Experimental and simulation study of copper recovery process from copper oxide ore using aspen plus software: Optimization and sensitivity analysis of effective parameters

被引:19
作者
Saidi, Majid [1 ]
Kadkhodayan, Hossein [1 ]
机构
[1] Univ Tehran, Coll Sci, Sch Chem, POB 141556455, Tehran, Iran
关键词
Taguchi method; Aspen plus software; Leaching process; Optimization; Simulation; DISSOLUTION KINETICS; LEACHING BEHAVIOR; MALACHITE ORE; SULFATE; ACID; ZINC; EXTRACTION; MODEL; LEAD;
D O I
10.1016/j.jece.2020.103772
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Aspen Plus software was used to simulate and measure the recovery efficiency of copper in leaching process of copper oxide in H2SO4 solution. The Taguchi experimental design method was applied to determine the optimum operating conditions for dissolution of copper oxide ore in H2SO4 solution. The experimental variables and their levels were as follow: (1) the weight ratio of sulfuric acid to copper content of ore (H2SO4/Cu ratio), 0.937-1.875; (2) leaching temperature (degrees C), 50-80; (3) agitation rate (rpm), 100-400; (4) reaction time (min), 30-120; (5) particle size (mm), 0.01-10; (6) solid/liquid ratio (Pulp density), 10%-40 wt. %; (7) additives values (kg/ton), 10-50 and (8) leaching pH, 1.4-2. The optimum conditions were found to be sulfuric acid/copper ratio: 1.25, temperature: 80 degrees C, agitation rate: 400 rpm, leaching time: 30 min, particle size: 0.1 mm, pulp density: 10 %, additives value: 20 kg/ton and pH: 1.8. The simulation results of the Aspen Plus software indicated that at optimum operating conditions obtained by Taguchi method, the copper recovery from copper oxide ore in H2SO4 solutions was 95 %.
引用
收藏
页数:11
相关论文
共 27 条
[1]  
A.G.S.B. ASPENTECH, 2010, RUNN PROC MOD
[2]   Leaching of zinc from a lead-zinc flotation tailing sample using ferric sulphate and sulfuric acid media [J].
Asadi, Tahereh ;
Azizi, Asghar ;
Lee, Jae-chun ;
Jahani, Mohammad .
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING, 2017, 5 (05) :4769-4775
[3]  
Ata ON, 2001, CHEM ENG TECHNOL, V24, P409, DOI 10.1002/1521-4125(200104)24:4<409::AID-CEAT409>3.3.CO
[4]  
2-S
[5]   A comparative analysis of the dissolution kinetics of lead from low grade oxide ores in HCl, H2SO4, HNO3 and citric acid solutions [J].
Azizi, Asghar ;
Ghasemi, Seyed Mahyar Seyed .
METALLURGICAL RESEARCH & TECHNOLOGY, 2017, 114 (04)
[6]   Thermochemical Equilibrium Model of Synthetic Natural Gas Production from Coal Gasification Using Aspen Plus [J].
Barrera, Rolando ;
Salazar, Carlos ;
Perez, Juan F. .
INTERNATIONAL JOURNAL OF CHEMICAL ENGINEERING, 2014, 2014
[7]   A comprehensive study of the leaching behavior and dissolution kinetics of copper oxide ore in sulfuric acid lixiviant [J].
Bayati, B. ;
Azizi, A. ;
Karamoozian, M. .
SCIENTIA IRANICA, 2018, 25 (03) :1412-1422
[8]   Dissolution kinetics of malachite in ammonia/ammonium carbonate leaching [J].
Bingöl, D ;
Canbazoglu, M ;
Aydogan, S .
HYDROMETALLURGY, 2005, 76 (1-2) :55-62
[9]   Extracting copper from copper oxide ore by a zwitterionic reagent and dissolution kinetics [J].
Deng, Jiu-shuai ;
Wen, Shu-ming ;
Deng, Jian-ying ;
Wu, Dan-dan .
INTERNATIONAL JOURNAL OF MINERALS METALLURGY AND MATERIALS, 2015, 22 (03) :241-248
[10]   Oxygen-steam gasification of karanja press seed cake: Fixed bed experiments, ASPEN Plus process model development and benchmarking with saw dust, rice husk and sunflower husk [J].
Dhanavath, Kotaiah Naik ;
Shah, Kalpit ;
Bhargava, Suresh K. ;
Bankupalli, Satyavathi ;
Parthasarathy, Rajarathinam .
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING, 2018, 6 (02) :3061-3069