Device and method for directly heating and cracking waste polyolefin by hydrogen-oxygen combustion method
A technology of waste polyolefin and combustion method, which is applied in the preparation of liquid hydrocarbon mixtures and the petroleum industry, etc. It can solve the problems of poor process control and increased costs, and achieve the effect of avoiding heat transfer process and uneven mixing
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Embodiment 1
[0099] Example 1 The high temperature cracking of waste polyolefin mild cracking liquid product
[0100] The waste polyolefin used in this example is a high-density polyethylene / polypropylene mixture, and the cracking raw material is a fraction with a boiling point -1 , Constant temperature residence time 40 ~ 90min. The liquid product obtained by mild cracking is distilled to obtain fractions with a boiling point <380°C. The cracking method and device used in this example are as described above.
[0101] In this example, under the conditions shown in Table 1, the pyrolysis raw materials are subjected to pyrolysis. The cracking results of this embodiment are shown in Table 2.
[0102] It can be seen from Table 2 that the polyolefin cracking liquid has good cracking performance, and the obtained ethylene and propylene have a relatively high molar content. With the increase of cracking temperature, the production rate of ethylene and propylene increases.
[0103] The pyrolys...
Embodiment 2
[0107] Example 2 High temperature cracking of waste polyolefin mild cracking waxy product and light diesel oil mixture
[0108] The waste polyolefin used in this example is a high-density polyethylene / polypropylene mixture, and the cracking raw material is a mixture of viscous soft solid paraffin and light diesel oil obtained by mild cracking of high-density polyethylene in a certain proportion. A 1L closed reactor is used for mild cracking, the cracking temperature is set at 400°C, and the heating rate is 3-5°C·min -1 , constant temperature residence time. The light oil used in this embodiment is the same as in Example 2, and the high-temperature cracking system used is the same as in Example 1.
[0109] In this embodiment, under the conditions shown in Table 3, the pyrolysis raw materials are subjected to pyrolysis. The cracking results of this embodiment are shown in Table 4.
[0110] Table 4 shows that the mixture of waxy products and petroleum hydrocarbons has good cra...
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