Method and device of refining separating zinc by bismuth method
A technology of fire refining and refining pot, which is applied in the direction of improving process efficiency, etc., can solve the problems of loss of metal zinc, pollution of the environment, etc., and achieve the effects of stable operation, uniform speed, and stable air pressure
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Embodiment 1
[0023] A method for separating zinc from bismuth liquid after adding zinc and removing silver by pyro-refining, the production steps are:
[0024] Step 1: Put the bismuth liquid in a closed vacuum container, and control its temperature at about 650°C, and stir it with a stirring device, so that the lower layer of bismuth liquid is continuously lifted to the liquid surface, and the zinc from the bismuth liquid Evaporate to get zinc vapor;
[0025] Step 2: Vacuumize the zinc vapor to rise to the condensing equipment, and the vacuum residual pressure is controlled at about 50Pa. On the condensing equipment, the zinc vapor solidifies into a solid after being cooled, and attaches to the condensing equipment to obtain solid metal zinc;
[0026] Step 3: Introduce the tail gas after condensing and recovering zinc into the sedimentation purification equipment for purification treatment and discharge.
[0027] A method for extracting zinc from silver-zinc slag after adding zinc and rem...
Embodiment 2
[0034] With embodiment 1, difference is: in the method for separating zinc from the bismuth liquid after pyro-refining adds zinc and removes silver:
[0035] The vacuum distillation temperature of the bismuth liquid in step 1 is controlled at about 450°C,
[0036] The vacuum residual pressure in step 2 is controlled at about 1Pa,
[0037] In the method for extracting zinc from the silver-zinc slag after adding zinc and removing silver by pyro-refining:
[0038] The temperature at which the silver-zinc slag in step 1 melts into a liquid is about 750°C;
[0039] The vacuum distillation temperature of the melt in step 2 is controlled at about 650°C;
[0040]The vacuum residual pressure in step 3 is controlled at about 1Pa;
[0041] For the device implementing the above method, the water temperature in the cooling water jacket 3 is controlled at 40° C., and the rotating speed of the circulating screw pump 4 is controlled at 1000 rpm.
[0042] It is proved by inspection that th...
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