Analogy with snow (soot deposits)Analogy with coal briquettes (ignition)General four ma<strong>in</strong> parametersIn a snowstorm at below-zero temperature,the snowflakes (dry soot particulates)will not easily deposit on the ground unlessthe w<strong>in</strong>d (gas) velocity is reduced,as it is for example beh<strong>in</strong>d a fence. Thelow w<strong>in</strong>d velocity will cause the snowflakesto deposit <strong>and</strong> form a snowdrift,<strong>and</strong> if the w<strong>in</strong>d direction changes(higher velocity), part of the snowdriftmay move. This means that at a certa<strong>in</strong>low w<strong>in</strong>d (gas) velocity, the snowflakes(dry soot particulates) will deposit.In a thaw, for example, when the snowflakesare wet (wet soot), the snowflakeswill deposit more easily, <strong>and</strong> a change<strong>in</strong> the w<strong>in</strong>d direction (higher velocity) willmake only a small part of the snowdriftmove. Thus, the wet snowflakes (wetsoot) will deposit, but will do so alreadyat a w<strong>in</strong>d velocity (gas velocity) which ishigher than the w<strong>in</strong>d (gas) velocity for theabove-mentioned frozen snowflakes(dry soot).In general, therefore, high w<strong>in</strong>d (gas) velocities<strong>and</strong> frozen snowflakes (dry soot) willreduce the tendency towards deposits.Ignit<strong>in</strong>g a coal briquette (dry soot) for a grillis quite difficult, as its ignition temperatureis rather high. On the other h<strong>and</strong>, if thebriquettes have been wetted with oil (wetsoot), the ignition temperature will be lower<strong>and</strong> it will be easier to ignite the briquettes(wet soot). The higher the temperatureof the wetted briquettes (wet soot), theeasier they are to set on fire.So <strong>in</strong> general, the drier the briquettes(soot), <strong>and</strong> the lower the temperature,the more difficult they will be to ignite.Analogy with putt<strong>in</strong>g-out a fonduefire (oxygen)If the oil <strong>in</strong> a fondue pot has becometoo hot <strong>and</strong> has been set on fire, theeasiest way to ext<strong>in</strong>guish the fire is toput a cover over the fire <strong>and</strong> stop thesupply of oxygen.When a soot fire occurs <strong>in</strong> an exhaust gasboiler, similar action has to be taken. Inthis case the oxygen supply is stopped bystopp<strong>in</strong>g the diesel eng<strong>in</strong>e, as the eng<strong>in</strong>e’sexhaust gas still conta<strong>in</strong>s about 14%oxygen.Wrong CorrectGiven the po<strong>in</strong>ts discussed above, therisk of soot deposits <strong>and</strong> ignition followedby soot fires may be m<strong>in</strong>imised by respect<strong>in</strong>gthe follow<strong>in</strong>g four ma<strong>in</strong> parameters- valid for both water <strong>and</strong> smoketube boilers:• The gas velocity <strong>in</strong> the boiler mustnot be too low,- this reduces the ma<strong>in</strong> risk factor forsoot deposits.• The gas temperature on the boilertube surfaces must not be too low,- this reduces the additional risk ofsoot deposits due to the formationof wet soot.• The eng<strong>in</strong>e smoke emission shouldnot be allowed to deteriorate,- s<strong>in</strong>ce this would <strong>in</strong>crease the tendencytowards soot deposits.• The circulation water flow velocity <strong>and</strong>ratio <strong>in</strong> the boiler must not be too low- this keeps the gas temperature at theboundary layer of the boiler tubes below the ignition temperature of the soot.The first three of these parameters relateto the soot deposits, whereas the numberfour parameter relates to the risk of ignitionof the soot.<strong>Soot</strong>depositsInletpip<strong>in</strong>g<strong>Boiler</strong>tubesectionRecirculationof gas<strong>Exhaust</strong>gasFig. 22: <strong>Exhaust</strong> gas boiler – <strong>in</strong>fluence of <strong>in</strong>let pip<strong>in</strong>gs<strong>Exhaust</strong>gas<strong>Boiler</strong>tubesectionInletpip<strong>in</strong>g UniformgasvelocityRecommended boiler designcriteriaThe boiler design criteria that can berecommended on the basis of the fourma<strong>in</strong> parameters mentioned <strong>in</strong> abovesection, with due consideration for the<strong>in</strong>fluence of the low gas velocity, are thusas follows:Referr<strong>in</strong>g to soot deposits:a) The design mean gas velocity of theboiler should be higher than about 20m/s, but the limit may, <strong>in</strong> fact, dependon how dry <strong>and</strong> sticky the soot is (fueltype/fuel additive).18This document, <strong>and</strong> more, is available for download at Mart<strong>in</strong>'s Mar<strong>in</strong>e Eng<strong>in</strong>eer<strong>in</strong>g Page - www.dieselduck.net
)The p<strong>in</strong>ch po<strong>in</strong>t temperature of theboiler should be higher than about15°C or, even better, 20°C.c)The boiler’s exhaust gas outlet temperatureshould not be lower thanabout 165°C as otherwise condensationof sulphuric acid <strong>in</strong> the exhaustgas could make the soot sticky.d)The <strong>in</strong>let pip<strong>in</strong>g to the boiler shouldbe designed so that the gas flow velocitydistribution is as uniform as possible,<strong>in</strong> order to avoid local po<strong>in</strong>tswith a particularly low gas velocity.e)The exhaust gas design pressureloss across the boiler should be ashigh as possible - <strong>in</strong>creas<strong>in</strong>g the gasvelocity <strong>in</strong> the boiler. This means thatthe pressure losses <strong>in</strong> the rema<strong>in</strong><strong>in</strong>gparts of the exhaust gas systemshould be dimensioned