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Process for reducing sulfur content of vacuum residuum

A technology for vacuum residue and sulfur content, which is applied in the treatment of hydrocarbon oil, refined hydrocarbon oil, petroleum industry, etc., and can solve the problem that the sulfur content of heavy oil cannot be reduced, the stability of the adsorbent is not good, and the desulfurization effect of oil products is unknown. and other problems, to achieve the effect of eliminating interphase mass transfer resistance, increasing transfer efficiency, and improving enterprise economic benefits.

Active Publication Date: 2021-02-26
CHINA PETROLEUM & CHEM CORP +1
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Problems solved by technology

[0004] Among the existing oil desulfurization related technologies, the patent CN108993526A discloses a gasoline desulfurization treatment method, which uses a fixed-bed reactor to catalyze gasoline to produce clean gasoline with ultra-low sulfur, low olefins, and high octane number. Gasoline, but the whole process needs to take place in a hydrogen environment, the volume ratio of hydrogen to oil is 160-460:1, the hydrogen consumption is large and the equipment requirements are high; patent CN108219835A proposes a naphtha desulfurization method, through the synthesis of solid particles The desulfurization adsorbent is a type of desulfurization adsorbent, and the adsorbent is put into the naphtha under static conditions to realize oil desulfurization, but the stability of the adsorbent itself is not good, the whole process needs to strictly control the water content, and the desulfurization effect of the oil product is unknown; the patent CN108795484A uses miscellaneous Polyacid quaternary ammonium salt-formic acid is used as a catalyst, and oxygen is used to catalyze the oxidation of diesel oil in the reactor, and a certain amount of N-methylpyrrolidone is added to the reaction product diesel oil for ultrasonic vibration extraction. After standing for 15-30 minutes, the collected Diesel layer, to obtain finished low-sulfur diesel oil. The whole process can effectively remove benzothiophene, dibenzothiophene and their derivatives in diesel oil. Using environmentally friendly oxygen as an oxidant can effectively reduce costs, but the processed object is still diesel oil It is impossible to reduce the sulfur content of heavy oil; the patent CN101612595 utilizes subcritical and supercritical hydrothermal synthesis reaction and the strong penetration of subcritical and supercritical water to prepare The medium-temperature desulfurizer with high desulfurization precision, good cycle stability and high mechanical strength can be applied to the removal of hydrogen sulfide in medium-temperature coal gas or natural gas, but it still does not involve the removal of sulfur-containing compounds in heavy oil products; CN101077980A discloses A method for preparing light oil by modifying vacuum residue oil with supercritical water, adding vacuum residue oil and water into an autoclave, stabilizing for 18-60 minutes at a pressure of 20-35MPa and a temperature of 380-460°C, and then cooling to obtain 60-87% light oil, the attachments in the kettle can be washed and recovered by using n-heptane, n-hexane, toluene or tetrahydrofuran as a solvent. This method has the effects of desulfurization, denitrogenation and demetallization while lightening heavy oil However, the steps of this method are complicated, and the washing liquid needs to be recovered by rotary evaporation after solvent washing, and the conditions are harsh, and the temperature and pressure are relatively high.

Method used

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  • Process for reducing sulfur content of vacuum residuum
  • Process for reducing sulfur content of vacuum residuum
  • Process for reducing sulfur content of vacuum residuum

Examples

Experimental program
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Effect test

Embodiment 1

[0022] Take by weighing 50g vacuum residue and 50g methanol, take the sulfur element quality in the vacuum residue as a benchmark, weigh the oxidant benzaldehyde with 200% oxygen element content and 5% catalyst cobalt oxide and add them in methanol as extracting solution, respectively Add the vacuum residue and extract to the reaction kettle, raise the temperature and pressurize to 260°C and 8.5MPa under a nitrogen atmosphere, and fully stir to carry out the catalytic oxidation reaction for 3 hours. After the reaction, the reactor was left to stand at room temperature for 1 hour, and the upper extractant was separated to obtain a vacuum residue with low sulfur content; the sulfur content of the residue product was measured using a microcomputer coulometer, and the sulfur content of the product and the reaction The desulfurization rate is shown in Table 3.

