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Abstract SYMPHOS 2011

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RECENT IMPROVEMENT OF THE GRANULATOR PIPE REACTOR FOR THE<br />

PRODUCTION OF GRANULAR AMMONIUM PHOSPHATES<br />

Donal S. Tunks<br />

Jacobs Engineering S.A., Casablanca, MOROCCO<br />

PH-O-14<br />

A Granulator Pipe Reactor can be used in the production of MAP/DAP to increase the production capacity while<br />

substantially reducing the overall fuel consumption. This is accomplished through the mixing of ammonia and<br />

phosphoric acid within the Granulator Pipe Reactor. From the high heat of reaction of this mixing, water is<br />

evaporated prior to the drying step and this causes the significant drop in fuel consumption.<br />

A recent development by Jacobs Engineering involves an elaborate continuous control scheme that maintains the<br />

desired product quality while minimizing fuel consumption by utilizing on-line and at-line measurements.<br />

Adding a Granulator Pipe Reactor to an existing facility is a relatively simple modification which and can pay itself<br />

off in as little as 4 months.<br />

fertilizers.<br />

HOW TO INCREASE THE OVERALL OUTPUT OF PHOSPHORIC ACID<br />

EVAPORATION LOOPS WHILE REDUCING THEIR TOTAL COSOWNERSHIP<br />

Loic BERNARD<br />

SGL Group Saint Martin d’Hères/FRANCE<br />

PH-O-15<br />

The phosphoric acid commercial concentration has been set at 54%. The different wet phosphoric acid processes<br />

used around the world produce green acids with concentrations between 28 and 44% P2O5.thus meaning that<br />

depending on the production process, the acid coming out from the reactor tanks must be concentrated in 1 to 3<br />

evaporation stages. Each evaporation stage consists in an axial pump, a heat exchanger, a flash tank, a scrubber,<br />

and condenser and a vacuum pump. Since industrial green phosphoric acid is extremely corrosive, rubber lined flash<br />

tank and piping, a graphite heat exchanger and an axial pump in nickel-alloy are usually used.<br />

In order to sustain a high productivity of the evaporation loop, the appropriateness between the axial pump<br />

characteristics (curve) and the heat exchanger characteristics (tube diameter, length, cross section) is one of the<br />

key to success. A high velocity in the heat exchanger means a better overall heat transfer coefficient and therefore<br />

a larger output. It might also result in a lower fouling and therefore longer evaporation cycles between cleaning<br />

cycles. However, throughout the complete evaporation cycle, the progressive fouling of the heat exchanger will<br />

result in lower performances, higher pressure drops and therefore lower velocities thus leading to the further<br />

reduction of the performances. The proper selection, design and sizing of the axial pump (construction design and<br />

materials, characteristic curve) and of the graphite heat exchanger (graphite quality, cross section, tube length,<br />

steam bustle, carbon fiber reinforced tubes, expansion system) associated with smooth operations (especially<br />

during start-ups and shut-downs) guaranty a higher productivity, a better reliability, a longer equipment life time<br />

and therefore overall a much higher output and a lower total cost of ownership.<br />

63

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