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1. Introduction - Firenze University Press

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Te 1000<br />

mp<br />

era<br />

900<br />

tur 800<br />

e<br />

[°C 700<br />

]<br />

600<br />

Temperatuur, °C<br />

500<br />

400<br />

300<br />

200<br />

100<br />

Stoom Steam>electricity > elektriciteit<br />

met With voorverwarming;<br />

preheating, potential<br />

Potentieel 191 GJ/h 191 GJ/h<br />

0 Stoom Steam>electricity > elektriciteit<br />

0 zonder 50 voorverwarming;<br />

100 150<br />

Without preheating,<br />

Potentieel 180 GJ/h<br />

200 250<br />

Enthalpy, GJ/h<br />

300 350 400 450<br />

potential 191 GJ/h<br />

Fig 4. Grand composite curve of the pinch analysis<br />

294<br />

Base_case<br />

Case 1 - mod. reactor pre-heat<br />

Case 2 - no reactor preheat<br />

voorverwarming Preheating above boven pinch pinch point<br />

verbetert does not increase electricity<br />

elektriciteitspotentieel potential<br />

niet<br />

The pinch analysis learns that there is an excess of heat. No heat source is required except for the<br />

zinc ore. The aim of the pinch analysis is, therefore, to maximise the amount of steam that can be<br />

used for power production. Nyrstar has a high power consumption, which is required during the<br />

entire year. The potential for energy saving is 180 GJ per hour without reactor preheating or 191 GJ<br />

per hour if the reactor is preheated.<br />

Two scenarios for heat integration have been made. In scenario 1 the thermal energy saving is 73<br />

GJ per hour leading to an electrical potential of 4.6 MWe and an investment of € <strong>1.</strong>8 million. In<br />

scenario 2 the thermal energy saving is 92 GJ per hour leading to an electrical potential of 5.3 MWe<br />

with an associated investment of € 2.1 million<br />

3.2.3. Process intensification<br />

The results of the process intensification scan are solutions or solution directions, and thereby differ<br />

from regular analyses.<br />

The process intensification scan suggests to increase the understanding of the processes in the<br />

boiler, by completing the mass and energy balances, making a chemical analysis of the scaling in<br />

the bed and determining the effect of the process parameters on the bed. On the basis of this<br />

information an improved redesign of the roaster and boiler can be made.<br />

For the gas cleaning section a process simulation study is suggested. For the long term new<br />

technologies can be considered. The leaching and purification section have different steps, which<br />

occur at different pH. It is proposed to investigate the possibilities of using membranes to extract<br />

water, when the pH needs to be decreased, i.e. acidity increased. It is expected that the process will<br />

become more stable and easier to control. Demands on the material of the membrane will be an<br />

important research parameter.

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