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1 hzkwekdd/^^/ke /ZdKZd 'EZ> >/D/KE / D ' d h d^ ' & d

2 d d / d d d ^ ' d d d /D' d d d h ' d d d d d d ^ d d ^ e d d e d d e d d d d d d d W d d, de d d & de d d W d d d d d W d d & d e d /D e de e d de e d de e d ^ d: de e d e de e d d / de e d d,w de e d d de d

3 d / d d ^ ' d D ^ h W /// hd^ K: d d h d^ /D E / D E/D d d E> & /^/ / d t ' t'/// D ^ / d D ^ / ',' D ^ d d /D' ^ /D d /D d /// d /D /D d / ' d ' d ' d / d

4 ' d E/D E / D d ' d ' e ' e ' e ' e /D d W /// hd^ ' / / h d^ ' Z hd^ /D d d h ' d W /// hd^ D ^ e /D E / D E/D d ee d d E D ^ d ee d

5 &Y d d ^ & d W, & W d

6 d d ^ d d d d d d d e d e

7 d d D s W, & ^ / /D ed d d: de d d: / /D, d - d - d - d - d e - d -, d^ d^ KZ d^ d^, d^ K D ' e & d - d - d - d - d KZ KZ Z e

8 d d D s W d ee W d - d - d K d / ee / /D K d K K d K d K K d K D/Eh^ ' e o d o d o d o o d o d Z E e

9 d ^ d d le ^ /D d d d d ' d / ^ ' d / d d ^ d & & / ' d e > > / // /D > & >& & ' d E D >& ' d > e

10 ^ d d / t / CO 2 Production process Benchmarked Product 1 Fuel Heat CO 2 Production process Benchmarked Product 2 d d ^ d K d d d E K E d

11 - d^ - - d d^ - - D d & ' d d E d E d E E,W / d^ d DW hd^ d d d^ ',' d t

12 ' d ^ d d d & d^ d d ^ d d K d D D / D D > d d d E d

13 d d K K W d d ^ W E e E & t ^ ' d ^ d d d ^ d d K d K d / ee EdK Kd h d^ d d d E d

14 EdK ' t W d d K d d d K d d d d D/Eh^ ^ ' e t ' t ' d d d d /D Z h W W W

15 & d / K d K d, e ^ d e / d W W & d^

16 d d & e d d W & d d d CO 2 Natural gas Fuel oil Heat Production process Benchmarked Product & d W ^ d d,> W /D ' e ^ d d & = DW,> t h & D W h,>, de

17 ^ ' e ^ ^ ' / / & d & d / / d /D ' e / + E, / & W = DW,> W + E, / + t & W h DW W h,> W, de

18 d de de d d^ d^ d^ E, / d^ d^ / K d E, / = E, / ed d t E, / d^ d^ d: d de de / / K d = d ded t Dt d de de / d^ d d^ d d^ ^ ' e de

19 d d, & d d d CO 2 Natural gas (TJ) Fuel oil (TJ) Heat (TJ) Production process & d, ^ d Non benchmarked Product d,> d: - d^ - E d^ ^ ' e / d d / ^ ' d ^ d & = D,> de

20 & W h D, ed d K d d: K / d^ d^ / d^ ^ ' e d d & & d d d CO 2 Natural gas (TJ) Production Non Fuel oil (TJ) benchmarked process Product Heat (TJ) & d & ^ d d,> d: d & /

21 , & ' e ^ d i & = D,> & W h D & de d K d d:,>, d: d d W & d d d Non-CO 2 CO 2 CO (incomplete combustion) & d Reducing agent (TJ) Heat (TJ) Production process W Non benchmarked Product ^ d d,> K d K d / ee K d d d

22 d d D/Eh^ d & ' e ^ d & = WZ&,> W & WZ& Z d ee,>, K d & K d / K K d K d / edl K d / ' e

23 d d d d = & & & d & i E/D d d W d ( ) & & & t = & W & & > & d d & & = & & ^& t & & ^&

