5 research outputs found
Evaluation of volumetric strain quantities and types of volumetric strain curves under failure-deformation process of hard brittle rocks
Purpose. The aim of this work is to show whether or not a relationship exist among the different volumetric strain quantities and to assess also whether the volumetric quantities are related to the different types of volumetric strain curves under failure-deformation process of hard brittle rocks.
Methods. Tests were conducted to determine the post failure stress-strain curves of different 83 rocks types under uniaxial compression using a closed loop servo-controlled testing system in accordance to ISRM (International Society for Rock Mechanics) suggested standards.
Findings. The result show that the volumetric strains quantities are related by power form law. It was established that there is a connection between the volumetric strains quantities and the types of the volumetric strains curves. The first type volumetric strain curves contains the Class I and progress to Class II while the type three volumetric strain curves are entirely Class II rock.
Originality. No experimental results have been published, which describe the connection between the type of volumetric strain curves and volumetric strain quantities or attempt to relate the volumetric strain quantities with type of post-failure stress-strain characteristic curves response of rocks under uniaxial compression. Most researchers in rock mechanics studies have so far been focused on the crack damage stress (Οcd) and uniaxial compressive strength (Οc) of characteristic stress levels during compression in which Οcd = Ζcd and Οcd = Οc to study deformation behavior of rocks.
Practical implications. It was also observed that the difficulty in obtaining the post-failure curves increases from type one to type two and type three volumetric strain curves respectively. It could guide personnel conducting tests using closed-loop servo-controlled testing system, if dangerous situation or equipment damage could occur (especially with the third type deformation process) so that testing is performed safely. It could also be useful in understand-ding the total process of specimen deformation and estimation of the rocks brittleness (e.g. brittle for Class II and less brittle or ductile for Class I).