Overview of LCP BREF Revision and Implementation Timeline

BREF VELK SPALOVAC ZAZEN (PR B H REVIZE A AKTU LN STAV) XVII. F RUM PRO V M NU INFORMAC O BAT MPO, 24.11.2016 Pavel Frolka EZ, a. s.

OBSAH Informace o projedn v n revize LCP BREF Aktu ln stav n vrhu, vybran BAT-AELs Dal postup 1

REVIZE LCP BREF DOSAVADN V VOJ St vaj c LCP BREF z 07/2006 Dotazn kov et en (2012) 580 dotazn k (8 za zen za R) D1 1.n vrh BREF (06/2013) P ipom nky k D1 8500 p ipom nek; 167 za R, v echny v souladu s IED (09/2013) esk iniciativa Dom c paliva Zohledn n podm nek specifick ch n rodn ch palivov ch z kladen (podpora BG, EE, EL, HU, PL, SK, RO, Eurelectric, EuroHeat&Power) Intermediate meeting (17.-18.6.2014) Zve ejn n Background Paper (vypo d n p ipom nek k D1) a n vrhu Z v r o BAT (2.4.2015) Final meeting (2.-10.6.2015) Split views (31.7.2015) P ipom nkov n z v r z FM (21.10.2015 zve ejn na 4.konsolidovan verze) Vypo d n split views a p edlo en p edfin ln ho n vrhu LCP BREF (22.2.2016) 06/2016 Final draft 20.10.2016 F rum dle l.13 IED 2

REVIZE LCP BREF PRIORITY R R vznesla 6 split views na FM a dal 2 split views k leftovers NOx BAT-AELs (Tab. 10.3), SO2 BAT-AELs derogace pro lignite, TZL BAT-AELs (Tab.10.7) rtu BAT-AELs (Tab.10.9), aplikovatelnost d vkov n halogenovan ch aditiv ke sn en emis rtuti (BAT 23), NH3 monitoring (zm na z kontinu ln ho na periodick u za zen s SCR/SNCR a WFGD) energetick innost n prava diskrimina n ch po adavk na tepl rny definice agrega n ch pravidel zesoulad n se sm rnic K projedn n na F ru dle l. 13 IED R vznesla 14 p ipom nek: BAT 19 nav en NOx BAT-AELs (Tab.10.3) ze 175 na 190 mg/m3 ( 300 MWt CU/HU FBC a HU PC) a nav en (pro CU PC 300 MWt, kde nelze SCR) ze 150 na 180 mg/m3 BAT 21 nav en SO2 BAT-AELs ze 130 na 170 mg/m3 ( 300 MWt) + derogace pro HU, BAT 22 - nav en TZL BAT-AELs (Tab. 10.7) z 8 na 10 mg/m3 ( 1000 MWt), BAT 23 nav en BAT-AELs pro rtu (Tab.10.9) z 10/7 na 14/10 mg/m3 (<300/ 300 MWt), BAT 23f-g omezen aplikovatelnosti d vkov n sorbent a halogenovan ch aditiv, NH3 monitoring (zm na z kontinu ln ho na periodick u za zen s SCR/SNCR a WFGD) + derogace pro HCl (PL CU), aplikovatelnost SCR 3

REVIZE LCP BREF IED PNP LCP BREF 2015 2016 2017 2018 2019 2020 2021 2022 IED PNP (tepl.) LCP BREF platnost z v r o BAT (od vyd n v edn m v stn ku EU p edpoklad v pol.2017) BAT-AELs aplikovateln pro nov za zen BAT-AELs aplikovateln pro st vaj c za zen (nejpozd ji 4 roky od vyd n z v r ) 4

Final draft vs. draft 1 - srovn n NOx, CO (BAT 19), NH3(BAT 4) [MWt] D1 vs. FD NOx CO NH3 (BAT 4) Yearly average or average over the sampling period [mg/Nm ] < 5 < 3 10 < 5 < 3 10 < 1-3.5 < 3 10 Yearly average [mg/Nm ] Daily average [mg/Nm ] Yearly average [mg/Nm ] New or existing plant New plant Existing plant (4) New plant Existing plant D1 FD D1 FD D1 FD 100-200 100 150 100-150 50-100 50-150 50-85 100-270 100-270 100-180 100-180 50-180 <85-150 (8)(9) (175) [190] 65-180 65-150 [180] ND ND 4-80 <100 155-200 ND 80-130 140-220 80 125 165-330 ND 155-210 140-220 140-165 (10) (220) (340) 80-220 <85-165 (6)(200) (340) < 30 140 4-80 < 30 140 4-80 < 30 100 (1) 100-300 300 coal/lignite FBC or lignite PC 300 coal PC D1 FD 65-100 65-85 80-125 80-125 4-80 < 1-3.5 < 3 10 < 5 100 (1) (1) The higher end of the range may be up to 140 mg/Nm3 in the case of limitations due to boiler design, and/or in the case of fluidised bed boilers not fitted with secondary abatement techniques for NOX emissions reduction. (4) These BAT-AELs do not apply to plants operated < 1500 h/yr. (6) In the case of plants put into operation no later than 7 January 2014, the higher end of the range is 200 mg/Nm3 for plants operated 1500 s h/yr, and 220 mg/Nm3 for plants operated < 1500 h/yr. (7) In the case of plants put into operation no later than 1 July 1987, which are operated < 1500 h/yr and for which SCR and/or SNCR is not applicable, the higher end of the range is 340 mg/Nm3. (8) The lower end of the range is considered achievable when using SCR. (9) The higher end of the range is 175 mg/Nm3 for FBC boilers put into operation no later than 7 January 2014 and for lignite-fired PC boilers. (10) The higher end of the range is 220 mg/Nm3 for FBC boilers put into operation no later than 7 January 2014 and for lignite-fired PC boilers. (11) These levels are indicative for plants operated < 500 h/yr. 5

