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Low Sulphur Fuel Operation<br />

<strong>MAN</strong> B&W low speed engines can op-<br />

erate on both heavy fuel oils (HFOs)<br />

with a varying amount of sulphur, marine<br />

diesel oil (MDO) and marine gas oil<br />

(MGO). All fuels are specified in accordance<br />

with ISO 8217 and CIMAC recommendation<br />

21. Also biofuels (with separate<br />

fuel specification) are now used on<br />

<strong>MAN</strong> B&W low speed engines.<br />

Local and international restrictions on<br />

sulphur emissions are the reason why<br />

an increased focus on low sulphur fuels<br />

is seen today. Sulphur emissions can<br />

be limited in two ways:<br />

By making rules for a maximum<br />

amount of sulphur in the fuel. Fig. 52<br />

shows the “road map” for such legislation<br />

globally and locally in so-called<br />

SECAs (Sulphur Emission Control<br />

Areas)<br />

By applying abatement technologies<br />

on board the vessels allowing the<br />

vessels to continue operating on a<br />

high sulphur content HFO. The driving<br />

force for such technologies is the large<br />

price difference between various HFOs<br />

and distillates, see Fig. 53.<br />

When running on low sulphur fuels, a<br />

number of issues of interest in relation to<br />

operational aspects can be mentioned.<br />

Many of these are dealt with in detail in<br />

our <strong>Service</strong> Letter, SL09-515/CXR, Ref.<br />

[3]. These issues are discussed one by<br />

one in the following.<br />

Catfines in Low Sulphur HFOs<br />

From a large number of bunker analyses,<br />

it can be seen that there is a tendency<br />

towards a higher amount of<br />

catfines in fuels with lower sulphur con-<br />

US$ per Ton<br />

1300<br />

1100<br />

900<br />

700<br />

500<br />

300<br />

100<br />

26 <strong>Service</strong> <strong>Experience</strong> of <strong>MAN</strong> B&W Low Speed <strong>Diesel</strong> Engines<br />

MEPC 57 IMO & CARB Fuel-Sulphur Content Limits<br />

Equivalent methods may be used as altemative<br />

Global 4.5→3.5→0.5<br />

SECA 1.5→1.0→0.1<br />

Global<br />

CARB MGO 1.5→1.5→0.1 (DMA)<br />

CARB MGO 2.0→0.5→0.1 (DMB<br />

SECA<br />

CARB Phase 1<br />

CARB Phase 2<br />

2000 2005 2010 2015 2020 2025<br />

Year<br />

5<br />

4,5<br />

4<br />

3,5<br />

3<br />

2,5<br />

2<br />

1,5<br />

1<br />

0,5<br />

0<br />

Fig. 52: Sulphur reduction ‘road map’<br />

US$ per Ton<br />

End of Period<br />

July 2009<br />

MDO<br />

380 CST<br />

85 86 87 88 89 90 91 92 93 94 95 96 97 98 99 00 01 02 03 04 05 06 07 08 09 A M J J A S O N D J F M A M J J A S O N D J F M<br />

Fig. 53: Cost difference: HFO vs. distillates<br />

March 2010<br />

tents. This requires increased focus on<br />

optimal function of the fuel treatment<br />

plants on board vessels operating on<br />

low sulphur fuels.<br />

Cylinder Lubrication and Low<br />

Sulphur Fuels<br />

It is well-established that <strong>MAN</strong> B&W<br />

low speed engines, to a certain degree,<br />

need cylinder oil feed rates proportional<br />

to the sulphur content in the fuel. This is<br />

due to the fact that we prefer to have a<br />

controlled amount of cold corrosion on<br />

Jan 2012<br />

2008 2009 2010<br />

the cylinder liner wall. However, we also<br />

have other requirements for lubrication<br />

apart from controlling the acid neutralisation.<br />

These requirements presently<br />

put a minimum limit to the feed rate of<br />

0.6 g/kWh. Fig. 54 illustrates the degree<br />

of over-additivation when operating on<br />

various cylinder oils (various BN numbers),<br />

and it can be seen that the need<br />

for lower BN cylinder oils will persist as<br />

fuel sulphur content limits are tightened.

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