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Production method of aromatic solvent oil and solvent oil selective hydrogenation catalyst

A technology for aromatic hydrocarbon solvent oil and hydrogenation catalyst, which can be applied to hydrocarbon oil treatment products, organic compound/hydride/coordination complex catalysts, physical/chemical process catalysts, etc., and can solve problems such as affecting the economics of hydrogenation industrial units. , to achieve the effect of active stability guarantee, increased specific surface area, excellent strength and hardness

Active Publication Date: 2021-02-02
NINGBO POLYTECHNIC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

If these high molecular compounds cannot be effectively removed or converted, it will seriously affect the economics of hydrogenation industrial units

Method used

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  • Production method of aromatic solvent oil and solvent oil selective hydrogenation catalyst
  • Production method of aromatic solvent oil and solvent oil selective hydrogenation catalyst

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Experimental program
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preparation example Construction

[0042] Preferably, the preparation method of the carrier includes: mixing alumina and fullerene, adding an extrusion aid, extruding into a strip, and then drying and calcining.

[0043] Further, the temperature of the drying treatment is 120-160°C.

[0044] Further, the temperature of the calcination treatment is 450-700° C., and the calcination time is 1-15 hours.

[0045] Preferably, the fullerene is used in an amount of 0.8-1.5 wt%, particularly preferably 1.0-1.5 wt%, of the total mass of the carrier.

[0046] Preferably, the fullerene solution is formed by dissolving fullerene in toluene.

[0047] In the catalyst of the present invention, before the fullerene in the carrier is mixed with alumina, it is first dissolved in toluene, the dissolution temperature used for the toluene dissolution is 20-40°C, the pressure is 0.10-0.25MPa, and the dissolution time 3-10 minutes; the mass ratio of toluene to fullerene used in the toluene dissolution is 200-350:1.

[0048] Further...

Embodiment 1

[0080] (1) Preparation of catalyst carrier:

[0081] a1. Dissolve 1.20 g of fullerene C60 powder with a purity of 99.5% in 400 g of toluene at a pressure of 0.25 MPa and 30° C. for 10 min to obtain a purple fullerene solution;

[0082] b1. Mix macroporous alumina (commercially available common macroporous alumina powder with a pore volume of 0.8 to 1.5ml / g) and small pore alumina (commercially available with a pore volume of 0.3 to 0.6ml / g) Ordinary small-pore alumina powder) is mixed and stirred according to the mass ratio of 1:1 as alumina raw material;

[0083] c1. Put the ultrasonic vibration introducing rod in the solution obtained in a1, the temperature is 30°C, and the ultrasonic power is 1000W;

[0084] d1. Take 99g of the alumina raw material mixed in step b1, add the fullerene solution in step c1, and mix thoroughly for 50 minutes, then add extrusion aids, such as citric acid, in an amount that satisfies the shape of the carrier, and then knead and roll Pressing and ...

Embodiment 2

[0093] (1) Preparation of catalyst carrier:

[0094] a1. Dissolve 1.40 g of fullerene C60 powder with a purity of 99.5% in 460 g of toluene at a pressure of 0.20 MPa and 40° C. for 3 minutes to obtain a purple fullerene solution;

[0095] b1, with embodiment 1;

[0096] c1. Put the ultrasonic vibration introducing rod in the solution obtained in a1, the temperature is 40°C, and the ultrasonic power is 500W;

[0097] d1. Take 99g of the alumina raw material mixed in step b1, add the fullerene solution in step c1, and mix thoroughly for 60 minutes, then add an extrusion aid, such as citric acid, in an amount that satisfies the shape of the carrier, then knead and roll Pressing and forming into strips;

[0098] e1 Dry the strip-shaped carrier extruded in step d1 at room temperature, then put it in an oven and bake it at 120°C for 4 hours, and then break it into about 2-3mm for later use;

[0099] fl. Put the dried bar in step e1 in a muffle furnace, and calcinate at 450° C. fo...

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Abstract

The invention discloses a production method of aromatic solvent oil and a solvent oil selective hydrogenation catalyst. The production method comprises the following steps: contacting an aromatic-richcomponent in aromatic hydrocarbon-containing components with a solvent oil selective hydrogenation catalyst, and carrying out a selective hydrofining reaction to obtain aromatic hydrocarbon solvent oil; the solvent oil selective hydrogenation catalyst comprises a metal active component and a carrier loaded with the metal active component, the carrier is mainly formed by mixing, extruding, molding, drying and roasting fullerene and aluminum oxide, and the metal active component comprises a metal oxide; the specific surface area of the catalyst is 280-350m < 2 > / g, the average pore diameter ofthe catalyst is 10-30nm, and pores with the diameter of 10-50nm account for 50-70%. The solvent oil selective hydrogenation catalyst provided by the invention has the advantages of good activity, highstrength, reasonable pore distribution, strong metal capacity and more uniform active component dispersion, also has good activity stability, and is suitable for production of aromatic hydrocarbon solvent oil.

Description

technical field [0001] The invention relates to a method for producing aromatic solvent oil and the field of preparation of a solvent oil selective hydrogenation catalyst used therefor, in particular to a selective hydrogenation catalyst used for C9 solvent oil hydrogenation treatment and a preparation method thereof. Background technique [0002] C9 distillate oil is a by-product of ethylene cracking units in the petrochemical industry, accounting for about 10wt% to 15wt% of the total ethylene production. Due to the large amount of alkenyl aromatics and dienes, the product is unstable and prone to rubber formation and discoloration. Therefore, it is mainly used as fuel oil for sale, or for the preparation of C9 petroleum resin, or for the separation of cyclopentadiene, or for the production of triphenyl, indane, and aromatic solvent oils. While producing C9 petroleum resin, a certain amount of high-boiling-point aromatic solvent oil will be co-produced. Molecular compounds...

Claims

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Application Information

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IPC IPC(8): B01J31/34B01J35/10C10G45/08
CPCB01J31/34C10G45/08C10G2400/18C10G2300/1096C10G2300/202B01J35/615B01J35/647Y02P20/52
Inventor 尹宏峰许杰
Owner NINGBO POLYTECHNIC