scholarly journals Ekstraksi Pemisahan Neodimium dari Samarium, Itrium dan Praseodimium Memakai Tri Butil Fosfat

EKSPLORIUM ◽  
2017 ◽  
Vol 38 (1) ◽  
pp. 19 ◽  
Author(s):  
Maria Veronica Purwani ◽  
Suyanti Suyanti
Keyword(s):  
Optimum Condition ◽  
Aqueous Phase ◽  
Organic Phase ◽  
Separation Factor ◽  
Extraction Efficiency ◽  
Extraction Time ◽  
Feed Concentration ◽  
Optimization Of Separation

ABSTRAKTelah dilakukan ekstraksi konsentrat Nd(OH)3 (neodimium hidroksida) yang mengandung Y(itrium), Sm (samarium) dan Pr (praseodimium) hasil olah pasir monasit. Tujuan penelitian ini untuk pemisahan Nd dari Y, Pr dan Sm dalam konsentrat Nd. Sebagai fasa air adalah konsentrat Nd(OH)3 dalam HNO3 dan ekstraktan atau fasa organik adalah Tri Butil Fosfat (TBP) dalam kerosen. Parameter yang diteliti adalah pH umpan, konsentrasi umpan, konsentrasi TBP dalam kerosen, waktu pengadukan dan kecepatan pengadukan. Dari hasil penelitian optimasi proses ekstraksi pemisahan neodimium dari samarium, itrium dan presedimium dalam konsentrat Nd(OH)3 hasil olah pasir monasit dengan ekstraktan TBP, diperoleh kondisi optimum  sebagai berikut: pH umpan = 0,2; konsentrasi umpan 100 gram/L, konsentrasi TBP dalam kerosen 5 %, waktu pengadukan 15 menit, kecepatan pengadukan 150 rpm. Pada kondisi ini diperoleh  FP (faktor pisah) Nd-Y, FP Nd-Pr, FP Nd-Sm masing-masing sebesar 2,242; 4,811; 4,002 dan angka banding distribusi (D) Nd = 0,236 dengan efisiensi ekstraksi Nd = 19,07%. ABSTRACTThe extraction of Nd(OH)3 (neodymium hydroxide) concentrate containing Y (yttrium), Sm (samarium) and Pr (praseodymium) as product of monazite processed has been done. The purpose of this study is to determine the separation of Nd from Y, Pr and Nd Sm in Nd concentrate. The aqueous phase was concentrated Nd (OH)3 in HNO3 and extractant while organic phase was Tri Butyl Phosphate (TBP) in kerosene. Parameters studied were pH and concentration feed, concentration of TBP in kerosene, extraction time and stirring speed. The result showed that the optimization of separation extraction neodymium from samarium, yttrium and praseodymium in Nd(OH)3 concentrated  with TBP, obtained the optimum condition of pH = 0.2, concentration of feed 100 g /L, concentration of TBP in kerosene 5%, extraction time 15 minutes and stirring speed 150 rpm. With the conditions, Separation Factor (SF) obtained for Nd-Y, Nd-Pr, Nd-Sm are 2.242, 4.811, 4.002 respectively, while D and extraction efficiency of Nd are 0.236 and 19.07%.

Recovery of Uranium (VI) from Water Solutions by Membrane Extraction

2013 ◽  
Vol 704 ◽  
pp. 66-71
Author(s):  
Grazyna Zakrzewska ◽  
Pawel Bieluszka ◽  
Ewelina Chajduk ◽  
Stanislaw Wolkowicz
Keyword(s):  
Aqueous Phase ◽  
Organic Phase ◽  
Extraction Efficiency ◽  
Membrane Extraction ◽  
Membrane Contactor ◽  
Shell Side ◽  
Real Solutions ◽  
Model Solutions ◽  
Capillary Membrane ◽  
Capillary Membranes

The extraction of uranium from aqueous model solutions, as well as from real solutions reulting from leaching uranium ores was carried out in the system equipped with the Liqui-Cel® Extra-Flow membrane contactor with polypropylene capillary membranes. D2EHPA in toluene was used as an organic phase. Different arrangements of flow inside the membrane module were tested. The better approach appeared to be the arrangement with aqueous phase in the shell side of the contactor and organic phase inside the capillary membrane. The extraction efficiency for model solutions reached 95% and 87% for real post-leaching liquors.

scholarly journals Pengaruh Tri-n-Oktil Posfin Oksida dan Tingkat Ekstraksi pada Pemurnian Konsentrat Thorium

