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172 SOLAR GRADE SILICON FEEDSTOCK<br />

• The process is operated batchwise.<br />

• Large amount of by-products need to be handled or recycled.<br />

More recent developed processes have attempted to overcome some of these<br />

disadvantages.<br />

5.4.2 The Union Carbide Process<br />

Research on this process was initiated in 1976 after the international oil crisis. The US<br />

Government funded several projects with the objective of finding a route to inexpensive<br />

solar grade polysilicon. The Union Carbide process for silane production, with fluidised<br />

bed production of polysilicon, was selected for further funding. When the funding was<br />

not provided for political reasons, Union Carbide decided to use the silane technology<br />

for the production of semiconductor grade polysilicon. Silane deposition technology for<br />

polysilicon rods was licensed from Komatsu Electronic Metals, Japan. In 1990, the business<br />

was sold to Komatsu, which became Advanced Silicon Materials (ASiMI). By 1998,<br />

two large industrial plants were constructed in the United States with the nominal capacity<br />

of 5500 MT polysilicon, thus ranking ASiMI as number two or three worldwide among<br />

the polysilicon producers. A schematic overview of the process is given in Figure 5.4.<br />

The main process steps are as follows:<br />

The hydrogenation of tetrachlorosilane through a mass bed of silicon metal is carried out<br />

in a fluidised bed reactor as already described by equation (5.33).<br />

The trichlorosilane is separated by distillation while the unreacted tetrachlorosilane is<br />

recycled back to the hydrogenation reactor.<br />

MG-Si: Metallurgical<br />

grade silicon<br />

TCS: Trichlorosilane<br />

TET: Tetrachlorosilane<br />

DCS: Dichlorosilane<br />

TCS synthesis<br />

MG-Si<br />

by<br />

Separation<br />

H 2<br />

hydrogenation<br />

TCS TCS/TET<br />

of<br />

TET by<br />

TET<br />

TET in<br />

DCS<br />

distillation<br />

fluidised bed<br />

Redistribution 2<br />

reactor<br />

Residues:<br />

spent mass<br />

TET<br />

Low boiling<br />

impurities<br />

TCS<br />

Redistribution 1<br />

in catalytic<br />

column<br />

Separation<br />

DCS/TET/TCS<br />

distillation<br />

in catalytic<br />

column<br />

Separation<br />

DCS/TET/SiH 4<br />

Purification<br />

of SiH 4<br />

distillation<br />

Electrical<br />

energy<br />

Pyrolysis<br />

on heated<br />

silicon rods<br />

SiH 4<br />

H 2<br />

Poly<br />

silicon<br />

TET<br />

Figure 5.4<br />

A schematic representation of the Union Carbide Polysilicon process

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