| نویسندگان | علی اکبر فرزانگان, |
| همایش | XV. INTERNATIONAL MINERAL PROCESSING SYMPOSIUM AND EXHIBITION |
| تاریخ برگزاری همایش | 2016-10-19 - 2016-10-21 |
| محل برگزاری همایش | 39 - استانبول |
| ارائه به نام دانشگاه | دانشگاه استانبول ITU |
| نوع ارائه | سخنرانی |
| سطح همایش | بین المللی |
چکیده مقاله
A numerical approach has been used to investigate the effect of vertical
baffling and height to diameter ratio on the axial mixing in flotation columns using a
two-phase computational fluid dynamics model. The baffle is a plate located
perpendicular to the cross section of the column with a length of 2.8 m and thickness
of 0.4 cm. The computational domain is a column with a circular cross section having
a height of 3.2 m and a diameter of 10 cm. In order to reduce computing demand and
simplify the problem, it was assumed that the column is already filled with water, and
air enters from the lateral and upper surfaces of a cylindrical sparger with a length of
15 cm and a diameter of 1 cm located vertically at the bottom of the column. To validate
simulation results, a series of laboratory flotation column experiments have been
performed under the above-mentioned conditions. Three-dimensional simulations
were executed using a Eulerian two-phase model for both non-baffled and baffled
columns. The simulated pressure values on the wall at 0.2 m and 2.8 m height of the
non-baffled column were in good agreement with experimentally measured values with
the highest relative difference of less than 1.33 %. Comparison of the computational
results for the non-baffled and baffled columns showed that baffling can reduce water
axial velocity up to 17 %, which consequently reduces the axial mixing in the column
and increases flotation recovery. Study of the effects of height to diameter ratio showed
that effect of baffling in columns with lower aspect ratios is more prevalent for reducing
the axial mixing.