Titlebook: Rare Metal Technology 2019; Gisele Azimi,Hojong Kim,Alafara Abdullahi Baba Conference proceedings 2019 The Minerals, Metals & Materials So

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書目名稱Rare Metal Technology 2019影響因子(影響力)




書目名稱Rare Metal Technology 2019影響因子(影響力)學(xué)科排名




書目名稱Rare Metal Technology 2019網(wǎng)絡(luò)公開(kāi)度




書目名稱Rare Metal Technology 2019網(wǎng)絡(luò)公開(kāi)度學(xué)科排名




書目名稱Rare Metal Technology 2019被引頻次




書目名稱Rare Metal Technology 2019被引頻次學(xué)科排名




書目名稱Rare Metal Technology 2019年度引用




書目名稱Rare Metal Technology 2019年度引用學(xué)科排名




書目名稱Rare Metal Technology 2019讀者反饋




書目名稱Rare Metal Technology 2019讀者反饋學(xué)科排名

SMART

SOBER

Recovery of Scandium by Leaching Process from Brazilian Red Mud a leaching process of Brazilian red mud to obtain scandium. Sulfuric acid 20 wt% was used as leaching agent, L/S ratio 1/10 (please add unit), temperature of 25?°C and 6?h of reaction time. Samples were analyzed using inductively coupled plasma optical emission spectroscopy (ICP-OES) and X-ray diffraction (XRD).

芳香一點(diǎn)

conjunctivitis

Esalate

osteopath

Reduction of TiCl4 to TiH2 with CaH2 in Presence of Ni Powderned for the sample reduced at 500?℃ with 50% Ni catalyst for 3?h. Samples with higher weight gain were characterized by X-ray diffraction (XRD) and scanning electron microscope (SEM). The results indicate that producing of TiH. from reduction of TiCl. with CaH. in the presence of Ni was feasible and could lead to low-temperature synthesis of TiH..

休閑

GEN

Feasibility of Copper Recovery from Spent Deposited Sludge of Transformer Oil (DSTO) for Industrial ic downfall. With increasing demands for metals and gradual depletion of non-renewable resources, there is a growing need to recover metals from secondary sources. The recycling from metal wastes is necessary as the cost of safe disposal of hazardous components is quite high compared to the amount o

共同給與

Leaching and Recovery of an Oxide Gold Concentrate Using Ammoniacal Thiosulfate Solutions concentrate. 80.5% of gold extraction could be achieved by thiosulfate leaching under the conditions of (NH.).S.O. 0.2?mol/L, CuSO. 0.025?mol/L, NH. 1.5?mol/L and leaching time 8?h, and the thiosulfate consumption was 53.6?kg/t-concentrate. IRA-400 anion exchange resin was used to recover gold from