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c 9 + Process method for producing xylene from heavy aromatics

A technology for heavy aromatic hydrocarbons and process methods, which is applied in the production of bulk chemicals, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc. strictness etc.

Active Publication Date: 2022-07-08
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The technical problem to be solved by the present invention is that in the prior art, only heavy aromatics are lightened, resulting in the waste of side chain methyl groups or the need for fresh benzene or toluene in raw materials to participate in the defects of strict raw material composition requirements, and to provide a new C 9 + Process for producing xylenes from heavy aromatics, which has the advantage of using only C 9 + The advantages of producing BTX with heavy aromatics as the raw material of aromatics, and the advantages of flexible and adjustable target product types among benzene, toluene and xylene

Method used

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  • c  <sub>9</sub>  <sup>+</sup> Process method for producing xylene from heavy aromatics
  • c  <sub>9</sub>  <sup>+</sup> Process method for producing xylene from heavy aromatics
  • c  <sub>9</sub>  <sup>+</sup> Process method for producing xylene from heavy aromatics

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Experimental program
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Effect test

Embodiment 1

[0060] Vector preparation

[0061] will Na 2 O is less than 0.05% by weight, SiO 2 / Al 2 O 3 Ammonium ZSM-5 zeolite with a molecular ratio of 80, 66.7 g and Na 2 O less than 0.05 wt% γ-Al 2 O 3 ·H 2 O 57.1 g are uniformly mixed, then add 7 g of nitric acid aqueous solution with a concentration of 65-68 wt%, 2 g of succulent powder and 60-70 g of water, knead evenly, extrude into strips, dry at 120 ° C for 4 hours, and bake at 550 ° C in an air atmosphere After 3 hours, the pellets were cut to obtain a cylindrical carrier with a length of 2 mm and a diameter of 1.5 mm.

[0062]catalyst preparation

[0063] Take 50 grams of carrier, use 35 ml of ammonium molybdate aqueous solution (equivalent to containing MoO 3 1.6 g) impregnated carrier, dried at 120 °C for 4 hours, and calcined at 550 °C for 3 hours to obtain MoO 3 3.1w% catalyst.

[0064] Catalyst Evaluation

[0065] use figure 1 Shown in the technological process, the hydrodealkylation and transalkylation rea...

Embodiment 2

[0075] Vector preparation

[0076] will Na 2 O is less than 0.05% by weight, SiO 2 / Al 2 O 3 Ammonium ZSM-5 zeolite with a molecular ratio of 80, 66.7 g and Na 2 O less than 0.05 wt% γ-Al 2 O 3 ·H 2 O 57.1 g are uniformly mixed, then add 7 g of nitric acid aqueous solution with a concentration of 65-68 wt%, 2 g of succulent powder and 60-70 g of water, knead evenly, extrude into strips, dry at 120 ° C for 4 hours, and bake at 550 ° C in an air atmosphere After 3 hours, the pellets were cut to obtain a cylindrical carrier with a length of 2 mm and a diameter of 1.5 mm.

[0077] catalyst preparation

[0078] Take 50 grams of carrier, use 35 ml of ammonium molybdate aqueous solution (equivalent to containing MoO 3 1.6 g) impregnated carrier, dried at 120 °C for 4 hours, and calcined at 550 °C for 3 hours to obtain MoO 3 3.1w% catalyst.

[0079] Catalyst Evaluation

[0080] use figure 1 Shown in the technological process, the hydrodealkylation and transalkylation re...

Embodiment 3

[0090] Vector preparation

[0091] will Na 2 O is less than 0.05% by weight, SiO 2 / Al 2 O 3 Ammonium beta zeolite 66.7 grams with a molecular ratio of 25 and Na 2 O less than 0.05 wt% γ-Al 2 O 3 ·H 2 O 57.1 g are uniformly mixed, then add 7 g of nitric acid aqueous solution with a concentration of 65-68 wt%, 2 g of succulent powder and 60-70 g of water, knead evenly, extrude into strips, dry at 120 ° C for 4 hours, and bake at 550 ° C in an air atmosphere After 3 hours, the pellets were cut to obtain a cylindrical carrier with a length of 2 mm and a diameter of 1.5 mm.

[0092] catalyst preparation

[0093] 50 g of carrier was taken, impregnated with 35 ml of nickel nitrate aqueous solution (equivalent to 1.3 g of NiO), dried at 120°C for 4 hours, and calcined at 550°C for 3 hours to obtain a catalyst with a NiO content of 2.5w%.

[0094] Catalyst Evaluation

[0095] use figure 1 Shown in the technological process, the hydrodealkylation and transalkylation reactio...

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Abstract

C 9 + Process method for producing xylene from heavy aromatics, including: C 9 + The heavy aromatics are separated into low-boiling heavy aromatics and high-boiling heavy aromatics in the heavy aromatics separation tower; in the presence of hydrogen, the low-boiling heavy aromatics are treated with hydrodealkylation in the hydrodealkylation and transalkylation reaction units. Contact reaction with a transalkylation catalyst to obtain a stream containing benzene, toluene, xylene aromatics, non-aromatic hydrocarbons, unreacted heavy aromatics and hydrogen; containing benzene, toluene, xylene aromatics, nonaromatic hydrocarbons, unreacted heavy aromatics The streams of aromatics and hydrogen are successively separated into hydrogen, non-aromatic hydrocarbons, benzene, toluene, xylene aromatic products and unreacted products in the gas-liquid separator, stripper, benzene separation column, toluene separation column and xylene separation column. Heavy aromatics.

Description

technical field [0001] The present invention relates to C 9 + Process method for producing xylene from heavy aromatics. Background technique [0002] Benzene, toluene, xylene and C can be obtained during naphtha reforming and cracking 9 + Heavy aromatics, in recent years, due to the development of plastics, synthetic fibers and synthetic rubber industries, the demand for benzene and xylene has grown rapidly, and its market price is also much higher than other aromatics. In terms of price, usually two Toluene>benzene>toluene>C 9 + Heavy aromatics. Using low-value aromatic hydrocarbons to increase the production of higher-value aromatic hydrocarbons is an effective means to make full use of aromatic hydrocarbon resources. So far, there are many countries using toluene and C 9 + A lot of research work has been done on the production of xylene from heavy aromatics, and certain achievements have been achieved. [0003] Refinery catalytic reformer by-produces a ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C4/18C07C15/08B01J23/28B01J23/755B01J23/30
CPCC07C4/18B01J23/28B01J23/755B01J23/30C07C15/08Y02P20/52
Inventor 李华英李经球杨德琴孔德金
Owner CHINA PETROLEUM & CHEM CORP