Control of Oxides of Nitrogen from Stationary Sources

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1 Control of Oxides of Nitrogen from Stationary Sources

2 Oxides of Nitrogen The gaseous oxides of nitrogen include:
N2O:nitrous oxide NO:nitric oxide (free radical) N2O3: nitrogen trioxide NO2:Nitrogen dioxide (free radical) N2O5:nitrogen pentoxide An unstable form NO3 also exists. Only N2O,NO, and NO2 present in the atmosphere in significant concentrations

3 NO and NO2 (NOx) NO is a colorless gas with average ambient concentration of 0.5 ppm No adverse health effect at this concentration but it is a precursor to the formation of NO2 and active compound in photochemical smog formation NO2 is a reddish brown gas. A concentration of 1 ppm can be detected by the eye. Adverse health effect is primarily associated with the pulmonary problems.On an annual basis air ambient air level standart is 0.05 ppm (100 ug/m3)

4 Sources and Concentrations of NOx
Over 90% of all man-made nitrogen oxides entering the atmosphere are from combustion sources For the US, 50% is from mobile sources For Turkey ambient NOx concentration is around xx At an emission source the concentration of oxided of nitrogen is much higher than ambient values For example the NOx concentration in the flue gas from the steam boiler of a power plant may reach 500 to 1000ppm From such combustion processes the NOx is the exhaust stack gas would be 90% or more NO and the rest NO2

5 NOx Control 1. Control over the reaction that produces the pollutant
2. Remove NOx after it is formed

6 NOx Formation Basic Chemistry,Thermodynamics and Kinetics of the Formation Reactions
There are two sources of N that contribute to the formation of oxides of nitrogen 1. Fuel N (Coal and fuel oil composition, note that no N in natural gas)(Fuel NOx) 2. Air N (78% of air is N)(Thermal NOx)

7 Thermodynamics of Thermal NOx Formation
It is essential to understand the thermodynamics and kinetic of nitrogen-oxygen reactions, especially at high temperatures NOx formation mechanism was first proposed by Zeldovich (1946): N2+O⇋NO + N (1) N+O2⇋NO +O (2) N+OH⇋NO +H (3) Reaction 1 and 2 are the most important reactions in the model.

8 Thermodynamics of Thermal NOx Formation
Let’s first consider only the NO and NO2 formation equilibrium reactions: N2+O2⇋2NO (4) NO+1/2O2⇋NO2 (5)

9 Equilibrium Constants:
Temperature (K) KP N2+O22NO NO+1/2O2NO2 300 10-30 1.4(10)6 500 2.7(10)-18 1.3(10)2 1000 7.5(10)-9 1.2(10)-1 1500 1.1(10)-5 1.1(10)-2 2000 4.0(10)-4 3.5(10)-3

10 Predicted Equilibrium Concentrations
Temperature (K) Flue Gas (ppm) NO NO2 300 1.1(10)-10 3.3(10)-5 800 0.8 0.1 1400 250 0.9 1873 2000 1.8

11 Predicted Equilibrium Concentrations
1. At flue gas exit T ( K), expect to observe very low NOx (<1 ppm) and primarily NOx in the form NO2 Temperature (K) Flue Gas (ppm) NO NO2 300 1.1(10)-10 3.3(10)-5 800 0.8 0.1 1400 250 0.9 1873 2000 1.8 1. At flame zone T ( K), expect to observe very high NOx (up to ppm) and primarily NOx in the form NO

12 Predicted Equilibrium Concentrations
1. At flue gas exit T ( K), expect to observe very low NOx (<1 ppm) and primarily NOx in the form NO2 At actual furnaces however typical flue gas consists of ppm NOx and mostly (90-95%) in NO form So there must be other factors other than equilibrium to explain this:

13 Kinetics of Nitric Oxide Formation in Combustion Process
The rate of NO formation is the major factor influencing NOx concentrations Considering reactions 1 to 3, the rate expression can be written: rNO= k+1[N2][O]-k-1[NO][N]+k+2[O2][N] -k-2[NO][O]+k+3[N][OH]-k-3[NO][H] rN= k+1[N2][O]-k-1[NO][N]-k+2[O2][N] -k-2[NO][O]-k+3[N][OH]+k-3[NO][H]

