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Abstract SYMPHOS 2011

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100<br />

MANUFACTURE OF HIGH-BULK DENSITY ALUMINIUM FLUORIDE FROM<br />

FLUOSILICIC ACID<br />

Alain Dreveton,<br />

AD Process Strategies Sarl, Rue Chaponnière 9, CH-1201<br />

Geneva / SWITZERLAND<br />

AP-O-12<br />

Fuosilicic acid finds its main application in the manufacture of aluminium fluoride being a large volume chemical<br />

mostly produced from fluorspar as high bulk density (HBD) aluminium fluoride and as well from fluosilicic acid<br />

as low bulk density (LBD) aluminium fluoride. Hereby is disclosed new processes for manufacturing anhydrous<br />

hydrofluoric acid (AHF) from fluosilicic acid (FSA) from which (HBD) aluminium fluoride can be produced. Aluminium<br />

fluoride is essentially used as a flux for smelting aluminium by adding it volumetrically to the cells of aluminium<br />

smelters in order to regenerate the cryolite bath. HBD aluminium fluoride is the preferred material and it is fully<br />

produced from fluorspar; none of this material being currently produced from FSA through AHF which process<br />

technology often referred to as the Dry/FSA Process is available, feasible and proven at this time. An opportunity<br />

to invest in profitable projects is really existing. Additionally the manufacture of other downstream products of HF:<br />

refrigerants, fluoropolymers, etc and downstream products of FSA: silicon metal, silicon tetrafluoride, silicas may<br />

offer extra opportunities.<br />

The first process known for manufacturing (LBD) aluminium fluoride from fluosilicic acid was patented by Chemie-<br />

Linz, Austria and many plants were built based on this technology or similar technologies. This process uses the<br />

direct neutralization of the fluosilicic acid with alumina hydroxide in a stirred reactor. It is often referred to as<br />

the Wet/FSA Process. Although this technology tends to be abandoned due to the low density and low fluidity<br />

(flowability) of the product, the high capital cost of the plant and environmental issues resolved partially only<br />

as neutralization of mother liquors may still be required, further developments of this process would refresh this<br />

technology being still accepted by very few players only.<br />

A process to produce AHF / HF from fluosilicic acid was disclosed first by Tennessee Corp., USA and<br />

further by Wellmann-Lord, etc and more lately by Flemmert (Sweden), and Lubon Works, Poland who operated a<br />

small pilot plant. More recently Wengfu, China built a first commercial plant with the technology of Buss Chemtech<br />

AG, Switzerland based on know-how from Lubon Works. The process is based on the mixing of strong fluosilicic<br />

acid with strong sulphuric in a stirred reactor and separating silicon tetrafluoride and extracting the anhydrous<br />

hydrofluoric acid using separation columns. Presently AD Process Strategies Sarl proposes a similar type of<br />

process with major improvements completed to suit the water balance of the phosphoric acid plant; sulphuric<br />

acid containing water that is generated from this HF plant has to be recirculated to the phosphoric acid plant. The<br />

technology is proven, resolves environmental issues, is very profitable as raw material costs are low, capital cost is<br />

reasonable and it offers access to promising markets for HBD aluminium fluoride and anhydrous hydrofluoric acid,<br />

both being large volume chemicals.<br />

For situations described above when the diluted sulphuric acid stream is not returned to the phosphoric<br />

acid plant or can not be recirculated due to technically reasons or not, AD Process Strategies Sarl proposes a new<br />

technology for stand alone HF plants. The proposed process uses fluosilicate as intermediate raw material, which is<br />

transportable not like FSA and reaction of fluosilicate with sulphuric acid. The silicon tetrafluoride and hydrofluoric<br />

acid obtained is treated as per the state of art mentioned above. The diluted sulphuric acid stream from this process<br />

can be preconcentrated and recycled to the phosphoric acid plant or used in production of fertilizers, concentrated<br />

and recycled to the HF reaction or purified and sold.<br />

These technologies are offering high flexibility and can be implemented with confidence in a cost effective manner.<br />

They are real innovations for the fertilizer industry and surely they will be implemented progressively. More and<br />

more projects are under study and hopefully some projects may be executed in the near future….

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