Presentation is loading. Please wait.

Presentation is loading. Please wait.

Flue Gas Treatment using Industrial EB Accelerators - Status and Challenges Andrzej G. Chmielewski Institute of Nuclear Chemistry and Technology, Warsaw,

Similar presentations


Presentation on theme: "Flue Gas Treatment using Industrial EB Accelerators - Status and Challenges Andrzej G. Chmielewski Institute of Nuclear Chemistry and Technology, Warsaw,"— Presentation transcript:

1 Flue Gas Treatment using Industrial EB Accelerators - Status and Challenges Andrzej G. Chmielewski Institute of Nuclear Chemistry and Technology, Warsaw, Poland NICSTAR-2018 NAARRI INTERNATIONAL CONFERENCE Advanced Applications of Radiation Technology March , 2018 Hotel Courtyard by Marriott, Mumbai, India TANGO 2

2 Fossil fuels

3 Environmental impact

4

5 Wet FGD + SCR

6 Electron beam

7 radiothermal SO2 + OH* + M  HSO3 + M HSO3 + O2  SO3 + HO2*
SO3 + H2O  H2SO4 H2SO4 + 2NH3  (NH4)2SO4 thermal SO2 + 2NH3  (NH3)2SO2 (NH3)2SO2 --> (NH4)2SO4 1. H. Namba: Materials of UNDP(IAEA)RCA Regional Training Course on Radiation Technology for Environmental Conservation TRCE-JAERI, Takasaki, September/October 1993, 2. A.G. Chmielewski: Nukleonika 45(1) (2000) 31

8 NO oxidation NO + O(3P) + M  NO2 + M O(3P) + O2 + M  O3 + M
NO + O3 + M  NO2 + O2 + M NO + HO2* + M  NO2 + OH* +M NO + OH* + M  HNO2 +M HNO2 + OH*  NO2 + H2O NO2 removal NO2 + OH* + M  HNO3 + M HNO3 + NH3  NH4NO3 H. Namba: Materials of UNDP(IAEA)RCA Regional Training Course on Radiation Technology for Environmental Conservation TRCE-JAERI, Takasaki, September/October 1993,

9 NO + N(4S)  N2 + O NO2 + N(4S)  N2O + O N(2D) + NH3  NH* + NH2*
NO + NH2*  N2 + H2O NO2 + NH2*  N2O + H2O NO + NH*  N2 + OH* NO2 + NH*  N2O + OH* H. Namba: Materials of UNDP(IAEA)RCA Regional Training Course on Radiation Technology for Environmental Conservation TRCE-JAERI, Takasaki, September/October 1993,

10

11 EPS Kawęczyn

12

13 EPS Pomorzany

14 EPS Pomorzany

15 Results

16 NPK Fertilizer

17 Pilot plant, China

18 The IEB-FGC Lab INET, Tsinghua University

19 Flue Gas Cleaning Plant in Changdu, China

20 Pilot Plant in Maritsa East 2 Thermal Plant

21 BULGARIA

22 Oil fired boiler

23 General view of the pilot plant
1- stack of F 1001 boiler bag filter 2- boiler F insulated duct part 3-flue gas duct cyclone 4-control room ammonia storage and injection unit 5-humidification unit EB mobile unit 6-pilot plant stack

24 Pilot plant process units
inlet to process vessel, ID fan EB-TECH mobile unit, stack cyclone, cartridge filter

25 Process vessel

26 EB mobile unit (EBTECH)

27 Monitoring system

28 Limits for heavy metals content in NPK fertilizer 41 39 300 17 420
As Cd Cr Co Pb Hg Ni Zn Remarks <0.02 <0.01 0.43 0.03 1.01 <0.03 63.5 18.3 averaged values for byproducts collected by cartridge bag filter 0.24 0.09 1.61 0.54 1.41 22.80 1476 byproducts collected by ESP Limits for heavy metals content in NPK fertilizer 41 39 300 17 420 2800 US EPA CFR40 Part 75 20 150 500 5 180 1350 Canadian Fertilizer Act (1996) 50 140 2 Polish standard 32.2 276.8 12.9 17.8 72.3 mean values of heavy metals concentrations in fertilizers marketed Contents of heavy metals (mg/kg) in the byproduct and limits for heavy metals content in the NPK fertilizer established in some countries

