Скачать презентацию Seminar on Environmental Requirements for Commercial and Navy Скачать презентацию Seminar on Environmental Requirements for Commercial and Navy

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Seminar on Environmental Requirements for Commercial and Navy Ships for Efficient Maritime Operations and Seminar on Environmental Requirements for Commercial and Navy Ships for Efficient Maritime Operations and Effective Environmental Stewardship Exhaust Gas After Treatment Wilson Chu Global Business Development Manager Johnson Matthey Hyatt Regency Atlanta, GA December 9, 2009

Marine Emissions Control – Market Drivers and Control Technologies Current • Norway NOx Tax Marine Emissions Control – Market Drivers and Control Technologies Current • Norway NOx Tax • Swedish Fairways Dues • Green Supply DOC and DPF to Reduce PM Current and Future • DERA • Voluntary SCR to Reduce NOx Future • EPA Cat. 1 & 2 NSPS • IMO ECA – Cat. 3 Marine Emissions Oxicat To Reduce CH 4 Scrubber To Reduce SOx Future • IMO ECA • Fuel Standards Future • GHG

Emission Control Technologies SCR (Selective Catalytic Reduction) for NOx Emission Control Technologies SCR (Selective Catalytic Reduction) for NOx

SCR Applications Power Plants Gas Turbines Waste Incineration Plants Heavy Duty Vehicles SINOx® Products SCR Applications Power Plants Gas Turbines Waste Incineration Plants Heavy Duty Vehicles SINOx® Products Wood-Fired Boilers Stationary Engines Marine Engines

SCR Catalyst Operating Temperatures 400°F 600°F SINOx® Low Temperature Catalyst 800°F Standard SINOx® Catalyst SCR Catalyst Operating Temperatures 400°F 600°F SINOx® Low Temperature Catalyst 800°F Standard SINOx® Catalyst 1000°F SINOx® High Temperature Catalyst Simple Cycle Gas Turbines Marine IC Engines Combined Cycle Power Plants Typical High Dust Applications in Power Plants Tail End Applications in Power Plants, Waste Incinerations 200°C 350°C Operating Temperature 550°C

SCR Process NOX NH 3 Basic Reactions 4 NO + 4 NH 3 + SCR Process NOX NH 3 Basic Reactions 4 NO + 4 NH 3 + O 2 à N 2 + 6 H 2 O 4 6 NO 2 + 8 NH 3 à N 2 + 12 H 2 O 7 Undesired Parallel Reactions SO 2 + 1/2 O 2 à 3 SO NH 3 + SO 3 + H 2 O à 4 HSO 4 NH N 2 H 2 O

SINOx®: Coated Honeycomb SCR l High specific surface area l High activity in low-dust SINOx®: Coated Honeycomb SCR l High specific surface area l High activity in low-dust flue gases (low volume) l Optimised pressure drop (thin metallic walls) l Variable length and number of cells (100 -400 cpsi) l Low-dust flue gas applications (high-grade coal, oil, gas, diesel or WIP applications)

SINOx®: Extruded Honeycomb SCR l High specific surface area l High activity in low-dust SINOx®: Extruded Honeycomb SCR l High specific surface area l High activity in low-dust flue gases (low volume) l Optimised pressure drop l Variable length and number of cells (6 -300 cpsi) l Low-dust flue gas applications (high-grade coal, oil, gas, diesel or WIP applications)

SINOx®: Coated Plate SCR l Variable pitch, minimal dust deposition l High erosion, poison SINOx®: Coated Plate SCR l Variable pitch, minimal dust deposition l High erosion, poison resistance l Low pressure drop l Plate-to-plate clearance, variable SSA l High-dust flue gas and special applications (coalfired, industrial processes & refinery power plants)

Typical Engine SCR Layout l SCR Catalyst l Catalyst Reactor Housing l Mixing Duct/Static Typical Engine SCR Layout l SCR Catalyst l Catalyst Reactor Housing l Mixing Duct/Static Mixers l Injection Lance l Reductant Dosing & Control System l NOx Analyser (optional) l Soot Blower (optional not shown) l Reductant Tank

Typical SCR Installation on an OGV SCR System Engine Pipe Silencer Exhaust Typical SCR Installation on an OGV SCR System Engine Pipe Silencer Exhaust

SCR Catalyst Reactor SCR Catalyst Reactor

SCR Catalysts Extruded Honeycomb SCR Catalyst SCR Catalysts Extruded Honeycomb SCR Catalyst

SCR Catalyst and Soot Blowers Soot blowing system: l Compressed air (only) in combination SCR Catalyst and Soot Blowers Soot blowing system: l Compressed air (only) in combination with solenoid valves l Recommended for applications with high particle concentration (or special high dust application) l Developed for use in conjunction with the multilayer concept with reduced air consumption (10 -20 Nm 3/h)

Urea Dosing & Control System Dosing Panel Dosing Pump Station Urea Dosing & Control System Dosing Panel Dosing Pump Station

Emission Control Technologies DPF and DOC for Reducing Diesel Particulate Emission Control Technologies DPF and DOC for Reducing Diesel Particulate

Diesel Particulate Matter (PM) Vapour Phase Hydrocarbons Solids (SOL) Solid Carbon Spheres (0. 010. Diesel Particulate Matter (PM) Vapour Phase Hydrocarbons Solids (SOL) Solid Carbon Spheres (0. 010. 08 mm dia) combine with Adsorbed Hydrocarbons to make Particle Agglomerates (0. 05 -1. 0 mm dia) Soluble Organic Fraction (SOF) / Particle Phase Hydrocarbons Adsorbed Hydrocarbons Liquid Condensed Hydrocarbon Particles Sulphate with Hydration Courtesy of SAE® Sulphate (SO 4)

