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Technical Papers

Lead recovery from cathode ray tube funnel glass with mechanical activation

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Pages 2-10 | Published online: 27 Dec 2012

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.

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.

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.

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.

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.

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.

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.

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.

Figure 9. Photo and XRD pattern of residue after leaching in 3 mol/L HNO3 at 95 °C for 1 hr (L/S = 150). (Color figure available online).

Figure 9. Photo and XRD pattern of residue after leaching in 3 mol/L HNO3 at 95 °C for 1 hr (L/S = 150). (Color figure available online).

Figure 10. O1s, Si2p, and Pb4f spectra of unactivated, activated, and leached samples.

Figure 10. O1s, Si2p, and Pb4f spectra of unactivated, activated, and leached samples.
Supplemental material

Supplementary Materials

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