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MAN Low Sulfur Fuel and Emission Advances (10) - Zdjęcie Do Inżynierki

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2009/04/01 © MAN Diesel Global Greenship, September 2009 Low Sulfur Fuel and Emissions Advances
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  • 2009/04/01 MAN Diesel

    Global Greenship, September 2009Low Sulfur Fuel and Emissions Advances

  • 2009/04/01 MAN Diesel 2

    1. Singapore

    5. South Korea, Busan

    9. Germany, Hamburg10. China, Qingdao

    6. Netherl., Rotterdam

    2. China, Shanghai

    8. Taiwan, Kaohsiung7. UAE, Dubai

    3. China, Hong Kong4. China, Shenzhen

    existing ECAs: Baltic Sea, North Sea planned ECAs: Coasts of USA, Hawaii and Canada

    Top Container Ports :

    discussed ECAs: Coasts of Mexico, Coasts of Alaska and Great Lakes, Singapore, Hong Kong, Korea, Australia, Black Sea, Mediterranean Sea (2014), Tokyo Bay (in 2015)

    Most used trading routes

    ECA and SECA Trends

  • 2009/04/01 MAN Diesel

    Proposed North American Emission Control Area

  • 2009/04/01 MAN Diesel

    Local SECA CARB, 2009

    CARB Regulations for California, starting July 2009:

    ZONE

    24 miles from coastal California

    Regulation -

    July 1, 2009 maximum 0.5% sulfur

    January 1, 2012 maximum 0.1% sulfur

  • 2009/04/01 MAN Diesel

    IMO & CARB Fuel-Sulphur Content Limits

  • 2009/04/01 MAN Diesel

    Low-sulphur Fuel Operation

    Engine

    Compatibilityof mixed fuels

    Tank systemconsiderations

    Viscosity

    OilCylinder Oil BN40-70

    Fuel changeover requirementHigh S% Low S%

  • 2009/04/01 MAN Diesel 2009.02.25 (LD/MZP)

    ViscosityThe engine fuel pump is designed for high viscosity, heavy fuel operation. Low viscosity fuels can cause excessive wear, and affect injection pressure, particularly during start, low load and low rpm.

    In worn pumps, if viscosity is too low, internal leakage can increase and starting the engine will be difficult because of lack of injection pressure.

    LubricityThe refinery process to remove sulfur also impacts lubricity, which could result in fuel pump seizures. While refiners add lubricity additives, MAN Diesel recommends that, prior to using distillates fuels with less than 0.05% sulphur, lubricity be tested.

    Low Sulphur Fuels / Viscosity and Lubricity

  • 2009/04/01 MAN Diesel

    Many factors influence viscosity tolerance during start and low load operation:

    Engine condition and maintenance

    Fuel pump wear

    Engine adjustment Temperatures in the fuel system

    Human factors

    Factors influencing viscosity tolerance

  • 2009/04/01 MAN Diesel

    Poor Fuel Switching Techniques

    Source: Gard

  • 2009/04/01 MAN Diesel

    Recommendations for Low Sulfur Operation in Large Diesel Engines

    Fuel Switch-over from HFO to MDO/MGO needs to be carefully performed and monitored. Automated devices are suggested to minimize potential for human error.

    Fuel Viscosity must be maintained at or above 2cst (40 deg C) atengine inlet to avoid fuel pump and injector sticking and scuffing problems.

    Fuels with viscosity above 3cst at 40 deg C are recommended to provide sufficient margin for safe and reliable engine performance.

    It is recommended to run through the change-over procedure, and perform start checks at regular intervals.

  • 2009/04/01 MAN Diesel 2009.02.25

    Low Sulphur / Viscosity fuels

    0

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    Fuel Viscosity (cSt) @ 40C

    Fuel Temperature vs Viscosity

    2.0 cSt

    4.0 cSt

    5.0 cSt

    1.5 cSt

    GOODFuel above 3 cSt

    MAN Diesel recommend to operate the engine on fuels with viscosities above 3 cSt

    DOUBTFULFuel viscosity 2 - 3 cSt

    MAN Diesel strongly recommend to make start checks prior to port operation

    3.0 cSt

    NOT GOODFuel below 2cSt

    MAN Diesel do not recommend to operate the engine on fuels with viscosities lower than 2 cSt

    The horizontal axis shows the bunkered fuel viscosity in cSt at 40 deg C, which should be informed in the bunker analysis report.If the temperature of the MGO is below the red curve at engine inlet, the viscosity is above 2 cSt.

