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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

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