Solvent dewaxing method of low-wax content heavy hydrocarbon oil
A technology of heavy hydrocarbon oil and dewaxing solvent is applied in the field of dewaxing of hydrocarbon oil, which can solve problems such as difficulty in removal, and achieve the effects of increasing the frequency of warm washing, increasing the filtration speed, and reducing the temperature difference of dewaxing.
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Embodiment 1
[0039] The raw oil is light deasphalted oil, and its properties are shown in Table 1. The mass ratio of microcrystalline wax to raw oil is 0.08:1, the dewaxing solvent is butanone-toluene mixed solvent, the volume content of butanone is 50%, the multi-point dilution process is adopted, and the total agent oil ratio is 4.2:1. The deoiling solvent is the same as the dewaxing solvent, and it is diluted once, and the ratio of agent to oil is 0.8:1 (relative to the raw material oil). Attached figure 1 The process of preparing dewaxed oil is as follows:
[0040](1) Add petroleum microcrystalline wax with a melting point of 82°C into the raw oil, heat to 100°C, fully melt and mix evenly, and then add dilution solvents in sequence. Cooled to -15°C, filtered to obtain dewaxed filtrate and dewaxed wax paste, and dewaxed oil was obtained after the filtrate was removed from the solvent. Add diluting solvent to the wax paste and mix evenly, heat to 30°C, and filter to obtain deoiled fil...
Embodiment 2
[0047] The raw material oil is light dehydrotreated oil, and its properties are shown in Table 1. The mass ratio of petroleum microcrystalline wax and raw material oil is 0.02:1, the dewaxing solvent is butanone-toluene mixed solvent, the volume content of butanone is 75%, the multi-point dilution process is adopted, and the total agent oil ratio is 2.5:1. The deoiling solvent is the same as the dewaxing solvent, and it is diluted once, and the ratio of agent to oil is 1.3:1 (relative to the raw material oil). Attached figure 1 The process of preparing dewaxed oil is as follows:
[0048] (1) Add petroleum microcrystalline wax with a melting point of 80°C into the raw material oil, heat it to 90°C, fully melt and mix evenly, and then add the dilution solvent successively. Cool to -20°C, filter to obtain dewaxed filtrate and dewaxed wax paste, and remove the solvent from the filtrate to obtain dewaxed oil. Add diluting solvent to the wax paste and mix evenly, heat to 15°C, an...
Embodiment 3
[0053] The raw material oil is light deasphalted solvent refining extracted oil, and its properties are shown in Table 1. The mass ratio of petroleum microcrystalline wax and raw material oil is 0.12:1, the dewaxing solvent is butanone-toluene mixed solvent, the volume content of butanone is 65%, the multi-point dilution process is adopted, and the total agent oil ratio is 6.0:1. The deoiling solvent is the same as the dewaxing solvent, and it is diluted once, and the ratio of agent to oil is 0.3:1 (relative to the raw material oil). Attached figure 1 The process of preparing dewaxed oil is as follows:
[0054] (1) Add petroleum microcrystalline wax with a melting point of 75°C into the raw material oil, heat to 75°C, fully melt and mix evenly, and then add each dilution solvent in turn. Cool to -10°C, filter to obtain dewaxed filtrate and dewaxed wax paste, and obtain dewaxed oil after removing solvent from the filtrate. Add diluting solvent to the wax paste and mix evenly...
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