rafako logo
polish version
  • Advanced search
  • Site map
  • RSS
    • Mission
      Activity
      Management Board
      Company basic documents
      Quality, Environment, Safety
      Photo gallery
      Interesting links
    • Production of boiler components
      Boilers
      Enviroment protection plants
      Service
      References
      Heat exchangers
      Liquidation of stocks
      Order the publication
      Survey
    • Current events
      Press releases
      Company in media
      Contact for media
    • Justyna Kowalczyk
    • Events calendar
      Current reports
      Periodic reports
      Basic financial data
      Stock-exchange listing
      Authorities
      Shareholders
      Shareholders General Meetings
      Share information
      Corporate governance
      Stock analysts
      Contact data for investors
    • Jobs offers
      Application form
      konkurs
    • Contacts
      Contact form
      Road access
  • Products
  • Production of boiler components
  • Boilers
  • Enviroment protection plants
    • Flue gas desulphurisation
      • Dry method
      • Semi-dry method
      • Wet lime method
    • Thermal waste utilisation
  • Service
  • References
  • Heat exchangers
  • Liquidation of stocks
  • Order the publication
  • Survey
  • Home Page
  • Products
  • Enviroment protection plants
  • Flue gas desulphurisation
  • Dry method

Dry method

FSI (FURNACE SORBENT INJECTION) DRY METHOD.

This method consists in dozing of dry sorbents to furnace chamber. The range of dry sorbents includes:

  • limestone with CaC03 contents above 90%;
  • hydrated lime Ca(OH)2;
  • quicklime - CaO;
  • dolomite CaCO3 + MgCO3

Sorbent dozing methods:

  1. Direct mixing with coal (e.g. in the mill);
  2. Blowing into the furnace chamberaround the flame area;
  3. Blowing into the furnace chamber above the flame area (preferred method).
 

 

Dry flue gas desulfurization method (also called direct method) consists in absorption of sulfur by Ca0 originating from pulverized limestone, hydrated lime ordolomite. After its introduction into the furnace chamber, sorbent is decomposed, i.e. decarbonized or dehydrated in accordance with below described reactions:

CaCO3 + Q CaO + CO2
Ca(OH)2 + Q CaO + H2O

and then, lime reacts with SO2 in accordance with below described reactions:

CaO + SO2 CaSO3 + Q
CaO + SO2 + 1/2 O2 CaSO4 + Q

Dehydration occurs at a temperature above 400°C and decarbonization takes place at a temperature above 750°C. Hitherto gathered operating experience demonstrates that the introduction of pulverized limestone into the furnace chamber shall be done within the field of temperatures ranging from 780°C to 1200°C.

Temperature in sorbent injection area is one of the most important parameters determining the achievement of required desulfurization efficiency. Excessively high temperature may cause agglomeration of sorbent particles and intensify the reactions between CaO and minerals contained in coal. Dry method desulfurization efficiency is also affected by following parameters:

  • quantity of sorbent injected (Ca/S molal ratio);
  • sorbent milling quality;
  • alkaline metals contents in sorbent (sorbent purity);
  • alkaline metals contents in coal ash;
  • residence time (contact time) of sorbent particles in flue gas within the furnace chamber;
  • homogeneous mixing of sorbent with flue gas.

Optimisation of all above mentioned factors during the operation is not an easy task, thus, practically achievable dry method desulfurization efficiency amounts to 20 - 40% (maximum: 45%).

  • Print  |  Add to bookmarks
  • © RAFAKO S.A. | ul. Łąkowa 33 47-400 Racibórz | tel. +48 032 410 10 00 | info@rafako.com.pl
  • Legal notice | Privacy Policy | Created by ENIGMATIS POLSKA