Visit the IMO and check into MARPOL Annex VI. (a search for MARPOL Annex Vi and search within your results for boilers/burners may take you where you want to go.
There are provisions for COX NOX and SOX reductions which may have some input for you.
I think the MARTOB report on "Onboard Ballast Water Treatment and the Application of low sulphur fuels" examines the necessary fuel systems changes on board vessels in some detail. This mainly applies o the engines but there ought to be some comment on marine boilers also.
Fuel quality is now defined by ISO 8217 2005E. FOBAS and others are very informative on this and you can visit sites such as Viswalab where there are useful comments on marine application of fuels plus also IBIA (International Bunker Industries Association) technical section.
You can visit this link (
for a spreadsheet which lets you calculate the injection or EVT temperature for the burners once you know the target viscosity.
Most engines operate between 10 and 20cst but there is an increasing trend from 380cst fuels to 500cst fuels for those who have the equipment to handle the higher temperatures.
For burners it may depend where you draw the fuel from as to your handling temps but for engines the fuel is first heated to around 98degC to drop the viscosity as much as possible without causing the water content to flash into steam before going through the centrifuges and then it goes to the high pressure circuit where it is heated up to optimise the viscosity. e.g., for an MAK type 43 engine the mas allowable fuel temperature is 150degC but for a 380cst fuel the injection temperature is typically 141degC and the optimum viscosity is 11cst. For burners the viscosity allowable may be higher and it will differ for different engines.
Some engines have a fuels envelope that is defined by the viscosity at 100degC, the density at 15degC and the ignition index (usually CCAI values calculated according to BS MA 100).
By the way, if your fuel viscosity lies between the data pre-loaded into the spreadsheet, and you only have the viscosity at one temperature for your fuel, I have another spreadsheet which allows you to infer the viscosity at a second temperature so you can use the spreadsheet you get from that download link. email via the website if you want it.
JMW