Production of high purity rare earth mixture from iron-rich spent fluid catalytic cracking (FCC) catalyst using acid leaching and two-step solvent extraction process

2018 ◽  
Vol 35 (5) ◽  
pp. 1195-1202 ◽  
Author(s):  
Le-Phuc Nguyen ◽  
Yen Thi Hai Pham ◽  
Phuong Thuy Ngo ◽  
Tri Van Tran ◽  
Loc Vinh Tran ◽  
...  
Keyword(s):  
Rare Earth ◽  
Solvent Extraction ◽  
High Purity ◽  
Catalytic Cracking ◽  
Acid Leaching ◽  
Extraction Process ◽  
Fluid Catalytic Cracking ◽  
Fcc Catalyst

scholarly journals Study on the Effect and Mechanism of Impurity Aluminum on the Solvent Extraction of Rare Earth Elements (Nd, Pr, La) by P204-P350 in Chloride Solution

Minerals ◽  
2021 ◽  
Vol 11 (1) ◽  
pp. 61
Author(s):  
Wenjie Zhang ◽  
Xian Xie ◽  
Xiong Tong ◽  
Yunpeng Du ◽  
Qiang Song ◽  
...  
Keyword(s):  
Rare Earth ◽  
Solvent Extraction ◽  
Rare Earth Elements ◽  
Organic Phase ◽  
Extraction Process ◽  
Industrial Applications ◽  
Separation And Purification ◽  
Aluminum Ion ◽  
Hydrochloric Acid Medium ◽  
Impurity Ion

Solvent extraction is the most widely used method for separation and purification of rare earth elements, and organic extractants such as di(2-ethylhexyl) phosphoric acid (P204) and di(1-methyl-heptyl) methyl phosphonate (P350) are most commonly used for industrial applications. However, the presence of impurity ions in the feed liquid during extraction can easily emulsify the extractant and affect the quality of rare earth products. Aluminum ion is the most common impurity ion in the feed liquid, and it is an important cause of emulsification of the extractant. In this study, the influence of aluminum ion was investigated on the extraction of light rare earth elements by the P204-P350 system in hydrochloric acid medium. The results show that Al3+ competes with light rare earths in the extraction process, reducing the overall extraction rate. In addition, the Al3+ stripping rate is low and there is continuous accumulation of Al3+ in the organic phase during the stripping process, affecting the extraction efficiency and even causing emulsification. The slope method and infrared detection were utilized to explore the formation of an extraction compound of Al3+ and the extractant P204-P350 that entered the organic phase as AlCl[(HA)2]2P350(o).

Recovery of Zinc and Manganese from Spent Zn-Mn Batteries Using Solvent Extraction

2018 ◽  
Vol 775 ◽  
pp. 427-433
Author(s):  
Wei Sheng Chen ◽  
Chin Ting Liao ◽  
Chen Hsi Chang
Keyword(s):  
Solvent Extraction ◽  
Magnetic Separation ◽  
High Purity ◽  
Ph Value ◽  
Acid Leaching ◽  
Extractant Concentration ◽  
Environmental Technology ◽  
Electronic Products ◽  
Waste Plastic ◽  
Purity Level

For several decades, zinc-manganese batteries have been created to serve many forms of electronic products. However, every creative act has its destructive consequence. Plenty of waste element inside has caused the irreversible contamination to our environment.This study will focus on dealing with zinc-manganese batteries using environmental technology and hydrometallurgy methods, such as physical pretreatment, acid leaching and solvent extraction. The goal of this research will concentrate on the recovery of zinc and manganese from zinc-manganese batteries. The pretreatment processes include crushing, sieving and magnetic separation to separate the waste plastic, scraps of paper and impurity from waste zinc-manganese batteries. Before the process of the solvent extraction zinc-manganese batteries will be leached by specific acid first. In next step, the solvent extraction will be carried out and investigated. The parameters such as extractant concentration, extraction time, equilibrium pH value and organic-aqueous ratio (O/A) are analyzed in detail. Finally, the products of Zn and Mn are obtained in high-purity level and the recovery rates are about 92% for Zn and 95% for Mn.

Transformations of FCC catalysts and carbonaceous deposits during repeated reaction-regeneration cycles

2019 ◽  
Vol 9 (24) ◽  
pp. 6977-6992 ◽  
Author(s):  
Qandeel Almas ◽  
Muhammad Awais Naeem ◽  
Maria Auxiliadora S. Baldanza ◽  
Jessica Solomon ◽  
Jeffery C. Kenvin ◽  
...  
Keyword(s):  
Catalytic Cracking ◽  
Fluid Catalytic Cracking ◽  
Carbonaceous Deposits ◽  
Fcc Catalyst ◽  
P Transformations ◽  
Fcc Catalysts

Transformations of an industrial zeolite-based fluid catalytic cracking (FCC) catalyst and its coke deposits during regeneration following FCC reactions of a representative refinery stream are investigated.

A Green Approach

2013 ◽  
Vol 1 ◽  
pp. 194308921350702
Author(s):  
Madhavi Madeti ◽  
Sharad V. Lande ◽  
Kalpana G ◽  
R. K. Mewada ◽  
R. V. Jasra
Keyword(s):  
Catalytic Cracking ◽  
Petroleum Refining ◽  
Temperature Programmed Desorption ◽  
Fluid Catalytic Cracking ◽  
Acidic Properties ◽  
X Ray ◽  
Green Approach ◽  
Fcc Catalyst ◽  
The Matrix ◽  
Temperature Programmed

We have attempted a green alternative to reuse the spent fluid catalytic cracking (FCC) catalyst that is used in petroleum refining industry for the upgradation and purification of various petroleum streams and residues. The spent FCC zeolite–based catalyst modified by enhancing the acidic properties by incorporating Zn and In metals in the matrix. The various prepared catalysts were systematically characterized by X-ray powder diffraction and Brunauer–Emmett–Teller (BET; adsorption isotherm) surface area. The acidity of the materials was studied by temperature-programmed desorption of ammonia (NH3-TPD). The well-characterized catalysts were applied for liquid phase benzylation of o-xylene using benzyl chloride.

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