Final draft vs. draft 1 - srovn n SO2BAT-AELs (BAT 21) [MWt] D1 vs. FD Yearly average [mg/Nm ] New plant 150-200 150-200 80-150 80-150 10-75 10-75 20-150 20-75 Daily average [mg/Nm ] New plant ND 170-220 ND 135-200 25-110 25-110 ND 25-110 Existing plant ND 170-400 ND 135-220 (5)(250) 25-220 25-165(4)(205) ND 50-220 Existing plant (3) 150-400 150-360 80-200 95-200 10-130 10-130 (6)[170] 20-180 20-180 D1 FD D1 FD D1 FD D1 FD <100 100-300 300 PC 300 FBC (1) (1) For circulating fluidised bed boilers, the lower end of the range can be achieved by using high-efficiency wet FGD. The higher end of the range can be achieved by using boiler in-bed sorbent injection. (3) These BAT-AELs do not apply to plants operated < 1500 h/yr. (4) The higher end of the BAT-AEL range is 220 mg/Nm3 in the case of plants put into operation no later than 7 January 2014 and operated < 1500 h/yr. For other existing plants put into operation no later than 7 January 2014, the higher end of the BAT-AEL range is 205 mg/Nm3. (5) In the case of plants put into operation no later than 7 January 2014, the upper end of the BAT-AEL range is 250 mg/Nm3. (6) The lower end of the range can be achieved when using low-sulphur fuel in combination with a wet abatement system. (7) These levels are indicative for plants operated < 500 h/yr. For a combustion plant with a total rated thermal input of more than 300 MW, which is specifically designed to fire indigenous lignite fuels and which can demonstrate that it cannot achieve the BAT-AELs mentioned in Table 10.5 for techno- economic reasons, the daily average BAT-AELs set out in Table 10.5 do not apply, and the upper end of the yearly average BAT-AEL range is as follows: (i) for a new FGD system: RCG x 0.01 with a maximum of 200 mg/Nm3; (ii) for an existing FGD system: RCG x 0.02 [0.03] with a maximum of 320 mg/Nm3; in which RCG represents the concentration of SO2 in the raw flue-gas as a yearly average (under the standard conditions given under General considerations) at the inlet of the SOX abatement system, expressed at a reference oxygen content of 6 vol-% O2. (iii) If boiler sorbent injection is applied as part of the FGD system, the RCG may be adjusted by taking into account the SO2 reduction efficiency of this technique ( BSI), as follows: RCG (adjusted) = RCG (measured) / (1- BSI). 6

Final draft vs. draft 1 - srovn n TZL BAT-AELs (BAT 22) [MWt] D1 vs. FD Yearly average [mg/Nm ] (1) Daily average or average over the sampling period [mg/Nm ] New plant ND 4-16 ND 3-15 ND 3-10 4-10 3-10 New plant 2-15 2-5 2-10 2-5 < 5 2-5 < 3 2-5 Existing plant (3) 2-20 2-18 2-20 2-14 1-15 2-10(4) (12) < 1-10 2-8 [10] Existing plant 4-28 4-22(2) (28) 4-25 4-22(3)(25) 4-20 3-11(5) (20) 4-20 3-11(6) (14) D1 FD D1 FD D1 FD D1 FD < 100 100-300 300-1000 1000 (1) These BAT-AELs do not apply to plants operated < 1500 h/yr. (2) The higher end of the BAT-AEL range is 28 mg/Nm3 for plants put into operation no later than 7 January 2014. (3) The higher end of the BAT-AEL range is 25 mg/Nm3 for plants put into operation no later than 7 January 2014. (4) The higher end of the BAT-AEL range is 12 mg/Nm3 for plants put into operation no later than 7 January 2014. (5) The higher end of the BAT-AEL range is 20 mg/Nm3 for plants put into operation no later than 7 January 2014. (6) The higher end of the BAT-AEL range is 14 mg/Nm3 for plants put into operation no later than 7 January 2014. (7) These levels are indicative for plants operated < 500 h/yr. 7

