Preparation method capable of increasing macropore volume of silicon dioxide carrier

A silica, macropore volume technology, applied in catalyst carriers, chemical instruments and methods, chemical/physical processes, etc., can solve the problems of reduced processing capacity, insufficient macropores, easy pulverization, etc., and achieve macropore volume. Increase, the effect of expanding the hole is obvious, the effect of adding a large amount

Active Publication Date: 2015-12-16
山东迅达化工集团有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] A common problem with silica supports is that there are few macropores. In some applications, the internal diffusion resistance of some components in the reaction system is relatively large, or the macropores are not enough. It is hoped to increase the macropores.
[0005] Mechanical strength is an important indicator of catalysts. For most industrial processes, if the strength is lower than 100N / cm, there will be more disadvantages, such as fragility and easy pulverization, which will cause further problems such as increased bed pressure drop, bias flow, etc., thereby reducing the processing capacity and shortening the service life of the catalyst
[0006] In recent years, some manufacturers have also used silica sol as a binder, mixed with silica powder, kneaded, extruded (addition of water, cellulose, sage powder, etc.), and then dried and roasted at about 650 ° C to prepare The silica carrier is used to improve the mechanical strength of the carrier, but there is basically no research on how to increase the macropore volume by adding more pore-forming agents under the premise of ensuring the mechanical strength.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Take by weighing 1000g precipitated silica powder (average particle diameter 32um, specific surface area 126m 2 / g,Na 2 (00.15%), 100g polypropylene ultra-fine powder (average particle diameter 8um, get 10g put crucible 600 ℃ of burning and have no visible residue), add in the high-speed mixer that is provided with pressure type atomizing nozzle, seal feed opening , start the mixer to stir, and use the plunger type high-pressure pump as the power, spray 1000g polyacrylamide aqueous solution (mass concentration 0.5%) into atomized spray, stop stirring after 5min, let stand for 5hr, start stirring, and then add 400g silicon Sol (SiO 2 Mass concentration 30%, Na 2 (0.04%, colloidal average diameter 25nm) atomization sprays in, stops the mixer to stir after 5min, discharges, extrudes into the strip of outer diameter 3mm with twin-screw extruder after kneading by kneader, 110 ℃ of drying, Calcined at 660°C for 3 hours to obtain a silica carrier with a measured lateral com...

Embodiment 2

[0027] Weigh 1000g of precipitated silica powder identical to that of Example 1, 300g of polyethylene ultrafine powder (average particle diameter of 16um, take 10g and place it in a crucible at 600°C for burning without visible residue) and add it to the tank equipped with a pressure atomizing nozzle. In the high-speed mixer, close the feed port, start the mixer to stir, and use the plunger type high-pressure pump as the power, first atomize and spray 800g of carboxymethyl cellulose aqueous solution (mass concentration 0.3%), and stop stirring after 5 minutes. Stand still 5hr and start stirring, 600g silica sol (SiO 2 Mass concentration 30%, Na 2 (00.04%, colloid average diameter 10nm) atomization is sprayed into, after 5min, stop mixer and stir, discharge, extrude into the strip of outer diameter 3mm with twin-screw extruder after kneading by kneader, dry at 110 ℃, Calcined at 600°C for 3 hours to obtain a silica carrier with a measured lateral compressive strength of 171N / c...

Embodiment 3

[0030] Take by weighing 1000g of precipitated silica powder identical to that of Example 1, 15g of turnip powder (1250 mesh), 200g of polystyrene superfine powder (average particle diameter 25um, get 10g and put in a crucible at 600°C for burning without visible residue ) into a high-speed mixer provided with a pressure-type atomizing nozzle, close the material opening, open the mixer to stir, and take the plunger type high-pressure pump as power, first 800g α-starch aqueous solution (mass concentration 0.3%, gelatinization temperature 65°C) atomized and sprayed in, stop stirring after 5min, let stand for 5hr and start stirring, then add 700g of silica sol (SiO 2 Mass concentration 20%, Na 2 (0.03%, colloid average diameter 15nm) atomization sprays in, stops the mixer to stir after 5min, discharges, after being kneaded by kneader, extrude into the strip of outer diameter 3mm with twin-screw extruder, 110 ℃ of drying, Calcined at 630°C for 3 hours to obtain a silica carrier wi...

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Abstract

The invention provides a preparation method capable of increasing the macropore volume of a silicon dioxide carrier. The preparation method comprises steps as follows: components comprising, in parts by mass, 100 parts of silicon dioxide powder with the specific surface area of 60 m<2>/g-250 m<2>/g and 10-30 parts of macromolecule ultrafine powder which basically doesn't have any residues after firing and basically doesn't absorb water to be swollen are sufficiently and uniformly mixed; 80-100 parts of a polymer aqueous solution with certain viscosity and with the mass concentration being 0.1%-0.5% is added, the mixture is sufficiently and uniformly mixed, 40-70 parts of silica sol with the concentration being 20%-30% is added, and the mixture is sufficiently and uniformly mixed and placed in an airtight manner; the average diameter of particles of the silica sol ranges from 10 nm to 30 nm, and the polymer basically doesn't have any residues after calcination and is selected from one of polyacrylamide, cellulose and modified starch; the mixture is kneaded and extruded to form strips, the extruded strips are dried and calcined at the temperature of 600 DEG C-670 DEG C for 2-4 hours, and the silicon dioxide carrier is obtained. According to the silicon dioxide carrier, the volume of macropores with the diameters larger than 100nm is higher than 0.10-0.35ml/g, the silicon dioxide carrier has higher mechanical strength, and the side pressure strength is higher than 150 N/cm.

Description

technical field [0001] The invention relates to a preparation method of a catalyst carrier, in particular to a preparation method for increasing the macropore volume of a silica carrier. Background technique [0002] Silica carrier is a common catalyst carrier. Its acid resistance and water resistance are better than commonly used high-temperature alumina such as α-alumina carrier, and it shows better performance in some reaction processes. For example, in the process of selective oxidation of hydrogen sulfide to elemental sulfur, catalysts made of silica carrier-supported active components have slower reaction performance degradation and generally have longer lifespan. Moreover, the Claus of silica carrier The reaction activity is much lower than that of high-temperature alumina, and the selectivity of the prepared catalyst to oxidize hydrogen sulfide to elemental sulfur can be higher than 95%, which is higher than about 90% of the catalyst prepared by loading the same acti...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J32/00B01J35/10B01J21/08
Inventor 崔国栋胡文宾王强
Owner 山东迅达化工集团有限公司
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