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Reaction of Si with CuCl

CuCl was found to effectively catalyze the direct process reaction and significantly

reduce the length of the induction period.

18

Its reaction with silicon is seen as a key

reaction and a model for forming catalytically active surface species in the direct

process.

19

The thermodynamics and kinetics aspects of the Si and CuCl reaction has

been extensively studied. It is proposed that the reaction pathway go through reactions

10 and 11 to generate SiCl

4

and copper silicides (Cu

x

Si, x = 3, 5, etc., depending on Si

and CuCl ratio).

20-22

This manuscript reports new methods for investigating this

reaction.

Si + 4CuCl ––> 4Cu + SiCl

4

(10)

Si + xCu ––> Cu

x

Si (x = 3, 5, etc., depending on Si and CuCl ratio)

(11)

Experimental details

Reaction mass was loaded into a reactor with a constant flow of N

2

passing through.

The reactor was heated up to and maintained at 320 °C. The gas products were

separated isothermally by an Agilent 7890 GC instrument with 100 °C column

temperature and 3.6 mL/min helium flow. A thermal conductivity detector (TCD) was

used. Peak identifications were confirmed by injecting known standards. Based on the

N

2

flow rate (45 sccm, 3.4 g/hr) and N

2

-to-SiCl

4

peak-intensity ratio, SiCl

4

formation

rate was calculated. The reaction was also performed in a chemisorption analyser

(Micromeritics AutoChem II) for better temperature control. The SiCl

4

product was

monitored by a mass spectrometer (MKS-Cirrus) with cycle-time of 0.1 minute. In

these experiments, ~0.5 g reaction mass was used and N

2

flow rate was set at 40

sccm.

Results and discussion

Figure 1 shows a GC chromatogram of the gas product mixture from the reaction of

Si with CuCl. The GC method described in the experimental details allowed good

separation of all the products exiting the reactor. The GC cycle time was slightly

shorter than 2 minutes. We found that increasing the column temperature or flow rate

did not significant decrease cycle time. On the other hand, the N

2

and HCl peaks co-

eluted at higher temperatures. SiCl

4

was found to be the main product, accounting for

greater than 95% of the mixture excluding N

2

. There were also small amounts of HCl

and HSiCl

3

. We speculate that HCl was generated from reaction of SiCl

4

with trace

amount of moisture left in the reaction mass. The HSiCl

3

could be generated from

reaction of HCl gas with Si. Less HCl and HSiCl

3

were generated from the reaction

mass with longer drying time, confirming that moisture was involved in formation of

these by-products. The finding here supports previous proposals that SiCl

4

is the main

gas phase product from the reaction of Si with CuCl.

20

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