29 CARGO SHIPS

30 Flow process and typical exhaust gas composition for 2-stroke diesel engine

31 A Hybrid SOx scrubbing system , operating in closed loop

32 SCR + FGD systems integration

33 The general scheme of the electron beam interaction with the flue gas

34 NO + O(3P) + M → NO2 + M (M is a third inert body in the reaction system)
O(3P) + O2 + M → O3 + M NO + O3 + M → NO2 + O2 + M NO + HO2∙ + M → NO2 + ∙OH + M SO2 + ∙OH + M → ∙HSO3 + M ∙HSO3 + O2 → SO3 + HO2∙ NO2 + ∙OH + M → HNO3 + M SO3 + H2O → H2SO4 Main reactions

35 EB +SWS+ OX block diagram
1)inlet to the installation, 2) inlet gas parameters, 3) heat exchanger (outlet temperature 70-90o C), 4) process chamber, 5) accelerator, 6) accelerator’s shelter, 7) wet simple spray tower scrubber, 8) demister, 9) outlet gas parameters (of scrubber), 10) process water (fresh), 11) NaClO2, 12) Michaelis buffer Na2HPO4 and KH2PO4 , 13) seawater, 14) NaCl solution, 15) fresh water, 16) centrifugal separator, 17) sludge tank, 18) post-reaction water tank, 19) monitoring system of post-reaction water, 20) sewage or sea, 21) exhaust fan, 22) stack 23) recirculation (optional) EB +SWS+ OX block diagram

36 The comparison of the NOX removal efficiency between technology using electron beam only, hybrid technology, where electron beam was coupled with wet scrubber and hybrid technology, where electron beam was coupled with wet scrubber as well as with NaClO2 and buffer (the inlet SO2 concentration was 700 ppm and NO was 1000 ppm), where : EB – Irradiation of gases with electron beam from accelerator, SWS – Sea water scrubber, buffer – Michelis buffer Hybrid technology

37 Conceptual scheme of the installation using EB technology for SOx and NOx removal as applied onboard, water closed or hybrid system

38

39 Electron accelerator with linear cathode

40 PAH treatment naphtalene acenaphtene anthracene fluoranthene pyrene
benzo(a)pyrene dibenzo(a,h) anthracene PAH treatment

41 VOC treatment (exp.vs.modeling)
Toluene, benzene over 50 kinetic equations in each case;SOx, NOx in presence of VOC

42 MUNICIPAL WASTE INCINERATION JAERI, Takasaki, Japan
Electron accelerator & Irradiation vessel Flue gas out Stack Electron accelerator House for test Irradiation vessel Self-shielded type and Curtain beams 300 keV max. and 40 mA max.

43 EB/Catalyst Konkuk , ROK
Acceleration of Electron Irradiation of Electron Activation of Catalyst & Oxidation of by-Products VOC Removal by Radical Reaction N2, O2, H2O, etc. e- OH , N , H , HO2 , O radicals VOC CO2 , O3 , By-products VOC Decomposition by EB Oxidation by Catalyst radical Surface Activation Surface Reforming Oxidation of by-products & VOC Catalyst O3 43

44 Conclusions EBFGT is the most advanced technology for simultaneous
SOx and NOx removal Feasibility of the technology has been demonstrated for coal fired plant in the full industrial scale Feasibility of the technology has been demonstrated for oil fired boiler in pilot industrial scale The process can be applied for diesel engine flue gas treatment at cargo ships (laboratory tests) The process can be applied for VOC and PAH treatment (laboratory and industrial pilot tests) The process can be applied for mercury emission control (laboratory tests)

45 Thank you !


Download ppt "Flue Gas Treatment using Industrial EB Accelerators - Status and Challenges Andrzej G. Chmielewski Institute of Nuclear Chemistry and Technology, Warsaw,"

Similar presentations


Ads by Google