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EPA-453/R-94-004 ALTERNATIVE CONTRO
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ALTERNATIVE CONTROL TECHNOLOGY DOCU
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Chapter Page 4.1 MECHANISMS OF NO F
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TABLE OF CONTENTS (con.) Chapter Pa
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LIST OF TABLES Number Page 2-1 UNCO
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CHAPTER 1 INTRODUCTION Congress, in
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CHAPTER 2 SUMMARY This chapter pres
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2.2 NO EMISSION CONTROL TECHNOLOGIE
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TABLE 2-2. ACHIEVABLE NO REDUCTIONS
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TABLE 2-4. CAPITAL AND ANNUAL COSTS
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TABLE 2-5. COST EFFECTIVENESS OF NO
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eductions ranged from 470 tons/year
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CHAPTER 3 INDUSTRY DESCRIPTION 3.1
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Type II. Moderate-heat-of-hardening
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3 a TABLE 3-2. UNITED STATES CEMENT
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Figure 3-1. U.S. Portland cement pl
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Table 3-3. (con.) Rank Clinker 3 (1
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5 cement processes: wet process and
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Figure 3-3. New technology in dry-p
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substantial levels of silica and al
- Page 41 and 42: are achieved by clinker coolers of
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- Page 48 and 49: 4.1.1 Thermal NO Formation x Therma
- Page 50 and 51: temperatures are on the order of 16
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- Page 54 and 55: expected to produce more fuel NO th
- Page 56 and 57: introduce a large proportion of com
- Page 58 and 59: will also mean a somewhat lower sec
- Page 60 and 61: ILC systems: In these systems, the
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- Page 66 and 67: Uncontrolled NO x emissions Plant c
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- Page 70 and 71: Capacity Heat in NO x emissions Met
- Page 72 and 73: TABLE 4-3. (con.) Capacity Heat in
- Page 74 and 75: TABLE 4-3. (con.) Capacity Heat in
- Page 76 and 77: TABLE 4-3. (con.) Capacity Heat in
- Page 78 and 79: in estimating uncontrolled and cont
- Page 80 and 81: 13. Letter from Sheridan, S.E., to
- Page 82 and 83: 44. Chemecology Corporation Source.
- Page 84 and 85: 73. Letter and attachments from Smi
- Page 86 and 87: NO control approaches applicable to
- Page 88 and 89: 5.1.2.2 Kiln Fuel Changing the prim
- Page 90 and 91: oxygen content of the primary air m
- Page 94 and 95: e about 15 to 38 percent depending
- Page 96 and 97: combustion system shown in Figure 5
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- Page 100 and 101: Figure 5-3. Schematic of hazardous
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- Page 104 and 105: higher than typical cement kiln flu
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- Page 108 and 109: Figure 5-4. Application of the sele
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- Page 112 and 113: 5.4 REFERENCES 1. Helmuth, R.A., F.
- Page 114 and 115: 25. Letter from Wax, J., Institute
- Page 116 and 117: TABLE 6-1. CEMENT KILN MODEL PLANTS
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- Page 122 and 123: The total capital cost is the sum o
- Page 124 and 125: TABLE 6-3. ANNUALIZED COST ELEMENTS
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- Page 128 and 129: 6.1.3.7 Administrative Charges. The
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- Page 134 and 135: The annualized costs for low NOx bu
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6-28
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PEC for model plant 300,000 ' Heat
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TABLE 6-9. ANNUALIZED COSTS FOR MID
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6-34
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TABLE 6-10. CAPITAL COSTS FOR A URE
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TABLE 6-11. ANNUAL OPERATING COSTS
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6-40
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TABLE 6-12. CAPITAL COSTS FOR AN AM
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TABLE 6-13. ANNUAL OPERATING COSTS
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6-46
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costs range from $9.9 million for t
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The estimated annualized costs for
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6.3 COST EFFECTIVENESS OF NOx CONTR
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emoved. Cost effectiveness were det
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TABLE 6-17. COST EFFECTIVENESS OF R
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6-58
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TABLE 6-18. COST EFFECTIVENESS OF M
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TABLE 6-19. COST EFFECTIVENESS OF U
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6.3.4 Selective Catalytic Reduction
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6-66
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TABLE 6-21. COST EFFECTIVENESS OF S
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6-70
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11. Letter and attachments from Nov
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Tables 7-1 7-2
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TABLE 7-2. REDUCTION IN NO x EMISSI
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model plants described in Section 6
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temperature and excess air may be u
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NOxemissions will form. The heater
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equirement for the flue gas reheati