EKSPLORIUM ◽  
2015 ◽  
Vol 36 (2) ◽  
pp. 109
Author(s):  
M.V. Purwani ◽  
Moch. Setyadji
Keyword(s):  
Organic Phase ◽  
Separation Factor ◽  
Extraction Efficiency ◽  
Phase 1 ◽  
Extraction Process ◽  
Air Stripping ◽  
Total Separation ◽  
Processing Product ◽  
Thorium Oxalate ◽  
Total Extraction

Telah dilakukan ekstraksi konsentrat thorium oksalat hasil olah monasit memakai ekstraktan Tri – n - Oktil Posfin Oksida (TOPO).  Pengotor  yang paling banyak  terkandung dalam konsentrat thorium oksalat adalah cerium (Ce) dan lantanum (La).  Tujuan penelitian ini adalah untuk memurnikan thorium (Th) dengan memisahkan Ce dan La dengan cara ekstraksi. Ekstraksi dilakukan secara batch dan bertingkat.  Larutan umpan atau fase air adalah 10 gram konsentrat Th oksalat yang dilarutkan dalam 10,08 M HNO3 sehingga volume menjadi 100 mL dan fase organik adalah TOPO dalam kerosen.  Stripping setiap tingkat ekstraksi dilakukan tiga kali, yaitu stripping pertama memakai air, stripping kedua memakai asam oksalat 5%, dan stripping ketiga memakai air. Waktu ekstraksi setiap tingkat 15 menit dan waktu stripping setiap tingkat  5 menit dengan perbandingan fase air dengan fase organik adalah 1 berbanding 1.  Parameter yang diteliti  adalah persentase TOPO dalam kerosen dan jumlah tingkat ekstraksi. Pemakaian TOPO dalam kerosen yang optimum 5% dan jumah tingkat ekstraksi 3.  Pada ekstraksi I diperoleh konsentrat Ce dan pada tingkat ekstraksi II dan III diperoleh Th.  Efisiensi ekstraksi Th  tingkat II sebesar 39,76% dan efisiensi ekstraksi Th tingkat III 26,33%. Koefisien distribusi (Kd) Th tingkat ekstraksi II adalah 0,7587 dan Kd Th tingkat ekstraksi III  1,0096. Efisiensi ekstraksi Th total adalah  80,08 %, efisiensi ekstraksi Ce total  56,12%,  efisiensi ekstraksi La total  1,54.  Faktor pisah (FP) Th – Ce pada ekstraksi I adalah 1,00, FP Th – La pada ekstraksi I  92,07, FP Th – Ce pada ekstraksi II adalah 250,24 dan FP Th – La  pada ekstraksi II adalah ∞,  FP Th – Ce pada ekstraksi III 124,22 dan FP Th – La pada ekstraksi III adalah ∞. Faktor pisah total Th – Ce sebesar 1,4270 dan Faktor pisah total Th – La  47,0459. Kadar Th oksalat pada ekstraksi II sebesar 97,06%, kadar Th oksalat pada ekstraksi III  98,00 %. The extraction of thorium oxalate concentrate as processing product  of monazite using  Tri  Octyl Posfine Oxide  (TOPO) has been done.  The most impurities contained in thorium oxalate concentrate are Ce (cerium) and La (lanthanum). The purpose of this study is to purify Th by separating Ce and La using extraction process. The extraction is done by bacth and multistage. The solution of  feed or water phase is 10 grams of Th oxalate concentrate dissolved in 10.08 M HNO3 so that the volume becomes 100 mL and the organic phase is TOPO in kerosene. Stripping in each stage conducted three times, first stripping use water, second stripping use 5 % oxalic acid and the third stripping use water. Extraction time at every stage is 15 minutes and stripping time at every stage is 5 minutes with  ratio of aqueous phase to organic phase = 1 : 1 . The parameters were studied % TOPO - kerosene and number of extraction stage. The optimum usage of TOPO in kerosene is 5 %.  On extraction I obtained Ce concentrate and on extraction II and III obtained Th concentrates. The extraction II efficiency of Th is 39.76 % and extraction III efficiency of Th is 26.33 % . Coefficient of distribution (Kd) of Th in stage II is 0.7587 and Kd of Th in stage III is 1.0096.  Total extraction efficiency of Th is  80.08 %, total extraction efficiency of Ce is 56.12 %,  and total extraction efficiency of La is 1.54 %. The separation factor of  Th – Ce in extraction I  is 1.00 and separation factor of  Th – La in extraction I  is 92.0,  separation factor of  Th – Ce in extraction II  is 250.24, and separation  factor of  Th – La in extraction II  is ∞.  Separation factor of  Th – Ce in extraction III  is 124.22 and separation factor of  Th – La in extraction III  is  ∞.  Total  separation  factor of  Th – Ce  is 1.4270 and total separation factor of  Th – La is 4.0459.  The content of Th oxalate in stripping product from the extraction II is 97.06 % and in stripping product from  the extraction III is 98.00%.