ΠΠ΅ΡΠ°. ΠΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½Π½Ρ ΡΠ° ΠΎΡΡΠ½ΠΊΠ° Π²Π·Π°ΡΠΌΠΎΠ·Π²βΡΠ·ΠΊΡ ΠΌΡΠΆ ΡΡΠ·Π½ΠΈΠΌΠΈ Π²Π΅Π»ΠΈΡΠΈΠ½Π°ΠΌΠΈ ΡΠ° ΡΠΈΠΏΠ°ΠΌΠΈ ΠΊΡΠΈΠ²ΠΈΡ
ΠΎΠ±βΡΠΌΠ½ΠΎΡ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΡΡ Ρ ΠΏΡΠΎΡΠ΅ΡΡ ΠΎΠ΄Π½ΠΎΠΎΡΡΠΎΠ²ΠΎΠ³ΠΎ ΡΡΠΈΡΠΊΡ ΠΆΠΎΡΡΡΠΊΠΈΡ
ΠΊΡΠΈΡ
ΠΊΠΈΡ
ΠΏΠΎΡΡΠ΄.
ΠΠ΅ΡΠΎΠ΄ΠΈΠΊΠ°. ΠΠΎΠ²Π½Ρ ΠΊΡΠΈΠ²Ρ Π½Π°ΠΏΡΡΠΆΠ΅Π½Π½Ρ ΠΉ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΡΡ Π²ΠΈΠ·Π½Π°ΡΠ°Π»ΠΈΡΡ ΠΏΡΠΈ Π½Π΅ΠΎΠ±ΠΌΠ΅ΠΆΠ΅Π½ΠΎΠΌΡ ΠΎΠ΄Π½ΠΎΠΎΡΡΠΎΠ²ΠΎΠΌΡ Π²ΠΈΠΏΡΠΎΠ±ΡΠ²Π°Π½Π½Ρ Π½Π° ΡΡΠΈΡΠΊ Π· Π²ΠΈΠΊΠΎΡΠΈΡΡΠ°Π½Π½ΡΠΌ ΡΠΈΡΡΠ΅ΠΌΠΈ ΡΠ΅ΡΠ²ΠΎΠΊΠ΅ΡΠΎΠ²Π°Π½ΠΎΠ³ΠΎ ΠΊΠΎΠ½ΡΡΠΎΠ»Ρ ΡΠ· Π·Π°ΠΌΠΊΠ½ΡΡΠΈΠΌ ΠΊΠΎΠ½ΡΡΡΠΎΠΌ Π΄Π»Ρ ΠΎΡΡΠ½ΠΊΠΈ ΠΌΠ΅Ρ
Π°Π½ΡΡΠ½ΠΈΡ
Π²Π»Π°ΡΡΠΈΠ²ΠΎΡΡΠ΅ΠΉ 83 ΡΡΠ·Π½ΠΈΡ
ΡΠΈΠΏΡΠ² ΠΏΠΎΡΡΠ΄ (53 Π²ΠΈΠ²Π΅ΡΠΆΠ΅Π½ΠΈΡ
, 10 ΠΎΡΠ°Π΄ΠΎΠ²ΠΈΡ
Ρ 20 ΠΌΠ΅ΡΠ°ΠΌΠΎΡΡΡΡΠ½ΠΈΡ
). ΠΡΠΎΡΠ΅Π΄ΡΡΠΈ Π²ΠΈΠΏΡΠΎΠ±ΡΠ²Π°Π½Ρ Π΄Π»Ρ Π²ΠΈΠ·Π½Π°ΡΠ΅Π½Π½Ρ ΠΏΠΎΠ²Π½ΠΈΡ
ΠΊΡΠΈΠ²ΠΈΡ
Π½Π°ΠΏΡΡΠΆΠ΅Π½Ρ Ρ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΡΠΉ Π³ΡΡΡΡΠΊΠΈΡ
ΠΏΠΎΡΡΠ΄, Π° ΡΠ°ΠΊΠΎΠΆ ΠΏΠ°ΡΠ°ΠΌΠ΅ΡΡΡΠ² ΡΡ
ΠΌΡΡΠ½ΠΎΡΡΡ ΠΏΡΠΎΠ²ΠΎΠ΄ΠΈΠ»ΠΈΡΡ Π²ΡΠ΄ΠΏΠΎΠ²ΡΠ΄Π½ΠΎ Π΄ΠΎ Π·Π°ΠΏΡΠΎΠΏΠΎΠ½ΠΎΠ²Π°Π½ΠΎΠ³ΠΎ ISRM ΠΌΠ΅ΡΠΎΠ΄Ρ.
Π Π΅Π·ΡΠ»ΡΡΠ°ΡΠΈ. ΠΠΎΡΠ»ΡΠ΄ΠΆΠ΅Π½Π½Ρ ΠΏΠΎΠΊΠ°Π·Π°Π»ΠΈ, ΡΠΎ Π·Π°Π»Π΅ΠΆΠ½ΡΡΡΡ Π²Π΅Π»ΠΈΡΠΈΠ½ ΠΎΠ±βΡΠΌΠ½ΠΎΡ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΡΡ ΠΎΠΏΠΈΡΡΡΡΡΡΡ ΡΡΠ΅ΠΏΠ΅Π½Π΅Π²ΠΈΠΌ
Π·Π°ΠΊΠΎΠ½ΠΎΠΌ. ΠΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½ΠΎ, ΡΠΎ ΡΡΠ½ΡΡ Π·Π²βΡΠ·ΠΎΠΊ ΠΌΡΠΆ Π²Π΅Π»ΠΈΡΠΈΠ½Π°ΠΌΠΈ ΠΎΠ±βΡΠΌΠ½ΠΎΡ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΡΡ ΡΠ° ΡΠΈΠΏΠ°ΠΌΠΈ ΠΊΡΠΈΠ²ΠΈΡ
, ΡΠΎ ΡΡ ΠΎΠΏΠΈΡΡΡΡΡ. ΠΠ΅ΡΡΠΈΠΉ ΡΠΈΠΏ ΠΊΡΠΈΠ²ΠΈΡ
ΠΎΠ±βΡΠΌΠ½ΠΎΡ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΡΡ Π²ΡΠ΄ΠΏΠΎΠ²ΡΠ΄Π°Ρ ΠΏΠΎΡΠΎΠ΄Π°ΠΌ ΠΊΠ»Π°ΡΡ I Π· ΠΏΠ΅ΡΠ΅Ρ
ΠΎΠ΄ΠΎΠΌ Π΄ΠΎ ΠΊΠ»Π°ΡΡ II, Ρ ΡΠΎΠΉ ΡΠ°Ρ ΡΠΊ ΠΊΡΠΈΠ²Ρ ΡΡΠ΅ΡΡΠΎΠ³ΠΎ ΡΠΈΠΏΡ ΠΏΠΎΠ²Π½ΡΡΡΡ Π²ΡΠ΄ΠΏΠΎΠ²ΡΠ΄Π°ΡΡΡ ΠΏΠΎΡΠΎΠ΄Π°ΠΌ ΠΊΠ»Π°ΡΡ II.
