Technique method of producing high-quality coke by residual oil or medium and low temperature coal tar
A low-temperature coal tar, high-quality coke technology, applied in the fields of oil refining, coal chemical industry, and petrochemical industry, can solve the problems of insufficient optimization of operating conditions and energy utilization, and achieve the effect of reducing energy consumption, reducing investment and simplifying the process flow
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Embodiment 1
[0041] In this embodiment, the vacuum residue A is used as the raw material, and the operation is carried out by organically combining the three units of residue hydrotreatment-delayed coking-PSA purification. After the vacuum residue passes through the hydrotreating unit, all products of the hydrotreating are directly sent to the delayed coking unit without separation. In the delayed coking unit, the residual oil after hydrogenation first enters the waste heat recovery device to exchange heat with the flue gas from the heating furnace, and then enters the coking heating furnace, coke tower and fractionation tower in turn after heat exchange. The fractionation tower sequentially obtains overhead gas, diesel oil and wax oil, and the overhead gas is separated by an oil-gas separator to obtain coke dry gas and gasoline. Coking dry gas enters the PSA purification unit after desulfurization, and the PSA purification unit adopts a 10-2-4 process (10 adsorption beds, 2 bed inlets, 4 ...
Embodiment 2
[0045] In this example, the vacuum residue B is used as the raw material, and the process method adopted is the same as in Example 1. The operating conditions, product distribution and coke properties are shown in Tables 3, 4 and 5, respectively.
[0046] Comparing the results of the invention, it can be seen that the method of organically combining the three units of residual oil hydrotreating-delayed coking-PSA purification can increase the yield of gasoline and diesel by 13.6% and 15% respectively, and the properties of coke have been significantly improved; the process of the present invention Compared with conventional residual oil hydrogenation and delayed coking processes, it can save energy by 30%.
[0047] Table 1 Properties of vacuum residue
[0048] Raw oil number Vacuum residue A Vacuum residue B Density at 20°C, g / cm 3 1.06 0.98 S content, m% 6.01 1.39 N content, m% 0.78 1.02 Carbon residue, m% 24.74 13.95 Metal (Ni+...
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