14 Rate constant k, m3/mol-s
Rate Constants Reaction Rate constant k, m3/mol-s (1)N2+O⇋NO + N k+1=1.8(10)8e-38,370/T k-1= 3.8(10)7e-425/T (2)N+O2⇋NO +O k+2=1.8(10)4e-4680/T k-2= 3.8(10)3e-20820/T (3)N+OH⇋NO +H k+3=1.8(10)7e-450/T k-3= 3.8(10)8e-24560/T k+1 k-1 k+2 k-2 k+3 k-3 T is in degrees Kelvin

15 Kinetics of Nitric Oxide Formation in Combustion Process
N atoms are much more reactive than NO, we can assume quasi steady state for N and an expression for [N]ss can be obtained: [N]ss= k+1[N2][O]+k-2[NO][O]+k-3[NO][H]/ k-1[NO]+k+2[O2]+k+3[OH] And substituting this into rate equation for NO rNO= k+1[N2][O]-k-2[NO][O]-k-3[NO][H]+( -k-1[NO]+k+2[O2]+k+3[OH])[N]ss

16 Kinetics of Nitric Oxide Formation in Combustion Process
The interesting thing about above rate equation is that the initial rate of formation of NO (when NO concentrations are small) is just equal to twice that of reaction 1. That is: rNO= k+1[N2][O]-k-2[NO][O]-k-3[NO][H]+( -k-1[NO]+k+2[O2]+k+3[OH])[N]ss N2+O⇋NO + N (1) rNOinitial= 2k+1[N2][O]

17 Example 16.2 Given a HC flame at 1870 C where the mole fractions of N2 gas and O atoms are 0.75 and 9.5(10)-4 respectively, a) calculate the initial rate of NO formation (in mole(m3-s) b) if this rate holds constant for 0.03 seconds, calculate the concentration in ppm of NO in the gases leaving the flame zone

18 Solution a) at T = 1870 C = 2143 K, k+1=1.8(10)8e-38,370/2143=3.015 m3/mol-s Assuming P= 1atm, the molar density of the gases: [N2]=0.75x5.686=4.26 mol/m3 [O]=9.5(19)-4x5.686= mol/m3 rNOinitial= 2k+1[N2][O]=2(3.015)(4.26)(0.0054) = mol/m3-s

19 Solution b) If this inital rate holds for 0.03 seconds then
[NO]=0.1388(0.03)=4.16(10)-3 mol/m3

20 Research on NOx Formation
Experimental results in various studies showed that NO concentrations in the flame zone are significantly higher than could have been formed by the Zeldovich mechanism This may be due to “prompt” NO formation Prompt NO: NO formed in the first five milliseconds ( ppm)

21 Research on NOx Formation
T (C ) NO conc. <1600 <200 ppm >1800 Several thousands =1950 12,000 1990 Peak value >2000 decreases MacKinnon worked with heated N2,O2, Ar samples NO concentrations increased rapidly with time up to about 4-5 seconds, after no further increases observed

22 Research on NOx Formation
MacKinnon developed a model predicts the NO concentration (in ppm) as a function of temperature (in K), N and O concentrations, and time (in s)

23 NOx Formation from Fuel Nitrogen
When a fuel contains organically bound N, the contribution of the fuel bound N to the total NOx production is significant

24 Example 16.3

25 Strategies for Combustion Modification
Reduce peak temperatures of the flame zone Reduce gas residence time in the flame zone 2017/4/6 Aerosol & Particulate Research Lab

26 Modification of Operating Conditions
Off-Stoichiometric Combustion/Staged combustion: combusting the fuel in two or more steps. Fuel rich then fuel lean. Flue gas recirculation: reroute some of the flue gas back to the furnace; lower O2 and allow NOx to proceed the “frozen” reactions Water injection: reduce flame temperature; energy penalty 2017/4/6 Aerosol & Particulate Research Lab

27 Aerosol & Particulate Research Lab
Gas reburning: injection of natural gas into the boiler above the main burner to create a fuel-rich reburn zone; hydrocarbon radicals react with NOx to reduce NOx to N2. 2017/4/6 Aerosol & Particulate Research Lab

28 Low-NOx burner: inhibit NOx formation by controlling the mixing of fuel and air; lean excess air and off-stoichiometric combustion Avoid Peak Temperature 2017/4/6 Aerosol & Particulate Research Lab

