Separation and extraction of cesium from salt lake brine by the calcium alginate-ammonium tungstophosphate composite adsorbent

2018 ◽  
Vol 104 ◽  
pp. 257-262
Author(s):  
Tan Guo ◽  
Shan Yun ◽  
Lei He ◽  
Quan Li ◽  
Zhijian Wu
Keyword(s):  
Calcium Alginate ◽  
Salt Lake ◽  
Composite Adsorbent ◽  
Ammonium Tungstophosphate ◽  
Salt Lake Brine

Preparation of Ammonium Tungstophosphate-Calcium Alginate Composite Adsorbent and its Adsorption Properties of Rubidium

2013 ◽  
Vol 652-654 ◽  
pp. 2524-2528 ◽  
Author(s):  
Xian Jiang Huang ◽  
Lian Ying An ◽  
Xian Yin Zhao ◽  
Xiao Qing Chen
Keyword(s):  
Calcium Alginate ◽  
Concentration Ratio ◽  
Adsorption Equilibrium ◽  
Adsorption Properties ◽  
Separation Coefficient ◽  
Adsorption Ability ◽  
Composite Adsorbent ◽  
Adsorption Time ◽  
Ft Ir ◽  
Ammonium Tungstophosphate

A spherical composite adsorbent AWP-CaALG was prepared by the calcium alginate(CaALG) and ammonium tungstophosphate(AWP). The composite adsorbent was characterized by XRD, FT-IR and TG-DTG-DTA, it proves that the crystal structure of AWP isn’t destroyed and the adsorption ability of the composite adsorbent can be retained up to 120°C. Effects of adsorbent dosage, adsorption time, pH, temperature, concentration of Rb and K were investigated. The results show that the adsorption capacity of composite adsorbent to rubidium is 20.64mg/g.The adsorption equilibrium is gained after 24h. When the concentration ratio of K to Rb is 16, the adsorption rate of Rb can still be up to 94.1% and the Rb/K separation coefficient is 86.

Preconcentration and Separation of Rubidium from Salt Lake Brine by Ammonium Phosphomolybdate - Polyacrylonitrile (AMP-PAN) Composite Adsorbent

2017 ◽  
Vol 2 (25) ◽  
pp. 7741-7750 ◽  
Author(s):  
Amin Bao ◽  
Hong Zheng ◽  
Zeyu Liu ◽  
Dongfang Huang ◽  
Shuya Wang ◽  
...  
Keyword(s):  
Salt Lake ◽  
Composite Adsorbent ◽  
Salt Lake Brine

Extraction of lithium from salt lake brine with triisobutyl phosphate in ionic liquid and kerosene

2015 ◽  
Vol 31 (4) ◽  
pp. 621-626 ◽  
Author(s):  
Daolin Gao ◽  
Xiaoping Yu ◽  
Yafei Guo ◽  
Shiqiang Wang ◽  
Mingming Liu ◽  
...  
Keyword(s):  
Ionic Liquid ◽  
Salt Lake ◽  
Triisobutyl Phosphate ◽  
Salt Lake Brine

scholarly journals Hydrothermal Stripping Synthesis of α-LiFeO2Nanoparticles from Qinghai Salt Lake Brine

2016 ◽  
Vol 67 ◽  
pp. 06090
Author(s):  
Yaqiang Yang ◽  
Dandan Li ◽  
Guangqin Wan ◽  
Feifei Lv ◽  
Danfeng Li ◽  
...  
Keyword(s):  
Salt Lake ◽  
Salt Lake Brine

Lithium recovery from salt lake brine by H2TiO3

2014 ◽  
Vol 43 (23) ◽  
pp. 8933-8939 ◽  
Author(s):  
Ramesh Chitrakar ◽  
Yoji Makita ◽  
Kenta Ooi ◽  
Akinari Sonoda
Keyword(s):  
Interlayer Space ◽  
Salt Lake ◽  
Lithium Ion ◽  
Steric Effects ◽  
Salt Lake Brine

The high lithium uptake of H2TiO3 from brine is due to its lithium ion-sieve property. Exchange sites are too narrow for Na, K, Mg and Ca to enter the interlayer space due to steric effects.

Basic Salt‐Lake Brine: An Efficient Catalyst for the Transformation of CO 2 into Quinazoline‐2,4(1  H ,3  H )‐diones

ChemSusChem ◽  
2018 ◽  
Vol 11 (24) ◽  
pp. 4219-4225 ◽  
Author(s):  
Jiayin Hu ◽  
Shangqing Chen ◽  
Yafei Guo ◽  
Long Li ◽  
Tianlong Deng
Keyword(s):  
Salt Lake ◽  
Basic Salt ◽  
Efficient Catalyst ◽  
Salt Lake Brine

Solubility Prediction for the Reciprocal Quaternary System (Li+, Mg2+//Cl-, SO42-–H2O) at 273.15 K Using Pitzer Ion-Interaction Model

2012 ◽  
Vol 549 ◽  
pp. 437-440 ◽  
Author(s):  
Shi Qiang Wang ◽  
Ya Fei Guo ◽  
Tian Long Deng
Keyword(s):  
Quaternary System ◽  
Salt Lake ◽  
Interaction Model ◽  
Linear Regression Method ◽  
Solubility Prediction ◽  
Temperature Dependent ◽  
Solubility Predictions ◽  
Multiple Linear Regression Method ◽  
Ion Interaction Model ◽  
Salt Lake Brine

Solubilities of the reciprocal quaternary system (Li+, Mg2+//Cl-, SO42-–H2O) at 273.15K were calculated using Pitzer and its extended HW model. The values of the Pitzer single-salt parameters β(0), β(1), β(2)and Cφfor LiCl, MgCl2, Li2SO4, and MgSO4, the mixed ion-interaction parameters θLi,Mg, θCl,SO4, ψLi,Mg,Cl, ψLi,Mg,SO4, ψLi,Cl,SO4and ψMg,Cl,SO4, and the Debye–Hückel parameter Aφin the system at 273.15K were derived either temperature-dependent equation or through fitting solubility data of the ternary system by multiple linear regression method. Based on the Jänecke indexes, the phase diagram was plotted. This study affords the necessary parameters for solubility predictions of complicated systems and establishes a theoretical basis for the separation of these valuable minerals from salt lake brine.

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