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Deep hydrodesulphurization and dearomatization method for fraction oil

A technology for deep hydrogenation and hydrodearomatization, which is used in chemical instruments and methods, hydrotreating processes, and hydrocarbon oil treatment to achieve the effect of reducing the amount of active metals, increasing the pore size and pore volume, and being easy to contact.

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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  • Deep hydrodesulphurization and dearomatization method for fraction oil
  • Deep hydrodesulphurization and dearomatization method for fraction oil

Examples

Experimental program
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Effect test

Embodiment 1

[0028] 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

[0030] 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

[0032] 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 deep hydrodesulphurization and dearomatization method for fraction oil. A two-section hydrogenation process is adopted in the method, wherein a non-noble metal hydrofining catalyst is adopted in a first hydrogenation reactor, and a special bulk phase hydro-dearomatization catalyst is adopted in a second hydrogenation reactor. The bulk phase hydro-dearomatization catalyst is a non-noble metal catalyst, and has a proper pore structure; the utilization rate of active metals is high; and the method reduces the preparation cost of the catalyst, has strong raw material adaptability, is favorable for reaction of macromolecular compounds, and particularly has good dearomatization and deep desulphurization effects.

Description

technical field [0001] The invention relates to a method for hydrogenation treatment of distillate oil, in particular to a method for removing sulfur-containing compounds and aromatics in distillate oil by two-stage hydrogenation treatment. Background technique [0002] In order to solve the global environmental protection problem, the problem of engine gas emission must be solved, and the development of low-sulfur, low-aromatic diesel production technology is one of the main research topics of clean fuel production in the 21st century. In recent years, countries around the world have successively revised diesel oil standards, putting forward stricter requirements on indicators related to environmental pollution such as sulfur content, aromatic content, cetane number and density in diesel oil. The content of aromatic compounds directly determines the properties of diesel oil such as density and cetane number, so its removal has attracted great attention. [0003] At present...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G65/08B01J27/19B01J23/888B01J35/10
Inventor 王海涛徐学军冯小萍刘东香王继锋
Owner CHINA PETROLEUM & CHEM CORP