Abstract:Incinerated ash with a relatively high Ca content, paper sludge ash, was converted to zeolitic materials with high cation-exchange capacities (CECs) by aging at 80 °C in NaOH solution via step-wise acid leaching with HCl to reduce the ash Ca content. The extraction of Ca, Mg, Si, and Al from the ash into the acid solutions during leaching and the products obtained from the leached ash by reaction with an alkali were examined. The contents of Ca and Mg in the ash were more easily extracted from the ash than tho… Show more
“…The WAT sample contains four aluminum phases, namely, Ca2Al2SiO7, Ca3Al2Si3O12, Mg3Al2Si3O12, and MgAl2O4 (Figure 1), but the solid residues obtained by HPAL of the WAT sample using 10 and 20% HCl contains no gehlenite, which fully dissolves at low leaching temperatures. These results correlate with the data of other researchers [54], where gehlenite passed into the solution in 1M HCl after 3-stage leaching during 2 hours at room temperature. Aluminum in the solid residues is in Ca3Al2Si3O12, Mg3Al2Si3O12, and MgAl2O4 phases that were incompletely dissolved at the experimental conditions.…”
Section: The Solid Residues Obtained From the Wat Samplesupporting
Red mud is a hazardous waste of alumina industry that contains high amounts of iron, aluminum, titanium and REEs. One of the promising methods for the extraction of iron from red mud is car-bothermic reduction with the addition of sodium salts. This research focuses on the process of hy-drochloric high-pressure acid leaching using 10–20% HCl of two samples of non-magnetic tailings obtained by 60-minute carbothermic roasting of red mud at 1300 °C and the mixture of 84.6 wt. % of red mud and 15.4 wt. % Na2SO4 at 1150 °C, respectively, with subsequent magnetic separation of metallic iron. An influence of temperature, leaching duration, solid-to-liquid-ratio and acid con-centration on dissolution behavior of Al, Ti, Mg, Ca, Si, Fe, Na, La, Ce, Pr, Nd, Sc, Zr were studied. Based on the investigation of the obtained residues, mechanism of passing of valuable elements into the solution was proposed. It has shown that 90% Al, 91% Sc and above 80% of other REEs can be dissolved under optimal conditions; Ti can be extracted into the solution or the residue depending on the leaching temperature and acid concentration. Based on the research results, novel flowsheets for red mud treatment were developed.
“…The WAT sample contains four aluminum phases, namely, Ca2Al2SiO7, Ca3Al2Si3O12, Mg3Al2Si3O12, and MgAl2O4 (Figure 1), but the solid residues obtained by HPAL of the WAT sample using 10 and 20% HCl contains no gehlenite, which fully dissolves at low leaching temperatures. These results correlate with the data of other researchers [54], where gehlenite passed into the solution in 1M HCl after 3-stage leaching during 2 hours at room temperature. Aluminum in the solid residues is in Ca3Al2Si3O12, Mg3Al2Si3O12, and MgAl2O4 phases that were incompletely dissolved at the experimental conditions.…”
Section: The Solid Residues Obtained From the Wat Samplesupporting
Red mud is a hazardous waste of alumina industry that contains high amounts of iron, aluminum, titanium and REEs. One of the promising methods for the extraction of iron from red mud is car-bothermic reduction with the addition of sodium salts. This research focuses on the process of hy-drochloric high-pressure acid leaching using 10–20% HCl of two samples of non-magnetic tailings obtained by 60-minute carbothermic roasting of red mud at 1300 °C and the mixture of 84.6 wt. % of red mud and 15.4 wt. % Na2SO4 at 1150 °C, respectively, with subsequent magnetic separation of metallic iron. An influence of temperature, leaching duration, solid-to-liquid-ratio and acid con-centration on dissolution behavior of Al, Ti, Mg, Ca, Si, Fe, Na, La, Ce, Pr, Nd, Sc, Zr were studied. Based on the investigation of the obtained residues, mechanism of passing of valuable elements into the solution was proposed. It has shown that 90% Al, 91% Sc and above 80% of other REEs can be dissolved under optimal conditions; Ti can be extracted into the solution or the residue depending on the leaching temperature and acid concentration. Based on the research results, novel flowsheets for red mud treatment were developed.
