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Cimac Congress | Shanghai 2013<br />
concerning invest and operation cost as well as reliability and performance<br />
are generated by smart combination of the subsystems.<br />
As example, when the desulphurisation is placed in front of the<br />
SCR unit, a much better quality of the exhaust gas is entering the<br />
catalyst, with a lower risk of blocking, fouling or poisoning. Therefore<br />
the complete system can be further optimised regarding volume<br />
and weight. The paper summarises the test results and challenges<br />
and concludes with an outlook to future developments.<br />
US EPA exhaust emissions certification of the<br />
Bombardier ALP-45DP locomotive<br />
Steven Fritz, Southwest Research Institute, USA<br />
Bernhard Kunz, Bombardier Transportation, Switzerland<br />
Werner Sonnleitner, Bombardier Transportation GmbH, Germany<br />
Dustin Osborne, Southwest Research Institute, USA<br />
The Bombardier ALP-45DP is a dual-power (electric and dieselelectric)<br />
locomotive manufactured for the North American market.<br />
It is rated at 5.0 MW in catenary-electric mode, and 3.0 MW<br />
in diesel-electric mode. In diesel-electric mode, power is provided<br />
by two 1.5MW Caterpillar 3512C-HD diesel engines. This paper<br />
describes the challenges and solutions in obtaining US EPA Tier<br />
III locomotive certification for this locomotive. There are several<br />
unique aspects of the Bombardier ALP-45DP locomotive that required<br />
dialogue with EPA for the exhaust emissions certification<br />
process. These included an infinitely variable throttle in contrast to<br />
the North American convention of ’throttle notches,’ where engine<br />
speed and load are predefined by the locomotive manufacturer,<br />
and hence selection of the exhaust emissions test modes is straightforward.<br />
Bombardier performed extensive analysis of the launch<br />
customer route (New Jersey Transit) to develop expected locomotive<br />
power requirements, and subsequently used this information<br />
to help define specific emissions test modes and associated dutycycle<br />
weighting factors. The two Caterpillar 3512C-HD engines in<br />
the ALP-45DP locomotive are each equipped with a diesel oxidation<br />
catalyst (DOC). This was relatively new for the North American<br />
locomotive market, and considerable effort was required to<br />
detail the DOC degreening requirements, and to provide sufficient<br />
technical basis for the deterioration factor (DF) required by EPA<br />
as part of the certification process. Exhaust emissions test results<br />
from US EPA certification testing are included in the paper, including<br />
regulated emissions of HC, CO, NOx, and PM, as well results<br />
for new EPA requirements for reporting greenhouse gas emissions<br />
of CO 2<br />
and methane (CH 4<br />
). Methane measurement and reporting<br />
is a new requirement by EPA for new locomotives starting in 2012,<br />
and these procedures are detailed in the paper.<br />
Design aspects of SCR systems for HFO-fired marine<br />
diesel engines<br />
Niko Soikkeli, Wärtsilä, Finland<br />
Marko Lehikoinen, Wärtsilä, Finland<br />
Kaj-Olof Ronnback, Wärtsilä, Finland<br />
The objective of the article is to present critical design aspects of<br />
SCR systems suited for high-sulphur fuels in combination with<br />
exhaust gas boilers, silencers and scrubber. The combination is<br />
presented by going through the challenges of the general system<br />
design. Regarding the challenges the main focus of the paper is in<br />
SCR operation when using high sulphur heavy fuel oil. The message<br />
is that by designing the exhaust gas treatment combination<br />
effectively, it is possible to meet IMO ECA requirements for NOx<br />
and SOx emissions in the future while utilising the whole exhaust<br />
gas system design also e.g. for noise attenuation. The intension is<br />
to explain the most important phenomena influencing on the design<br />
and by what terms the different exhaust gas equipment affect<br />
each other and the engine itself. The main focus of the article is on<br />
SCR operational requirements. Therefore the paper will review the<br />
exhaust gas temperature window requirements for SCR and will<br />
explain facts behind the recommended temperature limits. The<br />
paper will present how the SCR design is effectively implemented<br />
to high sulphur heavy fuel oil operation by optimised catalyst design<br />
and improved catalyst cleaning system and by following the<br />
temperature requirements. In some engines there is a certain need<br />
to control the temperature after the turbocharger during the operation<br />
with high sulphur HFO and SCR. The need for control also<br />
applies to applications that have significantly low engine intake air<br />
temperature. The most suitable way to carry out the temperature<br />
control strongly depends on the operation profile of the engine<br />
and SCR and if the SCR is operated only on certain sailing areas<br />
or continuously. Aspects of the combined engine and SCR design<br />
are reviewed in general level. The paper also reviews the whole exhaust<br />
gas line. Temperature changes, back pressures, and noise attenuation<br />
features of the different equipments are discussed. Back<br />
pressure of the whole exhaust gas line can be optimised by sufficient<br />
dimensioning and combination of the equipments. Sound<br />
attenuation features of the combination of integrated mixing duct<br />
silencer, SCR reactor, boiler and Wärtsilä CSS (compact silencer<br />
system) elements are discussed. This combination can be designed<br />
to meet various sound attenuation requirements. Space restrictions<br />
are a well recognised concern for many shipowners, ship operators<br />
and shipyards. The needed performance of the exhaust gas<br />
line after turbocharger plays a significant role in the design of the<br />
ship. The paper presents the typical sizes of different equipments<br />
and the feasible ways to minimise the needed space for the whole<br />
exhaust gas line.<br />
Advanced exhaust emission abatement – 144 MW<br />
diesel based power production with NOx, SOx, and<br />
PM abatement – design – commissioning – early<br />
production experience<br />
Lars Ellegaard, Burmeister and Wain Scandinavian Contractor AS, Denmark<br />
Knud Hvidtfeldt Rasmussen, Burmeister and Wain Scandinavian Contractor<br />
AS, Denmark<br />
Claus Albrechtsen, Burmeister and Wain Scandinavian Contractor AS,<br />
Denmark<br />
Burmeister & Wain Scandinavian Contractor AS has designed, constructed,<br />
and commissioned a 144 MW diesel engine based power<br />
plant for Enemalta Corporation in Malta in 2012 with an exceptionally<br />
low level of emissions. The low-emission level is based<br />
on a combination of well-proven and new advanced abatement<br />
techniques capable of complying with the most stringent emission<br />
norms. The power producing units of the plant are eight diesel generation<br />
sets, Wärtsilä 18V46 medium-speed diesel engines with ABB<br />
AMG1600 alternators, each rated 17.1 MWe, and as bottom cycle<br />
one common Dresser Rand steam turbine generator with a Converteam<br />
alternator, rated 13.2 MWe. The fuel of the plant is HFO<br />
with a maximum sulphur content of 1%. The flue gas abatement<br />
includes NOx abatement by SCR, SOx and particulate abatement<br />
by dry flue gas desulphurisation (FGD) with Sodium Bi-Carbonate<br />
injection followed by filtration in a Bag-House filter. The plant is<br />
cooled by sea water. The obtained <strong>net</strong> plant electrical efficiency<br />
with the extensive utilisation of the exhaust gas energy in boilers<br />
and the steam turbine generator is 46.9% with due consideration<br />
of auxiliary power consumption for emission abatement purposes.<br />
In addition, the plant includes two desalination units, each rated<br />
700 m 3 /day, driven by engine cooling water, thus achieving a total<br />
thermal efficiency exceeding 50%. The major unabated flue gas<br />
emission with the installed equipment would have been approxi-<br />
52 SPECIAL<br />
Schiff&Hafen | Ship&Offshore | May 2013