    Example: MGO with viscosity of 3 cSt at 40 deg C must have a temperature below 63 deg C at engine inlet to ensure a viscosity above 2 cSt. Example: MGO with a viscosity of 5 cSt at 40 deg C is entering the engine at 50 deg C. The green curves show that the fuel enters ,the engine at approximately 4.0 cSt.Example: MGO with a viscosity of 1.5 cSt at 40 deg C needs cooling t o 22 deg C to reach 2 cSt.

  • 2009/04/01 MAN Diesel

    Viscosities of Marine Distillate Fuels

    Characteristic Unit Limit DMX DMA DMB DMC

    Density at 15C kg/m max. - 890.0 900.0 920.0

    Viscosity at 40C mm/s min. 1.40 1.50 - -Viscosity at 40C mm/s max. 5.50 6.00 11.0 14.0Flash point C min. - 60 60 60

    Sulphur %(m/m) max. 1.00 1.50 2.00 2.00

    Marine Distillate Fuels

    (LEE4/KID)

  • 2009/04/01 MAN Diesel

    Auxiliary SystemDiesel Oil Cooler in Fuel Oil System

    In order to ensure a satisfactory hydrodynamic film between fuel pump plunger and barrel MAN Diesel requires a minimum viscosity of 2 cSt of diesel oil at inlet to engine .

    Viscosity at 40C

    Temperature to obtain Viscosity of 2 cSt

    Temperature to obtain Viscosity of 3 cSt

    DMX 1.4 cSt 17.4C -3.0CDMA 1.5 cSt 21.9C 1.2C

    (LEE4/KID)

    Limit for Viscosity at Inlet to Engine

  • 2009/04/01 MAN Diesel

    Methods to deal with Low Sulfur fuel operation

    Fuel Coolers or Chillers

    Diesel Switch

  • 2009/04/01 MAN Diesel

    HFO system with MDO cooler

  • 2009/04/01 MAN Diesel

    Auxiliary SystemDiesel Oil Chiller in Fuel Oil System

    (LEE4/KID)

  • 2009/04/01 MAN Diesel

    DIESELswitch S

  • 2009/04/01 MAN Diesel

    DIESELswitch Retrofit

    Retrofit Solution:

  • 2009/04/01 MAN Diesel

    DIESELswitch

    Safely controlled change-over process

    Minimized risk of damaged fuel injection parts due to abrupt temperature changes

    The system will stop the change over process if the temperature increase/ decrease is too fast, and will give an alarm signal and freeze the actual position

    Change over running at full load possibleNo need to run engine with lowest power for change over process

  • 2009/04/01 MAN Diesel

    DIESELswitch

    Displays status of change over Displays remaining change over time Able to run the change over process manually or stop the process at any

    point Remote operation possible by second touch screen

  • 2009/04/01 MAN Diesel

    Advances in Emission Control.

    Methods of achieving upcoming Tier 2 and Tier 3 emissions regulations.

  • 2009/04/01 MAN Diesel 22

    Tier 2 and Tier 3 Proposal

    NOX reduction in a 2-step approach:

    Tier II - from 2011 achieved by in-engine measures 15-25% reduction Tier III - from 2016 using special NOX reduction methods 80% reduction

    from Tier I (only in defined Emission Control Areas (ECAs)).

    Other Emissions Regulation Potentials -

    Requirement to retrofit older vessels (pre Annex VI) initially back to 2000, and potentially back to early 1980s.

    For older vessels - 20% baseline reduction + hardware changes known to positively influence emission characteristics.

  • 2009/04/01 MAN Diesel 23

    Proposed NOX Limits

    3335627

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  • 2009/04/01 MAN Diesel 24

    History and Future for SFOC and NOx

    3334808.2007.04.10 (LSP/LB)

    Year

    SFOC g/kWh

    Ideal Carnot cycleFull-ratedDe-rated

    84VT2BF180K98FF

    KGF

    GB/GBEGFCA

    MC/MC-C

    NOxNOx

    g/kWh

    SFOC

    0

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    100

    150

    200

    250

    1940 1960 1980 2000 2020

    10

    20

    ME/ME-C

    2007

    ?

