17.06.2013 Views

Trends in Nitrogen Fertilizer Industries from a Contractor's View

Trends in Nitrogen Fertilizer Industries from a Contractor's View

Trends in Nitrogen Fertilizer Industries from a Contractor's View

SHOW MORE
SHOW LESS

Create successful ePaper yourself

Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.

Energy Consumption of Ammonia Production<br />

Stoichiometric m<strong>in</strong>imum energy consumption: = 5 Gcal/tNH3<br />

(based on Methane as feedstock)<br />

“Perfect” plant could not work <strong>in</strong> transient conditions nor partial load<br />

Waste Heat available at low temperature can not be recovered, Cool<strong>in</strong>g System to be<br />

applied<br />

Limitations <strong>from</strong> Material of Construction<br />

(e.g. Metal Dust<strong>in</strong>g; Dew po<strong>in</strong>t <strong>in</strong> flue gas)<br />

Extra energy <strong>in</strong> product (pressure / refrigeration)<br />

Incremental <strong>in</strong>vestment <strong>in</strong> further efficiency to be balanced aga<strong>in</strong>st sav<strong>in</strong>gs <strong>in</strong> energy<br />

cost<br />

AFA Annual Conference<br />

Cairo, April 2011<br />

Dr. Richard Saure<br />

Energy Consumption of Ammonia Production<br />

M<strong>in</strong>imum Energy Consumption<br />

<strong>Nitrogen</strong> fixation (i.e. NH3 synthesis) is most energy-<strong>in</strong>tensive process step for production of<br />

nitrogenous fertilizers such as Urea and Ammonium Nitrate<br />

Energy Consumption<br />

[Gcal/tNH3]<br />

10<br />

9<br />

8<br />

7<br />

6<br />

5<br />

4<br />

3<br />

2<br />

1<br />

AFA Annual Conference<br />

Cairo, April 2011<br />

Dr. Richard Saure<br />

EFMA (2000) – Best Available<br />

Technologies<br />

0<br />

1960 1970 1980 1990 2000 2010 2020<br />

Year of Plant Commission<strong>in</strong>g<br />

<strong>from</strong> literature<br />

plants <strong>in</strong> operation<br />

plants under construction<br />

actual energy consumption ≥ 6.7 Gcal/tNH3 gap due to<br />

- limited convertibility of rejected heat<br />

(2 nd law of thermodynamics)<br />

- extra energy <strong>in</strong> product (pressure / refrigeration)<br />

- optimization for plant economics<br />

m<strong>in</strong>imum energy consumption <strong>from</strong><br />

stoichiometric po<strong>in</strong>t of view = 5 Gcal/tNH3 (based on Methane as feedstock)<br />

LHV of Ammonia = 4.44 Gcal/t NH3<br />

7

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!