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C8 aromatic isomerization-separation coupling reaction method

A kind of aromatic hydrocarbon isomerization and coupling reaction technology, applied in the field of alkyl aromatic hydrocarbon isomerization, can solve problems such as xylene loss, and achieve the effect of good adsorption isomerization reaction performance

Active Publication Date: 2016-12-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method results in the loss of xylene in the isomerization reaction due to the occurrence of non-target acid-catalyzed transalkylation reactions and cyclocracking reactions

Method used

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  • C8 aromatic isomerization-separation coupling reaction method
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  • C8 aromatic isomerization-separation coupling reaction method

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preparation example Construction

[0032] The preparation method of the phosphorus-modified molecular sieve of the present invention comprises: impregnating the hydrogen-type molecular sieve with a phosphorus-containing compound solution dissolved in water. The impregnation pressure is preferably 0.1-1.0 MPa, the impregnation temperature is preferably 75-180°C, the liquid / solid volume ratio of the impregnation liquid to the molecular sieve is 0.7-3.0, and the impregnation time is preferably 5-24 hours. The solid obtained after impregnation is dried and calcined to obtain phosphorus-modified molecular sieves. The phosphorus-containing compound used for impregnation is selected from one or more of ammonium phosphate, diammonium hydrogen phosphate, ammonium dihydrogen phosphate, aluminum phosphate, phosphoric anhydride, phosphorous acid, ammonium phosphite and phosphoric acid.

[0033] In the preparation method of the phosphorus and magnesium composite modified molecular sieve, the molecular sieve is preferably fi...

example 1

[0049] The following example prepares the phosphorus modified catalyst of the present invention.

[0050] Prepare 500ml with P 2 o 5 Add 450 grams of HZSM-5 molecular sieve with a silicon oxide / alumina molar ratio of 80 and a crystallinity of 85% to an aqueous solution of ammonium dihydrogen phosphate with a calculated phosphorus content of 5% by mass, and impregnate it at 120°C and 0.5MPa After 20 hours, the filtered solid was dried at 120°C for 8 hours, and calcined at 550°C for 5 hours in an air atmosphere to obtain P 2 o 5 HZSM-5 molecular sieve Z-1 with a content of 4.5% by mass.

[0051] Mix the above-mentioned phosphorus-modified molecular sieve Z-1 with alumina at a mass ratio of 85:15, add 4 mass% nitric acid aqueous solution at a solid / liquid mass ratio of 3:1, knead, extrude, and dry at 120°C After 6 hours, it was pelletized and calcined at 550°C for 6 hours to obtain catalyst A-1.

example 2

[0053] Prepare the phosphorus-modified HZSM-5 molecular sieve according to the method of example 1, the difference is that in the ammonium dihydrogen phosphate aqueous solution used, P 2 o 5 The calculated phosphorus content is 14% by mass, and P 2 o 5 HZSM-5 molecular sieve Z-2 with a content of 13.5% by mass.

[0054] Molecular sieve Z-2 was mixed with alumina at a mass ratio of 90:10, and then kneaded, extruded, dried and calcined according to the method of Example 1 to obtain catalyst A-2.

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Abstract

The invention relates to a C8 aromatic isomerization-separation coupling reaction method. The method comprises the following steps of enabling gaseous C8 arene to be led into an isomerization catalyst bed, performing an aromatic isomerization reaction under the condition of 170-400 DEG C and 0.2-2.0MPa, and then desorbing reaction materials, wherein the isomerization catalyst comprises 25-98% by mass of a modified hydrogen type molecular sieve and 2-75% by mass of aluminum oxide, the modified hydrogen type molecular sieve is a hydrogen type molecular sieve modified with phosphorus or phosphorus and magnesium, the content of the phosphorus (in terms of phosphorus pentoxide) in the modified molecular sieve is 0.5-20% by mass, the content of magnesium (in terms of magnesium oxide) in the modified molecular sieve is 0.1-10 % by mass, and the molecular sieve is selected from at least one of MFI, MEL, EUO, FER, MFS, MTT, NES and TON structural molecular sieves. According to the method, the isomerization reaction is coupled with separation, so that paraxylene of which the PX content exceeds a thermodynamic equilibrium value can be obtained.

Description

technical field [0001] The present invention relates to a kind of alkyl aromatic hydrocarbon isomerization method, specifically, a kind of C 8 Aromatics isomerization-separation coupling reaction method. Background technique [0002] C 8 Aromatics usually come from catalytic reforming, steam cracking and toluene disproportionation units, among which p-xylene (PX) is an important chemical raw material, mainly used to produce purified terephthalic acid (PTA), dimethyl terephthalate ( DMT), but also raw materials for the production of paints, dyes, pesticides and pharmaceuticals. px in various sources of C 8 The content of aromatics generally does not exceed 25%. In order to meet the growing demand, industrially use simulated moving bed adsorption separation or crystallization technology to separate mixed C 8 PX and OX in aromatics can be separated by rectification, and the remaining stream is converted into mixed C with PX content close to or reaching the thermodynamic equ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C5/27C07C15/08C07C7/12B01J29/40B01J29/44B01J29/70
CPCY02P20/52
Inventor 苑志伟刘宇兴王德华郁灼王辉国
Owner CHINA PETROLEUM & CHEM CORP