scholarly journals Tantalum and Niobium Selective Extraction by Alkyl-Acetophenone

2018 ◽  
Author(s):  
Moussa Toure ◽  
Guilhem Arrachart ◽  
Jean Duhamet ◽  
Stephane Pellet-Rostaing
Keyword(s):  
Physicochemical Properties ◽  
Aqueous Phase ◽  
Organic Phase ◽  
Extraction Efficiency ◽  
Selective Extraction ◽  
Extraction Process ◽  
Liquid Extraction ◽  
Waste Solution ◽  
Liquid Liquid Extraction ◽  
Kd Values

A study has been carried out on Ta and Nb recovery by liquid-liquid extraction process using 4-methylacetophenone (4-MAcPh) as organic phase. The 4-MAcPh was compared to methylisobutylketone (MIBK) with respect to extraction efficiencies (kD values) at different concentrations of H2SO4 in the aqueous phase. The results showed a similar extraction of Nb for both solvents. However, for Ta extraction efficiency is increased by a factor of 1.3 for 4-MAcPh. In addition, the MIBK solubilized completely after 6 mol L-1 of H2SO4 against only a loss of 0.14 to 4% for 4-MAcPh between 6 and 9 mol L-1 of H2SO4. The potential of 4-MAcPh has also been studied to selectively recover Ta from a model capacitor waste solution. The results showed a selectivity for Ta in the presence of impurities such as Fe, Ni, Mn. The 4-MAcPh also presents the advantage of having physicochemical properties adapted to its use in liquid-liquid extraction technologies such as mixer-settlers.

Biphasic Enantioselective Partitioning of R,S-Omeprazole Enantiomers Using Chiral Extraction

2014 ◽  
Vol 1030-1032 ◽  
pp. 2334-2339
Author(s):  
Yan Liang Li ◽  
Zhong Zhen Liu ◽  
Yu Fen Huang ◽  
Lan Wei ◽  
Lian Xi Huang ◽  
...  
Keyword(s):  
Tartaric Acid ◽  
Organic Phase ◽  
Separation Factor ◽  
Extraction Efficiency ◽  
Distribution Coefficients ◽  
Variable Parameters ◽  
Chiral Selectors ◽  
Tartaric Acid Derivatives ◽  
Hexyl Ester ◽  
Chiral Extraction

Enantioselective partitioning of racemic omeprazole enantiomers was studied using a biphasic recognition chiral extraction system. Hydrophilic hydroxypropyl-ڂ-cyclodextrin in aqueous phase and hydrophobic D-tartaric acid hexyl ester in organic phase as chiral selectors which preferentially recognize (R)-omeprazole enantiomer and (S)-omeprazole enantiomer, respectively. Different experimental variable parameters could affect the chiral extraction efficiency. The largest distribution coefficientskS,kRand separation factorځwere obtained at concentrations o f 0.1 mol/L HP-ڂ-CD and 0.2 mol/L D-tartaric acid hexyl ester, which were 47.38, 58.65 and 1.24, respectively.kRis always larger thankSwhen using different kinds of tartaric acid derivatives as chiral selectors in organic phase. The present study also reveal the mechanism of biphasic recognition chiral extraction forR,S-omeprazole enantiomers.

N,N,N′,N′-Tetra-Methyl-3-Oxy-Pentane-1,5-Diamide (TMPDA): A Promising Back Extractant for Ln(III) and Zr(IV)

2010 ◽  
Author(s):  
Meng Wei ◽  
Qian’ge He ◽  
Xuegang Liu ◽  
Jing Chen
Keyword(s):  
Crystal Structure ◽  
Aqueous Phase ◽  
Organic Phase ◽  
Extraction Efficiency ◽  
Phase Distribution ◽  
Decomposition Temperature ◽  
Water Soluble ◽  
Phase System ◽  
Acid System ◽  
Equilibrium Aqueous Phase