Final draft vs. draft 1 - srovn n HCl, HF BAT-AELs (BAT 21) HCl HF [MWt] D1 vs. FD Average of samples obtained during one year [mg/Nm ] New plant Existing plant (1) < 1-5 1-6 < 1-5 1-3 1-5 (2)(4)(7)(20) [MWt] D1 vs. FD Average of samples obtained during one year [mg/Nm ] New plant < 0.1-2 < 1-3 < 0.1-2 < 1-2 Existing plant < 0.1-2 < 1-6 (3)(7) < 0.1-2 < 1-3 (3)(7) D1 FD D1 FD < 1-5 D1 FD D1 FD <100 < 100 2-10 (2)(20) < 1-5 100 100 (1) The lower end of these BAT-AEL ranges may be difficult to achieve in the case of plants fitted with wet FGD and a downstream gas-gas heater. (2) The higher end of the BAT-AEL range is 20 mg/Nm3 in the following cases: plants combusting fuels where the average chlorine content is 1000 mg/kg (dry) or higher; plants operated < 1500 h/yr; FBC boilers. These levels are indicative for plants operated < 500 h/yr. (3) The higher end of the BAT-AEL range is 7 mg/Nm3 in the following cases: plants fitted with wet FGD with a downstream gas-gas heater; plants operated < 1500 h/yr; FBC boilers. These levels are indicative for plants operated < 500 h/yr. (4) In the case of plants fitted with wet FGD with a downstream gas-gas heater, the higher end of the BAT-AEL range is 7 mg/Nm3. 8

Final draft vs. draft 1 - srovn n Hg BAT-AELs (BAT 23) Hg (coal) [MWt] Hg (lignite) [MWt] D1 vs. FDYearly average or average of samples obtained during one year [ g/Nm ] New plant D1 0.5-5 FD < 1-3 D1 0.2-2 FD < 1-2 (2) The lower end of the BAT-AEL range can be achieved with specific mercury abatement techniques. D1 vs. FDYearly average or average of samples obtained during one year [ g/Nm ] New plant D1 1-10 FD < 1-5 D1 0.5-5 FD < 1-4 Existing plant Existing plant 2-20 <1-10(2) 0.5-10 < 1-7(2) 1-10 < 1-9(2) 0.2-6 < 1-4(2) < 300 < 300 300 300 - EIPPCB approved CAN Europe s split view on common BAT-AEL for all new and existing coal- and lignite-fired plants to be set to < 1 g/Nm3 (see SV assessement 11.15) EURACOAL introduced a report by prof. Kather, Hamburg University of Technology, where the BAT-AELs for mercury are discussed. The main outcomes of the report: there is a very large uncertainty for the continuous measurement of Hg (up to +/- 6 g/Nm3) there are very large spreads in Hg content of the different lignites the range for the new mercury BAT-AEL for existing lignite-fired power plants with PC boiler should be set between 5 and 9 g/Nm mercury contents in the fuel higher than 0.22 mg/kg (fuel input data gained within the LCP BREF revision process) have to be taken into account (CZ lignite: 0.10-0.60 mg/kg) - - - - - 9

ODHADY DOPAD LCP BREF, MCPD N klady spojen s implementac Z v r o BAT v r zn ch sektorech pr myslu v R a dopad spojen ch s MCPD V roba eleza a oceli nyn v provozu odhadovan n klady v jimky V roba skla nyn v provozu odhadovan n klady v jimky Cement a v pno nyn v provozu odhadovan n klady v jimky Velk spalovac za zen nyn v provozu odhadovan n klady v jimky Sm rnice MCP st edn spalovac zdroje odhadovan n klady 14 za zen 10-20 mld. K 0 24 za zen 2 mld. K 7 10 za zen 1-2 mld. K 0 cca 110 za zen cca 15-20 mld. K ? cca 11 mld. K 10

REVIZE LCP BREF N SLEDUJ C KROKY Stanovisko F ra dle l.13 IED (Q4/2016) Zapracov n stanoviska F ra a p edlo en n vrhu rozhodnut o z v rech o BAT v boru Komise dle l.75 IED (Q1/2017) Jedn n v boru Komise (Q1-2/2017) Stanovisko v boru Komise (Q1-2/2017) P ijet rozhodnut o z v rech o BAT Komis (Q2-4/2017) Zve ejn n rozhodnut v edn m v stn ku EU, vstup rozhodnut v platnost (Q3-4/2017). N sleduje 4 let lh ta pro uveden integrovan ch povolen st vaj c ch za zen do souladu s po adavky rozhodnut komise dle harmonogramu p ezkum integrovan ch povolen zve ej ovan ch M P. P EZKUM INTEGROVAN CH POVOLEN BUDE PROB HAT V RE IMU PODSTATN ZM NY. 11

REVIZE LCP BREF D kuji za pozornost. 12

TZL BAT-AELs Split view a p ipom nka R na F rum dle l.13 P ipom nka CZ: Horn mez ro n ho BAT-AEL zv it z 8 na 10 mg/Nm3pro st vaj c HU za zen >1000 MWt 13

Revize LCP BREF Odvozen BAT-AELs pro Hg 18-1,2 Tepl rna Komo any 25-1 Elektr rna Hodon n 390-1-6 Elektr rna Tur w 23 Elektr rna Tu imice 130 Neurath E 137 Neurath A 19 Tepl rna T bor K7 116 Niederau em K 127 Schwarze Pumpe 22 Plze sk tepl rensk 14