Method for extracting fuel from waste oil bag, waste throwaway and waste plastic
A technology for waste plastics and bulk orders, which is applied in the petroleum industry, biological raw materials, preparation of liquid hydrocarbon mixtures, etc., can solve the problems of sticking on the axe wall, easy coking, waste, etc. The effect of simple science
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Embodiment 1
[0018] A method for extracting fuel oil by utilizing waste oil bags, waste slips and waste plastics, the method is:
[0019] 1) Add waste oil bags, waste sheets and other raw materials into the 20 cubic meter reaction ax; add the depolymerization agent and cracking agent into the reaction ax along with the raw materials, and the addition amount is 4% of the raw material mass; add the catalyst into the reaction catalyst tower inside the catalytic unit;
[0020] 2) Heating: control the heating rate to 150 degrees per hour, and heat for 2 hours;
[0021] 3) Continue heating, control the temperature at 250, the water vapor starts to flow out through the condenser, and enters the oil-water separator; the reaction cracking gas is catalytically modified by a catalyst, and then passes through the condenser to obtain liquid oil and gas products, and the liquid oil is fractionated to obtain gasoline , diesel oil; the gas products are collected and stored for reuse; until a little resid...
Embodiment 2
[0028] The difference between this embodiment and the above-mentioned embodiment is: the method 1) adding raw materials such as waste oil bags and waste sheets into 40 cubic meters of reaction ax; Add-on is 5% of raw material quality; Catalyst is added in the catalytic device of reaction catalytic tower; 2) Heating: control heating rate is 250 degree / hour, heating 1 hour; 3) continue heating, control temperature at 350 degree; Catalyst addition is Fill 100kg at a time.
Embodiment 3
[0030] This is the difference between the embodiment and implementation 1: the method 2) heating: control the heating rate to 200 degrees / hour, and heat for 1.2 hours; 3) continue heating, and control the temperature at 450 degrees.
[0031] In summary, the raw materials of the present invention are oil-soaked polyethylene, polypropylene, polystyrene, etc.; the depolymerization agent and cracking agent are added to the reaction ax along with the raw materials, and the raw materials can be directly added to the ax without pre-treatment. In this way, time and labor are saved; the depolymerization agent and cracking agent are added according to the ratio of 4% to 5% of the amount of raw materials added, and the catalyst is added in the catalytic device of the reaction catalyst tower according to the size of the reaction ax. Add once, and replace the catalyst multiple times. For example, in a 20 cubic meter reactor, add 50 kg of the catalyst and replace it every 6-8 ax produced; st...
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