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ZSM-5 sieve material used for aromatic hydrocarbons alkylation reaction and preparation method thereof

A ZSM-5, aromatic hydrocarbon alkylation technology, applied in the direction of condensation between hydrocarbons and non-hydrocarbons to produce hydrocarbons, organic chemistry, borane silicone crystalline aluminum silicate zeolite, etc., can solve the stability of aromatic hydrocarbon alkylation reaction problems such as poor performance and low recovery rate of fine particle zeolite molecular sieves, to achieve the effect of improved catalyst stability, high recovery rate and good activity stability

Active Publication Date: 2013-01-23
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] One of the technical problems to be solved by the present invention is the low recovery rate of fine-grained zeolite molecular sieves in the prior art, and the problem of poor stability when used in aromatic hydrocarbon alkylation reactions. A new method for aromatic hydrocarbon alkylation is provided The ZSM-5 molecular sieve material of chemical reaction and its preparation method

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] Prepare the zeolite precursor in advance: take ethylamine as template agent, use silica sol (40% by weight aqueous solution) and sodium aluminate as silicon source and aluminum source respectively, according to Al 2 o 3 : 100SiO2 2 : 6CH 3 CH 2 NH 2 :80H 2 The mixture was prepared in a molar ratio of O, and the pH value of the system was adjusted to 12.5 with sodium hydroxide, and then hydrothermally reacted at 170° C. for 24 hours.

[0018] Water glass (containing 25.3% by weight SiO 2 ) and aluminum sulfate as silicon source and aluminum source, with tetrapropylammonium bromide (R) as template, with concentrated sulfuric acid to adjust the pH value of the system, according to 12Na 2 O:Al 2 o 3 : 120SiO2 2 : 13R 2 O: 650H 2 The crystallization mother liquor was prepared according to the molar ratio of O, and 5% by weight of zeolite precursor was added to the crystallization reaction mother liquor, and static crystallization was carried out at 180° C. for 48 ...

Embodiment 2

[0020] Prepare the zeolite precursor in advance: use n-butylamine as the template, use silicon powder and sodium aluminate as the source of silicon and aluminum respectively, according to Al 2 o 3 : 200 SiO 2 : 4CH 3 CH 2 CH 2 CH 2 NH 2 : 350H 2The mixture was prepared at a molar ratio of O, and the pH value of the system was adjusted to 12.5 with sodium hydroxide, and then hydrothermally reacted at 175° C. for 36 hours.

[0021] Respectively with silica sol (containing 40% by weight SiO 2 ) and aluminum nitrate as silicon source and aluminum source, with tetrapropyl ammonium hydroxide (R) as template, with sodium hydroxide to adjust the pH value of the system, according to 10Na 2 O:Al 2 o 3 : 180SiO 2 :3R 2 O: 400H 2 The molar ratio of O was used to prepare the crystallization mother liquor, and 6% by weight of zeolite precursor was added to the crystallization reaction mother liquor, and static crystallization was carried out at 160° C. for 36 hours. The XRD pa...

Embodiment 3

[0023] Prepare the zeolite precursor in advance: use tetrapropylammonium hydroxide as the template agent (R), use tetraethyl orthosilicate as the silicon source, and follow the 3SiO 2 : 2R 2 O: 50H 2 The mixture was prepared at a molar ratio of O, and the pH value of the system was adjusted to 12.5 with ammonia water, and then hydrothermally reacted at 120° C. for 12 hours.

[0024] Respectively with silica sol (containing 40% by weight SiO 2 ) and sodium aluminate as silicon source and aluminum source, with tetrapropylammonium bromide (R) as template, with sodium hydroxide to adjust the pH value of the system, according to 6Na 2 O:Al 2 o 3 : 260SiO2 2 : 12R 2 O: 360H 2 The crystallization mother liquor was prepared according to the molar ratio of O, 1% by weight of zeolite precursor was added to the crystallization reaction mother liquor, and static crystallization was carried out at 130° C. for 96 hours. The XRD pattern of the product shows that it has a ZSM-5 struct...

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Abstract

The invention relates to a ZSM-5 sieve material used for an aromatic hydrocarbons alkylation reaction and a preparation method thereof. The invention is mainly used to solve the problems in the prior art that the recovery rate of a fine grain zeolite molecular sieve is low and the stability of an original sieve material used for the aromatic hydrocarbons alkylation reaction is not ideal. According to the invention, the problems are well solved by the technical scheme of the ZSM-5 sieve material and its preparation method. The ZSM-5 sieve material is characterized in that the pore volume is larger than 30m<2> / g, the molar ratio of SiO2 and Al2O3 is between 15 to 800, the size of zeolite particles is between 200 to 2000nm, the sieve material is agglomerated from base nanometer zeolite particles having a size between 10 to 80nm, the diffraction peak (111), (501) and (151) suffer from severe attenuation and even disappear and a width phenomenon happens to the diffraction peak (011) and (051). The ZSM-5 sieve material can be applied to the industrial production of alkylation of aromatic hydrocarbons such as benzene and toluene.

Description

technical field [0001] The invention relates to a ZSM-5 molecular sieve material used for the alkylation reaction of aromatic hydrocarbons and a preparation method thereof. Background technique [0002] Paraxylene (PX) is an important chemical intermediate, which is widely used in the fields of polyester fiber, medicine, pesticide, dyestuff and solvent. Due to the increasing demand for PX, the direct extraction and separation of PX from reformed oil and pyrolysis gasoline is far from meeting the demand. The industrial production methods of p-xylene mainly include toluene and C 9 Aromatics disproportionation and transalkylation, mixed xylenes isomerization and toluene selective disproportionation. Therefore, maximizing the conversion of benzene and toluene into high value-added p-xylene required by the market has always been an important research direction in petrochemical technology. The shape-selective alkylation process of toluene or benzene and methanol produces little...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B39/38C07C15/08C07C2/86
Inventor 郑均林孔德金姜向东陈燕
Owner CHINA PETROLEUM & CHEM CORP