- Page 1 and 2: Alternative Control Techniques Docu
- Page 3 and 4: ALTERNATIVE CONTROL TECHNIQUES DOCU
- Page 5 and 6: TABLE OF CONTENTS iii Page 5.0 CONT
- Page 7 and 8: LIST OF TABLES v Page TABLE 2-1. NO
- Page 9 and 10: LIST OF FIGURES vii Page Figure 3-1
- Page 11 and 12: discussion of NO emission levels is
- Page 13: TABLE 2-1. NO EMISSIONS AND COST CO
- Page 17 and 18: Four plants in the United States pr
- Page 19 and 20: 3.0 DESCRIPTION OF NITRIC/ADIPIC AC
- Page 21 and 22: Figure 3-1. Basic nitric acid produ
- Page 23 and 24: plants operating at 0.8 megaPascals
- Page 25 and 26: 3.1.3 Plant Design Corrosive effect
- Page 27 and 28: . 3.1.3.2 Dual-Pressure Process. Th
- Page 29 and 30: . In the dual-pressure process, amm
- Page 31 and 32: Figure 3-4. Nitric acid concentrati
- Page 33 and 34: Figure 3-5. Nitric acid concentrati
- Page 35 and 36: Two methods of producing adipic aci
- Page 37 and 38: . Ninety-eight percent of adipic ac
- Page 39 and 40: and transported to the adipic acid
- Page 41 and 42: 4.0 CHARACTERIZATION OF NO EMIS x 4
- Page 43 and 44: 3 expensive to control. The difficu
- Page 45 and 46: typical for steady-state, continuou
- Page 47 and 48: factor represents NO in the form of
- Page 49 and 50: 5.0 CONTROL TECHNIQUES FOR NITROGEN
- Page 51 and 52: Figure 5-1. Extended absorption sys
- Page 53 and 54: Figure 5-2. Extended absorption sys
- Page 55 and 56: 5.1.1.3 Performance of Extended Abs
- Page 57 and 58: illustrates the levels to which ext
- Page 59 and 60: Figure 5-3. Nonselective catalytic
- Page 61 and 62: than 140 percent of stoichiometry).
- Page 63 and 64: Poor control of the fuel/oxygen rat
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illustrates the level of control th
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5.1.3.1 Description of SCR Systems.
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is a flow diagram for a typical nit
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Figure 5-5. SCR catalyst performing
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Figure 5-6. SCR catalyst performanc
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TABLE 5-3. NITROGEN OXIDES EMISSION
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European plants using SCR. The data
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TABLE 5-5. SUMMARY OF NO CONTROL TE
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Figure 5-7. Process flow diagram fo
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6.8 to 13.0 kPa (1-2 psi), which al
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. The process control device consis
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Figure 5-9. Schematic diagram of th
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Figure 5-10. Molecular sieve system
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level of achievable NO control. Sec
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is a flow diagram for the nitric ac
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0.41 to 1.23 kg per metric ton (0.8
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is a simplified flow diagram of an
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TABLE 5-6. NITROGEN OXIDES EMISSION
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Instead, the major sources of NO em
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5.3 REFERENCES 1. Review of New Sou
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30. Screening Study to Determine Ne
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maintenance materials, replacement
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TABLE 6-1. CAPITAL COST SUMMARY FOR
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TABLE 6-2. ANNUAL COST SUMMARY FOR
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than the direct and indirect operat
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Chapter 5. For costing purposes, it
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TABLE 6-4. ANNUAL COST SUMMARY FOR
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Estimates of indirect operating cos
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TABLE 6-6. CAPITAL COST SUMMARY FOR
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for blowers can be eliminated if pr
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shows the annual costs for an SCR s
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TABLE 6-8. COST EFFECTIVENESS FOR N
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system is described in detail in Ch
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presents the estimated annual costs
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6.2.2.2 Annual Costs. Table 6-10 6-
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shows the annual costs for a therma
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shows the cost presents the cost ef
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7.0 ENVIRONMENTAL AND ENERGY IMPACT
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. For each of the three model plant
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TABLE 7-2. ANNUAL ELECTRICITY REQUI
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TABLE 7-3. NO EMISSIONS FROM ADIPIC
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a significant amount of heat, which