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This document has not been fully peer reviewed and ong>theong> ong>informationong> within is not validated nor endorsed by ong>theong> TWG on LVIC-S or by ong>theong> European Commission, it is meant for ong>informationong>, only The use of alternatives to aluminium hydroxide, like bauxite, will create a waste coming out of ong>theong> process mainly consisting of an insoluble silica rest. This is, however, less than when bauxite is used for ong>theong> production of aluminium hydroxide [50, CEFIC-INCOPA, 2004]. In ong>theong> production of aluminium sulphate products containing iron, ong>theong> iron eiong>theong>r comes directly from ong>theong> raw material (bauxite), or is separately added to ong>theong> reactor, or is mixed with ong>theong> final product. The process flow diagram of aluminium sulphate production is given in Figure 1.4. 8 Rest Al (OH) 3 Liquid production Dilution Filtration Reaction H 2 SO 4 Water Solid production Crystallisation Screening Grinding Storage Storage Figure 1.4: Process flow diagram of aluminium sulphate production [50, CEFIC-INCOPA, 2004] Cooling (water or air) Dust to process Gas cleaning If air is used in direct contact with ong>theong> product, ong>theong> air is cleaned in a gas cleaning system. All dust that is separated is returned to ong>theong> process [50, CEFIC-INCOPA, 2004]. 1.2.3 Current consumption and emission levels 1.2.3.1 Consumption of raw materials Consumption figures for solid aluminium sulphate are about: 50 % sulphuric acid, 30 % aluminium hydroxide, and 20 % water. The consumption figures for liquid products are about: 20 – 25 % sulphuric acid, 12 – 15 aluminium hydroxide and 60 – 65 % water. The reaction is almost complete, ong>theong> yield of ong>theong> raw materials being nearly 100 % [50, CEFIC-INCOPA, 2004]. 1.2.3.2 Major environmental impacts Typical energy and water consumption figures and emissions values for liquid aluminium sulphate are given in Table 1.5.

This document has not been fully peer reviewed and ong>theong> ong>informationong> within is not validated nor endorsed by ong>theong> TWG on LVIC-S or by ong>theong> European Commission, it is meant for ong>informationong>, only Energy consumption kWh/tonne product Comments Electricity

This document has not been fully peer reviewed and <str<strong>on</strong>g>the</str<strong>on</strong>g> <str<strong>on</strong>g>informati<strong>on</strong></str<strong>on</strong>g> within is not validated nor endorsed by <str<strong>on</strong>g>the</str<strong>on</strong>g> TWG<br />

<strong>on</strong> LVIC-S or by <str<strong>on</strong>g>the</str<strong>on</strong>g> European Commissi<strong>on</strong>, it is meant for <str<strong>on</strong>g>informati<strong>on</strong></str<strong>on</strong>g>, <strong>on</strong>ly<br />

The use of alternatives to aluminium hydroxide, like bauxite, will create a waste coming out of<br />

<str<strong>on</strong>g>the</str<strong>on</strong>g> process mainly c<strong>on</strong>sisting of an insoluble silica rest. This is, however, less than when<br />

bauxite is used for <str<strong>on</strong>g>the</str<strong>on</strong>g> producti<strong>on</strong> of aluminium hydroxide [50, CEFIC-INCOPA, 2004].<br />

In <str<strong>on</strong>g>the</str<strong>on</strong>g> producti<strong>on</strong> of aluminium sulphate products c<strong>on</strong>taining ir<strong>on</strong>, <str<strong>on</strong>g>the</str<strong>on</strong>g> ir<strong>on</strong> ei<str<strong>on</strong>g>the</str<strong>on</strong>g>r comes directly<br />

from <str<strong>on</strong>g>the</str<strong>on</strong>g> raw material (bauxite), or is separately added to <str<strong>on</strong>g>the</str<strong>on</strong>g> reactor, or is mixed with <str<strong>on</strong>g>the</str<strong>on</strong>g> final<br />

product.<br />

The process flow diagram of aluminium sulphate producti<strong>on</strong> is given in Figure 1.4.<br />

8<br />

Rest<br />

Al (OH) 3<br />

Liquid<br />

producti<strong>on</strong><br />

Diluti<strong>on</strong><br />

Filtrati<strong>on</strong><br />

Reacti<strong>on</strong><br />

H 2 SO 4<br />

Water<br />

Solid<br />

producti<strong>on</strong><br />

Crystallisati<strong>on</strong><br />

Screening<br />

Grinding<br />

Storage Storage<br />

Figure 1.4: Process flow diagram of aluminium sulphate producti<strong>on</strong><br />

[50, CEFIC-INCOPA, 2004]<br />

Cooling<br />

(water or air)<br />

Dust to<br />

process<br />

Gas<br />

cleaning<br />

If air is used in direct c<strong>on</strong>tact with <str<strong>on</strong>g>the</str<strong>on</strong>g> product, <str<strong>on</strong>g>the</str<strong>on</strong>g> air is cleaned in a gas cleaning system. All<br />

dust that is separated is returned to <str<strong>on</strong>g>the</str<strong>on</strong>g> process [50, CEFIC-INCOPA, 2004].<br />

1.2.3 Current c<strong>on</strong>sumpti<strong>on</strong> and emissi<strong>on</strong> levels<br />

1.2.3.1 C<strong>on</strong>sumpti<strong>on</strong> of raw materials<br />

C<strong>on</strong>sumpti<strong>on</strong> figures for solid aluminium sulphate are about: 50 % sulphuric acid, 30 %<br />

aluminium hydroxide, and 20 % water. The c<strong>on</strong>sumpti<strong>on</strong> figures for liquid products are about:<br />

20 – 25 % sulphuric acid, 12 – 15 aluminium hydroxide and 60 – 65 % water. The reacti<strong>on</strong> is<br />

almost complete, <str<strong>on</strong>g>the</str<strong>on</strong>g> yield of <str<strong>on</strong>g>the</str<strong>on</strong>g> raw materials being nearly 100 % [50, CEFIC-INCOPA,<br />

2004].<br />

1.2.3.2 Major envir<strong>on</strong>mental impacts<br />

Typical energy and water c<strong>on</strong>sumpti<strong>on</strong> figures and emissi<strong>on</strong>s values for liquid aluminium<br />

sulphate are given in Table 1.5.

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