Water-soluble oxa-diamide ligand, N,N,N′,N′-tetra-methyl-3-oxy-pentane-1,5-diamid (TMPDA) has been synthesized and purified. Its crystal structure, melting point, decomposition temperature, solubilities in aqueous phase and organic phase, distribution ratio between aqueous and organic phase, etc. are reported. The effect of TMPDA concentration in aqueous phase and HNO3 concentration in the equilibrium aqueous phase on the extraction efficiency of La(III), Ce(III), Pr(III), Nd(III), Zr(IV), Fe(III), Y(III), Mo(VI), Ru(III) and Pd(II) by 30% TRPO/kerosene have been studied. The results indicate that TMPDA dissolve well in aqueous phase but almost insoluble in kerosene or 30%TRPO/kerosene in the bi-phase system. It can effectively reduce the extraction of Ln(III), Y(III) and Zr(IV) into 30%TRPO/kerosene at a moderate acid system (0.24mol/L∼0.27mol/L HNO3). TMPDA is a promising stripping agent for Ln(III), Y(III) and Zr(IV) from loaded TRPO.

Dysprosium (Dy) Separation from Yttrium Concentrate in Nitric Acid Solution Using Aliquat 336 Solvent

2020 ◽  
Vol 840 ◽  
pp. 573-579
Author(s):  
Kris Tri Basuki ◽  
Ridwan Arifudin ◽  
Wahyu Rachmi Pusparini ◽  
Andri Saputra
Keyword(s):  
Nitric Acid ◽  
Separation Factor ◽  
Extraction Efficiency ◽  
Nitric Acid Concentration ◽  
Main Concern ◽  
Aliquat 336 ◽  
Distribution Constant ◽  
Solvent Concentration ◽  
Feed Concentration ◽  
Stirring Time

Similarity of chemical and physical properties between rare-earth elements (REEs) and Dy is the main concern in order to get Dy with high purity, which it is necessary to do separation by extraction process. The purpose of this research is to obtain the optimum condition of operation (stirring time and rate, concentration of nitric acid, feed, and solvent) and determine the distribution constant, separation factor, and extraction efficiency of Dy using Aliquat 336. This research was conducted by varying stirring time (10, 15, 20, 30, 40 minutes), stirring rate (100, 150, 200, 250, 300 rpm), nitric acid concentration (2, 3, 4, 5, 6 N), feed concentration (25,000; 50,000; 100,000; 150,000; 200,000 ppm) and solvent concentration (10, 20, 30, 40, 50 % v/v). The optimum result is achieved when operation is carried out at stirring 100 rpm about 15 minutes in nitric acid 3 N with 100,000 ppm of feed concentration using 30% solvent concentration (v/v) which extract more Dy element than Yttrium (Y) and Godolinium (Gd). The highest distribution constant of Dy is 0.427, separation factor of Dy-Y is 6.831, separation factor of Dy-Gd is 1.799, and extraction efficiency of Dy is 31.604%.

Fundamental Study on Multistage Extraction Using TDdDGA for Separation of Lanthanides Present in Nd Magnets

JOM ◽  
2021 ◽  
Author(s):  
Yuji Sasaki ◽  
Keisuke Morita ◽  
Masahiko Matsumiya ◽  
Ryoma Ono ◽  
Hidenobu Shiroishi
Keyword(s):  
Aqueous Phase ◽  
Organic Phase ◽  
Separation Factor ◽  
Basic Research ◽  
Fundamental Study ◽  
High Separation Factor ◽  
High Separation

AbstractThe separation of Dy from Nd has been studied from the viewpoint of recycling Dy from Nd magnets. N,N,N′,N′-tetradodecyl-DGA (TDdDGA) has a relatively high separation factor between Dy and Nd (above 10) in HNO3 medium. After basic research on batchwise multistage extractions using eight extraction stages with 0.1 M TDdDGA in n-dodecane as organic phase, ten stages with an aqueous phase (0.7 M HNO3 with metals), and six stages with another aqueous phase (0.7 M HNO3 without metals), approximately 99% of Dy was recovered into the organic phase with 1% coextraction of Nd.

scholarly journals THE EFFECT OF CONCENTRATION OF CARRIER, pH AND TIME OF EXTRACTION ON SEPARATION'S FACTOR OF PENICILLIN G - PHENYL ACETATE BY REACTIVE EXTRACTION

2010 ◽  
Vol 7 (2) ◽  
pp. 185-189
Author(s):  
Imam Santoso ◽  
Buchari Buchari ◽  
M. Bachri Amran ◽  
Aminudin Sulaeman
Keyword(s):  
Aqueous Solution ◽  
Optimum Condition ◽  
Organic Phase ◽  
Separation Factor ◽  
Butyl Acetate ◽  
Reactive Extraction ◽  
Penicillin G ◽  
Phenyl Acetate ◽  
Second Phase ◽  
Phase Water

