oil irrespective of the oil content of the feed supplied to it.

  1.2.2 The influent, whether emulsified or non-emulsified, which the system has in practice to deal with, depends on:

  • .1 the position of the oil/water interface, with respect to the suction point, in the space being pumped;

  • .2 the type of pump used;

  • .3 the type and degree of closure of any control valve in the circuit; and

  • .4 the general size and configuration of the system.

 Therefore the test rig must be so constructed as to include not only the 15 ppm Bilge Separator, but also the pumps, valves, pipes and fittings as shown in figure 2. It is to be so designed for testing 15 ppm Bilge Separators with and without an integral supply pump.

  • For the testing of 15 ppm Bilge Separators having no integral pump, the centrifugal pump "A" (figure 2) is used to feed the 15 ppm Bilge Separator with valves 4 and 6 open, and valve 5 closed. The rate of flow from the centrifugal pump "A" is matched to the design throughput of the 15 ppm Bilge Separator by the adjustment of the centrifugal pump's discharge valve.
  • Where the 15 ppm Bilge Separator is fitted with an integral pump, the centrifugal pump "A" is not required.
  • A centrifugal pump "B" should be fitted to re-circulate the Test Fluid C in the tank to ensure that the Test Fluid C is maintained in a stable condition throughout the testing. Re-circulation is not required for Test Fluids A and B.
  • To ensure a good mix of the Test Fluid and the water, a conditioning pipe as specified in paragraph 1.2.5 of part 1 of this annex shall be fitted immediately before the 15 ppm Bilge Separator.
  • Other valves, flow meters and sample points should be fitted to the test rig as shown in figure 2.
  • The pipe work should be designed for a maximum liquid velocity of 3 metres/second.

Test Rig

  1.2.3 The tests should be carried out with a supply rate equal to the full throughput for which the 15 ppm Bilge Separator is designed.

  1.2.4 Tests should be performed using three grades of test fluids

  • .1 Test Fluid "A" which is a marine residual fuel oil in accordance with ISO 8217, type RMG 35 (density at 15°C not less than 980 kg/m3)

  • .2 Test Fluid "B" which is a marine distillate fuel oil in accordance with ISO 8217, type DMA (density at 15°C not less than 830 kg/m3).

  • .3 Test Fluid "C" which is a mixture of an oil-in-fresh water emulsion, in the ratio whereby 1 kg of the mixture consists of

    • 947.8 g of fresh water;

    • 25.0 g of Test Fluid "A"

    • 25.0 g of Test Fluid "B";

    • 0.5 g surfactant (sodium salt of dodecylbenzene sulfonic acid) in the dry form;

    • 1.7 g "iron oxides" (The term "iron oxide" is used to describe black ferrosoferric oxide (Fe3 O4) with a particle size distribution of which 90% is less than 10 microns, the remainder having a maximum particle size of 100 microns);

    Note Procedure for preparing Test Fluid C: (see example calculation)footnote

    • Preparation

      • (1) measure out 1.2 times the quantity of surfactant required for the "Test with Test Fluid C" as described in 1.2.11; and

      • (2) mix it with fresh water and stir well in a small container (e.g., a beaker or bucket) to make a mixture ("Mixture D") until the surfactant has been thoroughly dissolved.

    • To make Test Fluid C in the test fluid tank (figure 3),

      • (3) Fill test fluid tank with fresh water with a quantity 1.2 times the volume of the total quantity of water in the test fluid "C" needed for the test described in 1.2.11.

      • (4) Operate centrifugal pump B running at a speed of not less than 3,000 rpm (nominal) with a flow rate at which the volume of the test fluid has been changed out at least once per minute.

      • (5) Add "Mixture D" first, followed by oil and suspended solids (iron oxides) respectively, both 1.2 times of the required amounts, to the fresh water in the tank,

      • (6) To establish a stable emulsion keep running the centrifugal pump B for one hour and confirm no oil floats on the surface of the test fluid.

      • (7) After the one hour stated in paragraph (6) above keep running the centrifugal pump B at reduced speed to approximately 10% of original flow rate, until the end of the test.

    Note 1. The tank should be of a cylindrical shape. The level of the water should be:

    • 2D ≥ H ≥ 0.5D, when preparing Test Fluid "C".

    Note 2. Outlet going to centrifugal pump B should be placed at as low a position to the tank as possible.

    Note 3. Inlet to the tank should be fitted at the center of tank bottom so that the mixture flows upward to obtain uniform and stable emulsion.