as low aspossible (large pipe diameters).f) A dump<strong>in</strong>g condenser should be <strong>in</strong>stalledto control steam production/consumption.A gas by-pass valve <strong>in</strong>stalled to controlthe steam production would reducethe gas velocity <strong>in</strong> the boiler - <strong>and</strong>consequently <strong>in</strong>crease the risk of sootdeposits - <strong>and</strong> cannot, therefore, berecommended.The supplementary recommendationsbelow apply only to boilers of the watertube type:g)A by-pass duct with an automaticallyoperated on/off valve (open/closed at50% SMCR) may <strong>in</strong> certa<strong>in</strong> operat<strong>in</strong>gconditions be recommended for watertube boilers. If, for example, theship is often slow steam<strong>in</strong>g, i.e. thediesel eng<strong>in</strong>e operates at low load,such an <strong>in</strong>stallation will prevent sootdeposits on the boiler tubes by bypass<strong>in</strong>gall the gas <strong>and</strong> thereby avoid<strong>in</strong>glow gas velocities <strong>and</strong> the associatedrisk of soot deposits <strong>in</strong> the boiler.h)Automatic soot blowers for frequentclean<strong>in</strong>g should be <strong>in</strong>stalled <strong>in</strong> watertube boilers <strong>in</strong> order to clean the tubesof soot. The pressure of the soot blow<strong>in</strong>gmedium should be as high as possibledur<strong>in</strong>g the entire soot blow<strong>in</strong>g sequence.As the possible steam pressure usedis only about 7 barg, <strong>and</strong> <strong>in</strong> some cases6 barg, the use of high-pressure air willbe better.i) Fixed water wash<strong>in</strong>g system <strong>and</strong>/ormanual clean<strong>in</strong>g at regular <strong>in</strong>tervals.Water wash<strong>in</strong>g is performed <strong>in</strong> orderto clean the boiler completely of sootwhich has not been cleaned away bythe soot blowers. The exhaust gaspip<strong>in</strong>g between eng<strong>in</strong>e <strong>and</strong> boiler shouldbe so arranged that the boiler can becleaned more thoroughly from time totime when the eng<strong>in</strong>e is stopped <strong>in</strong>harbour without the risk of flood<strong>in</strong>g theeng<strong>in</strong>e/turbochargers with clean<strong>in</strong>g fluid.Water wash<strong>in</strong>g should preferably beundertaken while the tubes are stillhot, mak<strong>in</strong>g it easier to remove thesoot as it will “crack”.If the above-mentioned on/off exhaustbypass is <strong>in</strong>stalled, the boiler can bebypassed. Water wash<strong>in</strong>g shouldthen also be carried out dur<strong>in</strong>g seaservice as often as possible (when theexhaust pressure loss <strong>in</strong>creases), <strong>and</strong>not only dur<strong>in</strong>g stops <strong>in</strong> harbour. Afterwater wash<strong>in</strong>g, it should be checkedthat no soot is left, as rema<strong>in</strong><strong>in</strong>g wetsoot may <strong>in</strong>crease the risk of soot depositswhen cont<strong>in</strong>u<strong>in</strong>g operation.j) The water circulation temperature atthe boiler <strong>in</strong>let, for boilers with apreheater section, should be higherthan about 140°C as otherwise toolow temperatures could cause someof the gas constituents, such as fuel<strong>and</strong> lube oil vapour, to condense onthe cold boiler tube surfaces, <strong>and</strong> thiscould <strong>in</strong>crease the tendency towardssoot deposits.Another advantage of this is that thetemperature of the preheater tubesurfaces can then be higher than thedew po<strong>in</strong>t of the sulphuric acid <strong>in</strong> thegas, thus m<strong>in</strong>imis<strong>in</strong>g the risk ofsulphuric acid corrosion.Referr<strong>in</strong>g to ignition:k)The circulation water flow velocity<strong>and</strong> ratio at the boiler <strong>in</strong>let should beas high as possible <strong>in</strong> order to keepthe gas temperature at the boilertube surface as low as possible (<strong>in</strong>contrast to po<strong>in</strong>t j). The water flow ratio(water flow/steam production ratio)is recommended to be equal to orhigher than 6. This should reduce therisk of ignition of possible soot deposits,which can happen at temperaturesabove some 150°C <strong>and</strong>, underextreme conditions, even as low as120°C.It is therefore also very important toensure the best suction conditions sothat cavitation does not occur <strong>in</strong> thecirculat<strong>in</strong>g pumps under any work<strong>in</strong>gconditions, as otherwise the circulat<strong>in</strong>gwater flow could be reduced oreven stopped.A temperature monitor<strong>in</strong>g systemmounted above the boiler might be recommendableas a means of detect<strong>in</strong>g afire <strong>in</strong> the boiler as soon as it starts.Recommended operat<strong>in</strong>gconditionsIn view of the damage that can becaused by an extensive soot fire <strong>in</strong> theexhaust gas boiler, it is recommended,dur<strong>in</strong>g the operation of the ship, to givedue consideration to the follow<strong>in</strong>g:Normal operat<strong>in</strong>g conditionsa)<strong>Soot</strong>-blow<strong>in</strong>gIf soot-blow<strong>in</strong>g equipment is <strong>in</strong>stalled,we recommend check<strong>in</strong>g its efficiency<strong>and</strong> adjust<strong>in</strong>g the number ofdaily soot-blow<strong>in</strong>gs accord<strong>in</strong>gly.This document, <strong>and</strong> more, is available for download at Mart<strong>in</strong>'s Mar<strong>in</strong>e Eng<strong>in</strong>eer<strong>in</strong>g Page - www.dieselduck.net19