ΠΠ°ΡΠΊΠΎΠ²Π° Π½ΠΎΠ²ΠΈΠ·Π½Π°. ΠΠΏΠ΅ΡΡΠ΅ Π΅ΠΊΡΠΏΠ΅ΡΠΈΠΌΠ΅Π½ΡΠ°Π»ΡΠ½ΠΈΠΌ ΡΠ»ΡΡ
ΠΎΠΌ Π²ΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½ΠΎ Π²Π·Π°ΡΠΌΠΎΠ·Π²βΡΠ·ΠΎΠΊ ΠΌΡΠΆ ΡΠΈΠΏΠ°ΠΌΠΈ ΠΊΡΠΈΠ²ΠΈΡ
ΠΎΠ±βΡΠΌΠ½ΠΎΡ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΡΡ ΡΠ° ΡΡ Π²Π΅Π»ΠΈΡΠΈΠ½ΠΎΡ. ΠΡΠΎΠ±Π»Π΅Π½Ρ ΠΏΠ΅ΡΡΡ ΡΠΏΡΠΎΠ±ΠΈ ΠΏΠΎΠ²βΡΠ·Π°ΡΠΈ Π²Π΅Π»ΠΈΡΠΈΠ½Ρ ΠΎΠ±βΡΠΌΠ½ΠΎΡ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΡΡ Π· ΠΊΡΠΈΠ²ΠΈΠΌΠΈ Π½Π°ΠΏΡΡΠΆΠ΅Π½Π½Ρ β Π΄Π΅ΡΠΎΡΠΌΠ°ΡΡΡ ΠΏΠΎΡΡΠ΄ ΠΏΡΡΠ»Ρ ΡΡΠΉΠ½ΡΠ²Π°Π½Π½Ρ ΠΏΡΠΈ ΠΎΠ΄Π½ΠΎΠΎΡΡΠΎΠ²ΠΎΠΌΡ ΡΡΠΈΡΠΊΡ, Ρ ΡΠΎΠΉ ΡΠ°Ρ ΡΠΊ ΠΏΠΎΠΏΠ΅ΡΠ΅Π΄Π½Ρ ΡΠ΅Π·ΡΠ»ΡΡΠ°ΡΠΈ ΠΎΡΡΠΈΠΌΠ°Π½Ρ ΠΏΡΠ΄ ΡΠ°Ρ ΡΡΠΈΡΠΊΡ.
ΠΡΠ°ΠΊΡΠΈΡΠ½Π° Π·Π½Π°ΡΠΈΠΌΡΡΡΡ. Π‘ΠΊΠ»Π°Π΄Π½ΡΡΡΡ ΠΎΡΡΠΈΠΌΠ°Π½Π½Ρ ΠΊΡΠΈΠ²ΠΈΡ
Π΄Π»Ρ ΡΡΠ°Π½Ρ ΠΏΠΎΡΠΎΠ΄ΠΈ ΠΏΡΡΠ»Ρ ΡΡΠΉΠ½ΡΠ²Π°Π½Π½Ρ Π·Π±ΡΠ»ΡΡΡΡΡΡΡΡ Π· ΠΏΠ΅ΡΠ΅Ρ
ΠΎΠ΄ΠΎΠΌ Π²ΡΠ΄ 1 ΡΠΈΠΏΡ ΠΊΡΠΈΠ²ΠΈΡ
