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Cycloalkyl secondary processing gasoline and diesel hydrogenation method

A technology for secondary processing, naphthenic crude oil, applied in hydrotreating process, petroleum industry, treatment of hydrocarbon oil, etc., can solve the problem of difficulty in obtaining high-quality light products, single hydrogenation products, low cetane number, etc. problem, to achieve the effect of low total investment and operating cost of the device, increase dry point, and increase cetane number

Active Publication Date: 2012-06-27
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The above process is conducive to improving the cetane number of diesel products, but has the following defects: (1) coked gasoline needs other hydrogenation units to process; (2) the cetane number of naphthenic coked diesel oil is low, only by adding Hydrofining reaction has a limited range to increase the cetane number; (3) Using conventional refining catalysts, the activity of hydrodesulfurization, hydrodenitrogenation, aromatics saturation, etc. is limited; (4) The flexibility is small, and the hydrogenation product is single
If the usual hydrogenation technology is used, it is difficult to obtain high-quality light products

Method used

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  • Cycloalkyl secondary processing gasoline and diesel hydrogenation method
  • Cycloalkyl secondary processing gasoline and diesel hydrogenation method
  • Cycloalkyl secondary processing gasoline and diesel hydrogenation method

Examples

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preparation example Construction

[0031] The preparation process of bulk catalyst of the present invention comprises the following contents: (1) co-precipitation method generates Ni x W y o z Complex oxide precursors; (2) Ni x W y o z Complex oxide precursors and MoO 3 Beating and mixing, filtering; (3) forming and activating the final catalyst.

[0032] Wherein (1) described coprecipitation method generates Ni x W y o z The process of the precursor of the composite oxide can adopt the following method: add the salt solution containing tungsten and nickel into the glue tank according to the required ratio of the catalyst composition, and add the precipitant to make the gel mixture. The precipitating agent can be an inorganic or organic basic ammonia compound, preferably ammonia, and any concentration of ammonia water can be used.

[0033] The required catalyst aids and additional components can be added in one or more of the above steps. Auxiliaries generally include one or more of P, F, Ti, Si, B, Z...

Embodiment 1

[0045] Add 1000mL of water into the reaction tank, then add 40g of nickel chloride to dissolve, then add 52g of ammonium metatungstate to dissolve, then add 5g of zirconium oxychloride to dissolve, then add 10% ammonia water to form a gel until the pH value is 8, and then gel The temperature is 50°C, aging for 1 hour after forming the gel, and then filtering, adding 600ml of clean water, 16g of molybdenum trioxide and 32g of aluminum hydroxide to the filter cake, beating and stirring evenly, filtering, drying the filter cake at 80°C for 5 hours, and then extruding Molded, washed 3 times with clean water, dried at 120°C for 5 hours, and calcined at 500°C for 4 hours to obtain the final catalyst A. The composition and main properties are shown in Table 1.

Embodiment 2

[0047] According to the method of Example 1, according to the component content ratio of catalyst B in Table 1, add aluminum chloride, nickel chloride, sodium tungstate in the reaction tank, then add 16% ammonia water to form a gel, until the pH value is 9 , the gelling temperature is 80°C, aging for 3 hours after gelling, then filtering, washing the filter cake twice with 500mL clean water, adding clean water and molybdenum trioxide, beating and stirring evenly, filtering, and drying the filter cake at 70°C for 7 hours , and then extruded, washed twice with clean water, dried at 100°C for 8 hours, and calcined at 550°C for 3 hours to obtain the final catalyst B. The composition and main properties are shown in Table 1.

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Abstract

The invention discloses a hydrogenation technique for secondarily processing gasoline and diesel oil through naphthenic base. Naphthenic base coking diesel oil and catalytic diesel oil with low cetane value are mixed and then enter into the first reactor of a hydrotreatment device for carrying out hydrogenation-modifying reaction; the generating oil of the first reactor is mixed with the coking gasoline through a heat exchange facility and then enters the second reactor of the hydrotreatment device for carrying out deep hydrogenation-refining reaction; gas-liquid separation is carried out on the matter flows obtained hydrogenation refining; the gas obtained through separation circulates to a reaction part; the liquid phase product obtained through separation enters a fractionating tower through a stripping tower, thus respectively obtaining qualified hydrogenated naphtha, hydrogenated coal oil and hydrogenated diesel oil. In the invention, deep hydrogenation is carried out for obtaining secondarily processed gasoline and diesel oil of poor quality. The economic benefits of oil refinery enterprises can be remarkably improved.

Description

technical field [0001] The invention belongs to the hydroprocessing technology. Specifically, it is a combined process technology of hydrogenation upgrading and hydrofinishing of gasoline, kerosene, and diesel fractions. Background technique [0002] At present, the crude oil processed by refineries tends to become heavier and inferior, and with the development of the economy, the demand for light distillate oil, especially clean light distillate oil, is gradually increasing, all of which require the existing Refining technology is perfected and improved to produce products that meet the requirements at the lowest cost. How to make full use of existing hydrogenation units to produce high-quality, high-priced products and improve economic benefits is an important issue facing oil refiners. [0003] Catalytic cracking is an important means of lightening heavy distillate oil. However, catalytic cracking diesel oil has high sulfur and nitrogen content, poor stability, and low ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G65/04
Inventor 王震关明华刘继华李扬
Owner CHINA PETROLEUM & CHEM CORP
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