The aim of this research is to study the effect of concentration carrier, pH and time of extraction on separation's factor of penicillin g - phenyl acetate by reactive extraction technique. The 10 mL  aqueous  solution with variation of  pH : 5, 6 contains 0.001 M penicillin G and 0.001 M phenyl acetate has been extracted with 10 mL n-butyl acetate contains dioctylamine as carrier. Variation concentration  of carrier were 0.000; 0.002; 0.004; 0.006 and 0.008 M. Variation time of extraction were 1, 5, 10, 15 and 20 min. The penicillin G and phenyl acetate that dissolved in organic phase ha been  reextracted with 10 mL aqueous with variation of pH : 7, 8. The optimum condition obtained as follow : concentration dioctylamine was 0.002M ; pH the first phase water was 5 and the second phase water was 8 ; and the time of extraction was 10 min.   Keywords: Separation factor, Reactive extraction

Extraction of hafnium(IV) with organophosphorus reagents from solutions of mineral acids mixtures

1979 ◽  
Vol 44 (12) ◽  
pp. 3656-3664
Author(s):  
Oldřich Navrátil ◽  
Jiří Smola ◽  
Rostislav Kolouch
Keyword(s):  
Ionic Strength ◽  
Aqueous Phase ◽  
Organic Phase ◽  
Perchloric Acid ◽  
Synergic Effect ◽  
Salting Out ◽  
Initial Concentration ◽  
Mixed Complexes ◽  
Synergic Extraction ◽  
Mineral Acids

Extraction of hafnium(IV) was studied from solutions of mixtures of perchloric and nitric acids and of perchloric and hydrochloric acids for constant ionic strength, I = 2, 4, 6, or 8, and for cHf 4 . 10-4 mol l-1. The organic phase was constituted by solutions of some acidic or neutral organophosphorus reagents or of 2-thenoyltrifluoroacetone, 1-phenyl-3-methyl-4-benzoyl-5-pyrazolone, or N-benzoyl-N-phenylhydroxylamine in benzene, chloroform, or n-octane. A pronounced synergic extraction of hafnium proceeds only on applying organophosphorus reagents from an aqueous phase whose acidity is not lower than 3M-(HClO4 + HNO3) or 5M-(HClO4 + HCl). The synergic effect was not affected markedly by a variation of the initial concentration of hafnium in the range 1 . 10-8 -4 .10-4 mol l-1, it lowered with increasing initial concentration of the organophosphorus reagent and decreasing concentration of the H+ ions. It is suggested that the hafnium passes into the organic phase in the form of mixed complexes, the salting-out effect of perchloric acid playing an appreciable part.

scholarly journals Application of a cashew-based oxime in extracting Ni, Mn and Co from aqueous solution

2021 ◽  
Vol 8 (1) ◽  
Author(s):  
Chi M. Phan ◽  
Son A. Hoang ◽  
Son H. Vu ◽  
Hoang M. Nguyen ◽  
Cuong V. Nguyen ◽  
...  
Keyword(s):  
Organic Phase ◽  
Extraction Efficiency ◽  
Acidic Solution ◽  
Lithium Ion ◽  
Metal Extraction ◽  
Economic Potential ◽  
Cashew Nut ◽  
Valuable Metals ◽  
Loaded Organic Phase ◽  
Cashew Nut Shell

Abstract Background Cashew nut shell is a by-product of cashew (Anacardium occidentale) production, which is abundant in many developing countries. Cashew nut shell liquor (CNSL) contains a functional chemical, cardanol, which can be converted into a hydroxyoxime. The hydroxyoximes are expensive reagents for metal extraction. Methods CNSL-based oxime was synthesized and used to extract Ni, Co, and Mn from aqueous solutions. The extraction potential was compared against a commercial extractant (LIX 860N). Results All metals were successfully extracted with pH0.5 between 4 and 6. The loaded organic phase was subsequently stripped with an acidic solution. The extraction efficiency and pH0.5 of the CNSL-based extractant were similar to a commercial phenol-oxime extractant. The metals were stripped from the loaded organic phase with a recovery rate of 95% at a pH of 1. Conclusions Cashew-based cardanol can be used to economically produce an oxime in a simple process. The naturally-based oxime has the economic potential to sustainably recover valuable metals from spent lithium-ion batteries. Graphic abstract

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