ΠΎΠ±βΡΠΌΠ½ΠΎΡ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΡΡ Π΄ΠΎ 2 Ρ 3 ΡΠΈΠΏΡ, ΡΠΎ Ρ Π²Π°ΠΆΠ»ΠΈΠ²ΠΈΠΌ Π°ΡΠΏΠ΅ΠΊΡΠΎΠΌ Π΄Π»Ρ Π±Π΅Π·ΠΏΠ΅ΡΠ½ΠΎΠ³ΠΎ
ΡΠ΅ΡΡΡΠ²Π°Π½Π½Ρ ΠΏΠΎΡΡΠ΄ ΠΏΠ΅ΡΡΠΎΠ½Π°Π»ΠΎΠΌ. Π Π΅Π·ΡΠ»ΡΡΠ°ΡΠΈ ΡΠΎΠ±ΠΎΡΠΈ ΠΏΡΠ΅Π΄ΡΡΠ°Π²Π»ΡΡΡΡ ΡΠ½ΡΠ΅ΡΠ΅Ρ Π΄Π»Ρ ΡΠΎΠ·ΡΠΌΡΠ½Π½Ρ Π·Π°Π³Π°Π»ΡΠ½ΠΈΡ
ΠΏΡΠΎΡΠ΅ΡΡΠ²
Π΄Π΅ΡΠΎΡΠΌΠ°ΡΡΡ Π·ΡΠ°Π·ΠΊΠ° ΡΠ° ΠΎΡΡΠ½ΠΊΠΈ ΠΊΡΠΈΡ
ΠΊΠΎΡΡΡ ΠΏΠΎΡΡΠ΄ (Π½Π°ΠΏΡΠΈΠΊΠ»Π°Π΄, ΠΊΡΠΈΡ
ΠΊΡ ΠΏΠΎΡΠΎΠ΄ΠΈ ΠΊΠ»Π°ΡΡ II Ρ ΠΌΠ΅Π½Ρ ΠΊΡΠΈΡ
ΠΊΡ Π°Π±ΠΎ Π±ΡΠ»ΡΡ
ΠΏΠ»Π°ΡΡΠΈΡΠ½Ρ ΠΏΠΎΡΠΎΠ΄ΠΈ ΠΊΠ»Π°ΡΡ I).Π¦Π΅Π»Ρ. Π£ΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½ΠΈΠ΅ ΠΈ ΠΎΡΠ΅Π½ΠΊΠ° Π²Π·Π°ΠΈΠΌΠΎΡΠ²ΡΠ·ΠΈ ΠΌΠ΅ΠΆΠ΄Ρ ΡΠ°Π·Π»ΠΈΡΠ½ΡΠΌΠΈ Π²Π΅Π»ΠΈΡΠΈΠ½Π°ΠΌΠΈ ΠΈ ΡΠΈΠΏΠ°ΠΌΠΈ ΠΊΡΠΈΠ²ΡΡ
ΠΎΠ±ΡΠ΅ΠΌΠ½ΠΎΠΉ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΠΈΠΈ Π² ΠΏΡΠΎΡΠ΅ΡΡΠ΅ ΠΎΠ΄Π½ΠΎΠΎΡΠ½ΠΎΠ³ΠΎ ΡΠΆΠ°ΡΠΈΡ ΠΆΠ΅ΡΡΠΊΠΈΡ
Ρ
ΡΡΠΏΠΊΠΈΡ
ΠΏΠΎΡΠΎΠ΄.