Tank of Test Fluid "C"

 If the 15 ppm Bilge Separator is fitted with heating facilities to allow the separated oil retained in it to be discharged when the automatic discharge valve is activated, the Certificate of Type Approval should be endorsed under the heading "Limiting Conditions Imposed" with the following statement:

"The 15 ppm separator is fitted with heating facility."

  1.2.5 If the 15 ppm Bilge Separator includes an integrated feed pump, this 15 ppm Bilge Separator should be tested with that pump supplying the required quantity of Test Fluid and water to the 15 ppm Bilge Separator at its rated capacity.

 If the 15 ppm Bilge Separator is to be fed by the ship's bilge pumps, then the unit will be tested by supplying the required quantity of Test Fluid and water mixture to the inlet of a centrifugal pump operating at not less that 1,000 rpm (see dotted line in figure 2). This pump should have a delivery capacity of not less than 1.1 times the rated capacity of the 15 ppm Bilge Separator at the delivery pressure required for the test. The variation in Test Fluid/water ratio will be obtained by adjusting valves on the Test Fluid and water suction pipes adjacent to the pump suction, and the flow rate of Test Fluid and water or the Test Fluid content of the supply to the 15 ppm Bilge Separator should be monitored. If a centrifugal pump is used, the excess pump capacity should be controlled by a throttle valve on the discharge side of the pump.

 In all cases, to ensure uniform conditions, the piping arrangements immediately prior to the 15 ppm Bilge Separator should be such that the influent to the 15 ppm Bilge Separator should have a Reynolds Number of not less than 10,000 as calculated in fresh water, a liquid velocity of not less than 1 metre per second and the length of the supply pipe from the point of Test Fluid injection to the 15 ppm Bilge Separator should have a length not less than 20 times its diameter. A mixture inlet sampling point and a thermometer pocket should be provided near the 15 ppm Bilge Separator inlet and an outlet sampling point and observation window should be provided on the discharge pipe.

  1.2.6 In order to approach isokinetic sampling - i.e. the sample enters the sampling pipe at stream velocity the sampling arrangement should be as shown in figure 4 and, if a cock is fitted, free flow should be effected for at least one minute before any sample is taken. The sampling points should be in pipes running vertically.

Diagram of sampling arrangements

  1.2.7 In the case of the 15 ppm Bilge Separator depending essentially on gravity, the feed to the system of the test water and Test Fluid mixture should be maintained at a temperature not greater than 40°C, and heating and cooling coils should be provided where necessary. The water shall have a density of not more than 1,015 at 20°C. In other forms of separation where the dependence of separation efficiency on temperature is not established, tests should be carried out over a range of influent temperatures representing the normal shipboard operating range of 10°C to 40°C or should be taken at a temperature in this range where the separation efficiency is known to be worst.

  1.2.8 In those cases where, for the 15 ppm Bilge Separator, it is necessary to heat water up to a given temperature and to supply heat to maintain that temperature, the tests should be carried out at the given temperature.

  1.2.9 The tests with Test Fluid "A" should be carried out as follows:

  • .1 To ensure that the 15 ppm Bilge Separator commences the test with the oil section full of Test Fluid and with the supply line impregnated with Test Fluid, the 15 ppm Bilge Separator should, after filling with water (density at 20°C not more than 1,015) and while in the operating condition, be fed with pure Test Fluid for not less than 5 min.

  • .2 The 15 ppm Bilge Separator should be fed with a mixture composed of between 5,000 and 10,000 ppm of Test Fluid in water until steady conditions have been established. Steady conditions are assumed to be the conditions established after pumping through the 15 ppm Bilge Separator a quantity of Test Fluid/water mixture not less than twice the volume of the 15 ppm Bilge Separator. The test should then proceed for 30 min. Samples should be taken at the effluent outlet at 10 min and 20 min from the start of this period. At the end of this test, an air cock should be opened on the suction side of the pump and, if necessary, the oil and water valves should be slowly closed together, and a sample taken at the effluent discharge as the flow ceases (this point can be checked from the observation window).

  • .3 A test identical to that described in 1.2.9.2, including the opening of the air cock, should be carried out with a mixture composed of approximately 25%footnote Test Fluid and 75%footnote water.