  • 2009/04/01 MAN Diesel

    Operators Demand Fuel Savings

    253336254.2008.12.16 LSP/GT

  • 2009/04/01 MAN Diesel 26

    Compliance with Expected IMO/EPA C3 Regulation 2 Stroke engines

    IMO Regulation Reduction methodTier 1 Current IMO Regulation

    NOx speed limit curve Fuel nozzle & performance

    optimization

    From 3 to 5% SFOC toleranceTier 2 15 to 25% NOx reduction (from Tier 1)

    PM & SOx reduction by fuel Sulfur content

    Fuel nozzle & performance optimization

    Slide valves mandatory

    CO2 & SFOC penalty 1-3%

    Tier 3 Up to 80% NOx reduction (from Tier 1)From Jan. 2016

    EGR, SAM, SCR

    CO2 & SFOC penalty

  • 2009/04/01 MAN Diesel 27

    Emission Control Effect and Cost

    Reduction capability First costin % of

    engine price

    Running cost index

    Tier 1 = 100NOx CO HC PM

    Primary methods

    Engine adjustments 10-15% 0%/Small 102

    SL & Alpha lube- - 0%/Small 101

    Water emulsion 20-30%- - 10-20% *) 101

    SAM 40-50% 20-30% *) 101

    Secondary methods

    SCR (Sel. Cat. Reduction) 80-98% ? ? ? 50-70% 110

    *) Depending on installation

  • 2009/04/01 MAN Diesel

    EGR WIF

    32

    1

    5

    6

    78

    4

    SCR

    Tier 3 Technologies

  • 2009/04/01 MAN Diesel

    10K98MC-C and 6S35MC on the same Testbed

    L/74236-1.0/0402 (3000/OG)

  • 2009/04/01 MAN Diesel 30

    Slide Valve Fuel Injection Nozzles

  • 2009/04/01 MAN Diesel 31

    7S50ME-C 75% LoadMode Change Demonstration

    L/74496-0.1/0903 (2430/NK)

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    16:37 16:38 16:39 16:40 16:41 16:42 16:43 16:44 16:45 16:46

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    2003-02-17

    140 150 160 170 180 190 200 210 220 2300 0

    20 100

    40 200

    60 300

    80 400

    100 500

    120 600

    140 700

    160 800

    CylinderPump

    2003-02-17

    140 150 160 170 180 190 200 210 220 2300 0

    20 100

    40 200

    60 300

    80 400

    100 500

    120 600

    140 700

    160 800

    CylinderPump

    Economy mode Low NOX mode

    Time

  • 2009/04/01 MAN Diesel 323331562.2006.11.22 (3001/LB)

    CIMAC Kyoto June 2004

    NOx reduction at 100% Load

    20

    40

    60

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    100

    120

    0 10 20 30 40

    Water content - % mass

    Ultrasonic HomogenizerHigh pressure mixer

    NOx reduction by Water Emulsification

    1% of water reducesNOX by 1%

  • 2009/04/01 MAN Diesel 33

    SCR System

    L/71835-9.0/0801 (2160/PZS)

    32

    1

    5

    6

    78

    4 Deck

    1 SCR reactor2 Turbocharger bypass3 Temperature sensor after SCR4 Large motors for

    auxiliary blowers5 Urea injector6 SCR bypass7 Temperature sensorbefore SCR8 Additional flange in exhaustgas receiver9) Best suited for steady high-load conditions with limited use of HFO

    C

  • 2009/04/01 MAN Diesel 34

    Scavenge Air Moisturing (SAM)

    L/73394-7.0/0902 (2430/NK)

    HAMunit High heat capacity and low O2

    in scavenge air give low combustion temperatures

    Humidification/moisturing of scavenge air increases heat capacity and lower the O2content

    Low combustion temperatures give low NOx

    SAM influence on NOx formation

    Influence on reliability and safety: Field test

  • 2009/04/01 MAN Diesel 35

    Water Stages on SAM System

    3333238.2005.11.09 (2432/PZS)

    Sea Water Inlet

    Sea Water Outlet

    FW Stage1 InletFW Stage1 Outlet

    FW Stage2 Inlet

    FW Stage2 Outlet

  • 2009/04/01 MAN Diesel

    EGR Exhaust Gas Recirculation

  • 2009/04/01 MAN Diesel

    EGR Exhaust Gas Recirculation

    3335239.2007.11.12 (LDF/NK)

    NOx Crossover eq. to -20% per 1g/kWh

    NOx/SFOC crossover

    -60-40-20

    020406080

    100120

    0 10 20 30EGR (%)

    R

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    0123456789

    R

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    hNOx

    SFOC

  • 2009/04/01 MAN Diesel

    MAN Diesel EGR Unit for MAN B&W Low Speed Engines

    Exhaust gas into EGR scrubber from exhaust gas receiver

    Exhaust gas out of EGR scrubber, into EGR cooler

    Cooling sea water to/from EGR cooler

    Exhaust gas out of EGR blower, into charge air pipe

    EGR Scrubber

    EGR Cooler

    EGR Blower

  • 2009/04/01 MAN Diesel 39

    Thank you for your Attention

    3334660.2007.01.05 (3000/OG


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