A kind of unloading device and unloading method of solidified palmitic acid oil packed in liquid bag
A technology of palmitizing and unloading device, applied in the directions of packaging, transportation and packaging, loading/unloading, etc., can solve the problems of high labor intensity, difficult to heat, large volume of liquid bags, etc., to improve oil quality, high utilization rate, Simple to use effects
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Embodiment 1
[0096] A method for unloading the solidified palmitic acid oil packed in liquid bags, which comprises the following steps:
[0097] (1) Insert the feeding port of the screw conveyor 1 into the liquid bag, move the leakage collector 15 so that the first collecting part 151 of the leakage collector 15 is covered on the opening of the liquid bag, start the screw conveyor 1, palm The acidified oil is transported to the oil storage tank 2 through the screw conveyor 1; during this period, the screw conveyor 1 is moved according to the demand to adjust the insertion depth of the screw conveyor 1 in the liquid bag, and at the same time, the leakage collector 15 is moved to ensure that the first collecting part 151 cover is located on the opening of liquid bag.
[0098] (2) After the unloading of the palmitic acid oil is completed, start the first heating component 22 on the oil storage tank 2 to heat the oil storage tank 2, control the heating temperature to 50°C, keep it warm for 1 h...
Embodiment 2
[0104] The difference between this embodiment and the embodiment is:
[0105] The heating temperature in step (2) is 55° C., and the amount of phosphoric acid added in step (4) is 2% of the mass of the mixed phase in the separation tank 3 .
[0106] After testing, in this example, the water content of the first oil phase in step (2) was 2.5%, and the recovery rate of palmitic acid oil in step (5) was 35%.
Embodiment 3
[0108] The difference between this embodiment and the embodiment is:
[0109] The heating temperature in step (2) is 60°C, and the amount of phosphoric acid added in step (4) is 3% of the mass of the mixed phase in the separation tank 3 .
[0110] After testing, in this example, the water content of the first oil phase in step (2) was 2.2%, and the recovery rate of palmitic acidified oil in step (5) was 37%.
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