Gujarat Industrial Development Corporation Tender

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Gujarat Industrial Development Corporation - GIDC Tender

Works
Civil And Construction
Energy, Oil and Gas
Civil Works Others
Consultancy Services
Civil And Architectural Services
Opening Date18 Nov 2024
Closing Date9 Dec 2024
Tender Amount₹ 3,94,10,00,000 
Notes
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Costs

Summary

Work of Engineering, Procurement, Construction (EPC) with Commissioning including testing and O&M&R for setting up of Common Steam Plant -

Description

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BOQ Items

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DO_NOT_SHOW

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Type of support

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No. of Boilers

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Boiler design code

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Boiler Predicted Performance

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No of Boilers

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Boiler Capacity (MCR)

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Peak Capacity of Boiler

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Steam temperature at Superheater outlet

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Superheated steam control range

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Steam pressure at superheater outlet

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Minimum continuous rating of the Boiler with automatic controls

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Feed water temperature at Economiser inlet

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Excess air

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Oxygen content in flue gas at Boiler outlet

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Boiler efficiency based on G.C.V with 100% Imported coal

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Fuel consumption

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Lime stone consumption with 100% Imported coal and 70% Imported + 30% Biomass

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Sox in the flue gas : Without lime dosing

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Sox in the flue gas for 100 % Imported : With lime dosing

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Sox in the flue gas with 70 % Imported+30% Biomass : With lime dosing

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Boiler design for firing other fuels 100% Imported coal and 70% Imported + 30% Biomass on heat basis

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Breakup Losses Breakup Losses Breakup Losses

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a. Unburnt carbon loss

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b. Sensible heat loss through ashes

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c. Dry flue gas loss

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d. Loss due to moisture and Hydrogen in fuel

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e. Loss due to moisture in Air

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f. Radiation Loss

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g. Other loss - Manufacturer’s Margin

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h.Unaccounted loss

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i. Total losses

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Flue Gas Temperature Flue Gas Temperature

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a. Furnace temperature

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b. Economiser inlet

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c. Airpreheater inlet

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d. Airpreheater outlet

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e. APH outlet temperature with Petcoke firing

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f. ESP outlet

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g. Chimney outlet

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Water Temperature

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a. Economiser inlet

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b. Economiser outlet

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Ciculation ration of water

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Air Temperature leaving Airheater

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Air Pressure at

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a. FD Fan outlet

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b. Airheater inlet

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c. Airheater outlet

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d. Airbox

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e. PA Fan inlet

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f. PA Fan header

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Flue Gas Pressure at

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a. Furnace outlet

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b. Superheater inlet

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c. Superheater outlet

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d. Economiser outlet

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e. Airheater inlet

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f. Airheater outlet

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g. ESP inlet

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h. ESP outlet

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i. ID fan inlet

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j. ID fan outlet

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Flue Gas Velocities

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a. Fluidised bed

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b. Furnace

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c. Primary Superheater

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d. Secondary Superheater

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e. Economiser

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f. Air Preheater

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Water Velocities

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a. Economiser

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b. Feed water line

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Steam velocities

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a. Primary superheater

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b. Secondary Superheater

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c. Main steam line

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Steam Pressure Profile

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a. At main steam stop valve

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b. Superheater safety valve set pressure

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c. Pressure drop across Primary Superheater

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d. Drum Safety valve I set pressure

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e. Drum Safety valve II set pressure

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Auxiliary Power Consumption at MCR condition at MCC

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Provided Heat Transfer Areas

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a. Bed coil (Area is considered without ss studs. Bed coils are with SS studs)

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b. Furnace

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c. Primary Superheater

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d. Secondary Superheater

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e. Economiser

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Boiler bank

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pressure part area

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f. Air pre heater

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g. Total area

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Boiler Construction Details

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Drums

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a. Internal diameter

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b. Drum shell material

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e. Drum dished end thickness

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c. Drum dished end material

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d. Type of drum support

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e. Drum operating pressure at MCR

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f. Drum Design pressure

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g. No. of Direct level gauges on drum

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h. Type of Steam Drier / Separator provided

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Bed Tube Assembly

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a. Type of tube arrangement

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b. Tube size (OD x T)

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c. Bed Tube material

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d. Header size (OD x T)

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e. Pitch

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f. Stud material

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Water wall Assembly

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a. Type of construction

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b. Tube size (OD x T)

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c. Tube material

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d. Header Size (OD x T)

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e. Header material

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f. Fin material and thickness

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g. Water wall size (L x W)

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h. Water Wall height from Bottom Header to Top Header

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Convection Superheater

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Primary Superheater

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a. Type of flow

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b. Arrangement

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d. Tube size (OD x T)

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e. Tube material

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f. Inlet Header material

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g. Tube pitch arrangement

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Secondary Superheater

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a. Type of flow

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b. Arrangement

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d. Tube size (OD x T)

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e. Tube material

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f. Header Size ( OD X T )

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g. Inlet Header material

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h. Tube pitch arrangement

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Desuperheater

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a. Type

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b. Number

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c. Material of pipe

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Economiser

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a. Tube size (OD x T)

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b. Tube material

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c. Header size (OD x T)

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d. Header material

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e. Casing material

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Soot Blowers (Motorised)

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a. Economiser zone Rotory type

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b. SH Zone, Long rectractable

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PRDS I , (for HP steam)

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a. Inlet pressure

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b. Inlet temperature

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c. Outlet pressure

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d. Outlet temperature( Tentative)

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e. Outlet steam quantity (Tentative)

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PRDS II , (for LP steam)

