Method for recovering oil-containing waste active white clay by dichloroethane
A technology of activated clay and dichloroethane, which is applied in the field of comprehensive resource recovery, can solve the problems of internal structural damage of regenerated activated clay, low oil extraction rate, and secondary pollution of the environment, achieving low toxicity, high recovery rate, and low input costs. low effect
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Embodiment 1
[0016] A method for recovering oil-containing waste activated clay by using dichloroethane, including the following steps:
[0017] 1) The oily waste activated clay is leached more than once with a solvent, and the filter residue and oily components are obtained after solid-liquid separation. The solvent is 1,1-dichloroethane;
[0018] 2) Dry the filter residue obtained in step 1) to obtain regenerated activated clay;
[0019] 3) The oily components obtained in step 1) are distilled to separate distillate and grease.
[0020] Step 1) The mass ratio of solvent to oily waste activated clay during the medium extraction is 1.5:1.
[0021] The drying temperature in step 2) is 50-70°C, and the volatiles during drying are condensed and then refluxed to step 1) for use as a solvent.
[0022] The distillation temperature in step 3) is 60-70°C, and the separated fraction is refluxed to step 1) for use as a solvent.
[0023] Step 2) The regenerated activated clay obtained is used as a grease decolor...
Embodiment 2
[0026] A method for recovering oil-containing waste activated clay by using dichloroethane, including the following steps:
[0027] 1) Use a solvent to extract oil-containing waste activated clay more than once, and obtain filter residue and oily components after solid-liquid separation. The solvent is 1,1-dichloroethane;
[0028] 2) Dry the filter residue obtained in step 1) to obtain regenerated activated clay or regenerated diatomite;
[0029] 3) The oily components obtained in step 1) are distilled to separate distillate and grease.
[0030] Step 1) The mass ratio of the solvent to the oily waste activated clay during the medium extraction is 2:1.
[0031] The drying temperature in step 2) is 50-70°C, and the volatiles during drying are condensed and then refluxed to step 1) for use as a solvent.
[0032] The distillation temperature in step 3) is 60-70°C, and the separated fraction is refluxed to step 1) for use as a solvent.
[0033] Step 2) The regenerated activated clay obtained i...
Embodiment 3
[0036] A method for recovering oil-containing waste activated clay by using dichloroethane, including the following steps:
[0037] 1) Use a solvent to extract oily waste diatomaceous earth more than once, and obtain filter residue and oily components after solid-liquid separation. The solvent is 1,1-dichloroethane;
[0038] 2) Dry the filter residue obtained in step 1) to obtain regenerated activated clay or regenerated diatomite;
[0039] 3) The oily components obtained in step 1) are distilled to separate distillate and grease.
[0040] Step 1) The mass ratio of solvent to oily waste diatomaceous earth during medium extraction is 3:1.
[0041] The drying temperature in step 2) is 50-70°C, and the volatiles during drying are condensed and then refluxed to step 1) for use as a solvent.
[0042] The distillation temperature in step 3) is 60-70°C, and the separated fraction is refluxed to step 1) for use as a solvent.
[0043] Step 2) The obtained regenerated diatomaceous earth is used as ...
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