24 & & = & d ed & t & & & W

25 d e d /D d - - d e d /D & e d d /D ^h& d ^ d d d d d D d t d : de / / /D dl E e d d d : de d d d D d

26 D d d : de d d / ' d / d de d / d d d & ^h& d de

27 e d ^ e d ^ e d ^ e d e d e d / de de e d /D d d e d e d d d e d d de de,>l de KZ,>l de / e e /D d ^ e e d d ^,> d de

28 d ^ de d d de d d, de de de e e d d d d e e d /,> e e,> l de e e d d ld,> l de d d e e ld d,> e W e e W /D d d d d de d d, de de de E e d d e h d e d d d d d d de

29 d ^ de /,> e e,> l de e d d e le,> l de d e d d ld,> l de d d d d ld > d e e W /D : d: d de de de de e e e e e e e d d e e e e e e e e e d d,> e W d, e d ^ d: d,> d d: d: e d de

30 d d /D & ed ed l d ed ed d / ed ed d & d e e &, >,> d d d d d / d / de d : de d,> d,> d,> > d,>l > > de > de > de de >deld,>l > > de > de K de,> de de de,>l > de > de > de

31 d / d / d : de d d de d,> de K,> e e /D,>l Zh& t d Zh& / d : de d,> d d d d : / : d d / ^ / Zh& de d d Zh& l / & Zh& d

32 / D d d & & / Zh& d Zh& E Zh& dl d

33 ^ d d ^, de de D e d de D e d de de de e e de D e d de de D e d de de de e e e d e e d : : / K ^ d ^ d d d d

34 ^ d, d: : e e : : d d d W d d e d l W d e d d d d dl d l d dl d td l d td

35 ^ d d / d d d d d / d & d W E d d dl

36 & d de & l e d E, d, d: & / & de e e / l ^ d d - l KZ - d dl W d l d de

37 / d / d ed t d / d e d d ^ / d & e d & e d Z d ^ // / > e t ^ / / e / de

38 ^ /// > AL = AL AL aed, design Total average / d ed ed l > md d ed l > md d d d e d Aed design capacity (C aed,design ) Initial capacity (C initial) Initial capacity (C initial) & e Remaining design capacity (C remaining,design ) de

39 E l d W d d d dl d de de d ^ d K d dl / e e d d / d d ^ d d & e l de

40 d Aed capacity (C aed ) New capacity (C new ) Initial capacity (C initial) & e / d & e l / Z E & e / / d d d / d d d d l ^ d K d d d,> e e

41 ,> l,> l,> t,> d de de,> d E,> /,>,> d,>,>,> / de de,> l & & t ^ / / >,h& ALinitial = Cinitial HCUFinitial,> / d

42 ,> d,h&,> l,h& d,h&,h& l & d,h& d,h& / e d,> /,> l d,h& d : de / : de / l d / lde d e l le

43 z de de de d W de ^ z de de de / d e e d de de d W de l,h& ^,> &,>,> l de de de l ^,h&,h& l l ^,>,> l,h& le ld ^,>,> l,> l,> lldl d : de / : de / l d / le d e Z l l e

44 z de de de d W e d ^ z de de de E e e Z e e / d W e d e ^,> &,>,> l de de l ^,h&,h& l l ^,>,> l d,h& l d e l d ^,>,> l,> l,> l dld d d / d : de d de & e / ld d / d lded d e & d l d led

45 / d ld d e ^ d l d d l z de de de d W ed ded d d C a2 C a1 C new2 C new1 C initial & e d ^ z de de de / d d d d d d ed ed ed d d d d ded d d d W ed ded d d l,h& ed ed ed ed ^,> &,>,> l de led ^,h&,h& l led d E,h& ^,> d,> d,> d l d,h& led ed dlee,> d l d,h& l ed dlde d

