Toluene and methanol shape-selective alkylation catalyst and method thereof

An alkylation and catalyst technology, applied in the field of toluene and methanol shape-selective alkylation catalysts, can solve problems such as poor catalyst reaction stability, and achieve the effects of improving reaction stability, high activity and high selectivity

Inactive Publication Date: 2014-10-15
SHANGHAI HUAYI GRP CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] One of the technical problems to be solved by the present invention is the problem of poor catalyst reaction stability in the prior art, and a new catalyst for toluene and methanol shape-selective alkylation is provided

Method used

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  • Toluene and methanol shape-selective alkylation catalyst and method thereof
  • Toluene and methanol shape-selective alkylation catalyst and method thereof
  • Toluene and methanol shape-selective alkylation catalyst and method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] Using SiO 2 / Al 2 o 3 The molar ratio is 80g of 20MCM-22 molecular sieve and 20g of γ-Al 2 o 3 Mix, then add 6.0g of Tianqing powder and mix evenly, then add 3wt% dilute nitric acid as a binder, knead well and evenly, carry out extrusion molding, after drying at 120°C, roast at 540°C to obtain a shaped molecular sieve, which is recorded as MCM-22; The formed 50g MCM-22 molecular sieve is pre-vacuumized, impregnated with an equal volume of ammonium dihydrogen phosphate aqueous solution for 24 hours, dried at 120°C for 24 hours, and then roasted at 550°C for 4 hours, using a temperature program with a heating rate of 2°C / min, to obtain a catalyst loaded with phosphorus oxide; then impregnate it in a vacuum equal volume in an aqueous solution of lanthanum nitrate solution, dry at 120° C., and then roast at 540° C. for 4 hours. The solution was impregnated in equal volume for 24 hours, dried at 120°C, and then calcined at 540°C. The catalyst finally obtained contained ...

Embodiment 2

[0042] Using SiO 2 / Al 2 o 3 The molar ratio is 20MCM-22 molecular sieve 40g, silica sol (SiO 2 , 30%) 59g, γ-Al 2 o 3 Mix 19g and 5g of methyl cellulose evenly, extrude, dry at 120°C, and roast at 550°C to obtain a shaped molecular sieve, which is denoted as MCM-22; pre-vacuumize 50g of the formed MCM-22 molecular sieve, and use molybdic acid Immerse in an equal volume of ammonium aqueous solution for 24 hours, dry at 120°C for 24 hours, then roast at 550°C for 4 hours, use a temperature program at a rate of 2°C / min to obtain a solid that is impregnated with an equal volume of magnesium nitrate aqueous solution for 24 hours. Dry at 120°C for 24 hours, then calcinate at 550°C for 4 hours, use a temperature program at a rate of 2°C / min to obtain a catalyst loaded with molybdenum oxide and magnesium oxide; The petroleum ether solution of silicone oil is impregnated, and after impregnation, it is left to stand until the solvent is completely volatilized. After drying, it is ...

Embodiment 3

[0044] Using SiO 2 / Al 2 o 3 The molar ratio is 80g of 20MCM-22 molecular sieve and 20g of γ-Al 2 o 3 Mix, then add 5g of Tianqing powder and mix evenly, then add 3wt% dilute nitric acid as a binder and knead evenly, carry out extrusion molding, after drying at 120°C, roast at 540°C to obtain a molded molecular sieve, which is recorded as MCM-22; for 10g The formed MCM-22 molecular sieve is pre-vacuumized, vacuum-impregnated with the prepared aqueous solution of cobalt nitrate and ammonium molybdate, filtered off the excess solution, dried at 80°C for 24 hours, and then roasted at 540°C for 4 hours. Using a temperature program with a heating rate of 3°C / min, a catalyst loaded with cobalt oxide and molybdenum oxide was obtained; then pre-vacuumized, vacuum impregnated with an aqueous solution of magnesium nitrate and cerium nitrate, filtered off the excess solution, and dried at 80°C for 24 hours, then roasted at 540°C for 4 hours, using a temperature program, with a heatin...

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Abstract

The invention relates to a toluene and methanol shape-selective alkylation catalyst and a method thereof to mainly solve the problem of poor catalyst reaction stability in the prior art. The catalyst comprises the following components by weight: a) 40-90 parts of silicon-aluminum zeolite with a SiO2/Al2O3 mole ratio of greater than or equal to 20; b) 0.1-5.0 parts of a hydrogenation assistant; c) 0-10 parts of a nonmetallic oxide; d) 1.0-30 parts of at least one of rare earth metal oxides or alkali earth metal oxides; and e) 10-60 parts of aluminium oxide or a mixture of silicon dioxide and aluminium oxide. The technical scheme adopted by the invention well solves the problem, and the catalyst can be used in industrial production for synthesis of p-xylene through toluene and methanol shape-selective alkylation.

Description

technical field [0001] The invention relates to a catalyst for shape-selective alkylation of toluene and methanol and a method thereof. Background technique [0002] As the most important raw material for the synthesis of terephthalic acid and dimethyl terephthalate, the demand for xylene has been continuously increasing, and at present its main industrial production methods - xylene isomerization separation and toluene shape-selective disproportionation, There are the problems of low yield of xylene and low utilization rate of raw materials respectively. The synthesis of xylene from toluene and methanol through molecular sieve-catalyzed alkylation has always been considered as a production method that can replace the above two traditional processes, but the problem of poor reaction stability limits its large-scale industrialization. [0003] The document US7060864 discloses that the introduction of water during the alkylation reaction of toluene and methanol can effectivel...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/74B01J29/78B01J29/68B01J29/80C07C15/08C07C2/88
CPCB01J23/10B01J29/46B01J29/7088B01J29/7676B01J37/0009B01J37/28C07C2/864C07C2529/70C07C2529/74C07C2529/76C07C2529/78Y02P20/52C07C15/08
Inventor 唐建远朱志荣宁春利张春雷唐勇邢海军娄报华
Owner SHANGHAI HUAYI GRP CO
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