  • .4 The 15 ppm Bilge Separator should be fed with 100%footnote of Test Fluid for at least 5 min during which time the observation window should be checked for any oil discharge. Sufficient Test Fluid should be fed into the 15 ppm Bilge Separator to operate the automatic oil discharge valve. After the operation of the oil discharge valve, the test should be continued for 5 min using a 100%footnote Test Fluid supply in order to check the sufficiency of the oil discharge system.

  • .5 The 15 ppm Bilge Separator should be fed with water (density at 20°C not more than 1,015) for 15 min. Samples of the separated water effluent are taken at the beginning of the test and after the first 10 min.

  • .6 A test lasting a minimum of 2 h should be carried out to check that the 15 ppm Bilge Separator will operate continuously and automatically. This trial should use a cycle varying progressively from water to oily mixture with approximately 25%.footnote Test Fluid content and back to water every 15 minutes, and should test adequately any automatic device which is fitted. The whole test sequence should be performed as a continuous programme. At the end of the test, while the 15 ppm Bilge Separator is being fed with 25%footnote Test Fluid, a water effluent sample should be taken for analysis.

  1.2.10 The tests with Test Fluid "B" should be carried out as follows:

  • .1 The 15 ppm Bilge Separator should be fed with a mixture composed of between 5,000 and 10,000 ppm of Test Fluid in water until steady conditions have been established. Steady conditions are assumed to be the conditions established after pumping through the 15 ppm Bilge Separator a quantity of Test Fluid/water mixture not less than twice the volume of the 15 ppm Bilge Separator. The test should then proceed for 30 min. Samples should be taken at the effluent outlet at 10 min and 20 min from the start of this period. At the end of this test, an air cock should be opened on the suction side of the pump and, if necessary, the oil and water valves should be slowly closed together, and a sample taken at the effluent discharge as the flow ceases (this point can be checked from the observation window).

  • .2 A test identical to that described in 1.2.10.1, including the opening of the air cock, should be carried out with a mixture composed of approximately 25%.footnote Test Fluid and 75%footnote water.

  1.2.11 The tests with Test Fluid "C" should be carried out as follows:

  • .1 The 15 ppm Bilge Separator should be fed with a mixture composed of 6% Test Fluid "C" and 94% water to have emulsified oil content of 3,000 ppm in the test water until steady conditions have been established. Steady conditions are assumed to be the conditions established after pumping through the 15 ppm Bilge Separator a quantity of Test Fluid "C"/water mixture not less than twice the volume of the 15 ppm Bilge Separator.

  • .2 The test should then proceed for 2.5 h. Samples should be taken at the effluent outlet at 50 minutes and 100 minutes after conditioning. At the end of this test, an air cock should be opened on the suction side of the pump and, if necessary, the Test Fluid "C" and water valves should be slowly closed together, and a sample taken at the effluent discharge as the flow ceases (this point can be checked from the observation window).

  1.2.12 Sampling should be carried out as shown in figure 4 so that the sample taken will suitably represent the fluid issuing from the effluent outlet of the 15 ppm Bilge Separator.

  1.2.13 Samples should be taken in accordance with ISO 9377-2:2000. The sample is to be extracted on the same day of collection, and be sealed and labelled in the presence of a representative of the national authority and arrangements should be made for analysis as soon as possible and in any case within seven days provided the samples are being kept between 2°C and 6°C at laboratories approved by the Administration.

  1.2.14 The oil content of the samples should be determined in accordance with part 4 of the annex.

  1.2.15 When accurate and reliable oil content meters are fitted at inlet and outlet of the 15 ppm Bilge Separator, one sample at inlet and outlet taken during each test will be considered sufficient if they verify, to within ±10%, the meter readings noted at the same instant.

  1.2.16 In the presentation of the results, the following data testing methods and readings should be reported:

  • .1 Properties of test fluids A and B:

    • density at 15°C;
    • kinematic viscosity (centistokes @ 100°C /40°C);
    • flashpoint;
    • ash; and
    • water content;
  • .2 Properties of Test Fluid C:

    • type of surfactant;
    • particle size percentage of the non soluble suspended solids; and
    • surfactant and iron oxide quality verification;
  • .3 Properties of the water in the water tank:

    • density of water at 20°C; and
    • details of any solid matter present;
  • .4 Temperature at the inlet to the 15 ppm Bilge Separator;

  • .5 A diagram of the test rig;

  • .6 A diagram of the sampling arrangement; and

  • .7 The method used in analysis of all samples taken and the results thereof, together with oil content meter readings, where appropriate.


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