Kinetic Study for Platinum Extraction from Spent Catalyst in Cyanide Solution at High Temperatures

被引:9
|
作者
Naghavi, Z. [1 ]
Ghoreishi, S. M. [1 ]
Rahimi, A. [2 ]
Hadadzadeh, H. [3 ]
机构
[1] Isfahan Univ Technol, Dept Chem Engn, Esfahan 8415683111, Iran
[2] Univ Isfahan, Fac Engn, Dept Chem Engn, Esfahan, Iran
[3] Isfahan Univ Technol, Dept Chem, Esfahan 8415683111, Iran
关键词
kinetic model; platinum recovery; high temperatures; cyanide; leaching; spent catalyst; REFORMING CATALYSTS; ION-EXCHANGE; GROUP METALS; DEGREES-C; RECOVERY; DEHYDROGENATION; COMPLEXES; CARBON; GOLD; ORES;
D O I
10.1515/ijcre-2015-0046
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this research, the kinetics of platinum extraction from a selective linear paraffin dehydrogenation spent catalyst in cyanide solutions at high pressure and temperature was experimentally studied. Three variables, including reaction temperature, initial sodium cyanide concentration in solution and liquid to solid weight ratio were investigated. Based on the design of experiments via response surface methodology (RSM) by computer simulating software "Minitab 16", experiments were carried out at operating conditions including five solution temperatures, five initial concentrations of cyanide solution and five liquid/solid weight ratios. The effects of these operating conditions on the reaction kinetics and extraction time were determined. The obtained kinetics data were fitted into an empirical power-law rate equation. The kinetics model parameters were evaluated by using experimental data via non-linear regression analysis. It was found that the platinum extraction from a selective linear paraffin dehydrogenation spent catalyst in cyanide solution at high pressure and temperature can be appropriately modeled by the proposed correlation in the selected range of operating conditions.
引用
收藏
页码:143 / 154
页数:12
相关论文
共 50 条
  • [1] A novel method for extraction of platinum from spent automotive catalyst: utilization of spent fluid catalytic cracking catalyst as flux
    Liu, Chuan
    Sun, Shuchen
    Tu, Ganfeng
    Xiao, Faxin
    ENVIRONMENTAL TECHNOLOGY, 2023, 44 (02) : 139 - 149
  • [2] Recovery of platinum from spent catalyst
    Barakat, MA
    Mahmoud, MHH
    HYDROMETALLURGY, 2004, 72 (3-4) : 179 - 184
  • [3] Recovery of Platinum from Chloride Leaching Solution of Spent Catalysts by Solvent Extraction
    Sun, Pan Pan
    Lee, Man Seung
    MATERIALS TRANSACTIONS, 2013, 54 (01) : 74 - 80
  • [4] Platinum recovery from a spent industrial dehydrogenation catalyst using cyanide leaching followed by ion exchange
    Shams, K
    Beiggy, MR
    Shirazi, AG
    APPLIED CATALYSIS A-GENERAL, 2004, 258 (02) : 227 - 234
  • [5] Recovery of Platinum from a Spent Automotive Catalyst through Chloride Leaching and Solvent Extraction
    Mendez, Ana
    Nogueira, Carlos A.
    Paiva, Ana Paula
    RECYCLING, 2021, 6 (02)
  • [6] A Kinetic Model for Chelating Extraction of Metals from Spent Hydrodesulphurization Catalyst by Complexing Agent
    Orhon Alpaslan
    Ali Yaras
    Hasan Arslanoğlu
    Transactions of the Indian Institute of Metals, 2020, 73 : 1925 - 1937
  • [7] A Kinetic Model for Chelating Extraction of Metals from Spent Hydrodesulphurization Catalyst by Complexing Agent
    Alpaslan, Orhon
    Yaras, Ali
    Arslanoglu, Hasan
    TRANSACTIONS OF THE INDIAN INSTITUTE OF METALS, 2020, 73 (07) : 1925 - 1937
  • [8] Simultaneous extraction and preconcentration of palladium and platinum from alkaline cyanide solution by hexadecylpyridinium bromide
    School of Chemical Science and Technology, Yunnan University, Kunming
    650091, China
    Zhongguo Youse Jinshu Xuebao, 11 (2449-2460): : 2449 - 2460
  • [9] Preparation of platinum oxide catalyst from spent material
    Baldeschwieler, EL
    Mikeska, LA
    JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1935, 57 (01) : 977 - 978
  • [10] RECOVERY OF HCL FROM CHLORIDE LEACH SOLUTION OF SPENT HDS CATALYST BY SOLVENT EXTRACTION
    Banda, Raju
    Thi Hong Nguyen
    Lee, Man Seung
    CHEMICAL AND PROCESS ENGINEERING-INZYNIERIA CHEMICZNA I PROCESOWA, 2013, 34 (01): : 153 - 163