46 ^,>,> l,> l,> d l,> d ledlee dlde dle d de

47 e d e d d / CO 2 Natural gas (TJ) Product A - no benchmark - exposed to carbon leakage Fuel oil (TJ) Heat (TJ) Process Product B - no benchmark - exposed to carbon leakage Product C - no benchmark - NOT exposed to carbon leakage &, ^ / > d, > d, > d & > d & > d,> d,> d,> d,> d de

48 & ' d e d d,w /,W & d d d,w d^ d^ d,w d^ K,W E,W ^ ' e d^ /,W d^ d d^ d^ CO 2 Electricity Fuel CHP Heat Non-ETS consumer & ^,W ETS consumer de

49 e d d & d Input fuel P1 (fall-back, exposed) P2 (benchmark, exposed) Flare Non-ETS ext heat Consumers (not exposed) P3 (fall-back, exposed) Steam turbine 1 Ext elec consumers Steam gen H1 Steam turbine 2 Steam gen H2 Compressor Fuel Waste gases Heat Electricity - d - - d - d - Wd Wd Wd & Wd Wd Wd - Wd Wd Wd d - E de

50 & d Input fuel P1 (fall-back, exposed) P2 (benchmark, exposed) Flare Non-ETS Ext ext heat Consumers consumers (not exposed) P3 (fall-back, exposed) Steam turbine 1 Ext elec consumers Steam gen H1 Steam turbine 2 Steam gen H2 Compressor Sub-installation 1 Product benchmark Fuel Waste gases Heat Electricity ^ d d d ld & Wd ^ d - d d - / d Wd - d d ^ d - d Wd

51 & d Input fuel P1 (fall-back, exposed) P2 (benchmark), exposed Flare Non-ETS Ext ext heat Consumers consumers (not exposed) P3 (fall-back, exposed) Steam turbine 1 Ext elec consumers Steam gen H1 Steam turbine 2 Steam gen H2 Compressor Sub-installation 2 Heat benchmark, CL Fuel Waste gases Heat Electricity ^ d - d Wd Wd d^ - d Wd Wd d^ d ^ d d ^ d - ^ d Wd Wd - d d ^ d ^ d ^ d - d, > d Wd Wd

52 & d Input fuel P1 (fall-back, exposed) P2 (benchmark, exposed) Flare Non-ETS Ext ext heat Consumers consumers (not exposed) P3 (fall-back, exposed) Steam turbine 1 Ext elec consumers Steam gen H1 Steam turbine 2 Steam gen H2 Fuel Sub-installation 3 Heat benchmark, non CL Waste gases Compressor Heat Electricity ^ d d ^ d - ^ d > / d^ d^ / d^ - d d ' e ^ d d ^ d ^ d d, > d d^

53 & d Input fuel P1 (fall-back, exposed) P2 (benchmark, exposed) Flare Non-ETS ext heat Consumers (not exposed) P3 (fall-back, exposed) Steam turbine 1 Ext elec consumers Steam gen H1 Steam turbine 2 Steam gen H2 Compressor Sub-installation 4 Fuel benchmark Fuel Waste gases Heat Electricity ^ d - d Wd Wd > d ^ d ^ d - Z / ^ d ^ d - /, > d,> ' e

54 & e Input fuel P1 (fall-back, exposed) P2 (benchmark, exposed) Flare Non-ETS ext heat Consumers (not exposed) P3 (fall-back, exposed) Steam turbine 1 Ext elec consumers Steam gen H1 Steam turbine 2 Steam gen H2 Compressor Sub-installation 5 Historical emissions Fuel Waste gases Heat Electricity ^ d - / Wd Wd - & d d d -, d Wd Wd ^ d ^ d Z - d K d - d - d - d ^ d ^ d d K d D/Eh^ E d & ' e

55 & e Input fuel P1 (fall-back, exposed) P2 (benchmark, exposed) Flare Non-ETS ext heat Consumers (not exposed) P3 (fall-back, exposed) Steam turbine 1 Ext elec consumers Steam gen H1 Steam turbine 2 Steam gen H2 Compressor Fuel Waste gases Heat Electricity d Z

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