Separation method for indium leachate of waste liquid crystal display
A separation method and leachate technology, which is applied in the field of separation of indium leachate from waste liquid crystal screens, can solve the problems of high cost, unfriendly environment, low efficiency of indium recovery, etc., achieve low industrialization cost, solve the problem of recycling, and have a clear process Effect
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2022-02-01
Smart Images

Figure 1
Abstract
Description
technical field
[0001] The invention relates to the field of recycling waste liquid crystal panels, and more specifically relates to a method for separating the indium leaching solution of waste liquid crystal panels. Background technique
[0002] Indium is a scattered metal widely used in military, national defense, energy, electronics, medical and other fields, and its reserves in the earth's crust are only 1 / 6 of gold. The amount of indium used in new applications will increase at a rate of 10-20% per year, and 60-70% of indium products are used in the production of indium tin oxide for liquid crystal displays. ITO film has transparency and conductivity, and is mainly used in the electronics industry. ITO glass is widely used in transparent electrodes for flat panel displays. At present, developed countries in the world such as Japan, the United States, France, and the United Kingdom use about half of indium for the preparation of ITO targets, and the domestic preparati...
Examples
Embodiment 1
[0031] Such as figure 1 As shown, a method for separating the indium leachate of waste liquid crystal screens shown in this embodiment comprises the following steps:
[0032] (1) The waste liquid crystal panel is broken to obtain a 5cm strip, and the strip is rolled to break the glass stuck on the polarizer;
[0033] (2) Carry out acid leaching treatment to the product processed through above-mentioned steps (1), the used leaching solution of acid leaching is that concentration is 20%H 2 SO 4 solution, the acid leaching process temperature is 50°C, and the soaking time is 4 hours;
[0034] (3) Slowly add caustic soda to the leachate obtained in step (2) for neutralization, adjust the pH to -0.3, brown rubber is separated out, filter the separated impurities, and reclaim the filter residue tin hydroxide as a chemical raw material;
[0035] (4) filter the gained filtrate of step (3) gained acid dipping liquid and extract, get the leachate of 500ml and add in the separatory fu...
Embodiment 2
[0038] A method for separating the indium leaching solution of waste liquid crystal screens shown in this embodiment comprises the following steps:
[0039] (1) The waste liquid crystal panel is broken to obtain a 5cm strip, and the strip is rolled to break the glass stuck on the polarizer;
[0040] (2) Carry out acid leaching treatment to the product processed through above-mentioned steps (1), the used leaching solution of acid leaching is that concentration is 20%H 2 SO 4 solution, the acid leaching process temperature is 50°C, and the soaking time is 4 hours;
[0041] (3) Slowly add caustic soda to the leachate obtained in step (2) for neutralization, adjust the pH to 0.5, brown rubber is separated out, filter the precipitated impurities, and reclaim the filter residue tin hydroxide as a chemical raw material;
[0042] (4) filter the gained filtrate of step (3) gained leachate and extract, get the leachate of 500ml and add in the separatory funnel, then add 100ml organic...
Embodiment 3
[0045] A method for separating the indium leaching solution of waste liquid crystal screens shown in this embodiment comprises the following steps:
[0046] (1) The waste liquid crystal panel is broken to obtain a 5cm strip, and the strip is rolled to break the glass stuck on the polarizer;
[0047] (2) Carry out acid leaching treatment to the product processed through above-mentioned steps (1), the used leaching solution of acid leaching is that concentration is 20%H 2 SO 4 solution, the acid leaching process temperature is 50°C, and the soaking time is 4 hours;
[0048] (3) Slowly add caustic soda to the leachate obtained in step (2) for neutralization, adjust the pH to 1, brown rubber is separated out, filter the precipitated impurities, and reclaim the filter residue tin hydroxide as a chemical raw material;
[0049] (4) filter the gained filtrate of step (3) gained leachate and extract, get the leachate of 500ml and add in the separatory funnel, then add 100ml organic pha...