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TECHNOLOGY - TANK CLEANING<br />

It was also considered that cleaning<br />

persistent hydrocarbons from zinc silicate is<br />

one of the most challenging operations facing<br />

chemical/product tanker owners and operators<br />

so it could be assumed that the tank cleaning<br />

chemicals that performed the best under the<br />

conditions of the project, would most likely be<br />

some of the most effective in the market<br />

place.<br />

The efficiency of each tank cleaning<br />

chemical was monitored by means of wall<br />

washing the test panel with a fixed volume of<br />

methanol. This methanol was then tested for<br />

water miscibility (hydrocarbons) in<br />

accordance with ASTM D1722, but rather<br />

than just visually ‘passing’ 20 or ‘failing’ the<br />

sample (as stated in the ASTM procedure)<br />

the extent of the hydrocarbon failure was<br />

quantified using the L&I WAVE II UV / Vis<br />

Spectrometer.<br />

The following test protocol was agreed:<br />

1) Three zinc silicate coated test panels were<br />

fully immersed in Linear Alkyl Benzene<br />

(LAB) for 48 hours.<br />

2) The panels were removed from the LAB,<br />

flushed with cold freshwater for<br />

approximately 1 minute (in order to<br />

remove the free LAB from the surface of<br />

the test panels) and then naturally<br />

ventilated to dryness.<br />

3) The panels were then washed by recirculation<br />

using the tank cleaning<br />

chemical (at the concentration specified<br />

by the manufacturers) for 2 hours at<br />

60 deg C in fresh water.<br />

4) The panels were again flushed with cold<br />

freshwater to remove any residual<br />

detergent and then naturally ventilated to<br />

dryness.<br />

5) Each panel was then wall washed with<br />

methanol and tested for hydrocarbons<br />

using the LIM spectrometer to quantify<br />

the hydrocarbon content of the sample.<br />

The reported result was an average of all<br />

three results.<br />

It was agreed to limit the cleaning water<br />

temperature to 60 deg C, because this<br />

temperature is considered to be the lowest<br />

‘hot’ water temperature that can be readily<br />

achieved and maintained by most<br />

chemical/product tankers.<br />

The cleaning was carried out using a tank<br />

cleaning rig that LIM has made specifically<br />

for the purpose of replicating the tank<br />

cleaning action on board chemical/product<br />

tankers. The test panels were sprayed with the<br />

cleaning chemical solution, in a similar<br />

manner to the way the bulkheads of a cargo<br />

tank would be sprayed.<br />

In order to create a control (reference) for<br />

the project, the zinc silicate coated panels<br />

were initially treated in the same way as<br />

above, apart from the fact that no cleaning<br />

chemicals were added in part 3. It was<br />

expected that the cleaning effect on the test<br />

panels without using tank cleaning chemicals<br />

would be minimal and when the panels were<br />

wall washed the results would show the<br />

highest residual hydrocarbon readings.<br />

At the same time, when the panels were<br />

cleaned with the individual tank cleaning<br />

chemical solutions, the hydrocarbon readings<br />

from the wall wash samples would be<br />

expected to be significantly better. The most<br />

efficient cleaning chemical solutions would<br />

therefore be expected to show the lowest<br />

hydrocarbon readings.<br />

Cleaning chemicals from seven different<br />

THE DIFFERENCE IS OBVIOUS. SO ARE WE. OPERATIONS WITH A DIFFERENCE.<br />

EMIRATES ENVIRONMENTAL PROTECTION Co. L.L.C.<br />

A MARPOL Reception Facility in the Port of Khorfakkan, U A E<br />

Tank Cleaning/De-mucking, De-slopping, Treatment & Disposal of Oily Sludge, Slop & other petroleum waste.<br />

P.O.Box 43729, Dubai, U.A.E. Tel : +9714 397 2277, Fax : +9714 397 9212<br />

Email: eco@emirates.net.ae Website: www.ecouae.com<br />

November/December 2009 TANKER<strong>Operator</strong> 29

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