A kind of method that utilizes waste oil to prepare alkyl glycoside surfactant
A technology of surfactant and alkyl glycoside, which is applied in the field of preparation of nonionic surfactant, can solve the problems of high production cost and lower production cost of nonionic surfactant, achieve great social value, reduce production cost, good color effect
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Embodiment 1
[0033] (1) Refining of waste oil
[0034]After filtering 300kg of rough gutter oil to remove impurities at room temperature, add 2kg of phosphoric acid with a concentration of 75%, degumming at 60°C, and stir thoroughly for 20 minutes, then centrifuge to remove the precipitate; add 2kg of sodium hydroxide for alkali refining, and stir quickly for 20 minutes , after standing for 10 hours, separate the waste oil in the upper layer; heat up the obtained waste oil to 75 ° C, add 8 kg of 100-mesh activated clay for decolorization, filter after stirring for 30 minutes, and transfer the separated waste oil into the reaction kettle. Vacuumize to 10kPa at room temperature, stir for 1 hour, and obtain 230kg of refined waste oil when the moisture content in the waste oil is detected to be lower than 0.1%.
[0035] (2) Reduction of refined waste oil
[0036] The above-mentioned 230kg of refined waste oil is transferred to a high-pressure reactor, and 0.3kg of Ni / Pd type catalyst is loade...
Embodiment 2
[0042] (1) Refining of waste oil
[0043] After filtering 300kg of rough gutter oil to remove impurities at room temperature, add 2kg of phosphoric acid with a concentration of 75%, degumming at 65°C, stirring thoroughly for 20 minutes, and centrifuging; adding 2kg of sodium hydroxide for alkali refining, stirring rapidly for 15 minutes, and statically After standing for 10 hours, separate the waste oil in the upper layer; raise the temperature of the obtained waste oil to 80°C, add 8kg of 100-mesh activated clay for decolorization, stir for 30 minutes and then filter, transfer the separated grease into the reaction kettle, and evacuate to 10kPa, Stir for 1 hour, and obtain 230 kg of refined waste oil when the water content in the waste oil is lower than 0.1%.
[0044] (2) Reduction of refined waste oil
[0045] The above-mentioned 230kg of refined waste oil is transferred to a high-pressure reactor, and 0.3kg of Ni / Pd type catalyst is loaded into diatomite, which contains Ni...
Embodiment 3
[0051] (1) Refining of waste oil
[0052] After filtering 300kg of rough gutter oil to remove impurities at room temperature, add 2kg of phosphoric acid with a concentration of 75%, degumming at 65°C, stirring thoroughly for 20 minutes, and centrifuging; adding 2kg of sodium hydroxide for alkali refining, stirring rapidly for 15 minutes, and statically After standing for 24 hours, separate the waste oil in the upper layer; raise the temperature of the obtained waste oil to 75°C, add 8kg of crude oil with 100-mesh activated clay for decolorization, stir for 30 minutes and then filter under reduced pressure, and transfer the separated oil into the reaction kettle. Vacuumize to 10kPa, stir for 1 hour, and obtain 230kg of refined waste oil when the water content in the waste oil is lower than 0.1%.
[0053] (2) Reduction of refined waste oil
[0054] The above-mentioned 230kg of refined waste oil is transferred to a high-pressure reactor, and 0.3kg of Ni / Pd type catalyst is loade...
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