PRELIMINARY STUDY OF MANUFACTURING OF SILICON, FERROSILICON AND IRON METAL USING METHANE GAS AND HYDROGEN GAS REDUCTOR
Currently, silicon is widely applied in electronic devices and solar cells. The industrial production of silicon utilizes an electric furnace through the carbothermic reaction, but this process generates carbon dioxide emissions of 4,7-5 tons per 1 ton of silicon. Silicon production has not been...
Saved in:
Main Author: | |
---|---|
Format: | Final Project |
Language: | Indonesia |
Online Access: | https://digilib.itb.ac.id/gdl/view/72898 |
Tags: |
Add Tag
No Tags, Be the first to tag this record!
|
Institution: | Institut Teknologi Bandung |
Language: | Indonesia |
Summary: | Currently, silicon is widely applied in electronic devices and solar cells. The
industrial production of silicon utilizes an electric furnace through the carbothermic
reaction, but this process generates carbon dioxide emissions of 4,7-5 tons per 1 ton
of silicon. Silicon production has not been carried out in Indonesia. Besides silicon,
one of the most important metals in our lives is iron. Iron is further processed into
steel and applied in various sectors such as construction, infrastructure, and
transportation. Iron is reduced through the carbothermic process and generates
carbon dioxide emissions of 1,3-1,8 tons per 1 ton of steel. Increased carbon dioxide
gas can lead to an increase in the earth's surface temperature. Therefore, the metal
smelting industry needs to find environmentally friendly alternative reductants.
This research aims to study the influence of the type of reducing gas, the ratio of
silica sand and iron ore composition, and the reduction holding time, specifically
focusing on experiments with methane gas, on the silicon and iron content in the
metal and slag.
The experiment involved mixing silica sand and iron ore at composition ratios of
0:100, 20:80, 40:60, 60:40, 80:20, and 100:0. The mixture was placed in an alumina
crucible boat and reduced in a horizontal tube furnace at a temperature of 900°C
using methane gas (30 minutes and 3 hours) and hydrogen gas (3 hours). The
reducing gas was supplied at a rate of 0.75 L/minute, while argon gas was supplied
at a rate of 0.25 L/minute. The reduced samples were melted in a vertical tube
furnace for 2 hours at a temperature of 1550°C with an argon gas flow rate of 1
L/minute. The reduced samples were analyzed using XRD to determine phase
changes. Meanwhile, the melted samples were analyzed using SEM-EDS to
determine the chemical composition of the metal and slag.
Methane exhibited a more aggressive reduction rate compared to hydrogen in the
silica sand samples, with a silicon content of 71.39% in the metal. The iron content
in the metal from the reduction of iron ore using methane for 30 minutes and
hydrogen for 3 hours did not show significant differences. The silicon content in
the metal increased with an increase in the amount of silica sand in the mixture,
while the iron content decreased. The mixture with a composition of 60% silica
sand - 40% iron ore yielded the highest silicon content in the metal at 28.9%. A 3-
hour holding time in methane reduction of the iron ore and the mixture samples
resulted in carbon deposition and metal dusting. Meanwhile, in the 100% silica sand
sample, the silicon content in the metal increased with an increase in the reduction
holding time. |
---|