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Kaolinic heavy aromatic hydrocarbon transalkylation catalyst preparation method

A kind of heavy aromatic hydrocarbon alkyl, catalyst technology, applied in the field of catalysis

Active Publication Date: 2015-03-18
CHINA NAT OFFSHORE OIL CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For a long time, C 9 + (C 9 The comprehensive utilization of aromatics has always been a problem of common concern to scholars at home and abroad but has not been well resolved

Method used

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  • Kaolinic heavy aromatic hydrocarbon transalkylation catalyst preparation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0065] Take 600g (dry basis) particles of 200-mesh attapulgite clay, add it to 1200g of sulfuric acid solution with a concentration of 15%, and treat it for 4 hours at 60°C, filter, wash, and dry to obtain transcrystalline activated clay , add 13.76g safflower powder and mix with mass percent concentration and be 30% sodium hydroxide aqueous solution as peptizer, rolling molding makes in the formed bead that particle diameter is that the bead content of 0.30~0.50 millimeter is 25 (mass) %, The content of pellets with a particle diameter of 0.50-0.70 mm is 60 (mass)%, the content of pellets with a particle diameter of 0.70-1.00 mm is 12 mass%, and the content of pellets with a particle diameter greater than 1 mm is 3 (mass)%. Dry at 120°C for 12 hours, bake at 550°C for 2 hours (the same below), and detect the chemical composition by X-ray fluorescence diffraction, in which the content of silicon oxide is 69.03%, the content of aluminum oxide is 17.68%, the content of magnesium ...

Embodiment 2

[0067]All reaction raw materials are the same as example 1, and wherein acid treatment condition is to get 600g attapulgite, join in the concentration of 1200g and be in the sulfuric acid solution of 10%, under 60 ℃ of conditions, process 6 hours, obtain conversion after filtering, washing, drying Crystal activated clay, add 14.12g sodium carboxymethyl cellulose and mix well, use 30% sodium hydroxide aqueous solution as the peptizer, roll it into small balls of different sizes and ratios on a rolling ball machine, and dry at 120°C for 12h , Roasted at 650°C for 2 hours, and the chemical composition was detected by X-ray fluorescence diffraction. The content of silicon oxide was 68.44%, the content of aluminum oxide was 17.35%, the content of magnesium oxide was 1.93%, and the content of iron oxide was 1.27%. Under stirring conditions, put 700ml of sodium silicate, 200ml of lye, 87ml of directing agent, 150ml of deionized water and 500g of activated attapulgite microspheres into...

Embodiment 3

[0069] All reaction raw materials are the same as Example 1, wherein the acid treatment condition is to get 600g attapulgite, join in 1800g concentration and be in the sulfuric acid solution of 10%, under 70 ℃ of conditions, process 6 hours, after filtering, washing, drying, obtain transcrystal Activated clay, add 14.48g of celadon powder and mix well, use 20% sodium hydroxide aqueous solution as the peptizer, roll it into small balls of different sizes and proportions on a rolling ball machine, dry at 120°C for 12h, and roast at 550°C for 2h , using X-ray fluorescence diffraction to detect the chemical composition, wherein the silicon oxide content is 68.16%, the aluminum oxide content is 17.22%, the magnesium oxide content is 2.02%, and the iron oxide content is 1.35%. Under the condition of stirring, put 750ml of sodium silicate, 240ml of lye, 105ml of directing agent, 200ml of deionized water and 500g of activated attapulgite microspheres into a 2L stainless steel reaction ...

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Abstract

The invention provides a kaolinic heavy aromatic hydrocarbon transalkylation catalyst preparation method, which is characterized by comprising: adopting nature porous clay as a raw material, carrying out a sulfuric acid treatment to obtain white clay having crystal transition activity, uniformly mixing the crystal transition activity white clay, a dispersant, an auxiliary extruding agent and a peptizing agent, carrying out extrusion molding on a strip extruding machine or carrying out rolling molding on a bowl machine, carrying out drying and calcination on the molded body, carrying out in situ crystallization in the presence of sodium silicate, sodium hydroxide, deionized water, a directing agent and the like to obtain a crystallization product with a NaY zeolite mass percentage of 50-70%, a mole ratio of silicon to aluminum of 4.5-5.8, and a grain size of 0.2-0.6 mum, and carrying out two ion exchange modification treatments and one baking treatment on the crystallization product to obtain the kaolinic heavy aromatic hydrocarbon transalkylation catalyst with characteristics of low production cost, high catalysis activity and high selectivity.

Description

technical field [0001] The present invention relates to the technical field of catalysis, and relates to a preparation method of a heavy aromatic hydrocarbon transalkylation catalyst, which is a preparation method of an all-clay type heavy aromatic hydrocarbon transalkylation catalyst, more specifically, a preparation method using natural porous clay as a raw material. A method for all-clay type heavy aromatics transalkylation catalysts. Background technique [0002] Heavy aromatics generally refer to the C contained in catalytic reforming, disproportionation and isomerization reactions to generate oil and ethylene cracking hydrogenated gasoline 9 ~C 16 mono- and bicycloalkylaromatics. With the continuous expansion of reforming units and ethylene cracking capacity, the output of heavy aromatics continued to increase. For a long time, C 9 + (C 9 The comprehensive utilization of aromatics has always been a problem of common concern to scholars at home and abroad but has ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/16C01B39/24C07C15/08B01J35/10C07C4/18
CPCY02P20/52
Inventor 邢淑建于海斌范景新臧甲忠聂枫姜雪丹马跃谦
Owner CHINA NAT OFFSHORE OIL CORP