DPF (Diesel Particutale Filter) DOC (Diesel Oxidation Catalyst) DOC CRT® (Continuosly Regenerating technology) • DPF (Diesel Particutale Filter) DOC (Diesel Oxidation Catalyst) DOC CRT® (Continuosly Regenerating technology) • DPF – >85% PM reduction • DOC – Typical 25% PM reduction • ULSD required

DPF Applications Off Road Equipment Trucks CRT® Products Stationary Engines Locomotives Buses DPF Applications Off Road Equipment Trucks CRT® Products Stationary Engines Locomotives Buses

Emission Control Technologies Methane Oxidation Catalyst Emission Control Technologies Methane Oxidation Catalyst

Methane Oxidation Catalysts • Development of new catalysts required to improve low temperature activity Methane Oxidation Catalysts • Development of new catalysts required to improve low temperature activity and extend catalyst life

Emission Control Technologies SOx Scrubbing System Emission Control Technologies SOx Scrubbing System

Scrubber System Retrofit • Achieves >97% reduction in SO 2 • Sea water intake Scrubber System Retrofit • Achieves >97% reduction in SO 2 • Sea water intake and discharge • Fuel cost savings STEAM COIL FOR PLUME SUPPRESSION SEAWATER DISCHARGE 11, 349 kw DIESEL ENGINE

Johnson Matthey Marine Emissions Control Experience Johnson Matthey Marine Emissions Control Experience

Johnson Matthey Marine SCR and DOC Emissions Control Experience NOx Control (SCR) • 52 Johnson Matthey Marine SCR and DOC Emissions Control Experience NOx Control (SCR) • 52 Ocean Going Vessels • 162 SCR systems • Category 3 Diesel Engines • Boilers • APU Fuel: HFO, MDO And Diesel PM Control (DOC) • NY Water Taxi Fuel: ULSD

Staten Island Ferry - NYC Transit Alice Austen Staten Island Ferry Engines: Exhaust gas Staten Island Ferry - NYC Transit Alice Austen Staten Island Ferry Engines: Exhaust gas flow Temperature: NOx Reduction: SCR installed: 2 x CAT 3516 A 8507 ACFM 752°F < 3 g/k. Wh (~ 70%) 2004

New York Water Taxi • Seaworthy Systems, Inc. • 600 Hp Detroit Diesel Series New York Water Taxi • Seaworthy Systems, Inc. • 600 Hp Detroit Diesel Series 60 engine • DOC • 25% PM reduction • Direct muffler replacement • Installed 2006 Courtesy New York Water Taxi

LNG Carrier, Norway Project: „Golar Spirit“ SINOx® Installed: 2008 Application: 2 x Regas Boiler LNG Carrier, Norway Project: „Golar Spirit“ SINOx® Installed: 2008 Application: 2 x Regas Boiler (77 t/h) Exhaust Gas Flow: 70. 100 Nm³/h Fuel: LNG/HFO Temperature: 290°C Catalyst Type: Catalyst Volume: Exhaust NOx: NH 3 Slip: SW 30 Honeycomb 24, 12 m³ 180 mg/Nm³ 5 mg/Nm³

LNG Carrier, Belgium Project: SINOx® Installed: Exhaust Gas Flow: Application: Fuel: Temperature: Urea Consumption: LNG Carrier, Belgium Project: SINOx® Installed: Exhaust Gas Flow: Application: Fuel: Temperature: Urea Consumption: 2 x LNG Carrier, Exmar „Ecellence/Excelerate“ 2007 2 x 70. 100 Nm³/h 2 x 70 t/h Regas Boiler (each) HFO/MDO 380°C 40 % Catalyst Type: Catalyst Volume: Exhaust NOx : SW 30 Honeycomb 10, 62 m³ 30 mg/Nm³

Merchant Vessel, Sweden Project: „MS Timbus“ SINOx® Installed: 1999 Ma. K 8 M 32 Merchant Vessel, Sweden Project: „MS Timbus“ SINOx® Installed: 1999 Ma. K 8 M 32 (Main)/ MAN 6 L 16/24 (Aux. ) 3, 840 k. W / 540 k. W (Aux. ) 21, 000 / 3, 000 Nm 3/h HFO / MDO 320 / 336° C 97 / 8 l/h (@40%) Type Power Exhaust Gas Flow Fuel Temperature Urea Consumption : Catalyst Type SW 30 Honeycomb Catalyst Volume 3 m³/engine (Main) 0. 4 m³/engine (Aux. ) Exhaust NOx: 2 g/k. Wh

Supply Vessel Work Ship Project: Exhaust gas flow: Engine type: Fuel: Temperature: SINOx® Installed: Supply Vessel Work Ship Project: Exhaust gas flow: Engine type: Fuel: Temperature: SINOx® Installed: „Supply Vessel/Work ship“ Kleven 52. 290 m³/h 2 x MAN 6 L 32/40, 2 x MAN 8 L 21/31 MGO 335° C 2007 Catalyst type: Catalyst volume: NOx Reduction: SW 40 3, 8 m³ 2 g/k. Wh

Contact Us Wilson Chu Johnson Matthey chuw@jmusa. com 484 -320 -2119 Contact Us Wilson Chu Johnson Matthey chuw@jmusa. com 484 -320 -2119