“…The WAT sample contains four aluminum phases, namely, Ca2Al2SiO7, Ca3Al2Si3O12, Mg3Al2Si3O12, and MgAl2O4 (Figure 1), but the solid residues obtained by HPAL of the WAT sample using 10 and 20% HCl contains no gehlenite, which fully dissolves at low leaching temperatures. These results correlate with the data of other researchers [59], where gehlenite passed into the solution in 1 M HCl after three-stage leaching during 2 h at room temperature. Aluminum in the solid residues is in the Ca3Al2Si3O12, Mg3Al2Si3O12, and MgAl2O4 phases that were incompletely dissolved at the experimental conditions.…”
Section: The Solid Residues Obtained From the Wat Samplesupporting
confidence: 92%
“…Two samples of non-magnetic tailings were derived by reduction roasting-a magnetic separation process of red mud (RM) from the Bogoslovsky Aluminium Plant (Russian Federation, Krasnoturyinsk, 59.84 • N, 60.19 • E) at optimal conditions according to our previous work [53]. The first sample codenamed as without addition tailings (WAT) was obtained by the reduction roasting of RM at 1300 • C for 1 h. The second sample codenamed as sodium sulfate addition tailings (SSAT) was obtained by reduction roasting of the mixture of 84.6 wt.% RM and 15.4 wt.% Na 2 SO 4 at 1150 • C for 3 h. Both the roasted samples were ground, screened through a 300-mesh sieve, and magnetically separated using a wet method by the Davis tube XCGS-50 (Shaoxing Weibang Mining Machinery Manufacturing Co., Ltd., Zhejiang, China) at magnetic field intensity of 0.1 T. Table 1 demonstrates the chemical compositions including iron content of the RM, WAT, and SSAT samples.…”
Red mud is a hazardous waste of the alumina industry that contains high amounts of iron, aluminum, titanium and rare-earth elements (REEs). One of the promising methods for the extraction of iron from red mud is carbothermic reduction with the addition of sodium salts. This research focuses on the process of hydrochloric high-pressure acid leaching using 10 to 20% HCl of two samples of non-magnetic tailings obtained by 60 min carbothermic roasting of red mud at 1300 °C and the mixture of 84.6 wt.% of red mud and 15.4 wt.% Na2SO4 at 1150 °C, respectively, with subsequent magnetic separation of metallic iron. The influence of temperature, leaching duration, solid-to-liquid-ratio and acid concentration on the dissolution behavior of Al, Ti, Mg, Ca, Si, Fe, Na, La, Ce, Pr, Nd, Sc, Zr was studied. Based on the investigation of the obtained residues, a mechanism for passing valuable elements into the solution was proposed. It has shown that 90% Al, 91% Sc and above 80% of other REEs can be dissolved under optimal conditions; Ti can be extracted into the solution or the residue depending on the leaching temperature and acid concentration. Based on the research results, novel flowsheets for red mud treatment were developed.
“…The leaching conditions were decided by conferring previous papers [19][20][21][22] . Ash of 25 g was stirred in the 100 mL aqueous 28 J. ION EXCHANGE solution of 1 mol/L HCl or 0.5 mol/L H 2 SO 4 for 24 h with a magnetic stirrer at room temperature.…”
Alkali conversion of paper sludge ash into cation exchanger via acid leaching was examined. The extraction behaviors of major elements (Si, Al, Ca and Mg) from the ash into hydrochloric acid (1 mol/L HCl) and sulfuric acid (0.5 mol/L H 2 SO 4 ) aqueous solutions were almost same except Ca due to the formation of gypsum in the H 2 SO 4 solution. The ashes leached with 1 mol/L HCl and 0.5 mol/L H 2 SO 4 aqueous solutions were converted into zeolite-P and tobermorite, respectively, while the raw ash was converted into hydroxysodalite. The cation exchange capacities of the converted products from the ashes leached with HCl and H 2 SO 4 were 1.30 and 0.75 mmol/g, respectively, which were higher than that of the product from the raw ash (0.60 mmol/g). These results indicated that paper sludge ash could be converted into different types of cation exchanger via acid leaching.
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