Materials Flows and Investment Costs of Flue Gas Cleaning Systems of Municipal Solid Waste Incinerators

Achternbosch, M.; Richers, U.
Karlsruhe: Forschungszentrum Karlsruhe 2002
(Wissenschaftliche Berichte, FZKA 6726)



Contents

 
1    Introduction 1
2    Focus of Work 2
3    Technology for Combustion 4
4    Chemical Engineering for Flue Gas Cleaning 5
  4.1 Introduction 5
  4.2 Fly Ash Separation 6
    4.2.1 Cyclone 7
    4.2.2 Fabric Filter 7
    4.2.3 Electrostatic Precipitator 8
    4.2.4 Comparison of Separators 10
  4.3 Separation of acid pollutants 11
    4.3.1 Dry Flue Gas Cleanaing 11
    4.3.2 Semi dry Separation 13
    4.3.3 Wet Separation 13
  4.4 Removal of nitrogen oxides 16
    4.4.1 SCR Process 16
    4.4.2 SNCR Process 19
  4.5 Other Flue Gas Cleaning Methods 20
    4.5.1 Carbon Adsorber 20
    4.5.2 Entrained flow reactor 21
    4.5.3 Dosing of coke 22
    4.5.4 Oxidation Catalyst 22
 
5    Description of the Model Plant 24
  5.1 Furnace and Boiler 24
  5.2 Selection of balanced flue gas cleaning systems 26
 
6    Description of the Balancing Method 29
  6.1 System boundary 29
  6.2 Substances Balanced 30
  6.3 Sources of the Data Used for Materials Balancing 32
  6.4 Procedure 32
    6.4.1 Fly Ash Separation 33
    6.4.2 Wet Flue Gas Cleaning 36
    6.4.3 Semi Wet Flue Gas Cleaning 37
    6.4.4 Semi Dry Flue Gas Cleaning 38
    6.4.5 Stoichiometric Ratio 38
    6.4.6 Other Separation Units - Fine Cleaning 39
    6.4.7 Clean Gas Data 41
 
7    Balances of the Flue Gas Cleaning Systems 43
  7.1 Model Plant "wet 1" 43
  7.2 Model Plant "wet 2" 48
  7.3 Model Plant "wet 3" 52
  7.4 Model Plant "wet 4" 57
  7.5 Model Plant "wet 5" 60
  7.6 Model Plant "wet 6" 65
  7.7 Model Plant "semi wet 1" 70
  7.8 Model Plant "semi wet 2" 74
  7.9 Model Plant "semi dry 1" 76
  7.10 Model Plant "semi dry 2" 80
 
8    Use of Auxiliary Chemicals in the Model Plants 83
  8.1 The Neutralization Agents NaOH and Ca(OH)2 83
  8.2 Coke-containing Auxiliary Chemicals 84
  8.3 Heavy-metal Precipitant TMT-15TM 84
  8.4 Ammonia Solution 85
  8.5 Total Consumption of Auxiliary Chemicals 86
 
9    Residues and Effluents Arising in the Model Systems 88
  9.1 Residues of Wet Processes 88
  9.2 Residues of Semi Wet Processes 89
  9.3 Residues of Semi Dry Processes 90
  9.4 Total Amounts of Residues Arising in the Model Plants 90
 
10    Investment Costs 92
  10.1 General Preliminary Remarks 92
  10.2 Procedure and Data Sources 93
  10.3 Cost Calculation 94
  10.4   Survey of Costs 97
 
11    Summary of Results 99
12    Conclusions 103
13    References 104




Last update: 15.11.2002 - Comments to:     Matthias Achternbosch