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Columnar porous catalyst carrier and preparation method thereof

A porous catalyst and columnar technology, which is applied in the field of catalyst carrier preparation, can solve the problems of insufficient strength of amorphous silica, limitations of loading reaction and use, and reduced reaction efficiency, so as to facilitate large-scale production and application, and the design of process steps is reasonable , the effect of low impurity content

Active Publication Date: 2021-02-09
东营一鸣新材料有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Amorphous silica is not strong enough to break easily, so it has limitations in loading reaction and use
Spherical silica products are broken due to the adsorption stress during liquid phase modification, and the strength is not enough in the use after loading, which leads to increased loss, and the broken debris causes increased air resistance and reduces reaction efficiency, so it also has limitations.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] A kind of columnar porous catalyst support, its diameter 10mm, length 30mm, SiO 2 The mass fraction is 95%, the mass fraction of porous plasticizer is 50%, the pore volume is 1.2ml / g, the pore diameter is 20nm, and the specific surface area is 900㎡ / g; Na 2 The mass fraction of O is 0.07%, the mass fraction of CaO is 0.015%, the mass fraction of MgO is 0.012%, and the mass fraction of Fe 2 o 3 The mass fraction is 0.013%; the compressive strength is 120N.

Embodiment 2

[0032] A kind of columnar porous catalyst support, its diameter 1mm, length 3mm, SiO 2 The mass fraction is 50%, the mass fraction of porous plasticizer is 5%, the pore volume is 0.3ml / g, the pore diameter is 2nm, and the specific surface area is 250㎡ / g; Na 2 The mass fraction of O is 0.15%, the mass fraction of CaO is 0.03%, the mass fraction of MgO is 0.03%, and the mass fraction of Fe 2 o 3 The mass fraction is 0.03%; the compressive strength is 50N.

Embodiment 3

[0034] Take 80kg of 60-100 mesh mesoporous silica powder, 10kg of 80-120 mesh diatomite, 10kg of 60-80 mesh activated carbon powder and mix them in the mixer; 40min, mixed evenly to obtain component A; 80kg water, 1kg guar gum, 5kg silica sol, 0.5kg sodium carboxymethyl cellulose, 1kg polyethylene glycol, 1.5kg white oil were added to the mixer and mixed. The rotating speed of the stirring blade of the feeder is 100r / min, and the mixing time is 30min. After mixing evenly, component B is obtained; component A and component B are added to the mixer according to the mass ratio of 1:0.6 and mixed evenly. The rotation speed of the stirring paddle is 60r / min, and the mixing time is 50min. The material is conveyed to the flat-die pellet machine by the conveyor belt to form regular pellets with a diameter of 2.5mm and a length of 8mm; the columnar pellets are dried at 30°C for 24 hours, and the drying temperature is 120°C for 28 hours. The moisture content of the pellets is 8.6%. The...

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Abstract

The invention belongs to the field of catalyst carrier preparation, and discloses a columnar porous catalyst carrier and a preparation method thereof. The mass fraction of SiO2 in the columnar porouscatalyst carrier can reach 95%, the mass fraction of the porous molding agent can reach 50%, the pore volume can reach 1.2 ml / g, and the specific surface area can reach 900 m < 2 > / g; the mass fraction of Na2O is smaller than or equal to 0.15%, the mass fraction of CaO, MgO and Fe2O3 is smaller than or equal to 0.03%, and the compressive strength can reach 120 N. The preparation method of the columnar porous catalyst carrier comprises the following six production steps: preparing a component A, preparing a component B, mixing the component A with the component B, granulating, aging and drying.The columnar porous catalyst carrier is large in pore volume and specific surface area, high in compressive strength, low in metal ion impurity content, capable of avoiding particle breakage in loading or use, capable of effectively avoiding pollution to a reaction system and products in the use process, environmentally friendly in the production process and wide in application field.

Description

technical field [0001] The invention belongs to the field of catalyst carrier preparation, in particular to a columnar porous catalyst carrier and a preparation method thereof. Background technique [0002] The main chemical formula of mesoporous silica is mSiO 2 ·nH 2 O, its chemical properties are stable, non-combustible, non-toxic and tasteless, and does not react with other substances except hydrofluoric acid and liquid alkali. It is mainly used in the separation and purification of the pharmaceutical industry, catalysts and catalyst carriers in the petrochemical industry. Used in desiccant, impurity adsorbent in liquid phase and gas separation, etc. [0003] There are four main methods for preparing mesoporous silica in the prior art: sol-gel method, precipitation method, gas phase method and silicone grease hydrolysis method. The sol-gel method, precipitation method and gas phase method are used in industrial scale production. Both sol-gel method and precipitation m...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/78B01J32/00B01J35/10B01J37/00
CPCB01J23/78B01J23/002B01J37/0018B01J2523/00B01J35/30B01J35/615B01J35/617B01J35/633B01J35/638B01J35/647B01J2523/12B01J2523/22B01J2523/23B01J2523/41B01J2523/842
Inventor 王秀辉孙明成常朝霞徐海朋郭高中
Owner 东营一鸣新材料有限公司