1 / 17

BULK CONVEYOR SPECIALIST, INC.

SO3 Production in Boilers . All S converted into SO2 during combustionA part of SO2 is further oxidised into SO3 according to 3 mechanisms :Oxidation of SO2 by atomic O in the furnace Homogeneous oxidation of SO2 by molecular O2 Catalytic oxidation of SO2 by molecular O2 on ashes (400-700

heba
Download Presentation

BULK CONVEYOR SPECIALIST, INC.

An Image/Link below is provided (as is) to download presentation Download Policy: Content on the Website is provided to you AS IS for your information and personal use and may not be sold / licensed / shared on other websites without getting consent from its author. Content is provided to you AS IS for your information and personal use only. Download presentation by click this link. While downloading, if for some reason you are not able to download a presentation, the publisher may have deleted the file from their server. During download, if you can't get a presentation, the file might be deleted by the publisher.

E N D

Presentation Transcript


    1. BULK CONVEYOR SPECIALIST, INC. SO2/SO3 MITIGATION SYSTEMS

    2. SO3 Production in Boilers All S converted into SO2 during combustion A part of SO2 is further oxidised into SO3 according to 3 mechanisms : Oxidation of SO2 by atomic O in the furnace Homogeneous oxidation of SO2 by molecular O2 Catalytic oxidation of SO2 by molecular O2 on ashes (400-700°C)

    3. SO3 Control/Removal

    4. INJECTION LOCATIONS Economizer Outlet (~600 - 700F) SO2 Trona Air Heater Inlet (~600F) SO2 Trona, SO3 Trona Air Heater Outlet (~300F) SO2 Trona & Hydrated Lime SO3 Trona & Hydrated Lime Economizer Inlet (~700 - 750F) SO2 Trona

    5. TRONA VS LIME

    6. TESTING PERFORMED TVA WIDOWS CREEK-LIME SO3/OPACITY TVA PARADISE LIME-TRONA S02/S03 TVA CUMBERLAND-LIME SO3 TVA BULL RUN- LIME SO3 RELIANT CHESWICK-LIME SOUTHERN COMPANIES BOWEN LIME-TRONA SO2 SOUTHERN COMPANIES GASTON-TRONA SO2 MIRANT POTOMAC RIVER –TRONA SO2 KENTUCKY UTILITIES GHENT LIME-TRONA SO3 LG&E TRIMBLE LIME-TRONA SO3 SEMINOLE ELEC-PALATKA- LIME SO3 PRIMARY ENERGY-TRONA SO2

    7. BCSI TEST TRAILER SYSTEM TRAILER SYSTEM INSTALLED AND OPERATING MINIMAL SPACE REQUIRED CAPABLE OF CONTINUOUS OPERATION NO PERMITTING REQUIRED NO FOUNDATIONS REQUIRED

    8. BLOWER TRAILER 3 BLOWER TRAINS VARIABLE SPEED MONITOR FLOW, TEMP AND PRESSURES PLC CONTROLLED

    9. BCSI PERMANENT SYSTEM COMPLETE SILO SYSTEM WITH ALL COMPONETS PRE INSTALLED AND PREWIRED FOR EASE OF INSTALLATION MINIMAL SPACE REQUIREMENTS PLC/ COMPUTER CONTROLLED EASE OF OPERATION MINIMAL MAINTENANCE COMPLETE DATA STORAGE FOR LIME INJECTION CONTROL

    10. BCSI EXPERIENCE PERMANENT SYSTEM IN OPERATIONFOR 3 YEARS, 24/7/365 OVER 30 TESTS FOR SO3 AND S02 MITIGATION USING VARIOUS SORBENTS KNOWLEDGE OF INJECTION TECHNIQUES DRY INJECTION NOZZLE DESIGN TO ENHANCE MATERIAL DISTRIBUTION 25 YEARS OF MATERIAL HANDLING EXPERIENCE WITH LIME AND SODIUM PRODUCTS. OVER 150 LIME AND SODA ASH SYSTEMS OPERATING KNOWLEDGE OF POWER PLANT OPERATION AND REQUIREMENTS FOR SO2 AND SO3 REMOVAL KNOWLEDGE OF PLANT LAYOUTS AND REQUIREMENTS FOR INJECTION AND REMOVAL

    11. WHAT DOES BCSI BRING TO THE TABLE EXPERIENCE IN HOUSE DESIGN AND ENGINEERING IN HOUSE FABRICATION IN HOUSE ELECTRICAL DESIGN, PANEL BUILDING AND CONTROL PROGRAMMING IN HOUSE EXPERIENCE ON SO3 MITIGATION CAPABILITY TO DO TURNKEY PROJECT INCLUDING: ACTUAL MATERIAL TESTING MODELING ENGINEERING FABRICATION GUARANTEES ON STOICH DESIGN INSTALLATION STARTUP

    12. CRITICAL SO3 CONTROL PARAMETERS DUCT AIR TEMPERATURE (290 TO 340 F) DUCT VELOCITY (MINIMUM 2000 FPM) MULTIPLE INJECTION LOCATIONS (BEFORE AND AFTER ESP) MULTIPLE INJECTION LOCATIONS PER DUCT VARIABILITY OF INSERTION LENGTH OF NOZZLES INTO DUCTS MONITORING OF NOZZLES FOR PLUGGAGE

    13. WEIGH HOPPERS FOR CONTROL OF FEED RATES GUARANTEES FLOW DATA AND FLOW OF MATERIAL

    18. TYPICAL NOZZLE DESIGN

More Related