ΠΠ΅ΡΠΎΠ΄ΠΈΠΊΠ°. ΠΠΎΠ»Π½ΡΠ΅ ΠΊΡΠΈΠ²ΡΠ΅ Π½Π°ΠΏΡΡΠΆΠ΅Π½ΠΈΡ ΠΈ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΠΈΠΈ ΠΎΠΏΡΠ΅Π΄Π΅Π»ΡΠ»ΠΈΡΡ ΠΏΡΠΈ Π½Π΅ΠΎΠ³ΡΠ°Π½ΠΈΡΠ΅Π½Π½ΠΎΠΌ ΠΎΠ΄Π½ΠΎΠΎΡΠ½ΠΎΠΌ ΠΈΡΠΏΡΡΠ°Π½ΠΈΠΈ Π½Π° ΡΠΆΠ°ΡΠΈΠ΅ Ρ ΠΈΡΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°Π½ΠΈΠ΅ΠΌ ΡΠΈΡΡΠ΅ΠΌΡ ΡΠ΅ΡΠ²ΠΎΡΠΏΡΠ°Π²Π»ΡΠ΅ΠΌΠΎΠ³ΠΎ ΠΊΠΎΠ½ΡΡΠΎΠ»Ρ Ρ Π·Π°ΠΌΠΊΠ½ΡΡΡΠΌ ΠΊΠΎΠ½ΡΡΡΠΎΠΌ Π΄Π»Ρ ΠΎΡΠ΅Π½ΠΊΠΈ ΠΌΠ΅Ρ
Π°Π½ΠΈΡΠ΅ΡΠΊΠΈΡ
ΡΠ²ΠΎΠΉΡΡΠ² 83 ΡΠ°Π·Π»ΠΈΡΠ½ΡΡ
ΡΠΈΠΏΠΎΠ² ΠΏΠΎΡΠΎΠ΄ (53 ΠΈΠ·Π²Π΅ΡΠΆΠ΅Π½Π½ΡΡ
, 10 ΠΎΡΠ°Π΄ΠΎΡΠ½ΡΡ
ΠΈ 20 ΠΌΠ΅ΡΠ°ΠΌΠΎΡΡΠΈΡΠ΅ΡΠΊΠΈΡ
). ΠΡΠΎΡΠ΅Π΄ΡΡΡ ΠΈΡΠΏΡΡΠ°Π½ΠΈΠΉ Π΄Π»Ρ ΠΎΠΏΡΠ΅Π΄Π΅Π»Π΅Π½ΠΈΡ ΠΏΠΎΠ»Π½ΡΡ
ΠΊΡΠΈΠ²ΡΡ
Π½Π°ΠΏΡΡΠΆΠ΅Π½ΠΈΠΉ ΠΈ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΠΈΠΉ Π³ΠΎΡΠ½ΡΡ
ΠΏΠΎΡΠΎΠ΄, Π° ΡΠ°ΠΊΠΆΠ΅ ΠΏΠ°ΡΠ°ΠΌΠ΅ΡΡΠΎΠ² ΠΈΡ
ΠΏΡΠΎΡΠ½ΠΎΡΡΠΈ ΠΏΡΠΎΠ²ΠΎΠ΄ΠΈΠ»ΠΈΡΡ Π² ΡΠΎΠΎΡΠ²Π΅ΡΡΡΠ²ΠΈΠΈ Ρ ΠΏΡΠ΅Π΄Π»ΠΎΠΆΠ΅Π½Π½ΡΠΌ ISRM ΠΌΠ΅ΡΠΎΠ΄ΠΎΠΌ.
Π Π΅Π·ΡΠ»ΡΡΠ°ΡΡ. ΠΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½ΠΈΠ΅ ΠΏΠΎΠΊΠ°Π·Π°Π»ΠΈ, ΡΡΠΎ Π·Π°Π²ΠΈΡΠΈΠΌΠΎΡΡΡ Π²Π΅Π»ΠΈΡΠΈΠ½ ΠΎΠ±ΡΠ΅ΠΌΠ½ΠΎΠΉ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΠΈΠΈ ΠΎΠΏΠΈΡΡΠ²Π°Π΅ΡΡΡ ΡΡΠ΅ΠΏΠ΅Π½Π½ΡΠΌ Π·Π°ΠΊΠΎΠ½ΠΎΠΌ. Π£ΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½ΠΎ, ΡΡΠΎ ΡΡΡΠ΅ΡΡΠ²ΡΠ΅Ρ ΡΠ²ΡΠ·Ρ ΠΌΠ΅ΠΆΠ΄Ρ Π²Π΅Π»ΠΈΡΠΈΠ½Π°ΠΌΠΈ ΠΎΠ±ΡΠ΅ΠΌΠ½ΠΎΠΉ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΠΈΠΈ ΠΈ ΡΠΈΠΏΠ°ΠΌΠΈ ΠΎΠΏΠΈΡΡΠ²Π°ΡΡΠΈΡ
Π΅Π΅ ΠΊΡΠΈΠ²ΡΡ
. ΠΠ΅ΡΠ²ΡΠΉ ΡΠΈΠΏ ΠΊΡΠΈΠ²ΡΡ
ΠΎΠ±ΡΠ΅ΠΌΠ½ΠΎΠΉ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΠΈΠΈ ΡΠΎΠΎΡΠ²Π΅ΡΡΡΠ²ΡΠ΅Ρ ΠΏΠΎΡΠΎΠ΄Π°ΠΌ ΠΊΠ»Π°ΡΡΠ° I Ρ ΠΏΠ΅ΡΠ΅Ρ
ΠΎΠ΄ΠΎΠΌ ΠΊ ΠΊΠ»Π°ΡΡΡ II, Π² ΡΠΎ Π²ΡΠ΅ΠΌΡ ΠΊΠ°ΠΊ ΠΊΡΠΈΠ²ΡΠ΅ ΡΡΠ΅ΡΡΠ΅Π³ΠΎ ΡΠΈΠΏΠ° ΠΏΠΎΠ»Π½ΠΎΡΡΡΡ ΡΠΎΠΎΡΠ²Π΅ΡΡΡΠ²ΡΡΡ ΠΏΠΎΡΠΎΠ΄Π°ΠΌ ΠΊΠ»Π°ΡΡΠ° II.
