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A kind of preparation technology of hydrocracking catalyst

A cracking catalyst and hydrocracking technology, applied in physical/chemical process catalysts, molecular sieve catalysts, hydrocarbon oil cracking, etc., can solve problems such as unfavorable reforming units and reduce heavy naphtha aroma potential, so as to improve quality and reduce hydrogen consumption effect

Active Publication Date: 2018-06-15
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The hydrocracking process has different requirements for the hydrogenation of heavy naphtha and tail oil. The hydrogenation of heavy naphtha produced by cracking will reduce the aroma potential of heavy naphtha, which is unfavorable for reforming units.
The hydrogenation of the tail oil as ethylene material is beneficial to reduce the aromatics content in the tail oil, and to improve the yield and operation cycle of the ethylene plant. However, the existing hydrocracking catalysts do not solve the above problems well.

Method used

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  • A kind of preparation technology of hydrocracking catalyst
  • A kind of preparation technology of hydrocracking catalyst
  • A kind of preparation technology of hydrocracking catalyst

Examples

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Effect test

Embodiment 1

[0020] (1) Take Y molecular sieve with a dry basis weight of 150g and dry basis weight of 250g macroporous alumina, mix evenly, add 3g / 100ml dilute nitric acid 200ml, roll and extrude, then dry at 120°C for 4h, and roast at 550°C After 3 hours, the carrier was obtained, and the number was T-1; (2) Prepare W-Ni impregnation solution: take 241g of ammonium metatungstate and 240g of nickel nitrate and dissolve it in water to prepare 1000ml of impregnation solution. The active metal in the obtained impregnation solution is expressed as WO 3and NiO content are calculated as 20g / 100ml and 6g / 100ml respectively, coded as RY-1; take 300g of T-1 and soak in 600ml RY-1 for 2h, then take out the carrier at room temperature for 2h, dry at 100°C for 4h, and 500°C Roast for 3 hours to obtain a low metal content carrier, numbered CTL-1; (3) Take 300g of CTL-1 and place it in 600ml of n-heptane solvent for immersion for 2 hours, take it out and dry it at 110°C for 5 minutes to obtain CTL-2. T...

Embodiment 2

[0022] (1) Take Y molecular sieve with a dry basis weight of 200g and dry basis weight of 200g macroporous alumina and mix evenly, add 3g / 100ml dilute nitric acid 200ml for rolling and extrusion, then dry at 120°C for 4 hours, and roast at 550°C After 3 hours, the carrier was obtained, and the number was T-2; (2) Prepare W-Ni impregnation solution: take 241g of ammonium metatungstate and 240g of nickel nitrate and dissolve it in water to prepare 1000ml of impregnation solution. The active metal in the obtained impregnation solution is expressed as WO 3 and NiO content are calculated as 20g / 100ml and 6g / 100ml respectively, and the code is RY-3; take 300g of T-2 and soak it in 600ml RY-3 for 2h, then take out the carrier at room temperature for 2h, dry at 100°C for 4h, and 500°C Roast for 3 hours to obtain a low metal content carrier, numbered CTL-3; (3) Take 300g of CTL-3 and place it in 600ml petroleum ether solvent for immersion for 2 hours, take it out and dry it at 90°C for ...

Embodiment 3

[0024] (1) Take Y molecular sieve with a dry basis weight of 250g and dry basis weight of 150g macroporous alumina, mix evenly, add 3g / 100ml dilute nitric acid 200ml, roll and extrude, then dry at 120°C for 4h, and roast at 550°C After 3 hours, the carrier was obtained, and the number was T-3; (2) Prepare W-Ni impregnation solution: take 180g of ammonium metatungstate and 160g of nickel nitrate and dissolve it in water to prepare 1000ml of impregnation solution, and the active metal in the obtained impregnation solution is expressed as WO 3 The calculated NiO and NiO contents are 15g / 100ml and 4g / 100ml respectively, and the code is RY-5; take 300g of T-3 and soak it in 600ml RY-5 for 2h, then take out the carrier at room temperature for 2h, dry it at 100°C for 4h, and then dry it at 500°C Roast for 3 hours to obtain a low metal content carrier, numbered CTL-5; (3) Take 300g of CTL-5 and place it in 600ml of toluene solvent for immersion for 3 hours, take it out and dry it at 15...

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Abstract

The invention discloses a preparation technology of a hydrocracking catalyst, which includes the following contents: (1) the carrier material includes at least one acidic cracking material to prepare a hydrocracking catalyst carrier; (2) preparing an active metal salt solution, saturated impregnation step ( 1) The prepared hydrocracking catalyst carrier is then dried and calcined; (3) The calcined carrier obtained in step (2) is first supersaturated impregnated in a water-insoluble organic solvent and dried; (4) Preparation of active The metal salt solution is saturated with impregnating the dried carrier in step (3), and the finished product of hydrocracking catalyst is obtained after drying and roasting. The hydrocracking catalyst prepared by the method can selectively hydrogenate cracked products heavy naphtha and tail oil, which not only reduces the hydrogen consumption of the device, but also can simultaneously produce high-quality heavy naphtha and tail oil products.

Description

technical field [0001] The invention relates to a preparation technology of a hydrocracking catalyst, in particular to a preparation technology of a chemical type hydrocracking catalyst. Background technique [0002] As the quality of crude oil becomes heavier and worse year by year, environmental protection regulations become increasingly strict, and the market demand for clean oil products continues to grow, making hydrogenation technology for the production of clean fuels more and more widely used. In the secondary processing technology of crude oil, distillate oil hydrocracking technology has the characteristics of strong adaptability of raw materials, high flexibility of production operation and product plan, and good product quality. It can directly convert various heavy and low-quality raw materials into High-quality jet fuel, diesel, lubricating oil base materials, chemical naphtha and tail oil steam cracking ethylene raw materials, etc., play the role of product dis...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/16C10G47/20
Inventor 柳伟杜艳泽王凤来刘昶秦波张晓萍
Owner CHINA PETROLEUM & CHEM CORP