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Long Term Testing of Aluminium
Sacrificial Anode LONG TERM ANODE PERFORMANCE TEST |
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| Introduction | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| MPE commenced the long-term testing of sacrificial anode materials in according to DNV RP B401 Appendix B on 9th January 2004 and completed on 7th January 2005 (12 months testing duration). The test was conducted in MPE laboratory, verified and certified by ThirdParty Inspection Company, ABS Consulting Sdn Bhd, hereinafter referred to as “ABS”. Five different batches/melts of MPE III anode specification were taken from normal production during anode manufacturing. Result of MPE III anode test specimens is shown in this report. | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Test Condition | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
TEST SPECIMENS
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| Test Environments | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
The test set-up and test-cell are shown in figure 1. The testing environment was clean natural
seawater with salinity of approximately 34 ppK and at a temperature of 20º C + 2º C. Temperature and salinity were recorded weekly, shows in Table 2 . The seawater in the cell was continuously exchanged at a rate of approximately 2 liter/minute and continuously purged
with air.
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| Test Procedure | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
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APPARATUS: The following apparatus was used: i. The container with steel pipe as cathode is filled with natural seawater. ii. Titanium rod. iii. Constant power supply : DC constant power supply with variable resistance and DC milliammeter and attached with electronic totalizer. iv. Silver/Silver Chloride (Ag/AgCl) to measure potential reading. v. Voltmeter CIRCUIT: The circuit was arranged as shown in Figure 1. ![]() TEST SPECIMENS SET-UP Preparation - A hole was drilled and threaded on one of the ends for connection to a support titanium rod. The support rods (titanium rod) of the test specimen that were exposed to the test solution were coated with an epoxy resin. The test specimens were rinse thoroughly first in tap water and then dried with acetone. Test specimens were weighed and recorded to the nearest 0.1mg on an analytical balance. The test was performed as a “free running test” where the test specimens and cathode were connected to a 10-ohm precision resistance. During the initial one-week (7days) continuous run, the applied current flow was established based on anodic current density of 1 mA/cm2. Thereafter the current density was reduced to 0.5 mA/cm2 for the remaining duration of the test. Calculation of Applied Current Flow: Surface area of sample exposed = Pi(DL) + 2(Pi)2 = Pi(3) (8)cm2 + 2(Pi)(1.5)2 = 75.40 cm2 + 14.14 cm2 = 89.5 cm2 For the first one week, Current flow = Current Density x Surface area. = 1 mA/cm2 x 89.5 cm2 = 89.5 mA After one week test until completion = 0.5 mA/cm2 x 89.5 cm2 = 44.75 mA A totalizer measured the total applied current that passed through the system. Anode weight loss was determined at the end of the 12 months test when the samples were removed, cleaned and weighed. Anode current capacities are then determined from knowledge of the total charge passed through the system and the weight loss of the anode sample. Anode potential reading was measured using Ag/AgCl reference electrode. The anodic current density was calculated from measurement of the voltage drop across the 10- ohm circuit resistance. Measurement of both current and anode potential were collected once per week. After completion of the full test period, the test specimens were cleaned for 10 minutes at 80ºC in a solution containing chromium trioxide (CrO3) and 30mL concentrated phosphoric acid (H3 PO4) mixed with 1liter tap water. The specimens were then rinsed thoroughly with tap water and dried with acetone. (Note : Cr (VI) waste may be reduced to Cr (III) with sodium bisulfate ( NaHSO3). Dissolve 3.75g sodium disulfate per gram of Cr (VI) in the solution and mix for 1h.) Final weight of test specimens were obtained and recorded. CHEMICAL COMPOSITION ANALYSIS Table 3 : Chemical Analysis of Test Specimens
Table 4 : Chemical Composition Specification
DENSITY TEST Calculation of Density ? Density (g/cm3) = x (g)/ y (cm3) Where, x = weight of sample & y = the volume of water displaced Conversation ? 1 ml = 1 cm3 (Water density = 1.00 g/ml, therefore 1g = 1 ml)
The mean anode density of MPE III anode specification manufactured by MPE was 2.745 g/cm3. VISUAL EXAMINATION Photos after test to show the consumption pattern are shown below (Consumption pattern on the surface of anode samples fairly even corrosion throughout): Microstructure Test of Anode Test Specimens after exposure Five samples were selected for microstructure test conducted by certified laboratory (contact us for details). The visual microscopy of cross-section on all 5 samples shows NO indication of INTERGRANULAR CORROSION. The results and photomicrographs of the microstructure are available online .. .. view this report. ELECTROCHEMICAL RESULT CALCULATION OF CURRENT CAPACITY Current capacity (ampere. Hours/kg ) = (c x 1,000) / w where, c = Total charge passed in a year (amp. h) w = Weight loss of anode samples (grams) The results are given in Table 5. Table 5 : Result of Anode Current Capacity and Consumption Rate
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| Conclusion | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| The mean current capacity of MPE III anode specification manufactured by MPE Lindung Sdn
Bhd was 2698.58 +/- 50 Amp.Hr/kg and consumption rate was 3.246 Kg/Amp.yr complies to
DNV RPB40 table 6.6.1. The anodic current density Is 0.49 mA/cm2 and potential is -1055.71mV VS AglAgCI (seawater) reference electrode. No indication of passivation were found. No intergranular corrosion was found. End of report. (for a pdf version of this report, click here) |
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Deepwater Corrosion Services inc. +1 (713) 983 7117 www.stoprust.com |