ΠΠ°ΡΡΠ½Π°Ρ Π½ΠΎΠ²ΠΈΠ·Π½Π°. ΠΠΏΠ΅ΡΠ²ΡΠ΅ ΡΠΊΡΠΏΠ΅ΡΠΈΠΌΠ΅Π½ΡΠ°Π»ΡΠ½ΡΠΌ ΠΏΡΡΠ΅ΠΌ ΡΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½Π° Π²Π·Π°ΠΈΠΌΠΎΡΠ²ΡΠ·Ρ ΠΌΠ΅ΠΆΠ΄Ρ ΡΠΈΠΏΠ°ΠΌΠΈ ΠΊΡΠΈΠ²ΡΡ
ΠΎΠ±ΡΠ΅ΠΌΠ½ΠΎΠΉ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΠΈΠΈ ΠΈ Π΅Π΅ Π²Π΅Π»ΠΈΡΠΈΠ½ΠΎΠΉ. ΠΡΠ΅Π΄ΠΏΡΠΈΠ½ΡΡΡ ΠΏΠ΅ΡΠ²ΡΠ΅ ΠΏΠΎΠΏΡΡΠΊΠΈ ΡΠ²ΡΠ·Π°ΡΡ Π²Π΅Π»ΠΈΡΠΈΠ½Ρ ΠΎΠ±ΡΠ΅ΠΌΠ½ΠΎΠΉ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΠΈΠΈ Ρ ΠΊΡΠΈΠ²ΡΠΌΠΈ Π½Π°ΠΏΡΡΠΆΠ΅Π½ΠΈΡ β Π΄Π΅ΡΠΎΡΠΌΠ°ΡΠΈΠΈ ΠΏΠΎΡΠΎΠ΄ ΠΏΠΎΡΠ»Π΅ ΡΠ°Π·ΡΡΡΠ΅Π½ΠΈΡ ΠΏΡΠΈ ΠΎΠ΄Π½ΠΎΠΎΡΠ½ΠΎΠΌ ΡΠΆΠ°ΡΠΈΠΈ, Π² ΡΠΎ Π²ΡΠ΅ΠΌΡ ΠΊΠ°ΠΊ ΠΏΡΠ΅Π΄ΡΠ΄ΡΡΠΈΠ΅ ΡΠ΅Π·ΡΠ»ΡΡΠ°ΡΡ ΠΏΠΎΠ»ΡΡΠ΅Π½Ρ Π²ΠΎ Π²ΡΠ΅ΠΌΡ ΡΠΆΠ°ΡΠΈΡ.
