Microcrystalline wax hydrogenation method
A technology of microcrystalline wax and high-pressure hydrogenation, which is applied in the refining of petroleum wax, can solve problems that are difficult to meet at the same time, and achieve the effects of low cost, simple and flexible operation, and high yield
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Embodiment 1
[0012] The microcrystalline wax raw material containing 2.21w% oil is used, the properties are shown in Table 1, and the properties of the catalyst are shown in Table 2.
[0013] The mixture of microcrystalline wax and hydrogen heated to a certain temperature enters the reactor, and under the action of the catalyst, by controlling the appropriate reaction conditions, hydrodesulfurization, denitrogenation, deoxygenation and aromatic hydrocarbon saturation reactions are carried out; after the material flows out of the reactor, it passes through After gas-liquid separation and vacuum deodorization, it is a white microcrystalline wax product. The reduction condition of the catalyst is hydrogen reduction at 3.5 MPa and 320° C. for 20 hours. The process conditions and product properties are shown in Tables 3 and 4, and the products in Table 4 meet the standard requirements of food-grade microcrystalline wax.
Embodiment 2
[0015] The raw material used in this embodiment is an oil-containing 2.68% microcrystalline wax raw material (referring to Table 1), and the catalyst is the same as in Example 1. The reduction condition of the catalyst is to reduce with hydrogen for 25 hours at 5.5MPa and 300°C. The process conditions and product properties are shown in Tables 3 and 4, respectively.
Embodiment 3
[0017] The raw material used in this implementation is microcrystalline wax raw material containing 3.05% oil (referring to Table 1), and the catalyzer is the same as embodiment 1, and the reduction condition of the catalyzer is to use hydrogen to reduce 28 hours under 4.5MPa and 280 ℃ of conditions. The process conditions and product quality are shown in Table 3 and 4, respectively.
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