Method for preparing alumina supporter with large pore volume

A technology of alumina carrier and large pore volume, applied in catalyst carriers, chemical instruments and methods, chemical/physical processes, etc. Hole volume, simple operation effect

Active Publication Date: 2013-01-09
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since the carbon black powder is added to the carrier by mechanical mixing when the carrier is formed, it is difficult to make the carbon black powder evenly distributed in the carrier by this mechanical mixing, resulting in the dispersion and non-concentration of the final carrier pore distribution and poor mechanical strength.
In addition, most of the pe

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

[0027] Weigh 100 g of pseudo-boehmite dry rubber powder (produced by Shenyang Catalyst Factory, with an alumina dry basis content of 65%), add 2 g of scallop powder and mix evenly, dissolve 3 g of gluconic acid and 1.5 g of ammonium hydrogen phosphate in 80 mL of distilled water, Mix the obtained solution with the above-mentioned materials evenly, extrude into clover-shaped strips with a diameter of 1.8mm on a screw extruder, dry at 120°C for 3 hours, and roast the dried molding at a temperature of 450°C for 2 hours, then Calcined at a temperature of 650° C. for 3 hours to obtain the alumina carrier B1 provided by the present invention.

example 2

[0029] Same as example 1, except that the addition of gluconic acid is 6g, the ammonium hydrogen phosphate is changed to the addition of ammonium phosphate and is 1.0g, the molding is roasted at a temperature of 500°C for 1.5 hours, and then fired at a temperature of 700°C for 2 hours to obtain this Alumina carrier B2 provided by the invention.

example 3

[0031] With example 1, just gluconic acid is changed into the mixed acid of gluconic acid and citric acid, and add-on is gluconic acid 5g and citric acid 3g, and ammonium hydrogen phosphate add-on is 0.8g, and molded thing roasts 1.5 hours at the temperature of 500 ℃, Then calcined at a temperature of 650° C. for 2.5 hours to obtain the alumina carrier B3 provided by the present invention.

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PUM

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Abstract

The invention discloses a method for preparing an alumina supporter with large pore volume. The method comprises the following steps: (1) weighing a certain amount of pseudoboehmite dry glue power and a certain amount of extrusion assistant agent to be evenly mixed and then adding an aqueous solution containing a peptizing agent and a chemical pore-enlarging agent; (2) evenly mixing materials obtained in the step (1) and extruding a mixture into strips; and (3) drying and calcinating the material obtained the step (2) to prepare the alumina supporter; wherein the peptizing agent in the step (1) is gluconic acid or mixed organic acid containing the gluconic acid. The using amount of the gluconic acid or the mixed organic acid containing the gluconic acid is 3%-10% by weight of pseudoboehmite dry glue power. The catalyst prepared by means of the preparation method is large in pore volume and pore diameter, concentrated in pore distribution and moderate in mechanical strength and is suitable for the fields of preparation of heavy oil hydrogenation demetalization catalysts, residual oil hydrogenation demetalization catalysts and the like.

Description

technical field [0001] The invention relates to a method for preparing an alumina carrier, in particular to a method for preparing an alumina carrier with large pore volume and diameter and concentrated pore distribution. Background technique [0002] With the continuous reduction of oil resources and the increasing trend of heavy and inferior crude oil, heavy oil deep processing technology has been highly valued by refiners at home and abroad. Hydrodemetallization catalysts used for heavy oil, especially vacuum residue with high metal content, are prone to rapid decline and deactivation of catalyst activity due to the deposition of metal impurities such as nickel and vanadium. Catalysts with larger pore volume and larger pore diameter have strong metal and carbon capacity, which can slow down the deactivation of the catalyst and prolong the operation period of the catalyst. The pore structure of the catalyst is determined by the carrier that constitutes the catalyst. There...

Claims

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Application Information

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IPC IPC(8): B01J32/00B01J21/04B01J35/10C10G45/04
Inventor 季洪海沈智奇凌凤香王少军杨卫亚王丽华郭长友
Owner CHINA PETROLEUM & CHEM CORP
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