ΠΡΠ°ΠΊΡΠΈΡΠ΅ΡΠΊΠ°Ρ Π·Π½Π°ΡΠΈΠΌΠΎΡΡΡ. Π‘Π»ΠΎΠΆΠ½ΠΎΡΡΡ ΠΏΠΎΠ»ΡΡΠ΅Π½ΠΈΡ ΠΊΡΠΈΠ²ΡΡ
Π΄Π»Ρ ΡΠΎΡΡΠΎΡΠ½ΠΈΡ ΠΏΠΎΡΠΎΠ΄Ρ ΠΏΠΎΡΠ»Π΅ ΡΠ°Π·ΡΡΡΠ΅Π½ΠΈΡ ΡΠ²Π΅Π»ΠΈΡΠΈΠ²Π°Π΅ΡΡΡ ΠΏΠΎ ΠΌΠ΅ΡΠ΅ ΠΏΠ΅ΡΠ΅Ρ
ΠΎΠ΄Π° ΠΎΡ 1 ΡΠΈΠΏΠ° ΠΊΡΠΈΠ²ΡΡ
ΠΎΠ±ΡΠ΅ΠΌΠ½ΠΎΠΉ Π΄Π΅ΡΠΎΡΠΌΠ°ΡΠΈΠΈ ΠΊΠΎ 2 ΠΈ 3 ΡΠΈΠΏΡ, ΡΡΠΎ ΡΠ²Π»ΡΠ΅ΡΡΡ Π²Π°ΠΆΠ½ΡΠΌ Π°ΡΠΏΠ΅ΠΊΡΠΎΠΌ Π΄Π»Ρ Π±Π΅Π·ΠΎΠΏΠ°ΡΠ½ΠΎΠ³ΠΎ ΡΠ΅ΡΡΠΈΡΠΎΠ²Π°Π½ΠΈΡ ΠΏΠΎΡΠΎΠ΄ ΠΏΠ΅ΡΡΠΎΠ½Π°Π»ΠΎΠΌ. Π Π΅Π·ΡΠ»ΡΡΠ°ΡΡ ΡΠ°Π±ΠΎΡΡ ΠΏΡΠ΅Π΄ΡΡΠ°Π²Π»ΡΡΡ ΠΈΠ½ΡΠ΅ΡΠ΅Ρ Π΄Π»Ρ ΠΏΠΎΠ½ΠΈΠΌΠ°Π½ΠΈΡ ΠΎΠ±ΡΠΈΡ
ΠΏΡΠΎΡΠ΅ΡΡΠΎΠ² Π΄Π΅ΡΠΎΡΠΌΠ°ΡΠΈΠΈ ΠΎΠ±ΡΠ°Π·ΡΠ° ΠΈ ΠΎΡΠ΅Π½ΠΊΠΈ Ρ
ΡΡΠΏΠΊΠΎΡΡΠΈ ΠΏΠΎΡΠΎΠ΄ (Π½Π°ΠΏΡΠΈΠΌΠ΅Ρ, Ρ
ΡΡΠΏΠΊΠΈΠ΅ ΠΏΠΎΡΠΎΠ΄Ρ ΠΊΠ»Π°ΡΡΠ° II ΠΈ ΠΌΠ΅Π½Π΅Π΅ Ρ
ΡΡΠΏΠΊΠΈΠ΅ ΠΈΠ»ΠΈ Π±ΠΎΠ»Π΅Π΅ ΠΏΠ»Π°ΡΡΠΈΡΠ½ΡΠ΅ ΠΏΠΎΡΠΎΠ΄Ρ ΠΊΠ»Π°ΡΡΠ° I).We appreciated Rock Engineering Department, Aalto University Helsinkin Finland for granting permission to determine the post-failure curves of the samples using their closed-loop servo-controlled machine
Design of Comminution Circuit for Optimum Performance of the Gravity Separation Unit at Itakpe Iron Ore Processing Plant, Nigeria
Designing an efficient and economic mineral processing plant begins with the choice of the best and most economic comminution circuit based on ore properties and concentrate end-userβs specifications. This is because crushing and grinding for preparation of suitable feed for the downstream processes are cost intensive. The Itakpe iron ore processing plant presently produces a taiing material containing up to 22% iron minerals mostly fines produced inevitably during comminution. This article analyzed the existing circuit and ore properties, and presents specific comminution tests that were undertaken in order to recommend an alternate and more effective circuit. Sieve analyses of the various products of the existing circuit were carried out. The results show that fines exist in the circuit as a result of the brittleness of some portions of the ore which leads to crumbling and sloughing of the material during crushing and handling. It is revealed that mechanical stacking and reclamation also contributes to the generation of fines in the circuit. One possibility to a solution is to screen the product of secondary crusher ahead of grinding with a +2mm coarse screen between the reclaimer and the primary autogenous mills to prevent further production of fines during crushing unless the downstream recovery process is entirely designed for flotation. This option however still allows much fine material to the concentration lines. It is therefore recommended that materials less than 2mm be screened off the products of primary and secondary crushers and treated separately in gravity or magnetic unit without grinding. A +2mm screen is also recommended for installation as control for the product of primary autogenous mills which should be treated for concentration in the gravity unit. If flotation is to be employed, a regrind mill will be installed on either or both of the concentration lines or to a blend of the two. Keywords: sloughing, crumbling, userβs specifications, hardness, dropping impact, iron-rich, brittlenes
Design of Comminution Circuit for Optimum Performance of the Gravity Separation Unit at Itakpe Iron Ore Processing Plant, Nigeria
