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ACL Ambujanagar NOx Emission Reduction Possibilities by Primary Measures Thermal Process Technology 1

N ox reduction kick-off meeting presentation

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Page 1: N ox reduction kick-off meeting presentation

ACL Ambujanagar

NOx Emission Reduction Possibilities

by

Primary Measures

Thermal Process Technology 1

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NOx

Impact on Environment

Statutory Limits for Cement Plants

Formation in Cement Plants

Ways to reduce formation

Methods to control the emissions

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NOx: Impact on Environment

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NOx Measurement & Reporting

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Country Limit[mg/Nm3]

Comments

EU 500 / 800 IED (2011) – daily average

Germany 500

200-500

TA Luft (2007) – daily average

17th BImSchV – daily average

Switzerland 800

500 / 450

LRV - daily average

Sectoral NOx Agreement - yearly avg.

USA --

~200 - 400

Limits based on „annual loads“

NESHAP for new/modified kilns –

30 d rolling average

India 1000 Proposed limit (spot measurements)

Thailand 805 Spot measurements

Mexico 940 / 1028-1718 New / existing installations

Brasil 800 / 650 / 495 Existing / new installations

NOx Regulatory Requirements

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Holcim Group Average

NOx: ACC – ACL Performance in 2010

Basis: PEP 2010

695

mg

/Nm

3, d

ry a

t 1

0%

O2

CPCB expectation in 2 years

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NOx Formation in Cement Kilns

RT

-76500

14 e 10 x 2 k N NO O N2

O NO O N 2RT

-6300

9 e 10 x 6.3 k The NOX formation in calciner depends on

- Nitrogen content in the fuel

- O2 level in the firing zone.

- Initial NO concentrations in the combustion gas

- Temperature in firing region

- Volatile content in the fuel

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NOx Reduction Measures

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Process Optimization: Primary air and Excess air

NOx Reduction - Primary Measures

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Process Optimization: Fuel to Calciner

NOx Reduction – Primary Measures

Fuel with high volatile content*

Lump fuel(small portion at kiln inlet)

Low nitrogen fuel

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Process Optimization: Typical Nitrogen content of the fuels

NOx Reduction – Primary Measures

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Process Optimization: Burning Zone temperature

NOx Reduction – Primary Measures

Improve process stability

(Kiln feed / fuel feed uniformity, expert optimizer)

Improve kiln feed burnability

(feed mix, fineness)

Avoid over-burning

(strict control of clinker free lime, target >0.8 %)

Optimize burner operation

(Axial / tangential Momentum, fuel fineness)

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Flue gas re-circulation

NOx Reduction – Primary Measures

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Low NOx Burner

Burner designed to reduce flame turbulence by delaying the mixing of

fuel and air and by establishing fuel rich zones for initial combustion

NOx Reduction - Primary Measures

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Low NOx Calciner (Staged combustion)

NOx Reduction – Primary Measures

High Temperature:

Meal split for controlled

hot spot

Reducing Conditions:

Air Split or Calciner

fuel below tertiary air

entry

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Month average NOx emissions for the plants having CEMS

NOx Reduction – Primary Measures

Low NOx

calciners

Mg

/Nm

3, d

ry a

t 1

0%

O2

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Limitations of PRIMARY Measures

Primary measures can be applied as long as there is no negative

process, quality or emission impact.

Process optimizations have priority over NOx optimization

Clinker Quality ( Burning under reduced conditions).

NOx Reduction – Primary Measures

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NOx Reduction – Secondary Measures

Selective Non-Catalytic Reaction (SNCR)

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NOx Reduction – Secondary Measures

Selective Catalytic Reaction (SCR)

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0

20

40

60

80

100

Kiln

ope

ratio

n

Burn

er o

ptimiz

atio

n

Fuel m

ix

LowNOx

PC

SNCR

SCR

% N

Ox r

eduction

Effectiveness of NOx reduction measures

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NOx variations in a day - Normal Operation (13.10.11 00:01 hrs to

14.10.11 00:00 hrs.)

NOx emission at AM 1

~ 200 mg/Nm3

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NOx variations in a month (October 6 – 31, 2011)

NOx emission at GAJ 1N

Ox, m

g/N

m3, dry

@ 1

0%

O2

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NOx variations within the kilns (GAJ 1, GAJ2 and AM)

NOx emissions at Ambujanagar

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Thank You

24

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Typical exhaust gas amounts