Figures & data
Table 1. Chemical composition of the end-of-life CRT funnel glass analyzed by X-ray fluorescence (XRF)
Figure 1. SEM images of CRT funnel glass after mechanical activation for 2 hr at different rotational speeds under an ambient atmosphere: (A) raw material; (B) 100 rpm; (C) 300 rpm; (D) 500 rpm; (E) 700 rpm.
![Figure 1. SEM images of CRT funnel glass after mechanical activation for 2 hr at different rotational speeds under an ambient atmosphere: (A) raw material; (B) 100 rpm; (C) 300 rpm; (D) 500 rpm; (E) 700 rpm.](/cms/asset/acc8bd48-f109-47ea-8414-2a299dfc30a9/uawm_a_711796_o_f0001g.gif)
Figure 2. X-ray diffraction patterns of raw material and 120-min-activated CRT funnel glass at different rotational speeds.
![Figure 2. X-ray diffraction patterns of raw material and 120-min-activated CRT funnel glass at different rotational speeds.](/cms/asset/c1c3ff45-6c8f-4701-8913-6c155cb33fec/uawm_a_711796_o_f0002g.gif)
Figure 3. Dependence of recovery rate of major elements on milling rotational speed, under the following conditions: leaching temperature of 95 °C, HNO3 concentration 3 mol/L, and leaching time of 1 hr.
![Figure 3. Dependence of recovery rate of major elements on milling rotational speed, under the following conditions: leaching temperature of 95 °C, HNO3 concentration 3 mol/L, and leaching time of 1 hr.](/cms/asset/ae5b0b3b-129c-43bc-8b6e-f30ac232c5ca/uawm_a_711796_o_f0003g.gif)
Figure 4. Dependence of recovery rate of major elements on activation time, under the following conditions: leaching temperature at 95 °C, HNO3 concentration 3 mol/L, and leaching time of 1 hr.
![Figure 4. Dependence of recovery rate of major elements on activation time, under the following conditions: leaching temperature at 95 °C, HNO3 concentration 3 mol/L, and leaching time of 1 hr.](/cms/asset/6f90e3a2-f7ed-4336-b782-801d0dc5364d/uawm_a_711796_o_f0004g.gif)
Figure 5. Dependence of recovery rate of major elements on the leaching temperature, under the following conditions: leaching time of 1 hr and HNO3 concentration 3 mol/L.
![Figure 5. Dependence of recovery rate of major elements on the leaching temperature, under the following conditions: leaching time of 1 hr and HNO3 concentration 3 mol/L.](/cms/asset/d772f3d2-4d18-43ea-9b32-04c7aa39de1f/uawm_a_711796_o_f0005g.gif)
Figure 6. Dependence of recovery rate of major elements on the acid concentration, under the following conditions: leaching time for 1 hr and temperature at 95 °C.
![Figure 6. Dependence of recovery rate of major elements on the acid concentration, under the following conditions: leaching time for 1 hr and temperature at 95 °C.](/cms/asset/66a8c1bd-e888-4ca8-ac54-e1983244bb02/uawm_a_711796_o_f0006g.gif)
Figure 7. Dependence of recovery rate of major elements on the liquid-to-solid ratio, under the following conditions: HNO3 concentration 3 mol/L, leaching time of 1 hr, and temperature at 95 °C.
![Figure 7. Dependence of recovery rate of major elements on the liquid-to-solid ratio, under the following conditions: HNO3 concentration 3 mol/L, leaching time of 1 hr, and temperature at 95 °C.](/cms/asset/633e184e-f6cb-4eef-86fe-ea9228d06e2c/uawm_a_711796_o_f0007g.gif)
Figure 8. Dependence of recovery rate of major elements on the leaching time, under the following conditions: HNO3 concentration 3 mol/L and leaching temperature at 80 °C.
![Figure 8. Dependence of recovery rate of major elements on the leaching time, under the following conditions: HNO3 concentration 3 mol/L and leaching temperature at 80 °C.](/cms/asset/ff78fe8d-0135-4818-9498-fe974f8430fd/uawm_a_711796_o_f0008g.gif)