Designing an efficient and economic mineral processing plant begins with the choice of the best and most economic comminution circuit based on ore properties and concentrate end-userβs specifications. This is because crushing and grinding for preparation of suitable feed for the downstream processes are cost intensive. The Itakpe iron ore processing plant presently produces a taiing material containing up to 22% iron minerals mostly fines produced inevitably during comminution. This article analyzed the existing circuit and ore properties, and presents specific comminution tests that were undertaken in order to recommend an alternate and more effective circuit. Sieve analyses of the various products of the existing circuit were carried out. The results show that fines exist in the circuit as a result of the brittleness of some portions of the ore which leads to crumbling and sloughing of the material during crushing and handling. It is revealed that mechanical stacking and reclamation also contributes to the generation of fines in the circuit. One possibility to a solution is to screen the product of secondary crusher ahead of grinding with a +2mm coarse screen between the reclaimer and the primary autogenous mills to prevent further production of fines during crushing unless the downstream recovery process is entirely designed for flotation. This option however still allows much fine material to the concentration lines. It is therefore recommended that materials less than 2mm be screened off the products of primary and secondary crushers and treated separately in gravity or magnetic unit without grinding. A +2mm screen is also recommended for installation as control for the product of primary autogenous mills which should be treated for concentration in the gravity unit. If flotation is to be employed, a regrind mill will be installed on either or both of the concentration lines or to a blend of the two. Keywords: sloughing, crumbling, userβs specifications, hardness, dropping impact, iron-rich, brittlenes
Environmental Effects of Processing Marine Clay in Olotu, Ondo State, Nigeria
In this work, analysis of the released gas from calcined marine clay and lime shell was investigated. Study of the emitted gas/air from the calcined clay and shell showed that average concentration of carbon dioxide (CO2: 20.09PPM and 8.12PPM) are below the maximum standard natural concentration 600PPM of carbon dioxide in fresh air and the recommended World Health Organization Threshold Limit Value (TLV) of 500PPM. Average carbon monoxide (CO) concentration (0.004PPM, 0.010PPM) and sulfur dioxide (SO2) concentration (0.002PPM are below the Nigeria Ambient Air Quality Standards (NAAQS) and World Health Organization (WHO) maximum limit of 10PPM-20PPM (for carbon monoxide) and 0.01PPM- 0.5PPM (for sulfur dioxide) for an 8-hourly time. It was established that the average concentration of C0, C02, and S02 is so low and so pose no threat to the environment based on the review of the existing regulation, standards and codes (WHO and NAAQSO). Keywords: Ambient, Testo 350XL- Analyzer, PPM- Part Per Million, calcinin
Effects of varied process parameters on froth flotation efficiency: A case study of Itakpe iron ore
The dire need for Itakpe iron ore concentrates of appreciable iron content meets for smelting operation necessitated this study. Core samples of the iron ore sourced from Itakpe, Kogi State, Nigeria were prepared for petrological analysis followed by chemical and particle size analyses. Froth flotation was done using different collectors at varying particle sizes and pH values. Characterization studies carried out revealed that Itakpe iron ore is a lean ore assaying 36.18% Fe2O3 and contains predominantly quartz, sillimanite, and haematite. Its liberation size lies favourably at 75 ΞΌm. Processing the ore by froth flotation yielded appreciable enrichment. Optimal recovery (~92%) was achieved using potassium amyl xanthate (PAX) at pH 11 for fine feed sizes (<125 ΞΌm) yielding iron concentrate assaying 67.66% Fe2O3. Thus, processing at this set-of-conditions is recommended for the industrial production of more enriched Itakpe iron ore concentrates.
Keywords: Process parameters, Froth flotation, Efficiency, Itakpe iron or