Plant Name

 

 

Unit Name

 

 


1. Boiler Manufacturer

 
 
 

Company Supplier

 

Gross Capacity

 

 

Max. Continuous

 

Rate, Ton (steam) /hr

 


Main Steam Parameters

 

Pressure, Bar

 

Temperature ©

 

Flow Rate, ton/hr

 


1st. Reheat Steam Parameters

Pressure, Bar

 

Temperature ©

 

Flow Rate, ton/hr

 


2nd. Reheat Steam Parameters

Pressure, Bar

 

Temperature ©

 

Flow Rate, ton/hr

 


2. Boiler Configuration

FURNACE

 

 

a. Wall Design(Monowall Tubes)

 

b. Width, m

 

c. Depth, m

 

d. Height m (from Hopper Knuckle)

 


FURNACE NOSE

 

 

a. Projected Height, m

 

b. Base, m

 

c. Elevation, m (from Hopper Knuckle)

 


DIVISION WALLS

 

 

a. Height, m

 

b. Depth, m

 

c. Number of Division Walls

 


RADIANT SUPERHEATER

a. Orientation (Horiz./Vert.)

 

b. Height, m

 

c. Width, m

 

d. Number of Panels

 


CERAMIC LINING (Tiles)

 

a. Furnace Walls Coverage, %

 

b. Furnace Floor Coverage, %

 


3. Fuel & Handling System

 

 

COAL

 

 

a. Fuel Origin(S)

 

b. Coal Mill Manufacturer

 

c. Model Name

 

d. Mill Type

 

e. Number of Mills

 

f. Number of Burners (per Mill)

 

g. Mill Capacity Ton/hr

 

h. Pulverized Fuel Storage

 

Yes No

i. Classifier Type(s)

 

Static

Static Adjustable

Dynamic

J. Mill Pressure(Positive Vacuum)

 

K. Seal Air Flow (per mill kg/hr)

 


Typical Composition

 

 

l. Carbon, %wt

 

m. Hydrogen, %wt

 

n. Sulfur, %wt

 

o. Nitrogen %wt

 

p. Oxygen %wt

 

q. Moisture %wt

 

r. Ash %wt

 

s. HHV MJ/kg

 

t. Volatile Matter %wt

 

U. Fixed Carbon %wt

 


LIQUID FUEL

 

 

a. Fuel Origin(s)

 

b. Pump Fuel Pressure

 

c. Fuel Pressure at Burners

 

d. Fuel Recirculation @ Burners

 

Yes No


Typical Composition

 

 

a. Carbon %wt

 

b. Hydrogen %wt

 

c. Sulfur %wt

 

d. Nitrogen %wt

 

e. Oxygen %wt

 

f. Moisture %wt

 

g. Ash %wt

 

h. HHV, MJ/kg

 

I. Volatile Matter %wt

 

j. Fixed Carbon %wt

 


GASEOUS FUEL

 

 

a. Plant Pressure, Bar

 

b. Burner Pressure, Bar

 

c. Fuel Origin

 

d. HHV, MJ/m3

 


Approximate Composition, % vol.

 

 

Methane, CH4

 

Carbon Dioxide, CO2

 

Ethane, C2H6

 

Sulfur Dioxide, SO2

 

Propane, C3H8

 

Ammonia, NH3

 

n-Butane+Isobutane, C4H10

 

n-Pentane+Isopentane, C5H12

 

Acetylene, C2H2

 

Ethylene, C2H4

 

Propylene, C2H6

 

Hydrogen Sulfide, H2S

 

Nitrogen, N2

 

Hydrogen, H2

 

Carbon Monoxide, CO

 


BURNERS & RELATAED EQUIPMENT

Burner Design

 

No fo Air Registers

 

Adjustable Vanes (Axial or Radial)

 

Burner/Overfire Air Pports (OFA) Matrix
Single Wall Fired

 

Yes No


FRONT WALL

 

 

No of Burners in Columns

 

No of Burners in Rows

 

Columns

 

Distance Between Rows

 

Distance from the Burner Axis

 

To Hopper Knuckle

 

To Side Wall

 

No of OFAs in Column

 

No of OFAs in Row

 

Distance between OFA Axis
In Column(s)

 

Distance between OFA Axis
In Row(s)

 

Distance between Bottom Row

 

To Hopper Knuckle

 


Boundary Air Port Location

 

 

 

 

 


* Similar Data Required for REAR WALL


IGNITORS

 

 

Supplier

 

Fuel Oil/Gaseous/High Voltage

 

Retractable of Stationary

 

Purge Air Pressure

 

Spark Voltage KV

 

Installation (Air Register, Water Walls
Coal Injector)

 

Scanner Type

 


Main Scanners

 

 

Supplier

 

Type (optical, ionization, etc.)

 

Burner Management
System Supplier

 


GASEOUS EMISSIONS OPERATIONS

Current Annual Emissions as Reported

 

Sulfur Dioxide

 

Carbon Monoxide

 

NOx

 

Particulate Matter

 

Mercury, kg/yr

 


Current Allowable Emissions
Rate, kg/hr or ppm

Sulfur Dioxide

 

Carbon Monoxide

 

NOx

 

Particulate Matter

 

Mercury, kg/yr or ppm

 


FUEL PURCHASES (annual)

Fuel Oil m/Tons

 

Coal m/Tons

 

Orimulsion m/Tons

 

Gas cu/meters

 

Other

 

 

 




     
   

International Industries Inc.
1421 Sheepshead Bay Road #272
Brooklyn, NY 11235 U.S.A.

Tel. 917-213-4265
E-mail internind@aol.com