A method for increasing the recycling capacity of waste engine oil
A waste engine oil, processing capacity technology, applied in the direction of lubricating compositions, etc., can solve the problem of small processing capacity of waste engine oil regeneration process, and achieve considerable economic benefits, scientific design, and low energy consumption
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Embodiment 1
[0048] The raw material distillation data is:
[0049]
[0050]
[0051] The system used in this embodiment to increase the treatment capacity of waste engine oil includes a raw material buffer tank 1, a raw material pump 2, a first heater 3, an atmospheric distillation tower 4, an atmospheric tower bottom pump 6, The second heater 8, the first vacuum distillation tower 9, the first vacuum tower bottom pump 12, the third heater 13, the scraper evaporator 15, the second vacuum distillation tower 16; the atmospheric distillation tower 4 The top of the tower is connected with the first condensing tower 19, the first reflux tank 7, and the light oil transfer pump 5 in sequence. The light oil transfer pump 5 extracts the light oil in the reflux tank 7, and a part of the light oil returns to normal pressure. In the distillation tower 4, another part of the light oil is transported to the storage tank for storage; the first reflux tank 7 is provided with a water recovery pipeli...
Embodiment 2
[0069] The raw material distillation data is:
[0070]
[0071] The step of waste engine oil regeneration is the same as embodiment 1, and the difference is the process parameters in each process, and concrete process parameters are as shown in table 4:
[0072] Process parameter in table 4 embodiment 2
[0073] equipment parameter Atmospheric distillation column 4 feed temperature °C 290 Atmospheric distillation tower 4 top temperature ℃ 185 Feed temperature of the first vacuum distillation tower 9°C 330 Temperature at the top of the first vacuum distillation tower 9°C 80 The first vacuum distillation tower 9 minus the first-line temperature °C 170 The first vacuum distillation tower 9 minus the temperature of the second line ℃ 275 Circulation volume of the first vacuum distillation tower 9 tower kettle KG / h 20000 Scraper evaporator 15 feed temperature ℃ 330 Second vacuum distillation column 16 feed temperatur...
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