Boiler combustion
Upcoming SlideShare
Loading in...5
×
 

Boiler combustion

on

  • 1,751 views

5 inch gauge Boiler Combustion

5 inch gauge Boiler Combustion

Statistics

Views

Total Views
1,751
Views on SlideShare
1,751
Embed Views
0

Actions

Likes
0
Downloads
43
Comments
0

0 Embeds 0

No embeds

Accessibility

Categories

Upload Details

Uploaded via as Microsoft PowerPoint

Usage Rights

© All Rights Reserved

Report content

Flagged as inappropriate Flag as inappropriate
Flag as inappropriate

Select your reason for flagging this presentation as inappropriate.

Cancel
  • Full Name Full Name Comment goes here.
    Are you sure you want to
    Your message goes here
    Processing…
Post Comment
Edit your comment

Boiler combustion Boiler combustion Presentation Transcript

  • Boiler Combustion (Simplified) Coal Fired MODEL LOCOMOTIVES
  • HEAT INTO POWER
    • Fuel and Air combustion :- Chemical Reaction
    • Mechanical work :- Useful Work
  • Solid Fuel (Coal)
  • Anthracite
    • Almost consist of pure carbon
    • Smokeless
    • Ignites with difficulty
    • Burns slowly
    • Requires a thin fire
    • Requires strong draft
    • The larger the grate-area the more efficient the combustion
    • Effective radiant heat properties
    • Generally contains low moister content (average 1 ½ %)
  • Dry Welsh steam coal
    • Semi Anthracite
    • Requires a reasonable forced draft
    • Contains high % of Carbon
    • Burns off % of volatile gases
    • Hydro-carbons produce a luminous flame
    • Excellent radiant heat transmitting properties
    • High heat value ratio compared with non-luminous gases
  • Bituminous
    • Low in carbon content
    • High in volatile matter (gases)
    • Generally high in moister content (average 7%)
    • Burns freely produces a long flame
    • Emits smoke if not carefully handled ie:-correct drafting techniques
    • Cakes becomes very pasty
    • Produces volatile hydro-carbons
  • Effects of impurities in Coal
    • Ash None combustible material in certain temperature conditions forms a semi- molten liquid (silicate of iron) Clinker
    • Sulphur Introduced to excessive heat is converted to Sulphide Dioxide (SO 2 )
    • When absorbed by water it forms Sulphurous Acid (H 2 SO 3 )
    • In certain circumstances can oxidise further to become Sulphuric Acid (H 2 SO 4 )
    • Chemically corrosive !!
  • COMPOSITION of AIR
    • 23 parts Oxygen :- 77 parts Nitrogen in every 100 parts of air by weight.
    • 21 parts Oxygen and 79 parts Nitrogen by volume.
  • Primary Air Secondary Air Primary Air Fire Box Air intake in fire box Blast nozzle blower ring
  • Three stages of combustion
    • Distillation of the coal gasses (hydrocarbons)
    • For complete combustion to burn gasses:-
    • Sufficient supply oxygen
    • Sufficient high temperatures
    • Solid fuel remains behind as (carbon)
  • Units of heat
    • 1 lb Carbon effectively consumed produces
    • carbon dioxide 14,600 B.Th.U.s
    • 1 lb Carbon incompletely consumed produces
    • carbon monoxide 4,400 B.Th.U.s
    • 1 lb Hydrogen burned to water vapour produces
    • 62,000 B.Th.U.s
  • Primary Air Below the fire bed
    • Combustion of the volatiles hydrogen ( H ) combines with the oxygen (O 2 ) and forms water vapour steam (H 2 O)
    • The oxygen combines with the carbon (C) burns off forming a colourless gas known as carbon dioxide ( CO2 )
    • Passing through the fire bed looses part of its oxygen unites with the upper layers of carbon (C) and forms carbon monoxide (CO)
  • Secondary Air Above the fire bed
    • Insufficient oxygen incomplete combustion
    • Heat losses 70%
    • Example :- carbon consumed to ( CO 2 )
    • 14,600 B.Th.U.s per 1lb
    • carbon unconsumed to ( CO)
    • 4,400 B.Th.U.s per 1lb
    • Carbon Monoxide (CO) vapours re-ignite at 1200ºF
  • Hydrocarbons 1200 º Carbon Dioxide Carbon Monoxide Damper Lever Front damper Rear damper Ash Air Oxygen and Nitrogen At 60 º F Carbon Dioxide Water Vapour Nitrogen 2000 ºF Ash pan Air Oxygen and Nitrogen 700 ºF Blast Nozzle Blower Ring Coal - Carbon - Hydrogen + Ash Complete combustion of the coal at high temperatures upwards of 2000 ºF Gasses cool down on passage through tubes EXOTHERMIC REACTION Fire hole door partially open Incandescent fire bed
  • Incomplete combustion showing miss management of the fire Air- Oxygen and Nitrogen at 60 ºF Fire hole door fully open Holes in the fire bed Drop in fire box temperature Uneven thick fire bed Heat losses up to 70 % Clinker grate area reduced impeding draft
  • Deflector plate Stainless steel arch Promotes combustion absorbs the heat from the volatile gasses before being discharged reduces temperature drop Directs the path of air Other uses' of absorbing heat Volatile gasses
  • Combustion chamber Shortened tube length improved heat transfer Volatile gases Combustion chamber Larger heating service