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a. Inlet pressure

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b. Inlet temperature

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c. Outlet pressure

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d. Outlet temperature( Tentative)

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e. Outlet steam quantity (Tentative)

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PRDS III . (Process steam bypass)

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a. Inlet pressure

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b. Inlet temperature

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c. Outlet pressure

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d. Outlet temperature( Tentative)

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DSH for Process steam

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e. Outlet steam quantity (Tentative)

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Airheater

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a. Arrangement and type

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b. Tube size (OD x T)

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c. Tube material

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d. Flow medium

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• Inside tubes

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• Outside tubes

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e. No. of blocks of Airheater

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f. APH Dampers (Manual)

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Fluidised Bed

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a. Fluidised bed size

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b. Bed area / Compartment

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c. No. of Compartments

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d. Bed plate material

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e. Bed plate size (L x W)

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f. Fuel Nozzle material

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g. Fuel Nozzle cap material

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h. No. of fuel Nozzles / Compartment

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i. Material of Air Nozzle

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j. Recommended fuel particle size at the inlet of furnace (mm)

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k. No. of ash drain pipes /Compartment

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l. Ash drain pipe material

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Fuel Feeding System

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a. Type of feeders

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b. Location

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c. Number of feeders

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d. Feeder Drive Rating

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Overbed feeder Loading

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e. Type of feed control system

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f. Method of feed rate adjustment

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g. Method of feed rate adjustment

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h. Feeder motor capacity

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Ducting Specification

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a. Material of construction

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b. Thickness (mm)

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c. Blowdown Tank (common for CBD& IBD)

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d. Material

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Sample cooler

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a. Type

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b. Sampling Points

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c. MOC of Shell

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d. MOC of Coil

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Online SWAS for Ph and conductivity only

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Feed Water Pumps (1W + 1S)

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a. Pump Type

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b. Fluid Temperature

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c. Rated Flow

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d. Differential head at rated Condition

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e. Speed

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f. Recirculation type

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g. Intermediate low stage bleed for desuperheter.

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DEAERATOR CUM STORAGE TANK

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Deaerator

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a. Type

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b. Design standard

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c. Storage capacity - from NL to LL

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Design Conditions

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a. Deaeration capacity

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b. Design temperature

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c. LP Steam pressure at pressure control valve inlet

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d. LP steam temperature @ ( º C) :pressure control valve inlet

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e. Temperature of incoming water

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f. Deaerated Water temp.

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g. Dissolved Oxygen in Deaerated water

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h. Quantity of Steam required

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i. Corrosion Allowance considered

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j. Storage for normal capacity between NWL & LWL (Min 20 minutes storage)

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k. support type

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l. MOC of Shell,Dishedend & storage tank

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m. MOC of Pipe nozzles

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n. MOC of spray nozzle /trays

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o. Internals

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p. Piping between transfer pump and feedpump

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FANS - 10% extra capacity for flow and Head.

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a. Quantity/Boiler

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b. Flow at MCR ( margin of 20% extra on MCR)

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c. Flow at Test Block (TB)

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d. Head at MCR

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e. Head at Test Block (TB)

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f. SPEED

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g. DRIVE ( with star delta changeover system)

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CHEMICAL DOSING SYSTEM

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a. Type of system

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b. Tank Capacity

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c. Tank/Piping Material

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e. Type of stirrer

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f. Type of pump

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g. No. of pumps

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h. Capacity of the pump

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i. Head developed by pump

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j. Motor rating

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k. Chemical to be dosed

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FUEL STORAGE BUNKER

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a. No. of Bunker

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b. Type

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c.Material to be stored

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d.Material of construction

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e.Storage volume of the bunker

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f. Discharge gate type

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g. SS Lining in Bunker Conical portion Considered

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g. SS Lining in surge Considered

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h. Thickness of Lining

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i. Top cover (Chequered plate)

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j. Supports

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k. Valley angle (Degrees)

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BED MATERIAL HANDLING SYSTEM

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a. Bed material bunker

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b. Bed material handling system

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LIMESTONE HANDLING SYSTEM

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a. Limestone material bunker

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b. Limestone handling system

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ELECTRO STATIC PRECIPITATOR

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a. Type

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b. Number of precipitator/Boiler

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c. Number of gas path

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d. Number of Electrical fields in series, in the direction of gas flow

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e. Space between the centres of collecting Electrodes across the gas path

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f. Nominal width x height of collecting electrodes per field, in the direction of gas flow

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g. Nominal lengths of collecting electrodes per field, in the direction of gas flow

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h. Total effective collecting area provided

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i. Total number of HV TR units

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j. Rating of each HV TR units

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a). Collecting electrode plate

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b). Emitting electrode

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l. Flue gas flow

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m. Gas inlet temperature

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n. Inlet dust concentration (dry basis)

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o. Collecting efficiency with all the fields in service

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p. Collection efficiency with one field out of service

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q. Outlet dust concentration 100 % Imported and 70%Imported+30% Lignite mix.

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q. Outlet dust concentration with lime dosing 100 % Imported and 70%Imported+30% Lignite mix.

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r. Guaranteed outlet dust concentration with First field out of service

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s. Total power consumption of the ESP system for all fields

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t. Specific collecting area

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v. Casing thickness

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w. Insulation material and density

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x. Cladding material and thickness

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y. Remote indication for KV and mA provided through transducer for each TR of Rectifier unit

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z.ESP MCC/Rapper control panel/ TR set control panel bided

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All safety interlocks for HV bus system and earthing switch considered/supplied

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Predicted Boiler performace at various load for different fuel mix.

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