Embodiment 2

[0024] Take by weighing 50g of vacuum residue and 50g of methanol, take the sulfur element quality in the vacuum residue as a benchmark, take by weighing oxidant terephthalaldehyde with 300% of oxygen element content and 5% of catalyst manganese oxide and add in methanol as extracting solution, The vacuum residue and the extract were added to the reactor respectively, and the temperature was raised to 270° C. and 8.5 MPa under a nitrogen atmosphere, and the catalytic oxidation reaction was carried out with sufficient stirring for 4 hours. After the reaction, the reactor was left to stand at room temperature for 1 hour, and the upper extractant was separated to obtain a vacuum residue with low sulfur content; the sulfur content of the residue product was measured using a microcomputer coulometer, and the sulfur content of the product and the reaction The desulfurization rate is shown in Table 3.

Embodiment 3

[0026] Take by weighing 50g of vacuum residue and 50g of acetonitrile, take the sulfur element quality in the vacuum residue as a benchmark, weigh the oxidant cumene peroxide and 5% of the catalyst sodium tungstate with an oxygen element content of 400% and add it in acetonitrile as For the extract, add the vacuum residue and the extract respectively into the reactor, raise the temperature and pressurize to 280°C and 5.5MPa under a nitrogen atmosphere, and fully stir to carry out the catalytic oxidation reaction for 5 hours. After the reaction, the reactor was left to stand at room temperature for 1 hour, and the upper extractant was separated to obtain a vacuum residue with low sulfur content; the sulfur content of the residue product was measured using a microcomputer coulometer, and the sulfur content of the product and the reaction The desulfurization rate is shown in Table 3.

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Abstract

The invention belongs to the technical field of petrochemical engineering, and particularly relates to a method for reducing the sulfur content of vacuum residuum. The method comprises the following steps: mixing vacuum residuum, an oxidizing agent, a catalyst and an extracting agent, heating and pressurizing in a nitrogen atmosphere to enable the extracting agent to enter a supercritical state, carrying out catalytic oxidation reaction on the vacuum residuum in the supercritical state, performing standing for layering after the reaction is finished, and separating the extracting agent to obtain the vacuum residuum of which the sulfur content is reduced to be less than 2.0%. According to the method for reducing the sulfur content of the vacuum residuum, the whole operation process is carried out under a non-hydrogen condition, so that the requirements on devices and raw materials are reduced; the sulfur content of the obtained vacuum residuum is reduced, and the vacuum residuum can beused as a raw material for producing low-sulfur petroleum coke and other products meeting requirements; by improving the product quality of the inferior raw oil, namely the vacuum residuum, the processing amount, the operation rate and the economic benefit of the delayed coking device can be improved.

Description

technical field [0001] The invention belongs to the technical field of petrochemical industry, and in particular relates to a method for reducing the sulfur content of vacuum residue. Background technique [0002] With the decrease of conventional oil resources, the inferior and heavy crude oil has become a global trend. The production proportion of crude oil with high sulfur content, high density and high metal content is getting higher and higher. The deep processing of heavy oil has become the world's oil refining industry. common problems faced. Delayed coking process, as an important decarbonization process of residual oil, uses heavy oil such as vacuum residual oil as raw material, and is rapidly heated to about 500°C in a heating furnace, so that it is delayed into the coke tower for cracking and condensation reactions. Production of oil, gas, coke and other products has the advantages of low cost, high conversion rate (70% to 75%), and high return on investment. Un...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G53/14C10G27/12C10G27/00
CPCC10G53/14C10G27/12C10G27/00C10G2300/202C10G2300/1077C10G2300/70Y02P20/54
Inventor 许金山陈辉曹发海许晓斌许军
Owner CHINA PETROLEUM & CHEM CORP