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Diesel distillate hydrogenation method

A hydrogenation treatment and diesel oil technology, applied in the direction of hydrogenation treatment process, hydrocarbon oil treatment, chemical instruments and methods, etc., to achieve the effect of reducing processing cost, good effect and obvious effect

Active Publication Date: 2014-01-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the prior art, only emphasis is placed on the type and content of metals and the coordination and cooperation between different metals. How to make the catalyst have a reasonable pore structure and a high content of active metal components to fully play its role, and the catalyst has more Good hydrogenation activity and other aspects are not involved

Method used

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  • Diesel distillate hydrogenation method
  • Diesel distillate hydrogenation method
  • Diesel distillate hydrogenation method

Examples

Experimental program
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Effect test

Embodiment 1

[0033] Add 1000mL of water into the dissolution tank, add 40g of nickel chloride and 34g of ammonium metatungstate to dissolve, and add the solubility to 10.9g / cm -3 495 milliliters of aluminum chloride solution, preparation acid working solution A, the pH value of solution A is 1.8, gets 160g ammonium bicarbonate and is made into the aqueous solution that molar concentration is 2.5mol / l. Add 350mL of water into the reaction tank, and the temperature rises to 70°C. Under the situation of stirring, solution A, ammonium bicarbonate aqueous solution, and concentration are 18% (weight) ammonia water and flow into the reaction tank in parallel to form a gel. The gelation temperature is 70° C., and the gelation time is 0.5 hour. The value is 8.5. Aging for 1 hour after gel forming. Then filter, add 600ml of clean water and 6.3g of molybdenum trioxide to the filter cake, beat and stir evenly, filter, dry the filter cake at 80°C for 5 hours, then extrude it, wash it with clean water...

Embodiment 2

[0035] According to the method of Example 1, according to the component content ratio of catalyst B in Table 1, add aluminum chloride, nickel chloride, ammonium metatungstate and zirconium oxychloride to prepare acidic working solution A in the dissolution tank, take 100g Ammonium bicarbonate is made into a solution with a molar concentration of 2.0 mol / l. Add 350mL of water into the reaction tank, and the temperature rises to 55°C. Under the situation of stirring, solution A, ammonium bicarbonate aqueous solution and concentration are 10% (weight) ammonia water and flow into the reaction tank to form gel, the gel forming temperature is 55 ℃, the gel forming time is 2 hours, the pH The value is 8.0. Aging for 2 hours after gel forming. Then filter, wash the filter cake twice with 500mL of clean water, add clean water and molybdenum trioxide, beat and stir evenly, filter, dry the filter cake at 70°C for 7 hours, then extrude it, wash it twice with clean water, wet the bar It...

Embodiment 3

[0037] According to the method of Example 1, according to the component content ratio of catalyst C in Table 1, nickel nitrate, phosphoric acid, aluminum nitrate, ammonium metatungstate are added to the dissolution tank to prepare acidic working solution A, and 120g of ammonium oxalate is taken to make mole A solution with a concentration of 1.8 mol / l. Add 350mL of water into the reaction tank, and the temperature rises to 60°C. In the case of stirring, solution A, ammonium oxalate aqueous solution and ammonia water with a concentration of 15% (weight) are added into the reaction tank to form gels. The gelation temperature is 60°C, and the gelation time is 2 hours. 8.5, then add molybdenum trioxide, beating and stirring evenly, filter, and dry the filter cake at 120°C for 1 hour, then extrude into a strip, dry the wet strip at 130°C for 3 hours, and roast at 600°C for 3 hours to obtain the final catalyst C. The composition and main properties are shown in Table 1, and the por...

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Abstract

The invention discloses a diesel distillate hydrogenation method, which is to distil a diesel raw material into a light distillate and a heavy distillate, wherein the light distillate enters a first reaction area to be refined by hydrogenation by using the conventional method; the heavy distillate enters a second reaction area, and all or part of the heavy distillate is treated in the presence of a bulk-phase process hydrogenation refining catalyst; and the catalyst has a reasonable porous structure and realizes a high active metal utilization rate and is more favorable for removing substituted complex sulfides such as dibenzothiophene and saturated aromatic hydrocarbons. Compared with the prior art, a diesel super deep desulfuration effect can be realized without increasing hydrogenation severity, and thus, processing cost is reduced considerably.

Description

technical field [0001] The invention relates to a method for hydrogenation treatment of diesel fractions, in particular to a method for ultra-deep hydrogenation desulfurization of high-sulfur low-quality diesel oil. Background technique [0002] Since the combustion of sulfur compounds in fuels will cause serious harm to the world's environment and society, the standards for clean fuels formulated by countries around the world have greatly increased the restrictions on sulfur content. The U.S. Environmental Protection Agency has lowered the diesel sulfur content standard to 15ppm in June 2006. On the other hand, with the shrinking of the heavy oil market, the degree of deep conversion of heavy residue oil continues to increase, resulting in a decline in the quality of secondary processed products such as catalytic diesel (LCO), and it is difficult to find a new process for reducing the sulfur content of diesel . [0003] At present, the common method of processing diesel o...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G65/16C10G49/04B01J23/888B01J37/00B01J35/10
Inventor 王海涛徐学军刘东香冯小萍王继锋
Owner CHINA PETROLEUM & CHEM CORP