29 Case: Paşabahçe Glass Production

30

31 Aerosol & Particulate Research Lab
Flue Gas Treatment Selective Catalytic Reduction (SCR) Temperature ~ oC Q: Why is it called “selective”? Also good for Hg emission control!!! But it creates SO3. Selective Noncatalytic Reduction (SNR) Temperature ~ oC Above 1000 oC 2017/4/6 Aerosol & Particulate Research Lab

32 SCR Removal efficiency is over 90% Expenses from use of catalyst
High operation and capital cost Large area requirement Requires temperature control for optiumum reduction

33 SNCR No catalyst cost High temperatures (850-1100)
Low removal efficiency ( %30-%66 less than SCR)

34 Other Control Methods Absorption Adsorption Biological

35 Biological Control Technologies
 Under aerobic conditions, nitrification and chemical oxidation leads to NOx oxidation to nitrate. İlk denemelerde, yüksek O2 konsantrasyonlu aerobik şartlarda (>%17 Oksijen) NO giderimi toluenle muamele edilmiş silika pelet dolgulu bir biyofiltrede %97 mertebesinde başarılmıştır

36 Biological Control Technologies
 Anoksik koşullarda ise NOx denitrifikasyon prosesi yüksek bir verimle azot gazına indirgenmektedir. Toprak kompostu içeren laboratuar ölçekli bir biyofiltre çalışmasında NO2 için %100’e yaklaşan bir giderim verimi elde edilmiştir. (Okuno et. al, 2000). Tüm bunlar BiyoDeNox teknolojilerinin NOx kontrolü için gelecekte de artan oranlarda kullanılacağını göstermektedir.

37 Biological Control Technologies

38 Biological Control Technologies
BioDeNOx Process

39 BioDeNOx Process First nitrosyl complex was formed by the reactions 1 and 2: NO (g)  NO (aq) (1) NO (aq) + Fe(II)EDTA2- > Fe(II)EDTA − NO (2)

40 BioDeNOx Process To be able to regenarate the absorption liquid, formed Fe(III)EDTA- needs to be reduced to Fe(II)EDTA2- by the m/o Regeneration of Fe(II)EDTA2- is essential for the system NO removal performance: 12 Fe(III)EDTA- + C2H5OH + 3 H2O 12 Fe(II)EDTA CO H+

41 İTÜ XIII. Endüstriyel Kirlenme Kontrolü Sempozyumu
Jet-Loop Biyoreaktör JetLoop reaktörlerde sistem içinde draft tüpüne püskürtülen gaz reaktörü terk etmeden önce draft tüpün içerisinde birkaç kez devir yapmaktadır. Devir sayısı ve jet akımından kaynaklanan daha küçük çaplı gaz oluşumu NO gazının ortama bir kelat ilave etmeksizin daha fazla çözünmesini sağlamaktadır. İTÜ XIII. Endüstriyel Kirlenme Kontrolü Sempozyumu

42 İTÜ XIII. Endüstriyel Kirlenme Kontrolü Sempozyumu
Pilot Tesis Toplam hacim 20 L, Çamur yaşı 50 gün, 1. Su girişi 2. Hava/gaz girişi 3. Hava/gaz çıkışı 4. JetLoop biyoreaktör 5. Su boşaltma vanası 6. Soğutucu 7. Su debimetresi 8. ÇO, Redox, pH, Sıcaklık sensörleri haznesi 9. Pompa 10. Besleme girişi 11. MBR sistemi, V: vana) İTÜ XIII. Endüstriyel Kirlenme Kontrolü Sempozyumu

43 İTÜ XIII. Endüstriyel Kirlenme Kontrolü Sempozyumu
Pilot Tesis İTÜ XIII. Endüstriyel Kirlenme Kontrolü Sempozyumu

44 Pilot Tesis İşletme Sonuçları
Deney MLSS (mg/L) QGD (m3/sa) QGaz/QGD Besleme Şekli ORP (mV) Giriş NO (ppm) Çıkış NO (ppm) Verim (%) 1 3000 1.0 0.12 Sürekli -485 550 427 23 3* 2640 -476 1100 820 25 2 1.8 0.07 -488 175 70 4* 2400 -475 413 65 İTÜ XIII. Endüstriyel Kirlenme Kontrolü Sempozyumu